Energy Usage, GHG Reduction, Effi ciency and Load Management Manual
Brewers Association Energy Usage, GHG Reduction, Effi ciency and Load Management Manual
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 1 2 BrewersAssociation.org table of contents
Acknowledgements ...... 4 Best Practices - Kitchen Area ...... 39 Introduction ...... 5 Best Practices - Dining Room ...... 40 Section 1: Sector Profi le – Energy Use in Breweries ...... 6 Best Practices - Parking Lot/Outdoor Seating ...... 40 1.1 Overview of Current Energy Use/Greenhouse Gas 3.5 Concerts and Events ...... 41 Performance and Trends ...... 6 Section 4: Onsite Renewable Energy ...... 42 1.2 Regulatory Drivers ...... 7 4.1 Technology and Use Application Review ...... 43 1.3 Non-Regulatory Drivers – Image/brand, community ties. . . . 7 4.2 Fuel Availability ...... 43 1.4 Risks and Opportunities – Energy/Greenhouse 4.3 Fuel Supply and Cost ...... 43 Gas Reduction ...... 8 4.4 Size Selection and Infrastructure Impacts...... 44 Section 2: Data Management ...... 9 4.5 Cost and Savings Review ...... 44 2.1 Data Collection ...... 9 4.6 Renewable Energy Certifi cates ...... 45 2.2 Ensuring accuracy ...... 11 Section 5: Brewery Case Studies ...... 46 2.3 Benchmarking – Key Performance Indicators (KPIs) ...... 11 5.1 Usage and Reduction ...... 46 2.4 Guidelines for Setting Measureable Goals and Objectives . .13 Boulevard Brewing Company – Kansas City, Missouri . . . . . 46 Section 3: Usage & Reduction Best Practices ...... 15 Deschutes Brewery – Bend, Oregon ...... 46 3.1 Brewing ...... 16 Harpoon Brewery – Boston, Massachusetts ...... 47
Best Practices – CO2 Recovery Systems ...... 16 New Belgium Brewing Company – Fort Collins, Colorado . . 47 3.2 Packaging...... 18 Sierra Nevada Brewing Company – Chico, California . . . . 47 Best Practices - Variable Speed Drives ...... 18 Standing Stone Brewing Company – Ashland, Oregon . . . . 48 3.3 Support Systems (Utilities) ...... 21 5.2 Onsite Renewable Energy ...... 48 Best Practice - Lighting ...... 21 Lucky Labrador Brewing Company – Portland, Oregon . . . 48 Best Practice - Compressed Air ...... 23 New Belgium Brewing Company – Fort Collins, Colorado . . 49 Best Practices – Boiler Effi ciency ...... 26 Sierra Nevada Brewing Company – Chico, California . . . . 49 Best Practices - Boiler Heat Recovery ...... 31 Standing Stone Brewing Company – Ashland, Oregon . . . . 50 Best Practice - Condensate Recovery ...... 33 Victory Brewing Company – Downingtown, Pennsylvania . 50 3.4 Food Service ...... 37 Appendix A: Tool Box ...... 51 Best Practices - Refrigeration ...... 37 Guidance and Checklists ...... 51 Best Practice – Tankless Water Heaters Excel-Based Tools ...... 51 (On-Demand Hot Water) ...... 38 References ...... 52 Best Practices - Cleaning/Sanitization ...... 39 Selected Web Links ...... 53
Cover photos © Shutterstock, LLC. Interior photos provided by Antea Group unless otherwise noted.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 3 acknowledgements
This project would not have been possible without the support of many Brewers Association Members. The case studies they provided illustrate the creativity and application of sustainability best practices in the craft brewing sector.
Our particular thanks go to the following core review team members, who provided invaluable insight and direction throughout the development of this document:
Cheri Chastain, Sierra Nevada Brewing Company
Steve Crandall, Devils Backbone Brewing Company
Daniel Del Grande, Bison Brewing
Tom Flores, Brewers Alley
Matt Gilliland, New Belgium Brewing Company
Larry Horwitz, Iron Hill Brewery
Chris Opela, Brewmaster, Inc.
Chris Swersey, Brewers Association
Mike Utz, Boulevard Brewing Company
We would also like to thank the sustainability management consulting team from Antea® Group who developed this manual and related tools, and in particular acknowledge Antea Group’s Project Leader John Stier.
4 BrewersAssociation.org introduction
Craft brewers are an innovative segment of the greater This manual is a consolidated resource for effective brewing industry. It’s no surprise that many craft brewers energy management and greenhouse gas reduction have discovered innovative solutions for energy usage and solutions in the craft brewers segment. Solutions outlined GHG reduction opportunities at their facilities. Considering can apply to all breweries, regardless of location and the rising energy costs of today, reducing energy usage operational size. Guidance is provided for brewers that should be a high priority at all breweries. are just beginning to explore energy management and GHG reduction programs, as well as for brewers that are Owners and operators may consider energy costs as an looking to improve a well established program. expense they cannot control, and that it only rises and falls with the price of energy in the area. Depending on these In addition, there are checklists, resource lists, and other costs, energy reduction may not be a top priority within visual tools throughout the manual and in Appendix A to brewery operations, but breweries that do not pay attention help breweries make decisions about energy efficiency to the opportunities at all levels of their operations may and GHG reduction opportunities. miss out on potential cost saving and revenue generating measures. There are many best practices for energy effi ciency and conservation that can be easily incorporated Disclaimer: the following information provided constitute into daily operations, as well as solutions that can reach suggestions that may or may not fi t the need of each beyond greenhouse gas (GHG) reduction and lead to brewery specifi cally. Brewers should proceed with operating cost reductions, additional sources of income, and caution when implementing any new programs. It is not new community initiatives. These solutions help brewers save guaranteed that operating under the guidance of this money and become industry leaders in sustainable practices. manual will lead to any particular outcome or result.
The information presented is a pathway to effective and sustainable energy and GHG management from start to fi nish. This information is organized into fi ve sections:
1. Segment Profi le: A discussion of energy usage 3. Best Practices: Guidance on best practices to and GHG generation, where to fi nd infor- conserve energy and reduce GHG emissions mation on regulatory drivers, examples of within the craft brewers segment with a focus on non-regulatory drivers, and risks and oppor- opportunities in the brewing process, packaging, tunities for cost savings. warehousing, utilities, and food service/events.
2. Data Management: A guide to identifying 4. Onsite Energy Reduction: An overview of driv- the components of brewery energy usage, ers for onsite energy and GHG reduction and establishing key performance indicators example projects. and goals, managing energy and carbon footprint data, and benchmarking energy 5. Case Studies: Examples of successful energy efficiency and GHG reduction progress management and GHG reduction programs toward goals. used by craft brewers.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 5 section one Sector Profi le – Energy Use in Breweries
Energy is an operating cost that often gets treated either as a necessary evil, or, at worst, it is ignored all together. Energy Consumption In Breweries (All Sizes) Energy, in its various forms, touches all areas of the brewing Data from the U.S. Environmental Protection Agency (EPA) show business. Understanding just how energy is used throughout that refrigeration, packaging and compressed aire consume 70% of U.S. breweries’ electricity use (A), whereas the brewhouse the operation can turn a perceived necessary evil into a dominates natural gas and coal use at 45 percent (B). competitive advantage. A. Electricity B. Natural gas The intent of this section is to outline how energy is profi led Boiler house Lighting 5% within a brewery and brewpub. Knowing and understanding 6% Space heating how energy is used and where the largest users reside will 10% provide a fi rst step in managing energy costs. This leads to Brewhouse 7% improved effi ciency that will allow for long-term cost savings, Utilities lower GHG emissions, and improved competitive position. Refrigeration Compressed air 20% Brewhouse 35% 10% 45% Energy usage in breweries varies depending on size, location, Other 12% Packaging and product. Refrigeration generally creates the largest Packaging 25% electrical load, while brewing consumes the largest amount 25% of natural gas (used for heat). Below are graphs that illustrate the percentage of energy used throughout the operation. Energy Consumption Within The Food Service Environment (Ifma 2009) Energy usage also varies among brewpub operations. Food preparation and Heating Ventilating and Air Conditioning (HVAC) consume the greatest amount of energy. Refrigeration Sanitation 18% 6% HVAC 1.1 Overview of Current Energy Use/ 28% Greenhouse Gas Performance and Trends Lighting 13%
Energy used in a brewery breaks down into two primary Food preparation units. Thermal energy in the form of natural gas is used to 35% generate hot water and steam, which is then used in brewing, packaging and general building heating. Electrical energy is used to power all equipment, with the largest user being © E Source; data from the U.S. Environmental Protection Agency refrigeration. Thermal sources average 70% of the energy
6 BrewersAssociation.org Sector Profi le – Energy Use in Breweries
consumed in the brewery; however, it usually only accounts energy effi ciency requirements or Greenhouse Gas Emissions for 30% of the actual energy cost. Based on this, efforts to (GHG) requirements that will have a direct impact on energy reduce electrical energy should be given top priority when usage. Brewers need to take into account all state and local considering energy reduction opportunities, as they account regulatory requirements connected to these two areas to fully for the largest opportunity. understand the energy reduction potential within the brewery or brewpub. The following table shows the average kWh/BBL ranges for breweries of all sizes. In general, smaller breweries have higher kWh/BBL numbers because their smaller volumes do not offset The EPA Mandatory GHG accounting rule applies to the base energy required to brew a barrel of beer. The kWh/ facilities from specifi c industries that directly emit 25,000 BBL represents the amount of energy used to produce one metric tonnes of carbon dioxide equivalent or more barrel of beer. In real terms, at a cost of 6 cents per kWh, the per year. Assuming an average thermal requirement total cost for the numbers listed below would be $3.30 to $4.26 of 1.5 therms per barrel of production and an emission per barrel produced. This information provides details into factor of 5.29 kg CO2 emitted per therm, an average the actual cost of energy and provides real time insight to brewery would produce roughly 125 barrels of beer the operating cost impacts if the kWh/BBL changes month to per metric ton of CO2 emitted. It is unlikely that craft month or if the cost for energy changes. brewers under approximately 3 million barrels of annual production would be susceptible to this rule based on Average Relative Energy Use their size and operations. Naturally this threshold would Electrical Usage 12 to 22 kWh/bbl change if the EPA accounting rule limit changed. Thermal (Natural Gas) 1.3 to 1.5 Therms/bbl Combined 50 to 66 kWh/bbl 1.3 Non-Regulatory Drivers – Image/Brand, Community Ties 1.2 Regulatory Drivers Non-regulatory drivers that impact energy usage and cost are in place today to assist all brewers with lowering energy usage Energy profi les are not only infl uenced by day-to-day and cost. These different programs are designed to provide operations, but also by outside forces that infl uence the cost guidance, tools, and management practices that will allow of doing business. In the energy world, those costs can be for the most effi cient use of energy at the lowest cost possible. masked in the guise of regulatory requirements. Regulatory The programs are offered by both government agencies and drivers focused on energy use can be subject to direct the private sector, such as EPA Energy STAR, ISO50001, Green
Example Energy Effi ciency Programs ITEM ENERGY STAR ISO 50001 Governing Body EPA International Standards Organization Commitment Voluntary Voluntary Energy Effi ciency / Energy Management International Energy Management Standard for Industrial Focus of Standard guidelines for products and facilities and Commercial facilities to manage energy • Energy Management • Energy Measurement • Data collection and tracking • Tracking and reporting management practices Focus Areas • Energy usage reduction • Energy usage data collection • Communication and training • Standards for energy reduction systems and tools • Self-Managed • Adherence to ISO reporting, and verifi cation standards Main Criteria • Energy manage program • Energy Management program • 10% energy reduction over 3 yr period • Lower energy usage • International verifi ed energy practice member • Long-term energy cost savings • Aligns with ISO 9001 and ISO 14001 programs Advantages • Established energy reduction practices • Long term energy usage and cost management
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 7 Building and LEED, as well as through local environmental Many craft brewers are calculating their GHG emissions and centers, such as the Chicago Center for Green Technology. have set targets to reduce them. When calculating a GHG These programs offer low-cost or no-cost information on inventory, there are three areas (or scopes) that brewers track: improving energy effi ciency and conservation, as well as how to develop and implement energy management programs. • Scope 1: Direct emissions result from activities the This information will help brewers continuously implement brewery has direct control over. (e.g., combustion of and develop energy effi cient practices, resulting in lower fuel in an onsite boiler) operating costs and a lower carbon footprint. • Scope 2: Indirect emissions that the company cannot Stakeholder recognition can be achieved through reporting control, but are a direct result of brewery activities. initiatives, certifi cations, and achievement and innovation (e.g., purchased electricity and steam) awards (such as Energy STAR, LEED, and Climate Action Leader). • Scope 3: Other indirect emissions other than purchased electricity and steam. (e.g., GHG Standing Stone Brewery “Sustainable Business emitted during the production of packaging Oregon” award material). While brewers do not have control over how the packaging is produced, they can control Standing Stone Brewery efforts have received where and which packaging is purchased. recognition, including the State of Oregon Sustainability Award, Oregon Business “100 Best There are many different reporting standards and Green Businesses” and Sustainable Business Oregon’s protocols that help breweries calculate their emissions. “Sustainable Business Innovation” award (Operations), Good resources include the BIER (Beverage Industry as well as ongoing media spotlights. Environmental Roundtable) GHG emissions guidance, The Greenhouse Gas Protocol and the Publicly Available Specifi cation 2050 (PAS 2050). Community ties give breweries the unique opportunity to promote energy effi ciency and GHG reduction outside their In the brewing industry, many of the processes that consume facility walls, further supporting brand and image. energy will also create GHG emissions. In most cases, energy reduction efforts will carry the additional benefi t of GHG emissions reduction. New Belgium Brewery FortZED
As part of the FortZED (Zero Energy District) project, Case Studies Fort Collins, Colorado implemented a smart grid component of the city’s “Zero Energy District” plan. Boulevard Brewery installed a zone control strategy Fort Collins has begun implementing a smart grid in the Building Automation System. This system makes project with partners from the Fort ZED consortium. heating and cooling adjustments based on real-time The New Belgium Brewery is one of the test sites. The requirements in each zone, while leaving unoccupied, proposal to implement the smart grid is an $11.2 million non-critical zones relaxed regarding their temperature project with $6 million coming from a Department of requirements. Energy grant. Colorado State University will also take part in the pilot. In 2004, Victory Brewing Company upgraded their brewhouse with a system that recovers much of the primary energy fueling it. Approximately one-third 1.4 Risks and Opportunities – Energy/Greenhouse of the natural gas burned to heat and boil beer is Gas Reduction retained in the system for heating purposes, enabling them to reduce GHG emissions. In the brewing sector, energy can be a large source of GHG emissions, regardless of whether it is produced onsite from combustion of fossil fuels or purchased from an electric There are many different ways breweries can reduce provider. GHGs are also generated throughout the supply their GHG emissions. Once the facility has conducted a chain, from raw materials and packaging production to greenhouse gas emission inventory, their greatest sources of refrigeration, transportation of goods, and GHG emissions from emission can be identifi ed and the necessary improvements waste (carbon footprint). can be made.
8 BrewersAssociation.org section two Data Management
As discussed in Section 1, regardless of the size of the brewery, This section covers best practices in data management, from knowing where the brewery currently stands is the fi rst step establishing a data collection routine and ensuring the data in understanding what direction to take. Understanding the is accurate, to creating key performance indicators and current energy profi le and balance of the operation along setting goals. If followed, this information can result in energy with collecting metrics on energy usage will allow brewers to consumption and cost reduction on a continual basis at a start the journey on energy reduction without spending one spending level that will fi t within the brewer’s budget. dollar on capital projects.
Data management is more than just a component of a 2.1 Data Collection successful program; it is a necessity for a successful business strategy. As discussed previously, there are both risks and opportunities in energy and GHG reduction management. Making informed business decisions to minimize risk and Measurement Is the Key maximize opportunity requires effective data management. The most important step in energy management and conservation is measuring and accounting for energy Effective Data Management System consumption.
GATHERING EVIDENCE The best-kept secret within the energy world is that the most important energy effi ciency, conservation, or reduction opportunity that can be installed at a brewery or brewpub is an energy data and tracking program. Installing high effi ciency lighting, heat recovery, and energy star equipment are TARGET WORKING good practices that will lower energy usage and cost. When SETTING WITH DATA these saving opportunities are combined with an energy management program, continual long-term reductions in kWh usage and cost will be achieved. Managing the energy data will prevent the savings that are achieved by capital projects and operation practices from being maintained. READING AND ANALYSING DATA Energy data can be as simple as collecting and analyzing monthly gas and electric bills, to using energy management
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 9 systems that use meters and software to track energy Level 2 data collection involves the following tasks: usage. Typically, the more data available, higher degrees of analysis can be performed, which can result in higher • All Level 1 tasks reduction amounts. Even though each brewer is unique, • Breaking down energy profi le by area: each brewery shares in one common thing when it comes • Brewing (electrical and fuel kWh usage) to energy usage – each receives an energy bill. These bills • Packaging (electrical and fuel kWh usage) form the foundation for all energy data collection and • Utility Support (electrical and fuel kWh usage) tracking programs. It is from these statements that the • Warehouse (electrical and fuel kWh usage) energy data tree will be developed. • Offi ces (electrical and fuel kWh usage) • Brewpub/restaurant (electrical and fuel kWh Below are examples of different energy data levels that usage) can be incorporated at a given facility. The size of the • Additional metering (may be required for this level facility and its power consumption along with fi nancial and of data collection) human resources will determine what type of energy data collection and tracking program should be installed. Level 3 data collection involves the conducting Level 1 and Level 2 tasks at the following specifi c locations within the Level 1 data collection involves the following tasks: process or equipment:
• Collecting energy bills monthly • Brew Line 1 (energy usage) • Tracking data in a spreadsheet • Bottle Line 1 (energy usage) • Graphing data from electric bills, gas bills and • Draught line 2 (energy usage) produced barrels • Air compressor 1 (kWh usage) • Boiler 1 (energy usage) • Main offi ce (energy usage)
Tabular Example of One Full Year of Data Collection
Item January February March April May June July August Septem- November December Totals ber Electircal kWh 40,000 45,000 39,000 39,500 50,000 50,000 40,000 35,000 40,000 42,000 30,000 450,500 Fuel kWh 90,000 92,000 80,000 75,000 72,000 73,000 72,000 65,000 67,000 75,000 85,000 846,000 Elect Cost $4,000 $4,500 $3,900 $3,950 $5,000 $5,000 $4,000 $3,500 $4,000 $4,200 $3,000 $45,050 Fuel Cost $1,800 $1,840 $1,600 $1,500 $1,440 $1,460 $1,440 $1,300 $1,340 $1,500 $1,700 $16,920 Total Enegy Cost $5,800 $6,340 $5,500 $5,450 $6,440 $6,460 $5,440 $4,800 $5,340 $5,700 $4,700 $61,970 Total Energy kWh 130,000 137,000 119,000 114,500 122,000 123,000 112,000 100,000 107,000 117,000 115,000 1,296,500
Data in this tabular format provides a visual reference of the brewery’s energy usage and cost compared to the number of produced beer barrels. Data can be graphed to better trend and understand usage and cost data.
Energy Usage vs. Barrels Produced Trend Energy Cost vs. Barrels Produced Trend
6,000 3,000 100,00 3,000 90,000 5,000 2,500 80,000 2,500 70,000 4,000 2,000 2,000 60,000 3,000 1,500 Electrical Cost 50,000 1,500 Electrical kWh Fuel Cost 40,000 Fuel kWh 2,000 1,000 1,000 30,000 Barrels Produced Barrels Produced 1,000 500 20,000 500 10,000 0 0 r 0 0 ry y h l y e y r r e a r ri l st e e r rc n b y y h il t e u p Ju b r r r e ly s er ber n ua a Ma Ju gu mb a a rc p n u b b r A m e u a A May u J gu m a M em e nu r M J u m e J Au t v a b A tem c Feb p o ec J e e F ep ove e N D S N D S
10 BrewersAssociation.org Data Management
employees, management, etc.). Breweries which have Sierra Nevada Sustainability Report, Energy collected information for several years can report progress Monitoring toward energy and GHG reduction goals and overall cost savings. For breweries new to energy management and To track energy consumption and generation at the GHG reduction programs and those well established in facility, we installed an energy monitoring system this area, it is always important to communicate both called Green Energy Management Systems (GEMS) the starting point and the ultimate goals and targets it is that monitors solar output, all four fuel cells, purchased aiming to achieve. electricity, and electricity sold back to the grid during overproduction period. Tracking energy production and consumption on a real time basis allows us to Management Tips When Measuring and Accounting identify spikes and dips in consumption and be better For Energy Consumption prepared to minimize peak demand charges. In order to expand the benefi ts of monitoring, we plan to start • Consider developing meaningful energy monitoring large load use points within the plant to performance indicators specifi c to your help with load shedding and shifting during peak hours brewery’s needs when electricity is the most expensive. • Conduct seminars or awareness sessions for all operators to explain: We track electricity consumption by kWh consumed º The energy costs and the means of their per barrel (BBL) of beer produced. One of the road control blocks we face in our energy tracking program is that º The effect of good housekeeping on driving
the entire Sierra Nevada campus—restaurant, CO2 the energy costs down recover, waste water treatment facility, etc.—are all º The importance of proper operational on the same electricity meter, making it very diffi cult to practices break out brewing energy consumption. However, in the • Review the indicators regularly at operations last four years we have successfully reduced our overall management meetings electricity consumption while increasing production. • Keep employees informed - communicate the results • Use the energy cost results in developing and reviewing of business plans, alternate energy 2.2 Ensuring Accuracy plans and capital projects • Use the energy cost indicators as a management tool to improve performance After data measures for energy effi ciency and GHG reductions are identifi ed and quantifi ed, the information Source: Canadian Brewers Association 2010 Energy Guide should always be reviewed for accuracy. Without reliable data, especially as the starting point, it will be diffi cult to track progress. Having accurate initial data is also important to monitor for new energy effi ciency opportunities and GHG reduction points, identify mid-point goal milestones, and cost 2.3 Benchmarking – Key Performance savings. Indicators (KPIs)
To verify the data, three key questions are: Collecting and ensuring accurate tracking of energy data will help operators and management teams • Does the amount of energy used appear reasonable understand the relationship between energy usage and based on the amount of beer produced? costs and production, and month-to-month variances. • Is the amount of energy consistent with historical To improve energy reduction efforts, breweries should usage (e.g., last month and the same time last develop a brewery culture that manages energy usage year)? to Key Performance Indicators (KPIs). These KPIs should • Is there any missing data that should be included be developed and benchmarked at least monthly (e.g., new bottle line)? and annually. Monitoring of KPIs and corrective actions implemented from benchmark analysis will provide After the data are verifi ed and approved, the information continuous low cost opportunities for lowering energy cost should be shared with team members (e.g. brewery and carbon footprint.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 11 The most important part of developing a KPI is determining its variables. The denominator is the variable that is Calculation of Cost Savings intended to be reduced, while the numerator is expected to grow. In this particular manual, the denominator is kWh • At 49 kWh/BBL x 22,500 BBLS = 1,102,500 kWh/yr. and numerator is the number of produced barrels of beer • At average total energy cost of $0.047/kWh the (BBL). This KPI (kWh/BBL produced) will allow operators to total cost = $51,817 manage the energy intensity on a regular basis. As the goal • Potential savings: $61,970 - $51,817 = $10,153 or is to lower kWh for BBL produced, the KPI demonstrates the 17% of energy yearly cost brewery’s success at lowering its energy levels.
For example, the calculation used to determine the main This example shows the benefi ts of developing and energy KPI is as follows: tracking energy usage in comparison to barrels produced. Capturing 17% of savings on a consistent basis may not be Energy practical due to weather conditions, equipment, product Total kWh used / Total barrels produced = Intensity mix etc., however, the data provides a reference point Ratio and ideal goal. A potential next step could be to develop management techniques and goals that can be used to An example of successful energy reduction at a brewery is lower energy usage and capture a portion of the $10,153 shown below: savings.
190 A Level 1 energy data collection program performs the 180 calculations above and benchmarks monthly energy
170 intensity KPIs in order to lower energy usage and cost. Level 2 and Level 3 energy data collection programs may consider 160 additional energy KPIs. 150 MJ per HL 140 These examples outline additional KPIs that may be tracked
130 and used to manage energy usage in brewery operations. Each brewer can develop specifi c KPIs to help manage 120 F95 F96 F97 F98 F99 F00 F01 F02 F03 F04 F05 F06 F07 F08 their particular processes to improve energy effi ciency and lower cost.
Energy Intensity
Using examples in Section 2.1 the following KPI information can be derived:
Item January February March April May June July August Septem- November December Totals ber Electrical kWh 40,000 45,000 39,000 39,500 50,000 50,000 40,000 35,000 40,000 42,000 30,000 450,500 Fuel kWh 90,000 92,000 80,000 75,000 72,000 73,000 72,000 65,000 67,000 75,000 85,000 846,000 Total Enegry kWh 130,000 137,000 119,000 114,500 122,000 123,000 112,000 100,000 107,000 117,000 115,000 1,296,500 Barrels Produced 2,000 2,200 1,800 2,000 2,500 2,500 2,000 1,800 2,000 2,100 1,600 22,500
The KPI in the example above ranges from 49kWh/BBL to 72kWh/BBL. This data highlights potential savings that exist in the brewery’s operations. Based on total annual energy cost of $61,970 and an annual production of 22,500 BBLs, the total energy cost per barrel is $2.74/BBL. ($61,970/22,500 BBLs = $2.74/BBL).
12 BrewersAssociation.org Data Management
Additional KPIs to track AREA METRIC METRIC Brewhouse kWh/BBL brewed • Establish an energy baseline across the facility. • Determine a base year for data benchmarking. Packaging kWh/BBL packaged kWh/Case • Decide how the goal will be tracked - in absolute Refrigeration kWh/ BBL shipped kWh/kg energy usage reduction (kWh used) or normalized Steam System kWh/BBL shipped kWh/kg energy usage (kWh/BBL). Most breweries set targets Compressed Air kWh/BBL shipped kWh/cubic meters for both metrics. Electrical Energy kWh/BBL shipped • Review energy baseline data with all team members involved in developing and implementing the energy reduction program. Restaurants and brewpubs can also develop and use KPIs • Prepare a list of energy practices and projects that to manage energy usage. The denominator in most cases can be used to help lower energy usage. will depend on which variable will provide the best data for • Determine the potential impact savings will have benchmarking. Examples of denominators for restaurants and on the baseline energy usage. brewpubs include: • Determine what percentage of reduction can be achieved as well as a stretch percentage to allow • Hours of operation for innovation. • Total Sales • Establish the goal. • Number of meals and drinks served • Square footage (use if no other normalizer is available) Example Scenario The denominator should be a consistent variable that changes over time. Based on typical energy usage in restaurants as Based on discussion with operations, maintenance described in Section 1, 60-70% of energy is used within HVAC and and fi nance it was determined that fi ve separate food prep. The best denominator to adjust for one or both of these energy reduction projects can be developed variables may be the best choice for KPI or KPIs. and implemented resulting in a 2% overall energy reduction. Operations reported that through best practices, employee training and procurement 2.4 Guidelines For Setting Measurable Goals changes, an additional 1.5% reduction in energy And Objectives can be achieved. Combining the two could result in a 3.5% energy savings overall. A good target or goal must be realistic and achievable. Energy affects all aspects of brewery business, making Further discussion ensues and the team agrees to add energy reduction goals diffi cult to set and implement. It is 1% to the potential saving and establish an overall imperative to establish an energy management program goal of 4.5% energy reduction for the upcoming fi scal that tracks energy usage to review if the brewery’s energy year. reduction initiatives are achieving the target savings goals. The steps for developing short-term goals are:
Examples Of Goal Setting ENERGY EFFICIENCY GOAL PROGRESS TO GOAL Improve energy effi ciency by 20% between 2006 and 2010 with 2005 as Through 2008, energy effi ciency has been improved by 19.2%. the baseline year. Reduce the amount of electrical energy used by 5% from 2006 to 2010 Electrical energy consumed per square foot has decreased by using 2005 as the baseline year both on an absolute and normalized to 22% between 2005 and 2008. square footage basis. 7% reduction in energy use corporate-wide by 2018 with a baseline year 2.7% reduction corporate wide as of November 2008. of 2003. Reduce energy intensity by 2% per year through 2012 from 2001 base. 2012 goal was achieved in 2007, with a measure that was 23% below the 2001 base. Achieve 50% reduction in energy usage by 2012 with a baseline of 2002. Reduced total energy usage (both direct and indirect) by approximately 41% from the 2002 Baseline.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 13 Establishing a long-term reduction follows a similar path, Managing the Energy Reduction Goal however these goals should account for business growth, capital availability, and external considerations. Long- • Involve employees to implement energy savings term goals should be realistic and achievable, support and conservation practices short-term goals, and be fl exible to meet business needs. • Develop and implement energy reduction projects Long-term goals should extend 3 to 5 years and develop envisioned to achieve goal periodic milestones to ensure that the target is being met. • Form an energy team with an energy champion A benchmarking plan should be established based on and meet monthly to review the energy data and brewery size, data maturity, etc. After the goal has been variances to the target established, the target can be developed. • Implement corrective actions if necessary • Determine why any savings were achieved and if these actions can be permanent • Give business conditions priority over energy program goals; however, by taking immediate corrective action, over time the brewery will reduce energy usage, employees will be more aware of how energy is used, and the program will become more effi cient.
Tracking example
The example in Section 2.2 established an average energy intensity ratio of 58kWh/BBL using the short-term goal of 4.5% reduction. A new monthly target can be established and used to track progress towards the goal.
FY2012
Item January February March April May June July August Septem- November December Totals ber Electircal kWh 40,000 45,000 39,000 39,500 50,000 50,000 40,000 35,000 40,000 42,000 30,000 450,500 Fuel kWh 90,000 92,000 80,000 75,000 72,000 73,000 72,000 65,000 67,000 75,000 85,000 846,000 Total Energy kWh 130,000 137,000 119,000 114,500 122,000 123,000 112,000 100,000 107,000 117,000 115,000 1,296,500 Barrels Produced 2,000 2,200 1,800 2,000 2,500 2,500 2,000 1,800 2,000 2,100 1,600 22,500 Energy Intensity KPI (kWh/BBLs 65 62 66 57 49 49 56 56 54 56 72 58 produced)
FY2013
Item January February March April May June July August Septem- November December Totals ber Electircal kWh Fuel kWh
Total Energy kWh
Barrels Produced
Energy Intensity KPI (kWh/BBLs produced) Actual
Energy Intensity KPI (kWh/BBLs produced) 62 59 63 55 47 47 53 53 51 53 69 55 Monthly Target
14 BrewersAssociation.org Usage & Reduction Best Practices
section three Usage & Reduction Best Practices
This section will discuss opportunities within all brewery and • Cleaning exhaust fans and repairing or replacing restaurant operations that will help achieve energy reduction. loose or broken belts on fans The most important aspects of energy reduction processes • Cleaning condenser coils are engaging in data collection systems that manage • Insulating refrigerant suction lines energy usage and engaging employees and customers with • Checking walk-in coolers to ensure defrost timers the brewery’s energy effi ciency and conservation culture. are set properly Employees and customers alike can experience the benefi ts • Maintaining good air fl ow around evaporators of energy reduction in both their workplace and homes. remove debris and other objects that may block air fl ow Within brewery and restaurant operations there are numerous • Repairing or replacing leaky or damaged HVAC opportunities to lower energy usage and cost. Defi ning, duct work prioritizing, and implementing these opportunities can be an intimidating task. Follow the three steps below to get started: Moderate Cost: These projects tend to be a little more expensive to implement in the beginning, but still lead to 1. Ensure that a data collection and tracking system is in cost savings in the medium turn. The range of payback place or being developed. period could be between 2 to 4 years.
2. Defi ne business case priorities for implementing energy Examples include: savings opportunities: • Variable speed drives (process, HVAC, and support applications) 3. Defi ne and set a goal for energy reduction; communicate • High-effi ciency lighting systems and engage all employees. • Motion sensors • New insulation Potential energy reduction opportunities can be grouped by • High-effi ciency HVAC units brewery department (brewing, packaging, etc.) or by low, • Automated building energy management system moderate and major cost. (EMS) • Excess air control for boilers Low Cost: These opportunities typically have low capital cost, • Improving condensate return immediate payback, are easy to implement and are known • Certain brewhouse heat recovery projects as “low hanging fruit” in most circles. • Purchasing ENERGY STAR equipment • Replacing HVAC units older than 15 years with Examples include: higher effi cient SEER unit • Repairing steam and air leaks • Installing programmable controllers and using • Shutting down equipment when not used set back temperature settings during hours when • Shutting off lighting in areas where lighting is not facility is not occupied required • Installing window blinds or shades for daytime heat • Changing air fi lters reduction • Replacing incandescent bulbs with CFL or LED lamps • Reducing start up time for boilers, conveyors etc. • Repairing frail or missing insulation • Turning off warming cabinets when not in use
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 15 • Ensuring hot water heater set points for food prep, Factors that may infl uence plant energy levels include: restroom facilities etc. are set properly • Maintenance - Regularly performed maintenance activities can result in improved energy effi ciency Major Cost: These opportunities require the most capital within the brewery operation. Maintenance expenditure at the onset. The range of time to recoup personnel should inspect for leaks, broken belts, investment could be more than 3 years. stuck dampers, dirty fi lters and a host of other day-to- day operational equipment conditions. Employing Examples include: effi cient maintenance strategies in a timely manner • Boiler fl ue stack heat recovery condenser will result in lower operating cost as well as lower • Brew kettle stack heat recovery energy usage and can be accomplished without • Renewables using capital dollars. • New equipment (VSD air compressor, refrigeration • Occupancy - Is energy use consistent with chiller, etc.) occupancy? Compare usage during the week with • Installing high-grade energy-effi cient windows and usage at night, weekends or holidays and see if doors energy is being consumed outside of working hours. • Installing a “white” or “green” roof for the brewery • Production levels - Compare energy use against production levels. Increased production will usually These cost categories will be used throughout this section cause increased energy use. However, this may to align opportunities with cost, savings and payback. mask the true relationship, as the lighting or cooling/ Some opportunities could fall into more than one category heating energy use may not change much against - business objectives, capital restraints and other conditions production levels. Therefore try to separate out non- will determine how the opportunity is categorized. production related energy use in normalizing data. • Weather - Daily or seasonal variations in the Low-cost efforts should be defi ned and implemented before weather will infl uence energy use. There should be moving on to the higher cost categories. a direct relationship between weather conditions and energy use. The following table summarizes the top ten energy savings opportunities for breweries and brewpubs/restaurants: 3.1 Brewing Top 10 Energy Best Practices; Breweries and Brewpubs/Restaurants The previous section provided best practice examples ITEM TOP 10 BREWERY RELATED ENERGY BEST PRACTICES grouped into low, moderate and major cost initiatives. (1) Turn off equipment when not in use It also introduced the concept of a top ten list for energy (2) Engage employees on how to conserve and use energy reduction. This section focuses on additional best practices more effi ciently specifi c to brewing. (3) Replace air fi lters on air handlers, HVAC units etc. on regular intervals Best Practices – CO2 Recovery Systems (4) Identify and repair compressed air, steam and water leaks
(5) Repair or Replace damaged or missing insulation A major byproduct of the brewing process is CO2. CO2 is (6) Eliminate the use of compressed air for cleaning, cooling or generated during the fermentation process and depending
other applications on the brewer the CO2 will be vented or captured for reuse
(7) Review all energy set points on a regular basis within the brewing system. CO2 gas is also needed in the brewing process for bottling, fl ushing, carbonation, tank (8) Upgrade incandescent, T-12 Fluorescent to more effi cient lighting types blankets and other uses. Capturing CO2 and reusing the gas (9) Collect steam condensate will lower operating cost, reduce the risk to the product and provides the opportunity to improve energy effi ciency within (10) Purchase and install energy effi cient equipment the brewery.
16 BrewersAssociation.org Usage & Reduction Best Practices
There are different types of CO2 recovery systems that are CO2 recovery systems that transform CO2 collected available to capture and reuse CO2. The system incorporated earlier in the fermentation process incorporates the use will depend on the operation, the size of the brewer, the of a liquefaction/stripping system that allows for CO2 to physical footprint of the brewery and the cost to purchase be collected at 80% to 99.5% impurities levels and be
CO2 within a given region. transformed to purity levels of <5ppmv O2. Collecting CO2
earlier will allow for larger quantities of CO2 to be collected
CO2 recovery systems can be purchased in modular skid- which results in third party purchases being reduced, lower mounted standard design systems for smaller breweries to risk to CO2 quality impacts, and supply. systems that are designed to match the process fl ow and equipment to the CO2 recovery needs. These systems can The diagram below shows the traditional CO2 collection range in size from 18 kg/h to 9,000 kg/h. methods and the installation of CO2 stripper/reboiler
that allows for less pure CO2 to be collected and purifi ed
CO2 recovery begins within 24 hours of fermentation; meeting brewing quality requirements. Please note that however, due to the impurities in the CO2 gases, venting of many manufactures provide solutions with this technology. the gas may occur until the high concentrations of nitrogen This system can be provided for CO2 collection for small- and oxygen are reduced to 99.5 or greater volume %. The volume and large-volume breweries. gas is then collected cleaned, dried and in some cases compressed to be storage for later use. With this process Traditional CO2 Collection Methods and the Installation of CO2 the gas will then be re-vaporized when needed within Stripper/Reboiler2 the brewing process. With this process about 50% of the released CO2 can be captured for reuse. The remaining
CO2 needed within the brewery will need to be purchased Fermentation from a third party. C0 Vapor 2
The Standard Method for CO Recovery1 2 Foam drain
Foam separator Gas washer
C02 condenser Refrigeration unit
Stripper Reboiler (optional)
C0 to consumers C02 evaporator 2
C02 compressor Activated carbon filter/driers
Energy effi ciency can be achieved within the CO2 recovery
system as well. If CO2 is collected and stored as a liquid under pressure for future use it must be vaporized from a liquid to a gas for use in the brewing process. The vaporization process
Collecting the CO2 earlier in the fermentation process, when requires heat to change the state of the CO2. In some cases concentrations of nitrogen and oxygen are higher, would this vaporization process uses steam, hot water or electric result in less CO2 being released to the atmosphere and also heaters to convert the liquid to gas. allow for larger quantities of CO2 to be captured for reuse within the brewing process. In some cases the amount of CO2 However, there is an opportunity to convert the cold energy recovered may exceed the needs of the brewer allowing stored in the CO2 to secondary refrigeration system. Installing the brewer to be self-suffi cient in CO2 production. a heat exchanger with cold CO2 liquid on one side.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 17 3 CO2 Cold Energy Conversion 3.2 Packaging
Best Practices - Variable Speed Drives
A variable speed drive (VSD) works by converting the incoming electrical supply of fi xed frequency into a variable frequency output. This variation in frequency allows the drive to control how the motor operates — a low frequency for a slow speed and a higher frequency for a faster speed. The output can also be changed which enables the motor to generate more or less torque as needed. The motor and drive combination can therefore be used for turning a large load at fairly slow speeds, or turning a lighter load at high speeds, thus maximizing effi ciency.
VSDs are supplied in a wide range of sizes (from 0.18 kW to several MW) and may be optimized to suit particular applications. Though not all applications benefi t from variable control, the main benefi ts are: and warm glycol or water returning from the process to the
refrigeration chillers can be used to vaporize the CO2 and • Improved process control resulting in output the heat extracted from the warm stream will help lower product quality energy usage as well. This heat recovery process will help • Programmable soft starting, soft stopping and lower energy usage and cost associated with the steam, dynamic braking, which reduce excessive stress
hot water or electricity used to vaporize CO2. placed on the motor and extend its life • Wide range of speed, torque and power output
Advantages of CO2 Recovery giving a greater degree of control (For example, • Lower operating cost (limit third-party purchase) the electronically controlled VSD has the ability to
• Lower environmental impact (less CO2 vented) set various parameters such as allowing differing Reduce risk to beer quality (use brewery-produced acceleration rates for different speed changes or
CO2) having the ability to increase/decrease the torque
• Reduce risk to supply (changes in CO2 suppliers) output at different speeds. • Improved effi ciency through an increase in the
Barriers to CO2 Recovery power factor of the system - this means that more
• Low cost and ample supply of third party CO2 of the current drawn is actually used to drive the
• Low volume of CO2 generation load, making it more effi cient. • Limited footprint to install CO2 recovery system • Dynamic response comparable to DC drives • Capital restraints or low ROI for collecting CO2 leading to better control • Energy savings in many applications - there are a
Factors to Consider When Investigating CO2 Recovery number of applications where it is possible to reduce
• Amount of CO2 vented on an annual basis the speed of a motor while keeping the same
• Amount of CO2 purchased outcome (such as in ventilation systems designed to
• Cost of CO2 purchased satisfy a building’s maximum occupancy). In most
• CO2 supplier network (stability, quality, availability etc.) cases, installing an electronic VSD is the most effi cient
• Available footprint for CO2 recovery equipment method of doing this.
• Capital cost for CO2 recovery system • Type of system required When applied properly, variable frequency drives (VFDs)
• Partial collection that collects CO2 at high purity or VSDs are very effective motor controllers in bottling
levels (may need to purchase additional CO2) operations. Modern VSDs are affordable and reliable, have • Complete system that includes stripper/reboiler fl exibility of control, and offer signifi cant electrical energy
allowing for earlier collection of CO2 (may allow savings (savings from 10 – 60%) through greatly reduced
brewer to be CO2 self-suffi cient) electric bills.
18 BrewersAssociation.org Usage & Reduction Best Practices
VSDs and VFDs are used in a wide variety of applications for Consequently, a 20% reduction of the rotational speed leads various reasons, such as in pump and fan applications where to a 49% reduction in power requirement. These relationships they are the most effective energy savers. and resulting energy savings achieved by VSDs are due to the pressure difference across the impeller or valve. When To obtain a clear understanding of the proper and most less pressure is produced, less acceleration of air or fl uid effective application of VSDs, it is essential to gain a working across the impeller is required. It is the simultaneous reduction knowledge of VSD basic theory as well as a strong familiarity of acceleration and pressure that multiplies the savings. with practices. It is important to note that a VSD does not constrain the rotational VSD4 speed of a motor to a certain level in order to achieve energy savings. This would mean that the power input would at times be insuffi cient. The main advantage of a VSD is that it can alter the rotational speed of a motor so that the power input can match the duty required and diminish energy wasting.
When the system operates without the use of a VSD, the power input remains constant regardless of changes in the load output over time, because the controlling device is a throttle or damper. When a VSD is used, the input power is tailored to suit the output duty. The throttle or damper is eliminated with savings in maintenance. Applying a VSD to a specifi c application is much easier if the requirements of the load are understood. Simply put, the VSD Operation of a System With and Without VSD must have ample capability for the motor so that the motor can produce the required torque for the load. Remember that machine torque is independent of motor speed and POWER DUTY POWER DUTY INPUT REQUIRED INPUT REQUIRED that load horsepower increases linearly with rpm.
Know your load torque requirements. Every load has V distinct torque requirements that vary with the load’s S D CONTROL operation; the motor via the VSD must supply these VALVE CONTROL VALVE ELIMINATED OR LOCKED IN OPEN POSITION requirements. It is important to have a clear understanding Without Variable Speed Drive With Variable Speed Drive of the torque load for each application in which a VSD is being considered. Data can be retrieved from the pump or fan vendor. Although dampers are often used to regulate the output of fans, reducing the speed is a much more effi cient way The speed of an induction motor is proportional to the frequency to achieve the same effect. With damper control, the of the AC voltage applied to it, as well as the number of poles in input power reduces as the fl ow rate decreases. However, the motor stator. This is expressed by the equation: under VSD control, the variable torque characteristics of the fan means that the relationship between fl ow and speed RPM = (f x 120) / p, where f is the frequency in Hz and p is the of the fan is such that the input power reduces in a cube number of poles in any multiple of 2 law relationship with the speed reduction. This is shown in the graph, where the energy expended using a VSD is Therefore, if the frequency applied to the motor is changed, signifi cantly less than the damper-controlled motors. It also the motor speed changes in direct proportion to the shows the limitations of a VSD that it is normally not able to frequency change. The VSD controls the frequency applied reduce the fl ow all the way to zero. to the motor. In a similar way to using damper control in fan applications, VSD’s primarily operate to convert electrical system frequency using throttle control for pumping applications results in a and voltage to the required levels to drive a motor at a speed poor effi ciency as the pump is not being run at its design other than its rated speed. The two most basic functions are point. This is particularly true for applications with a steep to provide power conversion from one frequency to another fl ow/head characteristic, where there is a high static head and to enable control of the output frequency. such as in heating circuits and for small pumps.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 19 Using a VSD to control the pump instead of simple throttle applications where only one speed change is required, a control can result in signifi cant power and cost savings. Note VSD may not be necessary or practical. that on systems with a high static head (for example, boiler feed water pumps), where the pump must overcome the Evaluate the possible application of a VSD on the motors inherent resistance of the system before any fl ow starts, the from the survey. If you answer any of the following questions benefi ts of using VSDs will be slightly reduced. This is because with YES, be extra careful in your VSD selection and setup the additional resistance affects the relationship between parameters of the VSD. the speed of the pump and the fl ow. Factor this into any calculations and consult an equipment supplier for further Will the VSD operate more than one motor? The total peak information if needed. currents of all motor loads under worst operating conditions must be calculated. The VSD must be sized based on this Make an overview of all motors in the plant using the maximum current requirement. following format. Check the following motors specifi cally: • Water pumps that currently use a control valve to Will the load be spinning or coasting when the VSD is vary fl ow or pressure. started? This is very often the case with fan applications. • Conveyer systems that do not have a control of When a VSD is fi rst started, it begins to operate at a low varying line speeds. frequency and voltage and gradually ramps up to a • All pumping systems that control on pressure or fl ow preset speed. If the load is already in motion, it will be (boiler pumps, bottle washer pumps, CIP pumps, out of sync with the VSD. The VSD will attempt to pull the etc.) motor down to the lower frequency, which may require • Fans that control air fl ow, like HVAC, boiler fans, etc. high current levels, usually causing an overcurrent trip. • Compressors (Chillers, compressed air) Because of this, VSD manufacturers offer drives with an option for synchronization with a spinning load; this VSD Data Collection and Documentation of Pumping Equipment ramps at a different frequency.
Location Motor ID Motor Installed power Variable Annual Will the power supply source be switched while the VSD is application (hp or kW) torque / operating demand (Y/N) hours running? This occurs in many buildings, such as hospitals, where loads are switched to standby generators in the event of a power outage. Some drives will ride through a brief power outage while others may not. If your application is of this type, it must be reviewed with the drive manufacturer for a fi nal determination of drive capability.
Defi ne the operating profi le of the load to which the VSD is Is the load considered hard to start? These are the motors to be applied. Include any or all of the “torques” discussed that dim the lights in the building when you hit the start above. Using a recorder (A, V, kW) to record the motor’s button. Remember, the VSD is limited in the amount of current draw under all operating conditions will help in doing overcurrent it can produce for a given period of time. this. Obtain the highest “peak” current readings under the These applications may require oversizing of the VSD for worst conditions. Also, see if the motor has been working in higher current demands. an overloaded condition by checking the motor full-load amps (FLA). An overloaded motor operating at reduced Are starting or stopping times critical? Some applications speeds may not survive the increased temperatures as a may require quick starting or emergency stopping of the result of the reduced cooling effects of the motor at these load. In either case, high currents will be required of the lower speeds. drive. Again, oversizing of the VSD may be required.
Determine why the load operation needs to be changed. Are external motor disconnects required between the motor Very often VSDs have been applied to applications where and the VSD? Service disconnects at motor loads are very all that was required was a “soft start” reduced-voltage often used for maintenance purposes. Normally, removing a controller. The need for the VSD should be based on the load from a VSD while operating does not pose a problem ability to change the load’s speed as required. In those for the VSD. On the other hand, introducing a load to a VSD
20 BrewersAssociation.org Usage & Reduction Best Practices
by closing a motor disconnect while the VSD is operational 3.3 Support Systems (Utilities) can be fatal to the VSD.
Are there power factor correction capacitors being switched Best Practice - Lighting or existing on the intended motor loads? Switching of power factor capacitors usually generates power disturbances in There are many low-cost and no-cost measures that can the distribution system. Many VSDs can and will be affected be utilized to help reduce energy costs, without adversely by this. Isolation transformers or line reactors may be required affecting working conditions. In most cases upgrading for these applications. the existing lighting system will save 30% to 40% of the current electrical energy consumed for lighting systems in While there are many specifi cations associated with drives, an average-sized plant. Choosing a sustainable lighting the following are the most important: solution is an excellent way to reduce energy consumption and overall operational costs. Likewise, sustainable lighting • Continuous run current rating. This is the maximum solutions can provide better, task-appropriate lighting that rms current the VSD can safely handle under all can increase productivity, reduce errors, and improve operating conditions at a fi xed ambient temperature employee well-being throughout a facility. (usually 40 °C (104 F). • Overload current rating. This is an inverse time/ This section provides background knowledge and some current rating that is the maximum current the VSD practical tips on using lighting as cost effectively as possible. can produce for a given time frame. Typical ratings Through strategic planning and performance management are 110% to 150% overcurrent for 1 min, depending of the overall lighting system, costs can be reduced and on the manufacturer. Higher current ratings can lighting quality improved. The objective of this guideline is to be obtained by oversizing the VSD. This rating is show how lighting systems impact your energy consumption very important when sizing the VSD for the currents and help with maintenance and design tips on how to needed by the motor for breakaway torque. reduce the lighting costs across your facility. • Line voltage. As with any motor controller, an operating voltage must be specifi ed. VSDs are Daylighting designed to operate at some nominal voltage such as 240VAC or 480VAC, with an allowable voltage Daylight is an acceptable and desirable light source for variation of plus or minus 10%. Most motor starters building interiors. It uses the light from the sky, or occasionally will operate beyond this 10% variation, but VSDs will sunlight refl ected off building surfaces. Since daylighting not and will go into a protective trip. A recorded components are normally integrated with the original voltage reading of line power deviations is highly building design, it may not be possible to consider them for a recommended for each application. retrofi t project. Light is a key factor (rivaled only by air quality) in a healthy and productive work environment. Therefore, Energy savings depend on operating hours of the motors. A daylighting technologies may provide opportunities to offer safe way of calculating the potential savings is using a 25% the wellness benefi ts of natural light to workers. The guideline saving potential on the current energy use of your motor will focus on electric powered lights given that bottling and (current energy use = kW*operating hours). offi ce facilities employ this type of system as their primary source of light. There are many types of lamps, ballast and A certifi ed electrical engineer or VSD, pump or fan vendor lighting systems used around the world in many different must install the VSD. The supplier will also provide instructions industries this guideline describes lighting sources found at on how to install the VSD and set the right parameter settings. many bottling operations worldwide and will be updated on a regular basis to include new systems as they are introduced. The brewery needs to make sure that the VSD and the motor that the VSD will control are a match. New installations Electric Lamps should have inverter duty rated motors, installed with the VSD to accommodate the necessary cooling for the different The lamp is the source of electric light, the device that speeds. If the VSD is installed with an existing motor that is converts electric power into visible light. All lighting systems, not inverter duty rated the motor life may be shorten due to no matter how complex, have basic performance principles overheating. It is not required to change the motor but the which include the following: reader needs to be aware that this condition may exist and • Lumen output – the amount of light emitted by a the motor may have a shorter life cycle. lamp
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 21 • Effi cacy – the effi ciency of lamps, measured in including high bay applications (indoor spaces with lumens of light per watt of energy. high ceilings), fl ood lighting and street lighting. • Rated lamp life – expected lamp life typically • Incandescent/Halogen lamps - A halogen lamp reported in hours. is a form of incandescent lamp that introduces • Lamp lumen depreciation – the loss of light output traces of halogen gas and a quartz envelope to over time, usually reported as a percentage. burn hotter and prolongs the fi lament life. Halogen • Color temperature (CT) and color rendering (CRI) should be used in lieu of standard incandescent. – a numerical value related to light appearance. Whenever possible, the use of more effi cient • Luminaire – a light fi tting that incorporates the lamp. CFL or ceramic metal halide sources should be • Controls – manual or automatic switching explored. Incandescent/halogen lamp types are equipment, which operates the lighting system very ineffi cient (roughly fi ve times less effi cient than fl uorescent); these lamps should not be used at a A part of a lighting maintenance plan is to fi rst, identify your minimum. lamp types. In manufacturing and industrial facilities lamps • Light Emitting Diodes (LEDs) - Lamps are made of that are primarily utilized are fl uorescent, high intensity an advanced semi-conductor material that emits discharges (HID), incandescent/halogen lamps and light visible light when current passes through it. LEDs emitting diodes (LEDs). The fi rst step in planning a lighting are beginning to see extensive use in a variety maintenance strategy is to defi ne the existing condition of of applications including parking lot lighting and the lighting systems. refrigerated display case lighting. One major disadvantage of LEDs is that these lamps are Fluorescent lamps are typically used in offi ces and currently more expensive, price per lumen, on an commercial buildings and most low bay industrial initial capital cost basis, than more conventional applications: lighting technologies. Also LEDs emit a more tightly • T12 lamps – Linear fl uorescent lamps that are now focused beam that may prove to be too bright. considered obsolete. These were the standard fl uorescent lamps until T8 lamps came on the Fluorescent and high intensity discharge (HID) lamps require market over 20 years ago. ballasts (incandescent lamps do not). Ballasts typically are • T8 lamps - These lamps became popular in the designed to effi ciently operate a specifi c lamp type, so industrial/commercial lighting industry and have lamps and ballasts are chosen together. Electronic ballast become the standard for offi ces and general and magnetic ballast are the two main types of ballasts used applications. Since they are 22% more effi cient than today. Since magnetic ballasts are not as sophisticated as T12s, it is generally always cost-effective to retrofi t electronic ballasts and can be problematic, they are being or replace fi xtures that use T12 lamps in existing replaced by the electronic versions. Electronic ballasts are applications. T8 lamps use the same socket as T12, energy effi cient and therefore lower your monthly energy but not the same ballast. bill. T8 lamps using electronic ballasts are more effi cient than • T5 lamps - These cannot replace T8 lamps because using T12 lamps with magnetic ballasts. they have different characteristics and different lengths, socket confi gurations and ballasts. T5s are Lighting requirements will vary at different times and in smaller lamps than T8s, but have similar effi cacy different parts of a building throughout the day. Ensure that (lumens per watt). lighting controls are set to match demand, that is, when • Compact Fluorescent Lamps (CFLs) - Fluorescent required during business hours. lamps with a single base and bent-tube construction. The fi rst CFLs had a screw-type base. While A comprehensive strategy may use manual or automatic screw base lamps are still available, commercial control devices in concert, responding to plant specifi c applications typically use lamps with a 4-pin base. usage patterns. However, automatic controls allows for greater savings in cost and usage. Other lighting options include: • High Intensity Discharge (HID) - Lamps use a gas- Today most lighting controls are focused on fl uorescent fi lled tube to generate light, but use arc current and lamps and fi xtures due to their ability to function in a rapid vaporized metals at relatively high temperatures start mode. The inclusion of motion sensors in areas where and pressures. There are two main types in current traffi c is infrequent or limited may increase the energy use – metal halide (MH) and high-pressure sodium savings attributed to the lighting upgrade by an additional (HPS). Both can be used for industrial lighting 5 to 10%.
22 BrewersAssociation.org Usage & Reduction Best Practices
Automatic controls provide benefi ts in user comfort and ballasts in pairs since they are operated and wired energy conservation. Automatic controls can deliver reliable in pairs (two fl uorescent lamps from a four-lamp energy savings without personnel or employee participation. fi xture). With electronic ballasts, each lamp can be controlled individually. The following are examples of automatic controls: • If the ballast operates in parallel, lamps can be • Occupancy sensors turn off the lights when they de- removed without removing all the lamps. tect that no occupants are present. The occupancy • Use compact fl uorescent lighting (CFLs) in place of sensor includes a motion sensor, a control unit, and incandescent lamps. a relay for switching the lights. Ultrasonic and Passive • Consider connecting outdoor and indoor lighting to Infrared sensor technology are utilized in detecting an energy management system if not already, for motion and heat of occupants. They can be used indoor and outdoor lighting. together in a dual-technology fashion. High quality occupancy sensors use the dual technology, since it Maintenance Planning is more reliable than each of the separate technolo- gies used independently. A pro-active maintenance plan should be used to maintain • Switching, dimming, or a combination of the two the lighting system at most energy effi cient level possible. functions can be automatically preprogrammed Many facility managers are hesitant to replace lamps that so that the user can select an appropriate lighting are still operating. But group re-lamping and cleaning can environment. A pre-set can be included for the be less expensive than spot replacement. Through strategic cleaning crew, which then can use the most energy- planning and performance management of the overall effi cient lights that will allow them to do their work. lighting system, costs can be reduced and lighting quality • Time clocks are devices that can be programmed improved. Examples include: to turn lights on or off at designated times. These • Cleaning of lamps and luminaires at regular are a useful alternative to photoelectric sensors in intervals. applications with very predictable usage, such as in • Never clean lamps that are operational or still hot. parking lots. Use very mild soaps and cleaners, followed by a • Daylight controls are photoelectric devices that clean rinse on most surfaces. This can be done on turn off or dim the lights in response to the natural a yearly basis. illumination available. • Group re-lamping on a scheduled basis of all luminaires in an area. Key Lighting Strategies • One simple method of determining when to re- lamp: When group re-lamping, one may buy 10% • Upgrade incandescent and fl uorescent T12s to high- more lamps than are needed to re-lamp the area. lumen T8s, T5s or T5Hos Example: a standard 40 watt The use of this 10% overstock is limited to spot re- T12 lamp on standard magnetic ballast uses 172 lamping only. When you have depleted the 10%, watts of energy. The same fi xture retrofi tted with this indicates that it is time to group re-lamp again. T8 lamps and electronic ballast uses 112 watts of This method typically results in group re-lamping at energy – that’s a 35% reduction in energy usage. about 70% rated lamp life. • Replace magnetic ballasts with energy-effi cient • Inspection and repair of lighting equipment at electronic ballasts regular intervals. Any repairs should be completed • Ballasts and lamps should be replaced at the same by an experienced or licensed electrician. time. Consider rapid start and dimmable ballasts to • Yearly have ballasts and lighting controls be factory coordinate with an energy management system pre-set to the greatest extent possible by a lighting • Replace High-Intensity Discharge (HIDs) systems with contractor. fl uorescent T8s and T5s or T5Hos -6-lamp T5 and T8 fi xtures are becoming very popular for industrial use. Best Practice - Compressed Air • De-lamp unneeded fi xtures (remove lamps). Fluorescent Fixtures can be de-lamped to save Compressed air services many purposes in breweries. It the energy consumption in the area which the helps position kegs, bottles and cans for fi lling, moves spent luminance level is higher than what is necessary. grain, is necessary for control valves to operate, and is used Convert multi-lamp T12 fl uorescent fi xtures to T8 to push liquid from vessels when pumping is not available. fl uorescent fi xtures with fewer lamps per fi xture. In some cases it is used to operate agitators and hand tools • Remove fl uorescent lamps controlled by magnetic and as packaging equipment.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 23 Compressed air is considered to be a free source of energy Compressed air leaks cost money! Below are a few by many employees, but is actually one of the most examples of the cost savings that can be incurred when expensive utilities within a brewery. At its best, the system is air leakage is reduced. 12 to 15% effi cient. This means that for every kW of energy used to produce compressed air, only 12-15% is delivered to Cost of Compressed Air Leaks the source. The remainder of the energy is lost in the form of heat. Therefore it is imperative to reduce compressed air Leak Diameter Air loss cfm Energy loss (kWh) Costs (Us$)/YR usage whenever possible. Set compressor air pressure to the inch 85 PSI 85 PSI 85 PSI lowest possible level, and above all fi nd and fi x air leaks on 1/16 2 0.4 320 a continuous basis. 1/8 20 3.7 2,960 1/4 55 10.3 8,240 The following items provide a quick reference on simple 3/8 221 41.4 33.120 ways to improve energy effi ciency within the compressed (*) kW x $0.1/kWh x 8,000 annual operating hours air system: • Set air pressure at the lowest possible level to Fixing compressed air leaks provides the highest payback in maintain operations (rule of thumb lowering header the shortest period of time. pressure by 2 PSI will improve air compressor energy effi ciency by 1%) Air leaks occur all the time - though some are easy to identify • Replace compressed air knives (nozzles) used to while others can be diffi cult. The best time to identify air leaks blow off water on cans or bottles with low pressure is when the equipment is shut down; however, this will only fan blowers allow a certain amount of leaks to be identifi ed. Others will • Do not use air for cleaning equipment or fl oors need to be located when the equipment is running. where dry clean up would be more appropriate • Do not use air tools or compressed air for personnel A system drawing outlining the compressed air system cooling components will help employees identify where the • Avoid using air to power motors if possible leaks are located. The drawing should show the major • Exhaust hot air out of compressor room and bring pieces of the equipment, piping layout, possible areas in cool outside air whenever possible (rule of thumb that have the highest potential for air leaks, and track dropping the suction temperature by 10F will improve where leaks have occurred. compressor energy effi ciency by approximately 2%. (Note: Check with compressor manufacture to Compressed Air System Components5 determine what lowest suction temperature at which the compressor can operate without damaging the compressor) • Repair air leaks as soon as possible.
Compressed air leaks are very common. Leaks are a major source of ineffi ciency and in some cases will account for 30% - 40% of compressed air system. Leaks also increase the system pressure drop, requiring additional compressors to be put on line or operating the single compressor at full load to maintain system pressure. This higher pressure takes more energy to produce, shortens the life span of equipment, and causes equipment that need compressed air to operate less effi ciently.
Although all possible measures should be taken to limit compressed air leaks, it is nearly impossible to operate with zero air leaks. In general, if air leaks are limited to 5% or Providing pictures, posters and training on what equipment 10% of the compressed air produced, then the system will requires compressed air will also help identify air leaks. This operate effi ciently. is a simple way to engage employees in energy reduction
24 BrewersAssociation.org Usage & Reduction Best Practices
efforts. The following charts show a few examples of where To ensure continuous lowering of compressed air usage, the air leaks may occur. following benchmark parameters should be used: • Compare normal air fl ow totals on a weekly basis Common Leak Locations • Compare normal air fl ow totals to down time totals on a weekly basis • Develop trends and checkpoints to determine normal range • Assign individuals to act immediately on deviations and ensure that root cause for excursion is identifi ed and acted upon • Document reasons for excursions and methods Common Locations Where Air Leaks Can Occur executed to improve the operation - this information 1. Branch line connection should be documented and archived to allow for 2. Rubber hoses future problem solving
3. Automatic drain trap Action items to be taken by the brewery team include: 4. Quick couplers • Collecting plant air pressure and air fl ow data on 5. Desiccant filters a daily basis. Enter the plant pressure and fl ow into a book or spreadsheet. The air pressure and 6. Isolating valves air fl ow should be measured once per shift at the 7. Filter/regulator/lubricator assembly same time every day. If the air pressure and air 8. Control valves fl ow data is available electronically, set up trends to monitor the air pressure on a continuous basis. 9. Filter/regulator/coalescent filter assembly Identify air pressure and air fl ow measurements 10. Coil hose during both normal operations and when the 11. Regulators production is shutdown. • Totalize air fl ow on a weekly basis and create a 12. Pneumatic cylinders trend that shows weekly air fl ow totals. Totalize plant air fl ows for each shift, daily and weekly. Any changes in air fl ow from week to week should be investigated and what caused the change should Cost profi le for different methods and practices to identify be determined. and repair air leaks: • Identify and stop at once ($) Compressed Air Leak Tracking • Use the look and listen method after normal working hours ($) • Invest in an ultrasound listening device to identify leaks ($) 1500 Weekly Plant air • Consider purchasing a compressed air leak tester to 1000 detect pressure drops due to leaks and measure the unit capacity ($$) 500 • Consider implementing an automatic leak- measuring process to be conducted on weekends 0 through a computerized control, regulation and Line 1 CFM Line 2 CFM Total PLt CFM monitoring system and installation of enough section valves ($$)
The following KPI parameters should be used for compressed The plant airfl ow should also be tracked when the line air systems: is shut down and when the plant is shut down. When • Plant air fl ow during normal operations compared from week to week, an increase in air fl ow during • Plant air fl ow during down time shutdown may indicate the presence of new leaks, or that • Plant air pressure during normal and down time operation some equipment may have been left on. A decrease in
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 25 air fl ow may indicate that air leaks have been reduced. of options that can further improve boiler effi ciency. Some Benchmarking this data weekly will help identify leaks and can be applied to existing boiler installations, and others are confi rm that air leaks are being repaired in a timely manner. only suitable when replacing boilers.
Compressed Air Leak Tracking To get the most out of the boiler system it is necessary to implement a complete maintenance/effi ciency plan to maintain every aspect of effi ciency. Providing that a 800 maintenance/effi ciency plan is put into place and plant 700 personnel can perform the tuning with the appropriate tools a cost savings in energy use can be realized. 600 As discussed before, boilers are pressure vessels designed to 500 heat water or produce steam, which can then be used to provide space heating, process heating and water heating 400 to a facility. The heating source in the boiler can be a natural gas fi red burner or oil fi red burner and electric resistance 300 heater can be used as well. 200 Basically, boiler effi ciency represents the difference 100 between energy input and energy output. Boiler effi ciency describes the fraction of fuel energy that is converted into 0 useful steam energy. In the end, effi ciency comes down to Line 1 CFM Line 2 CFM Total PLt CFM properly evaluating the performance of the boiler and the performance of the burner.
Week to week benchmarking will begin to develop trends There are three terms that infl uence boiler effi ciency; that will help identify wasted air through leaks or operational combustion effi ciency, fuel-to-steam effi ciency and thermal issues. Benchmarking will also verify that air leaks are being effi ciency. They are defi ned as follows: reduced and compressed air usage optimized • Combustion Effi ciency - Combustion effi ciency Best Practices – Boiler Effi ciency is an indication of the burner’s ability to burn fuel and the ability of the boiler to absorb the heat Today, in the brewing industry, process and heating generated. The amount of unburned fuel and applications continue to be powered by steam and hot excess air in the exhaust gas are used to assess a water. The mainstay technology for generating heating or burner’s combustion effi ciency. Burners performing process energy is the traditional boiler. Whether fi retube or with extremely low levels of unburned fuel while the various watertube forms, the commercial or package operating at low excess air levels are considered boiler has proven to be highly effi cient and cost effective effi cient. In other words, combustion effi ciency is in generating energy for many process and heating measured by dividing the usable heat produced applications. by the fuel input in MJ/h content. This calculation is based on the actual heat available produced by In order to maintain the highest possible boiler effi ciency, the system after heat loss up the stack and other the boiler system should be tuned on a regular basis by heat losses which do not provide usable heat. a boiler control professional. It is recommended that this • Fuel-To-Steam Effi ciency - Fuel-to-steam effi ciency practice take place at a minimum of every three years. is a measure of the overall effi ciency of the boiler. Best practice would be to tune the boiler yearly during It accounts for the effectiveness of the heat the annually scheduled boiler maintenance period. This exchanger as well as the radiation and convection guideline describes the parameters used to determine the losses. optimal boiler effi ciency and should be incorporated into • Thermal Effi ciency – Thermal effi ciency of a boiler is normal operational activity. defi ned as the percentage of (heat) energy input that is effectively useful in the generated steam. While good maintenance is the fi rst essential step in It is related to how effi cient the heat exchanger is achieving high boiler effi ciency, managers have a number working. Certain conditions such as soot build-up
26 BrewersAssociation.org Usage & Reduction Best Practices
or water scaling can reduce the overall effi ciency and maintenance. of the boiler system resulting in additional operating • Blow-down losses - The boiler water must be cost due to higher fuel usage to produce steam. suffi ciently free of deposit forming solids to allow rapid and effi cient heat transfer and it must not be As briefl y mentioned before, heat losses do occur. These corrosive to the boiler metal. Deposits and corrosion losses can be looked at as avoidable and unavoidable result in effi ciency losses and may result in boiler energy losses. tube failures and inability to produce steam. • Condensate losses - Recover the largest possible Heat Losses6 amount of condensate. Hot condensate that is not returned to the boiler represents a corresponding loss of energy. The energy savings is the energy Heat loss in flue gases 18% contained in the condensate being returned. • Convection and radiation losses - Radiation and convection losses represent the heat losses Radiation and convection radiating from the boiler vessel. Boilers are insulated heat loss 4% to minimize these losses. Radiation and convection Energy input 100% Energy output (boiler losses, are essentially constant throughout the fi ring thermal efficiency) 75-77% range of a particular boiler, but vary between different boiler types, sizes, and operating pressures. Boiler Having proper insulation of the boiler is a good Energy in heating medium (e.g. steam) solution to this issue. Energy in fuel
Heat loss in blowdown 3% Two methods for measuring boiler effi ciency include the Direct Method Procedure, and the Heat Loss Method. Both methods will assist the plant in calculating boiler effi ciency the method chosen will depend on the available data for A heat balance will help to identify avoidable and each procedure. If the data is not available for the Heat unavoidable heat losses. A heat balance is an attempt Loss Method the Direct Method measured consistently will to balance the total energy entering a boiler against that provide a KPI for boiler effi ciency that can be benchmarked leaving the boiler in different forms. Conducting boiler over time to optimize steam generation. effi ciency tests help fi nd out the deviation of boiler effi ciency from the best effi ciency and target problem areas for Direct Method Procedure: corrective action. • Measure steam fl ow over a set period, e.g. one The goal is to minimize or reduce the avoidable losses and hour. Use steam integrator readings, if available, thereby improve energy effi ciency. The following losses can and correct for calibration pressure. Alternatively, be avoided or reduced: use the feedwater integrator, if available, which will • Stack gas losses - Stack temperature is a measure in most cases not require a correction for pressure. of the heat carried away by dry fl ue gases and • Measure the fl ow of fuel over the same period. Use the moisture loss. The stack temperature is the the gas or oil integrator, or determine the mass of temperature of the combustion gases dry and water solid fuel used. vapor leaving the boiler and refl ects the energy that • Convert steam fl ow, feedwater fl ow and fuel fl ow to did not transfer from the fuel to the steam or hot identical energy units, e.g. Btu/kg or kJ/kg. water. The lower the stack temperature is, the more • Calculate the effi ciency using the following effective the heat exchanger design and the higher equation: Effi ciency = 100 x (steam energy – the fuel-to-steam. Stack gas temperature can be feedwater energy) ÷ fuel energy reduced by optimizing maintenance and cleaning, better burner and boiler technology. Heat Loss Method: • Excess air - It uses energy from combustion which takes away potential energy for transfer to water The Heat Balance effi ciency measurement method is based in the boiler. In this way, excess air reduces boiler on accounting for all the heat losses of the boiler. The actual effi ciency. Minimize air to the necessary minimum measurement method consists of subtracting from 100 which depends on burner technology, operation % the total percentage of: A) stack, B) radiation, and C)
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 27 convection losses. The resulting value is the boiler’s fuel-to- Boiler Blow-down: When water is boiled and steam is steam effi ciency. The heat loss method accounts for stack, generated, any dissolved solids contained in the water radiation and convection losses. remain in the boiler. The deposits can lead to scale formation inside the boiler, resulting in localized overheating and fi nally causing boiler tube failure. It is therefore necessary to control Effi ciency of boiler (n) = 100 - (i + ii + iii + iv + v + vi + vii) the level of concentration of the solids in suspension and dissolved in the boiled water. This is achieved by process of Whereby the principle losses that occur in a boiler are ‘blowing down’, where a certain volume of water is blown loss of heat due to: off and is automatically replaced by feed water – thus i. Dry fl ue gas maintaining the optimum level of total dissolved solids in the ii. Evaporation of water formed due to H2 in fuel boiler water. In general boiler water (make up water) will be iii. Evaporation of moisture in fuel treated with chemicals and dissolved solids to ensure higher iv. Moisture present in combustion air effi ciencies and reduce the scaling. Never use untreated RO v. Un-burnt fuel in fl y ash water as boiler make up water. vi. Un-burnt fuel in bottom ash vii. Radiation and other unaccounted losses A recommended method of removing these solids is via short, sharp blasts using a relatively large valve at the bottom of the boiler. The objective is to allow the sludge NOTE: The following items are intended to assist with improving time to redistribute itself so that more can be removed on boiler effi ciency. All facilities must be aware of any codes, the next blow-down. regulations and insurance requirements that are required in order to safely operate a boiler at a given location. It is recommended that: A single four-second blow-down every eight hours is much more effective than one, twelve- These measures, taken together and combined with a second blow-down in the fi rst eight hour shift period, and comprehensive maintenance program, can result in signifi cant then nothing for the rest of the day. energy savings. Equally important, unexpected downtime due to breakdowns will be reduced, and the overall safety of the Signifi cant energy savings can be accomplished by installation will improve. The following steps can be taken to recovering heat from boiler blow-down. For example, an ensure peak boiler effi ciency and minimum excess air operation: effi ciency improvement of over 2 percent can be achieved • Check the calibration of the combustion gas analyzer at a 10 percent blow-down rate on a 150 psig boiler. frequently and check the zero point daily. The control may be manually altered to reduce excess Blow-down of boilers to reduce the sludge and solid content air, without shortcutting the safety of operation. allows heat to go down the drain. Installing a heat exchanger • The physical condition of the forced-draft damper should in the blow-down line allows this waste heat to be used in be checked to ensure it is not broken or damaged. preheating makeup and feed water. This provides a great • Casing leakage must be detected and stopped. opportunity in energy and cost savings. • Check the burner fl ame confi guration during each shift and note any changes. Uncontrolled continuous blow-down is very wasteful. For • Stack temperature should be as low as possible. example, a 10% blow-down in a 15 kg/cm2 boiler results in However, it should not be so low that water vapor in 3% effi ciency loss. Automatic blow-down controls can be the exhaust condenses on the stack walls. installed that sense and respond to boiler water conductivity and pH, thereby increasing boiler effi ciency. For proper boiler operation that can lead to greater effi ciency, the following measures can be applied: Proper Excess Air: Oxygen trim controls can be added to the • Boiler Blow-down, Heat Recover and Control burner-control system. These controls continuously monitor • Proper Excess Air the oxygen level in the boiler-fl ue gases and adjust the • Reduce Scaling and Soot Losses quantity of air delivered to the burner, minimizing the excess • Radiation and Convection Heat Loss Minimization air delivered. In conventional control systems, excess air • Reduction of Boiler Steam Pressure levels typically are 10-20 percent. With oxygen trim controls, • Variable Speed Control excess air levels can be reduced to 5 percent or less.
28 BrewersAssociation.org Usage & Reduction Best Practices
An electronic sensor is inserted into the boiler fl ue, near the The brewery team can collect data to optimize boiler boiler, ahead of any dampers or other sources of air leakage effi ciency by recording and tracking boiler performance into the boiler or fl ue. The sensor is connected to a control to ensure good operation. The following tables can be panel that measures oxygen and sends a signal to a control used to maintain effi ciency in addition to monthly boiler damper on the burner air supply. maintenance:
Reduce Scaling and Soot Losses: In oil and coal-fi red boilers, Sample Boiler Data Collection Form soot buildup on tubes acts as an insulator against heat Boiler Name/ Boiler Type Age Purpose- Date last transfer. Any such deposits should be removed on a regular Location Steam heat update or hot water (Name) basis. An estimated 1% effi ciency loss occurs with every heat 22 ºC or 72 ºF increase in stack temperature. Stack temperature should be checked and recorded regularly as an indicator of soot deposits. An upward trend in fl ue gas temperatures over weeks or months usually indicates that a deposit has built up on either the fi reside or waterside of boiler heat-exchange surfaces. The boiler should be inspected promptly.
When the fl ue gas temperature rises to about 20 ºC above the temperature of a newly cleaned boiler, soot deposits should be removed. A dial type thermometer can be Boiler Maintenance Checklist installed at the base of the stack to monitor the exhaust Description Comments Monthly fl ue gas temperature. Maintenance Flue gases Measure and compare last Radiation and Convection Heat Loss Minimization: The month’s readings fl ue gas composition over entire fi ring external surfaces of a shell boiler are hotter than the range surroundings. The heat loss from the boiler shell is normally Combustion air Check combustion air inlet to a fi xed energy loss, regardless of the boiler output. It is supply boiler room and boiler to make recommended that repairing or augmenting insulation can sure openings are adequate reduce heat loss through boiler walls and piping. and clean Check fuel system Check pressure gauge, pumps, Reduction of Boiler Steam Pressure: This is an effective means fi lters and transfer lines. Clean of reducing fuel consumption by as much as 1 to 2%. Please fi lters as required. keep in mind that any reduction of boiler pressure reduces Check belts Check belts for proper tension. the specifi c volume of the steam in the boiler, and effectively reduces the boiler output. The team should therefore consider Check for air leaks Check for air leaks around access openings and fl ame the possible consequences of pressure reduction carefully, scanner assembly. before proceeding with this measure. Pressure should be Check all blower Check for tightness and reduced in stages, and no more than a 20% reduction should belts minimum slippage. be considered. Check all gaskets Check gaskets for tight sealing, replace if do not provide tight Variable Speed Control: Variable speed control is an important seal means of achieving energy savings. Basically, combustion Inspect boiler Inspect all boiler insulation and air control is affected by throttling dampers fi tted at forced insulation casings for hotspots and induced draft fans. If the load characteristic of the Steam control Calibrate steam control valves boiler is variable, the possibility of replacing the dampers by valves as specifi ed by manufacturer a VSD should be evaluated with a boiler specialist or boiler Pressure reducing/ Check for proper operation manufacturer. regulating valves
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 29 Boiler Pressure and Temperature Log • Repeatable air/fuel control - The effi ciency of Item Boiler Checkpoints Units Readings Date the boiler depends on the ability of the burner to # (notes) provide the proper air-to-fuel mixture throughout 1 Type of Boiler the fi ring range consistently without the need for 2 Steam Pressure Kg/cm2 complex set-up or adjustments. The burner should (g) also be able to provide suitable turndown (ability of 3 Steam Quantity TPH the boiler to achieve a wide range of output) and 4 Steam 0C low excess air which will improve boiler effi ciency. Temperature • Fuel-to-steam - When evaluating a boiler purchase, 5 Fuel Used (oil, ask boiler vendor to go through the fuel-to-steam gas, coal etc.) or fuel-to-water effi ciency calculation to verify that 6 Fuel Quantity TPH it is realistic and proven. Review the type of boiler being evaluated to check if the unit’s performance 7 Feed Water 0C Temperature will be consistent and repeatable. 8 Flue Gas 0C Temperature Boiler Checklist Evaluation 9 Ambient (room) 0C Item Boiler Evaluation Reviewed Remarks Issues Temperature # Checklist 1 Pressure Vessel Review the following points when evaluating a new boiler 2 Number Boiler Passes system for your facility: 3 Maintenance Costs • Pressure vessel design – When reviewing various 4 Air/Fuel Control boiler designs/types consider the pressure vessel design. Water circulation (forced or natural), 5 Fuel – to steam (Effi ciency) low stress and accessibility are key criteria for proper pressure vessel design. The boiler should 6 Other include a proper heat exchanger. Fully accessible maintenance points for ease of inspection and low When reviewing an effi ciency guarantee or calculation, maintenance costs are also important factors to check the excess air levels. If 15% excess air is being used to seek out. For example, ensure boiler maintenance calculate the effi ciency, the burner should be of a very high can be performed readily by comparing tube quality design with repeatable damper and linkage features. length with working space within the plant footprint. You should ask the vendor to recalculate the effi ciency at • Number of boiler passes - The number of boiler realistic excess air values if necessary. Designing, installing passes simply represents the number of times the and commissioning a new boiler system is a specialized hot combustion gas travels through the boiler. A project that needs to involve the supplier. boiler with two passes provides two opportunities for the hot gasses to exchange heat to the water in the NOTE: The following items are intended to assist with boiler. A 4-pass unit provides four opportunities for improving effi ciency through boiler maintenance steps heat transfer. The 4-pass will have higher effi ciencies and depending on the location may not be an inclusive and lower fuel costs. Fire tube boilers are classifi ed list. All facilities must be aware of any codes, regulations by the number of passes the combustion gases and insurance requirements that are required in order to make through the water to be heated into steam. safely operate a boiler at a given location. So in a 2-pass fi re tube boiler, half of the tubes have hot combustion gas passing from left to right. As • Drain boiler, tag valves and controls. DO NOT the gasses exit these tubes they are redirected into attempt to remove a manhole cover without fi rst the second half of the tube, making a second pass properly venting the water or steam side of a boiler traveling right to left. to the atmosphere. Prior to opening or entering a • Maintenance costs - Review maintenance costs boiler, it must be at atmospheric pressure. To protect carefully. The current unit may be costing money the boiler from unnecessary stresses the boiler water in various ways, which may include emergency temperature should be allowed to reach the boiler maintenance, downtime, diffi cult-to-fi nd parts and room temperature before draining. burner issues. Evaluate current maintenance costs • Brush all tubes clean of scale. to that of the proposed system. • Brush plate surfaces clean, use vacuum cleaner.
30 BrewersAssociation.org Usage & Reduction Best Practices
• Clean ducts, main fi re tube and fl ue passages. return water is pre-heated by the economizer; therefore, the • Check and replace worn or damaged insulation. boiler’s main heating circuit does not need to provide as Repair damage and remove debris. much heat to produce a given output quantity of steam or • When the boiler has cooled to the ambient boiler hot water. room temperature, wash and fl ush boiler. • Refi ll boiler with water and chemicals. The concept of waste heat recovery can be illustrated by • Examine all steam and water line to controls to looking at the boiler system. Feed water enters the boiler determine that they are clear of scale and arranged to produce process steam. The energy for the steam to insure proper control operations. production normally comes from the combustion of diesel • Clean stems and shafts, and tighten packing nuts on or fuel oil, which produces an exhaust with a temperature of valves and pumps. about 220 to 270 °C. For older boilers, the temperature of the • Replace old gaskets before reassembling. exhaust may be even higher. The exhaust fl ue gas, which still contains a substantial amount of waste heat, is discharged Best Practices - Boiler Heat Recovery directly to the atmosphere. As a result, energy is wasted.
This section provides information on control techniques Steam Principle and measures that are available to mitigate energy costs and greenhouse gas (GHG) emissions from industrial and Steam commercial boilers. Boiler Industrial equipment and facilities such as boilers, incinerators, and process plants generate heat when used. Some heat is actually discharged and thus wasted. Waste heat is Feed water heat discharged from this process into the environment 30°C - 90°C even though the heat can be tapped for useful purposes. It presents great opportunities for heat recovery and fuel savings is the most obvious benefi t of waste heat recovery. Combustion air Exhaust gas (220 - 270°C) discharged This is a key motivating factor for plants to consider given the 30°C to atmosphere signifi cant opportunity in cost and energy savings.
Energy effi ciency can be increased by using waste heat gas The graphic presents a process fl ow diagram of a typical recovery systems to capture and use some of the heat from industrial boiler system. Combustion for heat generation the fl ue gas. The most commonly used waste heat recovery begins in the boiler burner system and the heat is transferred methods are preheating combustion air and water heating. to the water in the boiler. The boiler produces steam and hot Heat recovery equipment includes various type of heat water for industrial process applications. Boilers can utilize exchangers (economizers and air heaters), typically located an economizer to preheat the process water before it is fed after the gases have passed through the steam generating to the boiler using waste heat from the exhaust gas. sections of the boiler.
Our focus will be on economizers given they are more widely Boiler Effi ciency Rule of Thumb: A 4°C reduction in used and they do not adversely impact the combustion air fl ue gas temperature will improve boiler effi ciency temperature and the resulting NOX formation. Economizers by about 1%. The waste heat from the fl ue gas can are basically tubular heat transfer surfaces used to preheat be used to preheat boiler feed water, preheat boiler boiler feed water before it enters the steam drum or furnace makeup water and heat process water/fl uids. surfaces. Economizers also reduce the potential of thermal shock and strong water temperature fl uctuations as the feed water enters the boiler. Operators of economizers must consider potential corrosion problems, particularly in fuels containing sulfur. Moisture The economizer recovers heat from the boiler exhaust gas containing corrosive sulfuric acid is likely to condense on any and is used to pre-heat the boiler feed water. Capturing this heat exchanger surfaces that fall below the acid dew point. normally lost heat reduces the overall fuel requirements for This usually occurs near the inlet of the combustion air or feed the boiler. This is possible because the boiler feed-water or water to be heated.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 31 Process Flow Steam System7 value of the reduction in the cost of make-up water, sewage disposal, and water treatment chemicals.
Blow-down contains energy, which can be used instead of being wasted. This waste heat can be recovered with a heat exchanger, a fl ash tank, or fl ash tank in combination with a heat exchanger. Blow-down can be either intermittent bottom blow-down or continuous. Use of continuous rather than intermittent blow-down saves treated boiler water and can result in signifi cant energy savings. The higher the blow- down rate and boiler pressures, the more attractive the option of recovering the blow-down becomes. Any boiler with continuous blow-down exceeding 5% of the steam rate is a good candidate for considering blow-down waste heat recovery. Manufacturers specifi ed that a 1 % thermal effi ciency can be achieved by this method. For example, an effi ciency improvement of over 2% can be achieved at Each boiler has its specifi c limit of low fl ue gas temperature, a 10% blow-down rate on a 1034 kpag or 150 psig boiler. which should be determined individually if supplementary heat exchange is being considered. Since the fl ue gas Boiler Steam Recovery temperatures are decreased at lower loads, economizers often have some form of by-pass control that maintains the
fl ue gas temperature above a preset minimum. Boiler
Flash Condensing economizers can increase the boiler effi ciency Tank by 10%-15%. To optimize their performance the return water Low- Pressure temperature from the heating system should be no more Steam Heat than (49 °C) and less than (41 °C) if possible. These can be Exchanger used on gas or low sulfur fuel oil boilers, but it is important Hot Water Out that the water temperature after the economizer is raised to Water In at least (54 °C) to prevent condensation of the fl ue gases in Drain the boiler. These economizers can improve the effectiveness of reclaiming fl ue gas heat. They cool the fl ue gas below the dew point. Thus they recover heat from the fl ue gas and heat from the moisture which condenses. This drawing shows Flash Steam recovered for the steam distribution system and the hot blow-down condensate When steam transfers its heat in a manufacturing process, fl owing into a heat exchanger to pre-heat incoming make- heat exchanger, or heating coil, it reverts to a liquid phase up water. called condensate. An attractive method of improving boiler effi ciency is to increase the condensate return to NOTE: Installing an economizer or blow-down heat the boiler. Energy savings come about from the fact that exchanger is a project that requires external resources most condensate is returned at a very hot temperature, to design, and install. This work should be performed by compared to the cold makeup water that must be heated. qualifi ed engineers, suppliers and installers. A return condensate system must be a function of the specifi c boiler and water/condensate quality, but essentially The following items should be checked with the supplier: involves a new distribution line confi guration. • Cost of heat recovery system (materials and installation). The energy savings is the energy contained in the condensate º Detailed cost specifi cation being returned. The energy effi ciency improvement for a º Detailed overview of necessary materials to particular boiler is, therefore, the ratio of kj/hr (BTU/hr) saved execute tests by supplier from the condensate return to the original kj/hr (BTU/hr). • Time needed for installation by supplier. heat input to the boiler. Overall cost savings accrue from º How much downtime of the line is needed to the fuel savings due to the effi ciency improvement, plus the implement heat recovery system?
32 BrewersAssociation.org Usage & Reduction Best Practices
• Actions needed by plant to assist with installation. Based on the answers from the supplier, together º Is any assistance by plant personnel needed with the supply chain department, the costs of this during the installation? downtime should be calculated and used in the • Commissioning procedure evaluation. º How many test runs would be needed to verify • Plant personnel needed for assistance during successful implementation? installation, testing and commissioning. If special • The suppliers calculated energy and cost savings plant personnel is needed for the installation º Detailed calculation of energy and cost savings. and testing, and meaning these employees are • How does the supplier guarantee results? not available for other work, the cost of these º How does the supplier measure energy savings? employees should be taken into account as well. • How does the supplier guarantee these savings? This all sums up to a total cost needed for purchasing, The table outlines the some key points to discuss with installing and testing of a heat recovery system. Based on your supplier when considering industrial heat recovery these total costs and the provided data about energy equipment. and cost savings, a business case evaluation should be set up together with plant management and the fi nancial Boiler Effi ciency Checklist department(s) and funding should be requested. Item Heat Recovery Comments Notes # Checkpoints This means that the payback time of the project should be 1 Hot fl ue gas or Quantity, temperature, determined. Payback Time can be thought of simplistically other pressure and as the time required for the savings generated by a project composition to pay back the initial investment. One relatively easy 2 Heat recipient Timing, quantity and formula for determining Payback Time is Total Project Cost / characteristics temperature Total Financial Savings Realized per unit time (usually years). 3 Max permissible Measured for the More involved payback formulae consider the time value pressure drop plant to which the heat recovery of money, expected lifespan of a project or other factors. equipment is being fi tted. Ideally, consult After a positive evaluation of the business case and after the original supplier or the funding is approved, the heat recovery system can be manufacturer. purchased by the purchasing department. Special attention 4 Access or space For installation and should be paid in the contract with the supplier about the maintenance. guarantees the supplier can give about the savings, and 5 Bypass provision To facilitate how they will prove these savings are achieved. maintenance without plant shutdown. Best Practice - Condensate Recovery 6 Heat exchanger Taking into account design and operating temperature materials and the presence of When steam transfers its heat in a manufacturing process, contaminants. heat exchanger, or heating coil, it reverts to a liquid phase 7 Impact on plant Any modifi cations to called condensate. Increasing the condensate return to the accommodate heat boiler is another way to conserve energy. recovery. 8 Control Condensate is distilled water that is formed when steam is Requirements condensed. Ideally, all produced steam should return to the boiler in the form of hot condensate, requiring no additional After all information is received from the supplier, the overall water to produce steam or heat to extract water from business case should be evaluated. Therefore the following ambient temperatures to condensate. costs should be taken into account: • Investment costs for heat recovery system. Costs The condensate return system is the return portion of the based on the proposal submitted by the supplier. steam system. Condensate is the liquid residue of steam • Material needed for testing and commissioning. that is used in heating equipment such as brew kettles, mash • Downtime needed for installation, testing and tuns, CIP installations, hot water heaters, etc. It also comes commissioning. What are the costs for the fact that from steam that condenses out in steam pipes due to heat there can be no production during this period? loss from steam transport or lack of insulation.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 33 The boiler feed water system is the input system for the boiler, Condensate systems consist of a condensate tank or receiver or the purifi ed and treated water that is pumped into the and a system of pipes that lead condensate from the steam boiler. The condensate system feeds into the boiler feed to the tank. Satellite condensate receivers are sometimes water system. In many cases these two systems are merged installed in larger systems, which pump condensate to a so a single set of equipment can perform both condensate primary condensate receiver located in the boiler room. and feed water system functions. Makeup water is treated water added to the feed water or condensate system Returning hot condensate to the boiler has several benefi ts: to compensate for system losses. The following graphic • As more condensate is returned, less make-up represents an example steam system, which shows the water is required. different components. • Saving fuel, makeup water, chemicals and treatment costs. Additionally, more steam can be Steam System Diagram produced from the boiler. • Less condensate discharged into a sewer system reduces disposal (sewer) costs. Cooker Cooker Space • Return of high purity condensate reduces energy heating Process system vessels losses due to boiler blow down. Steam • Signifi cant fuel savings occur as most returned
Steam condensate is relatively hot (54°C to 107°C), reducing the amount of cold makeup water (10°C Condensate ake-up to 16°C) that must be heated. ater Brew kettle Brew kettle Condensate A simple calculation indicates that energy in the condensate Steam can be 10% to 20% of the total steam energy content of Feedtank a typical system. Reducing this loss would mean signifi cant energy savings. Boiler
Feedpump Schematic Overview of A Standard Steam System
Condensate and feed water systems perform the following functions: • Filling the boiler system and replacing water that is lost • Collecting and returning condensate from steam using equipment • Draining liquid water from steam lines and idle equipment • Injecting water into the boiler against the boiler’s internal pressure • Purifying and/or treating the boiler water to prevent damage and ineffi ciency in the boiler and steam using equipment • Preheating feed water, usually with recovered heat • Recovering heat from condensate, such as the heat of condensate fl ash steam • Creating a vacuum in a condensate return system to improve condensate fl ow and to improve A simple way to calculate the condensate return is to condensate fl ow and temperature control of steam determine the difference between makeup water and feed heating equipment water, divide this by the feed water, and multiply by 100%.
Each of these functions consumes energy or affects the Maximizing the return of hot condensate to the boiler effi ciency of the boiler system. reduces the operating costs of the boiler(s). The best
34 BrewersAssociation.org Usage & Reduction Best Practices
operating plants return 80% to 90% of the steam generated steam traps, steam leaks, blowing steam vents, and as hot condensate. Average bottling plants will return 70% direct steam injection. to 80%, and the below average plants return below 70% or • Provide equipment data where possible, contact less. Increasing the amount of hot condensate returned to vendors, suppliers and maintenance fi rms to supply the boiler reduces energy and water cost and improves the missing data and to provide guidance on proper overall steam system operation for the entire plant. sizing and application parameters. • Develop a fl ow chart of the condensate system and Hot condensate is returned to the boiler, retaining checklist of items that make up the condensate approximately 10% to 20% of the energy carried by the system. steam. For every 10% of the condensate returned to the boiler feed water system, boiler fuel consumption is reduced Condensate System Audit Checklist by approximately 1.5%. Since energy costs for steam are Location Item Use How can condensate be lost? almost half of total energy costs, the savings for returning condensate are signifi cant.
Saved energy results from not heating makeup water used to replace hot condensate that is sent down the drain or lost as vapor. For example, if a liter of condensate has a temperature of 80 °C and is not returned, a liter of ambient water is used to make up for the lost liter of condensate. The energy saved is the additional energy that would be used to heat one liter of water from 20 °C to 80 °C (temperature of the makeup water usually averages around 20 °C). • Identify all places were condensate can be lost From this example, it is evident that maximizing the return of and add them to the steam users table. condensate and keeping the condensate as warm as possible • Assign special team members and stakeholders to as it returns to the boiler feed water system is highly important. identify areas in the condensate system that require attention, repair, replacement or addition. If the team identifi es the percentage of condensate that is • Prepare maintenance work orders or develop returned on a daily basis is below 75%, an action plan will capital projects and implement fi xes to the need to be developed. This percentage is the minimum to condensate system. achieve if no direct steam contact is used in the process. The • Monitor each repair, upgrade or modifi cation to best systems return 85-90% condensate. the condensate system to verify that condensate collection is improving. This action should take The team should develop a plan with the following items: place on a regular basis and be documented to • Set targets and time frames to improve condensate ensure that the fi x can be reviewed in the future if return. (For example; improve condensate return issue with the condensate system arises. from 60% to 65% in 8 weeks and 70% in 16 weeks and be at or near 80% in 24 weeks. Or keep the The team should conduct a monthly survey to check condensate percentage above 75% continuously). locations where condensate can be lost. The team should • Review the steam system overview with a heavy follow the complete steam and condensate system focus on the condensate return system. The team lines and check for losses, making use of the steam and should use steam system drawings, layouts or condensate survey and tables that were developed earlier fl ow charts that were developed for identifying in this guideline. steam leaks and condensate return system. The condensate drawings will include all condensate If the team identifi es locations with direct steam injection, piping, heat exchangers, hot water heaters, steam investigate the possibilities of using heat exchangers or traps, coffee cookers, hot fi ll equipment etc. other solutions. When condensate is drained, investigate • Identify where condensate can be lost. Special the possibilities of reusing the drainage and see if the focus should be given to condensate leaks, failing condensate can be returned to a receiver.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 35 The condensate system will produce carbonic acid as Common Areas and Causes that Condensate Can a result of excessive carbon dioxide in the system. The Be Lost In A Steam System highest concentration of carbonic acid will be in the condensate return lines as carbon dioxide dissolves in • Ensure that the condensate pumps (if used) are cooling condensate. properly sized to the correct net positive suction head (NPSH). Most breweries today have condensate lines installed with • Consult with the supplier that provided the schedule 80 steel pipe and threaded connections. When equipment or with your boiler maintenance carbonic acid attacks the pipe and joints, the steel will technicians to determine if your condensate deteriorate and create leaks. During the monthly survey pumps are sized properly and are functioning in all condensate piping will be checked to ensure that leaks a proper manner. have not formed. • Failure to size the pump for the proper NPSH will cause the pump to cavitate damaging pump To slow condensate leaks from carbonic acid or to prevent seals and impeller. leaks from occurring insulation, stainless steel pipe and valve • Check the pump to verify that the temperature should be installed on the condensate system. Also, wherever rating for the condensate pump is designed to possible welded connections should be used on condensate collect condensate at atmospheric saturation systems and threaded connections should be avoided. temperature of 212 °F or 100 °C if the pump is not sized to handle these temperatures the pump will Insulation allows the collected hot condensate to retain fail to operate properly. the majority of its heat on the way back to the boiler feed water tank. The condensate system should insulate
Calculate current condensate return
Calculate the current condensate return by using the formula in the examples below:
Example 1: Steam fl ow meter, make up water meter Example 2: Make up water meter, boiler blow-down installed, boiler blow-down meter meter, fuel meter
Measure total steam fl ow for 24 hours and convert to Total fuel usage for generating steam. Use design data water units either kilograms, cubic or meters (X); provided with boiler to calculate estimated steam fl ow based on fuel usage (X); Measure total make up water fl ow for 24 hours to the boiler feed water tank (Y) and convert to either Measure total make up water fl ow for 24 hours to the kilograms, or cubic meters; boiler feed water tank (Y);
Measure the total amount of boiler blow-down for 24 Measure the total amount of boiler blow-down for 24 hours and convert to water units either kilogram, or hours (Z); cubic meters (Z); Formula: Formula: ((Z + X)-Y) ((Z + X)-Y) %Condensate Return= *100% %Condensate Return= *100 (X + Z) (X + Z)
36 BrewersAssociation.org Usage & Reduction Best Practices
all equipment over 50 °C. The following items should be 3.4 Food Service considered for insulation: • Condensate lines • Condensate tanks Many craft brewers have brewpubs, restaurants or food • Valves service establishments associated with the company. • Some steam trap types In general, always look for ENERGY STAR rated or high- effi ciency appliances and fi xtures when purchasing or A major source of condensate loss is steam leaks. Leaks replacing equipment in order to lower energy costs during result in additional fuel and water to be used to generate operation. Though these may cost slightly more initially, most steam that is lost to atmosphere (refer to steam leak ENERGY STAR or high-effi ciency appliances and equipment guide line for more information on identifying and fixing usually will pay you back in lower operating costs. steam leaks). Fixing a steam leak is the best low cost item that you can perform to improve overall steam system This section outlines items that are simple and inexpensive energy efficiency. updates, all the way through full equipment replacement. There are also checklists and operational procedures your Monitoring Condensate Return establishment can use to optimize and reduce energy use with running a food service establishment.
condensate % The National Restaurant Association has developed the 78 Conserve Sustainability Education Program. It is an excellent 76 online resource to help restaurants reduce operating target = 75% 74 expenses and leave a lighter footprint on the environment. 72 Many of the ideas presented in this section are from the condensate % 70 Conserve program. action required! 68 66 Best Practices - Refrigeration 64 62 The following items can be installed inside the brewery to 60 optimize energy used in refrigeration: 58 week nr • Use strip curtains, plastic swing doors, or automatic door closers on walk-in refrigeration and freezer units. These barriers block warm moist air from entering the Continue monitoring the makeup water and feed water use. units when you open your door. Strip curtains used in Develop a monitoring system that checks the percentage busy kitchens can reduce compressor runtime – the of condensate return on a weekly basis. Instruct the boiler heaviest user of energy within a refrigeration unit. maintenance crew to make up water, blow-down and feed Ensure strip curtains cover the entire door opening water samples, and monitor the fuel use every week on the for optimal effectiveness – missing pieces or gaps same day. The team should calculate the condensate return within a strip curtain means warm moist air is entering percentage based on the reported data and monitor data your units. Check with your local utility to see if they in a condensate log and graph to analyze trends. may offer rebates for these upgrades.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 37 • Buy night curtains for display cases and open-case • Minimize the amount of time the door is open. refrigerators. These are fairly inexpensive and work Minimize the number of trips into walk-in units. Do well to trap cold inside when the business is not not prop the door open. open. • Keep the auto-closer on the door maintained and • Replace door seals if the doors are not airtight and lubricate the door hinges. you feel cold air escaping. • Set the appropriate temperature, don’t over cool • Realign or rehang entry doors if seals appear in or freeze goods. good condition but there are still gaps between the • Keep heat sources such as ovens and dishwashers door and the opening. away from unit. If mobile, keep out of direct sunlight. • Shade the remote condensers on large refrigerators • Allow circulation near unit. Keep material away and freezers. These are typically installed on the from condenser coils and if movable, leave a few roof and support a walk-in sized unit. Some shade inches between the wall and unit. paneling on the remote condenser will increase its • Keep coils clean – both for the cold one inside the effi ciency. unit (evaporator coil) and the hot one outside the • Insulate the lines between a remote condenser and unit (condenser coil). Hardware stores sell brushes the walk-in unit. Similar to insulating water pipes, this to make this easier and never use caustic cleaners is a simple way to reduce energy loss between the on either of these coils! two units. • Inspect and set defrosting cycles. Most units have • Install compact fl uorescent lights (CFL) or light auto-defrost cycles, find the timer or clock that emitting diodes (LED) lights inside your refrigeration controls the frequency and set to the minimum units. In addition to using less energy than traditional amount needed to keep frost from building up. incandescent bulbs, they produce less waste heat A good starting setting is 15 minutes, four times that must be removed from your refrigeration unit, a day. area, which reduces your energy use even further. • Check refrigerant and keep refrigerant fully • Install motion-sensing switches in walk-ins. If the unit charged. Running a unit with too little refrigerant has a wall switch, install a motion activated switch requires more energy and can wear out the to prevent the light being on when no one is inside. compressor. Typically a sight glass or bubble • Upgrade fan motors in walk-in units. Look specifi cally window is mounted near the condenser for for Electrically Commutated (ECM) motors. Rebates these checks. are commonly available for this upgrade and • Try turning off the refrigeration unit’s door heaters. should be done before failure of an existing fan. These built-in heaters prevent frost and moisture • Purchase ENERGY STAR rated ice machines, buildup around the doors. In some geographical refrigerators and freezers where possible. There may areas, these may be required. If either frost or even be incentives or rebates available through moisture forms around the doors after turning the your local utility to help offset the initial costs of such door heating off, turn them back on. equipment. • Consider replacing ineffi cient units – most Best Practice – Tankless Water Heaters refrigerators and freezers manufactured prior to (On-Demand Hot Water) 1993 use signifi cantly more energy than newer models. ENERGY STAR has a site to calculate energy The need for hot water within the restaurant operation use and savings for replacing old refrigerators. requires either electric or gas fi red heaters. The traditional means to provide this water has been a 40- to 75-gallon tank After completing some of the capital investments listed with a heating element that would heat and store hot water above, there are some best management practices that, if for use within the facility. An alternative to the traditional implemented consistently, will result in continuous optimizing way to heat water is tankless or on demand hot water the effi ciency needed for refrigeration. heating sources.
38 BrewersAssociation.org Usage & Reduction Best Practices
The traditional hot water heater collects water in a tank and Best Practices - Cleaning/Sanitization heats the water to a desired temperature (120 °F to 140 °F). Over time as the water is used the tank is replenished and the The following items are capital improvements that can be water heated to required temperature. During periods when installed for the brewery to optimize energy used in cleaning hot water is not required the tank loses heat and needs to and sanitation processes: engage the heating element to maintain the temperature set • Installing a new or replacing your existing hot water point. It is during these times that energy is wasted. heater with an ENERGY STAR rated or high effi ciency water heater may well be the most energy effi cient The tankless water heater does not store water. A tankless item you can do for this area. The lower lifetime water heater incorporates technology that will only heat operating costs of condensing water heaters, water that is required for a given application. The benefi ts to tankless water heaters, and (of course), condensing using a tankless or on-demand water heater results in energy tankless water heaters will well outweigh the slightly savings over the traditional water heater by only using energy higher initial cost of such units. Depending on your on demand when hot water is needed. When energy is only requirements, there may be an opportunity to install used when needed and not used to maintain a set point, less multiple smaller high-effi ciency units throughout your energy is consumed over time for the same application. On establishment. Check with your local utility to see average the savings can range from 10% to 40% depending if there are incentives or rebates available to help on water use and fl ow rates. Even though energy is saved offset the initial purchase cost for such appliances. when using a tankless water heater, the initial cost to purchase • Consider installing a high-effi ciency (low fl ow) pre- and install this technology can be as 2 to 4 times the cost of a rinse spray valve for your dishwashing process. traditional water heater. When considering a tankless water In addition to saving water and waste water heater the following items should be considered: discharge, a low fl ow pre-rinse spray valve will reduce the overall energy needed to heat the Pros: water needed for your dish washing purposes. • Energy savings in that can range from 10% to 40% over traditional hot water heaters As for best management practice, the most important thing • Less footprint required than hot water tank to do is to ensure there are no leaks, especially hot water • Heater can be located closer to the user leaks, inside the establishment. • No fl ooding risks • On average tankless water heaters have a longer Best Practices - Kitchen Area service life then hot water tanks • Potential tax credits The following items are capital improvements that can be installed for the brewery to optimize energy used in the Cons: kitchen area: • Cost can range from 2X to 3X traditional tank hot • If your establishment uses steam kettles, invest in water heaters one with insulation and a lid, even if it is slightly more • May require larger gas line /separate venting expensive. The overall energy use for these will pay off requirements quickly. • Annual servicing may be required • Invest in high-effi ciency gas fryers, which can use up • Minimum fl ow rate required to operate properly to 50% less energy than a low-effi ciency gas fryer. • Installation cost / code requirements more expensive • Consider upgrading to a convection oven or than hot water tanks steam/convention oven from a standard oven to
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 39 increase both the speed of cooking your food, as • Installing motion sensors or timers for lighting in areas well as increasing the effi ciency of the overall unit. that experience occasional foot traffi c, such as rest • Look for ENERGY STAR rated equipment for warming rooms or overfl ow seating areas. trays or hot food holding containers. • Installing skylights where possible to allow for natural lighting. In addition to reducing energy needed for Best practices to reduce energy use in the kitchen are lighting, there are fewer light bulbs to change for simple and easy. But the key item here is to make sure they overhead. are done consistently. • Selecting ENERGY STAR – rated entertainment equipment for your audio and video equipment, as • For steam kettles, cover the lid! Merely covering the lid well as TVs – especially the big screens. Remember can reduce energy use for these appliances by 50%. to look for ENERGY STAR equipment for all your offi ce • Install broilers as close to a range as possible, to equipment as well. reduce energy needed to keep the kitchen cool. • Installing overhead fans to reduce the need for • Turn off the ‘backup’ fryer when you don’t need your HVAC system to be on. Fans can uniformly it and you can reduce four hours daily of standby distribute air conditioning and heating throughout time. Deep fryers are typically idle more than 75% your establishment and reduce ‘hot spots’ or ‘cold of the time, even in high-volume food service spots’ in your dining room. establishments. • Consistently inspect gas lines for leaks • Completely turn off, or turn off half of the griddle, Best practices to continuously implement include: steamer, range, and oven during slower service • Using natural lighting whenever possible. Assuming periods. Eliminating only three hours a day of outdoor and indoor temperatures do not differ standby time can save up to $250 per year, per unit. signifi cantly, keep curtains and blinds open during • Do not preheat your oven or other appliances until daylight house to reduce the need for artifi cial you need to use it. Reducing the time your oven or lighting. other appliances are on ‘standby’ or ‘backup’ will • Keeping your HVAC equipment regularly serviced lower energy costs signifi cantly. and maintained, and sized right for the space. • Install motion sensors or timers for lighting in areas of lower traffi c, such as closets, storage areas or Best Practices - Parking Lot/Outdoor Seating break rooms. • Get rid of old back-up refrigeration or freezer Opportunities to reduce energy use for the brewery’s units. If you are keeping old units plugged in and parking lot and outdoor seating for the restaurant include: on because they’re ‘free’, consider the signifi cant • Installing metal halide or high-pressure sodium energy costs you are paying to keep those lamps. For lighting poles, install metal halide ineffi cient units running. (preferably pulse start) or high-pressure sodium lights, which can be paired with timers and only Best Practices - Dining Room turned on when needed. A slightly more expensive up-front option is high-effi ciency induction lighting The dining room is the most visible area for customers and which will generally last longer than metal halide is a great place to showcase how the brewery is being and sodium lamps. responsibly energy effi cient. Some capital replacement • Upgrading to LED lights. If lighting poles are not items that have quick return on investments include: needed, LED lighting may be adequate and • Replacing all incandescent bulbs with more suitable for the space. LEDs also have an instant effi cient lighting options – whether they are on/off capability and do not require a ‘warm up’ compact fl uorescent, light emitting diodes, or other period as metal halide and high pressure sodium types. If you need dimmable lighting, install LED, lights require. CFL with electronic ballast, or cold cathode bulbs. If dimmable lighting is not needed, look at installing Best practices to monitor and adopt include: CFL or T5 fl uorescent bulbs. • Turning off outdoor lighting when the area is not in • Using LED bulbs in lighted Open/Closed and Exit use. This will also reduce ‘light pollution’ signs to reduce energy use with these always-on • Reducing or eliminating the use of external heating fi xtures. and air systems
40 BrewersAssociation.org Usage & Reduction Best Practices
3.5 Concerts and Events needs. These sources of energy can reduce noise and air pollution associated with diesel / biodiesel generators as well. The visible sustainability impact a brewery can have during • Reduce the time the generator is in idle mode, if large events and concerts is through the waste management generators are used. Only start up the motor if and program, such as recycling. Large, outdoor events which when it is needed. are temporary in nature can pose a problem for energy use • Consider providing food that requires low since such events require a reliable energy source for a short refrigeration or (re)heating needs. In addition to period of time, and some events may even require a backup reducing energy needed to keep food at the source of energy. However, there are efforts which can be optimal temperature, you can reduce or eliminate taken to optimize energy use during outdoor events and the use of electrical cables running from your source concerts. of energy to the food holding containers. • Turning off A/V and large screen projectors Some opportunities at concerts and events to reduce energy when not in use and reduce the time use include: entertainment equipment is on stand-by mode. • If generators are needed to supply energy for Even minor efforts such as turning off hand held outdoor events, consider using (or requesting, if using microphones in between sets will reduce your a third-party provider) biodiesel for the fuel supply. overall energy use. • Explore whether solar powered fuel cells can meet • Using insulated cups for cold beverages during hot all your necessary electricity needs as well. events, if feasible. This can reduce the replenishment • Depending on your geographical location, you of ice for customers, which will reduce energy may be able to request solar, wind, or other off-grid needed to keep the ice cold and produce it in the source of energy to power your outdoor electrical fi rst place.
Energy Usage, GHG Reduction, Effi ciency and Load Management Manual 41 section four Onsite Renewable Energy
Renewable energy is a means by which low carbon emission however, the fl ow chart provides a good way of ensuring sources of energy are used to supply or supplement the that all aspects of the project are reviewed when renewable energy requirements of a brewery and brewpub. energy is being considered.
Renewable energy in most cases should not be considered Energy Effi ciency Evaluation Loop an energy savings application since it is only substituting delivered energy from another source such as fossil fuel supplied electricity, natural gas or diesel oil. Renewable energy will offset the cost to purchase fossil fuel and in cases Identify Business Justification for Renewable Energy of PV Solar panels will take the cost of energy to zero.
For all the advantage of renewable energy the biggest
disadvantage to incorporating renewable energy is the Technology /Application Review 'OVERNMENT 2EGULATIONS high capital cost to purchase and install the technology s !NALYZE 4ECHNOLOGY /PTIONS s 0OLITICAL )MPACTS and the low return on capital deployed. s #ONNECT SYSTEM POWER s 3OCIAL )MPACTS generation, heat generation, etc. s %NVIRONMENTAL )MPACTS
Most sources of renewable energy are not considered primary energy sources due to the fact that the energy )DENTIFY &UEL