Odor Control System

Total Page:16

File Type:pdf, Size:1020Kb

Odor Control System ODOR CONTROL SYSTEM What is an Odor? An odor is defined as a sensation resulting from the reception of a stimulus by the olfactory sensory system. Controlling odors is an important consideration for protecting the environment and our community amenity. Odors can be generated from a vast range of sources including sewage treatment processes and industrial effluents. Odor Control Technologies Typical odor emission control applications are the removal of odor from sewage treatment plants & sewage wet waste. Odor related complaints from communities surrounding WWTPs have been increasing for many WWTPs. Here, several emission sources need odor control equipment, e.g. such as pump stations, wet wells, sludge dewatering, manholes, air valve chambers, and sludge trans-shipment operations from silo into trucks. Sewage odor consists of mainly hydrogen sulphide & H2S is dangerous to be released to the environment. Hydrogen sulphide, the gas, also contains organic sulphur components (mercaptans, hydrocarbons) and ammonia. Odor control technologies can be grouped into three distinct categories: 1. Chemical Absorption (acid and caustic wet scrubbing) 2. Biological Oxidation (bio-filtration and bio-scrubbing / bio trinkling filtration) 3. Adsorption (activated carbon and other adsorptive medias) 4. The Combination of above systems are usually used for Biological Oxidation & Chemical Scrubbing Chemical Absorption: Chemical scrubbers achieve odor removal by mass transfer absorption via contact of air stream with aqueous solution on random packing material in a scrubbing chamber. The liquid is typically water, adjusted to the proper pH and CHEMICAL DOSING oxidation potential by chemicals. TANK CHEMICAL STORAGE TANK CHEMICAL Two parameters define the performance of any absorption SCRUBBER scrubbing system. These are the efficiency of gas/liquid CHEMICAL DOSING PUMPS CHEMICAL contact and the adequacy of a chemical within the aqueous SCRUBBER CHEMICAL CHEMICAL TANK CIRCULATION phase to promote reaction and absorption. Corodex Industries FILLING PUMPS FRESH WATER uses a special media which increases the efficiency of the TANK SOFTENER scrubber in smaller tower size. FEED PUMPS Main features: 1. Scrubbing liquid make-up system AIR FAN 2. Scrubbing liquid re-circulation system 3. Scrubbing liquid discharge system SOFTENER 4. Scrubbing liquid system (chemical for adjusting the pH and ORP value ) 5. Ventilation system Odor Control System Biological Oxidation Biological oxidation is a process by which the bacteria and other types of micro-organisms consume dissolved oxygen and organic substances in wastewater, using the energy released to convert organic carbon into carbon dioxide and cellular materials. BIO SCRUBBER Biological oxidation is broken into two broad categories: 1. Bio-oxidation using inorganic media (bio-scrubbers or bio-trickling filters) 2. Bio-oxidation using organic media AIR FAN (traditionally referred to as biofilters) Main features: 1. Scrubbing liquid make-up system 2. Scrubbing liquid re-circulation system NUTRIENT DOSING 3. Scrubbing liquid discharge system PUMPS 4. Nutrient dosing system NUTRIENT TANK 5. pH controller system BIO CIRCULATION PUMPS 6. Ventilation system TSE MAKE UP PUMPS TSE TANK Adsorption Adsorption is a process that uses activated carbon to adsorb odorous compound into activated carbon material. This is accomplished by passing the odorous air across a DEODORIZER bed of activated carbon, allowing the adsorptive process to occur and releasing the clean air to atmosphere. AIR FAN Main features: DEMISTER 1. Prefiltration system (demister) 2. Ventilation system 3. Carbon media Combined Technologies When a situation arises, where an odor stream contains both high levels of H2S and significant level of organic sulfur compounds. In a combined systems consisting of 2 technologies become more pratical. For this particular instance, a first stage system such as a bio-scrubber or catalytic carbon system might be used for removing the CHEMICAL H2S. A second stage bio-filter system would then be SCRUBBER CLEAN AIR STACK OUTPUT ideal to treat the mercaptans and any remaining H2S, which at this point would be at a very low level. AIR FAN CHEMICAL Another situation that often requires a combination DOSING PUMPS approach is that of odor control in sensitive areas. There are times when the odor source is quite close to facility fence line. Some odor control technologies BIO SCRUBBER have an odor unit level at their discharge that might not be acceptable if the neighbors are close to the fence line. For example, bio-filters have an effluent odor unit (OU) level between 200 and 400 OU. This level may CHEMICAL represent a considerable reduction of odors prior to the STORAGE TANK bio-filter but may still be too high for the neighbors. In CHEMICAL TANK FILLING this case, a solution would be to add a second stage OROROUS CHEMICAL AIR CIRCULATION activated carbon system to further reduce the OU level PUMPS BIO SOFTENER FRESH to 100 or less. This odor control technique is known as CIRCULATION WATER TANK PUMPS polishing. SOFTENER FEED PUMPS FRESH WATER TANK SOFTENER Odor control technologies comparison chart Odor Control Types of odor H2S Concentration Air ow range Eciency Technology treated ppm m3/h % Adsorption VOCs, H2S, broad range of Peak Less than 250 500 - 15,000 Greater than 99% (Activated Carbon) compounds Average Less than 50 Bioscrubber VOCs, NH3, H2S Less than 1000 500 - 50,000* Greater than 99% Chemical Scrubber Soluble odorous compounds Up-to 2000 Greater than 2000 99.9% including NH3 500 - 50,000* *Capacity can be supplied as per cilent requirments Common Odor Scenarios and Potential Solutions Odors can be produced at a number of points within the wastewater collection system as well as within wastewater treatment plant (WWTP) itself. These odors can be caused by a combination of inorganic and organic compounds. Three common odor scenarios have been examined as follows. 1. Collection System - Pumping Station 2. WWTP - Headworks 3. WWTP - Sludge Dewatering Looking at each scenario, the typical odor conditions such as types of odorous compounds present, how they are generated and their relative intensity is described. Then the best technology or combination of technology is recommended to solve the problem. 1. Collection System – Pumping Station The collection system which brings wastewater to the central wastewater treatment facility can be a major source of odor generation. When the waste water reaches the pumping station, the water is agitated and the H2S is liberated frvom the liquid phase to vapor phase, resulting in odor. The average H2S concentration is assumed to be 10 ppm. Other odorous compounds may be present but in very low concentrations. Solution The predominance of H2S combined with the lack of significant organic odorous compounds allows this application to be effectively solved with a single stage technology. At lower end of H2S range (10 ppm or less), an engineered biofilter or catalytic carbon system would be a good choice. At higher H2S levels, the biofilter becomes less of an adequate solution but a bioscrubber might now become an acceptable alternative. The particulars of pump stations include the proximity to neighbors and limited foot print space. For these additional reasons, activated carbon technology is highly preferred. 2. WWTP – Headworks Waste water from the collection system is brought into the treatment plant at the headworks. Hydrogen sulfide is typically the most prevalent odorous compound at the end headworks and can be present in concentrations from 5 ppm up to 50 ppm and beyond. Reduced sulfur compounds are usually also present from 50 ppb and higher. Solution The combination of significat level of H2S and reduced sulfur compounds requires a combination system for most effective solution. Here we can make a two stage system, consisting of a first stage bio-scrubber for H2S removal, followed by either an engineered biofilter or an activated carbon system. 3. WTTP – Sludge Dewatering Solids processes present some of the most intense odor challenges of all wastewater operations. The average H2S concentration can be assumed to be 10 ppm. Solution This challenging odor application is best solved with a combination technology. In this case, the significant loadings of all major types of odorous compounds would argue in favor of a bio-scrubber first stage (assuming the H2S levels are 20 ppm or less) to treat both H2S and ammonia followed by a biofilter second stage to reduce organic odors as well as to polish any remaining H2S or NH3. If average H2S levels are below 20 ppm, a first stage biofilter followed by a carbon polisher is a good choice. Three decades of engineering excellence Corodex has been supplying top quality water and wastewater treatment solutions for over 30 years. We have supplied over 250 water treatment systems, over 500 wastewater treatment plants, and numerous odor control systems. The type of odor control systems we have supplied include Adsorption, Biological Oxidation, and Chemical ab- sorption.Corodex has supplied more than 40 odor control systems for various applications to clients like Dubai Airport, Jebel Ali Airport zone, Palm Jumeirah Island, Dubai and Abu Dhabi Municipality,Qatar Airport and Oman. Project Profile Adsorption Odor Control System Client: Nakheel, Dubai Capacity: 2,520 m3/hr Client Need: Treatment of odor from Sewage Pumping Station H2S level: Average 30 ppm CRIN.CAT3.003.1010 Wet Chemical-scrubber Odor Control System Client: Sharjah Municipality, Dibba Al Hisin Capacity: 1,250 m3/hr Client Need: Treatment of odor from Main Lifting Station H2S level: Average 40 ppmv Peak 250 ppmv Combine Bio-scrubber and Carbon Adsorption Odor Control System Client: Sharjah Municipality, Sharjah Capacity: 3,011 m3/hr Client Need: Treatment of odor from main pumping station H2S level: Average 40-80 ppmv Peak 250 ppmv.
Recommended publications
  • Comparison of Chemical Wet Scrubbers and Biofiltration For
    Journal of Chemical Technology and Biotechnology J Chem Technol Biotechnol 80:1170–1179 (2005) DOI: 10.1002/jctb.1308 Comparison of chemical wet scrubbers and biofiltration for control of volatile organic compounds using GC/MS techniques and kinetic analysis James R Kastner∗ and Keshav C Das Department of Biological and Agricultural Engineering, The University of Georgia, Athens, GA, 30602, USA Abstract: Increasing public concerns and EPA air regulations in non-attainment zones necessitate the remediation of volatile organic compounds (VOCs) generated in the poultry-rendering industry. Wet scrubbers using chlorine dioxide (ClO2) have low overall removal efficiencies due to lack of reactivity with aldehydes. Contrary to wet scrubbers, a biofilter system successfully treated the aldehyde fraction, based on GC/MS analysis of inlet and outlet streams. Total VOC removal efficiencies ranged from 40 to 100% for the biofilter, kinetic analysis indicated that the overall removal capacity approached 25 g m−3 h−1, and aldehyde removal efficiency was significantly higher compared with chemical wet scrubbers. Process temperatures monitored in critical unit operations upstream from the biofilter varied significantly during operation, rising as much as 30 ◦C within a few minutes. However, the outlet air temperature of a high intensity scrubber remained relatively constant at 40 ◦C, although the inlet air temperature fluctuated from 50 to 65 ◦C during monitoring. These data suggest a hybrid process combining a wet scrubber and biofilter in series could be used to improve overall VOC removal efficiencies and process stability. 2005 Society of Chemical Industry Keywords: odor; volatile organic compounds (VOC); aldehydes; wet scrubber; biofilter; gas chromatography; mass spectrometry INTRODUCTION and odor complaints have resulted in the need for low Rendering operations convert organic wastes (feathers, cost, effective treatment options.
    [Show full text]
  • Application Note Wet Flue Gas Desulfurization Scrubbers Power: Environmental
    Application Note Wet Flue Gas Desulfurization Scrubbers Power: Environmental Coal fi red power plant emissions are a global concern. collects in the bottom of the absorber. A paste-like calcium The burning of coal produces sulfur dioxide (SO2). When sulfi te (CaSO3) sludge forms in the liquid. CaCO3 can be released into the atmosphere SO2 combines with water very diffi cult to remove if it settles out at the bottom of the to form sulfuric acid (H2SO4). Coal fi red power plants will absorber. More recent scrubber designs will blow outside use a fl ue gas desulfurization (FGD) scrubber to remove air through liquid to convert the sulfi te to sulfate in the the SO2 before release up the stack. The scrubbing following reaction. process is pH dependent. In this paper we will explore some of the challenges in this type of pH measurement. CaSO3 + H2O + 1/2O2 ► CaSO4 + H2O The FGD scrubber uses chemical reagents sprayed into The addition of air is referred to as forced oxidation. The the fl ue gas to react with the SO2. Many different reagents resulting calcium sulfate (CaCO4) crystallizes in the liquid have been used over the years. Examples include and is easily removed through fi ltration. An added benefi t ammonia, caustic, lime, limestone, and sodium carbonate. from the process is that CaCO4 (known as gypsum) can Due to cost, the most common reagents are Lime (CaO) be sold as additive for wallboard and cement production. and Limestone (CaCO3). Since both chemicals are very similar we will limit the scope of this paper to them.
    [Show full text]
  • 2.2 Sewage Sludge Incineration
    2.2 Sewage Sludge Incineration There are approximately 170 sewage sludge incineration (SSI) plants in operation in the United States. Three main types of incinerators are used: multiple hearth, fluidized bed, and electric infrared. Some sludge is co-fired with municipal solid waste in combustors based on refuse combustion technology (see Section 2.1). Refuse co-fired with sludge in combustors based on sludge incinerating technology is limited to multiple hearth incinerators only. Over 80 percent of the identified operating sludge incinerators are of the multiple hearth design. About 15 percent are fluidized bed combustors and 3 percent are electric. The remaining combustors co-fire refuse with sludge. Most sludge incinerators are located in the Eastern United States, though there are a significant number on the West Coast. New York has the largest number of facilities with 33. Pennsylvania and Michigan have the next-largest numbers of facilities with 21 and 19 sites, respectively. Sewage sludge incinerator emissions are currently regulated under 40 CFR Part 60, Subpart O and 40 CFR Part 61, Subparts C and E. Subpart O in Part 60 establishes a New Source Performance Standard for particulate matter. Subparts C and E of Part 61--National Emission Standards for Hazardous Air Pollutants (NESHAP)--establish emission limits for beryllium and mercury, respectively. In 1989, technical standards for the use and disposal of sewage sludge were proposed as 40 CFR Part 503, under authority of Section 405 of the Clean Water Act. Subpart G of this proposed Part 503 proposes to establish national emission limits for arsenic, beryllium, cadmium, chromium, lead, mercury, nickel, and total hydrocarbons from sewage sludge incinerators.
    [Show full text]
  • Lime / Limestone Wet Scrubbing System for Flue Gas Desulfurization
    Application Data Sheet ADS 4900-02/rev.D Power Industry December 2014 Lime / Limestone Wet Scrubbing System for Flue Gas Desulfurization BACKGROUND will therefore add more lime when pH drops below 12 and a limestone based system will be controlled around 6. Unless Wet scrubbers are used in utilities, paper mills, and chemical one or the other is added, the SO gas will quickly drive the plants to remove sulfur dioxide (SO ) and other pollutants 2 2 pH acidic. from gas streams. Undesirable pollutants are removed by contacting the gases with an aqueous solution or slurry The calcium compounds produced in scrubbers tend to containing a sorbent. The most common sorbents are lime accumulate in recirculation loops and can cause a buildup of scale. Scale on the spray nozzles affects the atomization (Ca[OH]2) and limestone (CaCO3). Rosemount Analytical pH equipment is used to control the feed rate of these of the water droplets and reduces the scrubbing efficiency. chemicals. Scale on the return piping reduces flow rate and changes the thermal balance of the system. The tendency to scale is limited by additives such as chelating agents and phos- PROCESS phates, but these additives are generally only effective at After fly ash removal, the flue gas (seen in Figure 1) is bubbled higher pH levels. pH control is necessary to forestall the through the scrubber, and the slurry is added from start of scaling, as it is much easier to prevent scaling than above.The lime or limestone reacts with the SO2 in the flue to remove it.
    [Show full text]
  • Air/Gas Cleaning & Odor Control
    Air/Gas Cleaning & Odor Control Air/Gas Cleaning & Odor Control The Monroe Advantage For over forty years, Monroe Environmental has been designing and manufacturing air quality systems for industrial manufacturers, government agencies, and municipal treatment plants. Table of Complete Air Quality Solutions Contents Monroe Environmental offers a broad range of stand-alone equipment as well as complete 2 The Monroe systems to effectively manage dust, mist, odors, and Advantage fumes associated with both industrial manufactur- 4 Scrubbing ing and municipal water/wastewater treatment. Applications Monroe continues to solve challenging air 6 Packed Bed and gas cleaning problems with our skilled team of engineers, shop technicians, and knowledgeable Fume Scrubbers sales staff. The largest manufacturing companies in 8 Venturi the world routinely look to Monroe to solve their Particulate most demanding mist, dust, and fume control Scrubbers problems. 10 Carbon Monroe Systems and Services Adsorbers Packed Bed Wet Air Scrubbers 15,000 CFM Packed Bed Scrubber to remove ethylene • glycol and NMP fumes from a glass coating operation 12 Multi-Stage • Venturi Particulate Scrubbers Scrubbing • Carbon Adsorbers • Design and manufacture new air quality and odor control systems Systems • Multi-Stage Scrubbing Systems Retrofit existing systems to maximize 14 Mist and Dust Dust Collectors • • performance and removal efficiency Collection • Oil Mist Collectors • Ductwork design 16 Dry Dust • Permit assistance for EPA compliance Collectors • Industrial and municipal
    [Show full text]
  • Design Guidelines for Carbon Dioxide Scrubbers I
    "NCSCTECH MAN 4110-1-83 I (REVISION A) S00 TECHNICAL MANUAL tow DESIGN GUIDELINES FOR CARBON DIOXIDE SCRUBBERS I MAY 1983 REVISED JULY 1985 Prepared by M. L. NUCKOLS, A. PURER, G. A. DEASON I OF * Approved for public release; , J 1"73 distribution unlimited NAVAL COASTAL SYSTEMS CENTER PANAMA CITY, FLORIDA 32407 85. .U 15 (O SECURITY CLASSIFICATION OF TNIS PAGE (When Data Entered) R O DOCULMENTATIONkB PAGE READ INSTRUCTIONS REPORT DOCUMENTATION~ PAGE BEFORE COMPLETING FORM 1. REPORT NUMBER 2a. GOVT AQCMCSION N (.SAECIP F.NTTSChALOG NUMBER "NCSC TECHMAN 4110-1-83 (Rev A) A, -NI ' 4. TITLE (and Subtitle) S. TYPE OF REPORT & PERIOD COVERED "Design Guidelines for Carbon Dioxide Scrubbers '" 6. PERFORMING ORG. REPORT N UMBER A' 7. AUTHOR(&) 8. CONTRACT OR GRANT NUMBER(S) M. L. Nuckols, A. Purer, and G. A. Deason 9. PERFORMING ORGANIZATION NAME AND ADDRESS 10. PROGRAM ELEMENT, PROJECT. TASK AREA 6t WORK UNIT NUMBERS Naval Coastal PanaaLSystems 3407Project CenterCty, S0394, Task Area Panama City, FL 32407210,WrUnt2 22102, Work Unit 02 II. CONTROLLING OFFICE NAME AND ADDRE1S t2. REPORT 3ATE May 1983 Rev. July 1985 13, NUMBER OF PAGES 69 14- MONI TORING AGENCY NAME & ADDRESS(if different from Controtling Office) 15. SECURITY CLASS. (of this report) UNCLASSIFIED ISa. OECL ASSI FICATION/DOWNGRADING _ __N•AEOULE 16. DISTRIBUTION STATEMENT (of thia Repott) Approved for public release; distribution unlimited. 17. DISTRIBUTION STATEMENT (of the abstract entered In Block 20, If different from Report) IS. SUPPLEMENTARY NOTES II. KEY WORDS (Continue on reverse side If noceassry and Identify by block number) Carbon Dioxide; Scrubbers; Absorption; Design; Life Support; Pressure; "Swimmer Diver; Environmental Effects; Diving., 20.
    [Show full text]
  • Evaluating the Effectiveness of Scrubber Installation on Sulfur Dioxide Emissions from Coal Electricity Generating Units
    Evaluating the Effectiveness of Scrubber Installation on Sulfur Dioxide Emissions from Coal Electricity Generating Units Jayson Toweh Submitted in partial fulfillment of the requirements for the degree of Master of Science in Environmental Health Harvard T.H. Chan School of Public Health Boston, MA August 16, 2019 2 Abstract Background: Electricity generated by coal represents the second-largest contribution to the United States energy portfolio. Resulting emissions, such as sulfur dioxide (SO2) can lead to various adverse health impacts. Research Question: The goal of this study was to evaluate how SO2 scrubber installation affected SO2 emissions from electricity generating units (EGUs). EGU characteristics were analyzed to determine what led EGUs to install scrubbers and the types of scrubbers that were installed. Methods: EPA Air Markets Program Data was analyzed to compare emissions from EGUs that installed SO2 scrubbers between 1995-2015, to EGUs that had no scrubbers. We evaluated emissions changes from three years before to three years of post- scrubber installation. The HYSPLIT Average Dispersion metric model was used to map exposure concentration a year post scrubber installation. Results: SO2 emissions three years post-installation were 10% the levels of three years before installation. Locations in the eastern United States experienced the most significant reduction in exposure from coal EGUs. Wet Limestone scrubbers were installed most frequently contributing to the significant decrease. Discussion: The most extensive and highest emitting EGUs installed scrubbers and some of the best scrubber technology. Finding incentives to increase scrubber installation in lower generating EGUs is critical moving forward. 3 Introduction Electricity Generating Units Emissions Coal power plants are the second-largest contributor to the United States electricity supply, with 1,146 billion kWh produced equating to 27.4% of the energy generated in 2018 (EIA, 2019).
    [Show full text]
  • INVESTIGATION of POLYCYCLIC AROMATIC HYDROCARBONS (Pahs) on DRY FLUE GAS DESULFURIZATION (FGD) BY-PRODUCTS
    INVESTIGATION OF POLYCYCLIC AROMATIC HYDROCARBONS (PAHs) ON DRY FLUE GAS DESULFURIZATION (FGD) BY-PRODUCTS DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Ping Sun, M.S. ***** The Ohio State University 2004 Dissertation Committee: Approved by Professor Linda Weavers, Adviser Professor Harold Walker Professor Patrick Hatcher Adviser Professor Yu-Ping Chin Civil Engineering Graduate Program ABSTRACT The primary goal of this research was to examine polycyclic aromatic hydrocarbons (PAHs) on dry FGD by-products to determine environmentally safe reuse options of this material. Due to the lack of information on the analytical procedures for measuring PAHs on FGD by-products, our initial work focused on analytical method development. Comparison of the traditional Soxhlet extraction, automatic Soxhlet extraction, and ultrasonic extraction was conducted to optimize the extraction of PAHs from lime spray dryer (LSD) ash (a common dry FGD by-product). Due to the short extraction time, ultrasonic extraction was further optimized by testing different organic solvents. Ultrasonic extraction with toluene as the solvent turned out to be a fast and efficient method to extract PAHs from LSD ash. The possible reactions of PAHs under standard ultrasonic extraction conditions were then studied to address concern over the possible degradation of PAHs by ultrasound. By sonicating model PAHs including naphthalene, phenanthrene and pyrene in organic solutions, extraction parameters including solvent type, solute concentration, and sonication time on reactions of PAHs were examined. A hexane: acetone (1:1 V/V) ii mixture resulted in less PAH degradation than a dichloromethane (DCM): acetone (1:1 V/V) mixture.
    [Show full text]
  • A Review of the Scrubber As a Tool for the Control of Flue Gas Emissions in a Combustion System
    EJERS, European Journal of Engineering Research and Science Vol. 4, No. 11, November 2019 A Review of the Scrubber as a Tool for the Control of flue Gas Emissions in a Combustion System N. Harry-Ngei, I. Ubong, and P. N. Ede Depending on the design, specific factors govern the Abstract—This paper focuses on the description, function application and operation of the scrubber; reference [4] and working principles of the wet gas scrubber required to listed the following vital variables to look out for in control air pollution emissions from a combustion system of a deciding the optimal scrubber for use: boiler. Important points to note in the selection and operation i. Characteristics of the particulate matter of the scrubber as well as the different types of scrubbers commonly deployed in the industries to cut down on emissions considered to be removed were addressed. A comprehensive review of the removal ii. The size categorization of the particulate matter mechanisms and schemes of the scrubber were reported for iii. Concentration of the emission in the flue gas various research on the subject. The packed tower scrubber, iv. Characteristics of the scrubber liquid, for however, was recommended because of varying advantages example, whether it is flammable or combustible and ease of operations. v. Desired removal efficiency Index Terms—Scrubber, Gas Emission, Combustion, vi. Important actual process parameters of the flue Environmental Pollution. gas as this will determine the scrubber sizing vii. Required space for the scrubber The potency and quality of separation and cleaning of I. INTRODUCTION flue gases with regards to air pollution control is depended Reference [1] described scrubbers as devices utilised to on the solvent, therefore, the characteristics, operation, remove gaseous constituents that has debilitating effects on optimum condition must be evaluated before a choice is the environment.
    [Show full text]
  • Appendix B WET SCRUBBERS for GASEOUS CONTROL
    Review DRAFT B.5 WET SCRUBBERS FOR GASEOUS CONTROL1,2,9,15 B.5.1 Background Wet scrubbers use a liquid to remove pollutants from an exhaust stream. In gaseous emission control applications, wet scrubbers remove pollutants by absorption. For this reason, wet scrubbers used for gaseous pollutant control often are referred to as absorbers. Absorption is very effective when controlling pollutant gases present in appreciable concentration, but also is feasible for gases at dilute concentrations when the gas is highly soluble in the absorbent. The driving force for absorption is related to the amount of soluble gas in the gas stream and the concentration of the solute gas in the liquid film in contact with the gas. Water is the most commonly used absorbent, but nonaqueous liquids of low vapor pressure (such as dimethylaniline or amines) may be used for gases with low water solubility, such as hydrocarbons or hydrogen sulfide (H2S). Water used for absorption may frequently contain other chemicals to react with the gas being absorbed and reduce the concentration. When water is not used, absorbent separation and scrubbing liquid regeneration may be frequently required due to the cost of the scrubbing liquid. Wet scrubbers rely on the creation of large surface areas of scrubbing liquid that allow intimate contact between the liquid and gas. The creation of large surface areas can be accomplished by passing the liquid over a variety of media (packing, meshing, grids, trays) or by creating a spray of droplets. There are several types of wet scrubber designs, including spray tower, tray-type, and packed-bed wet scrubbers; these are generally referred to as low-energy scrubbers.
    [Show full text]
  • Section 5 SO2 and Acid Gas Controls
    Section 5 SO2 and Acid Gas Controls Chapter 1 Wet and Dry Scrubbers for Acid Gas Control John L. Sorrels Air Economics Group Health and Environmental Impacts Division Office of Air Quality Planning and Standards U.S. Environmental Protection Agency Research Triangle Park, NC 27711 Amanda Baynham, David D. Randall, Randall Laxton RTI International Research Triangle Park, NC 27709 April 2021 DISCLAIMER This document includes references to specific companies, trade names and commercial products. Mention of these companies and their products in this document is not intended to constitute an endorsement or recommendation by the U.S. Environmental Protection Agency. i Contents 1.1 Introduction ............................................................................................................................ 1 1.1.1 Process Description .................................................................................................... 2 1.1.2 Gas Absorber System Configurations ........................................................................ 2 1.1.3 Structural Design of Wet Absorption Equipment ...................................................... 5 1.1.4 Factors Affecting the Performance ............................................................................ 6 1.1.5 Structural Design of Dry Absorption Equipment ...................................................... 7 1.1.6 Equipment Life .......................................................................................................... 8 1.2 Flue Gas Desulfurization
    [Show full text]
  • Capture of Co2 Using Water Scrubbing
    CAPTURE OF CO2 USING WATER SCRUBBING Report Number PH3/26 July 2000 This document has been prepared for the Executive Committee of the Programme. It is not a publication of the Operating Agent, International Energy Agency or its Secretariat. Title: Capture of CO2 using water scrubbing Reference number: PH3/26 Date issued: July 2000 Other remarks: Background to the Study The leading options for CO2 capture are based on scrubbing with regenerable solvents. A potentially simpler alternative would be once-through scrubbing with seawater, followed by direct discharge of the CO2-laden seawater into the deep ocean. This would avoid the cost, complexity and energy losses associated with regenerating the scrubbing solvent and compressing the CO2 gas. This report presents the results of a scoping study on options for CO2 capture using water scrubbing. The study was carried out for IEA GHG by URS New Zealand Ltd. (formerly Woodward Clyde (NZ) Ltd.) Approach Adopted A range of power generation processes involving seawater scrubbing has been examined. A scoping assessment has been carried out to identify the most promising processes based on coal and natural gas fuels. Outline designs of CO2 capture processes have been prepared and comparative plant performances and costs estimated. From this, the key parameters that influence the potential for water-based capture processes are identified and the sensitivity of costs and performance to variations in these parameters assessed. CO2-la den seawater would normally need to be discharged at depths greater than about 1500m, to minimise environmental impacts and to ensure that the CO2 remained in the ocean for a long period of time.
    [Show full text]