Renewable Propane Synopsis
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SAFETY DATA SHEET Nonflammable Gas Mixture: Carbon Dioxide / Carbon Monoxide / Nitric Oxide / Nitrogen / Propane Section 1
SAFETY DATA SHEET Nonflammable Gas Mixture: Carbon Dioxide / Carbon Monoxide / Nitric Oxide / Nitrogen / Propane Section 1. Identification GHS product identifier : Nonflammable Gas Mixture: Carbon Dioxide / Carbon Monoxide / Nitric Oxide / Nitrogen / Propane Other means of : Not available. identification Product type : Gas. Product use : Synthetic/Analytical chemistry. SDS # : 002173 Supplier's details : Airgas USA, LLC and its affiliates 259 North Radnor-Chester Road Suite 100 Radnor, PA 19087-5283 1-610-687-5253 24-hour telephone : 1-866-734-3438 Section 2. Hazards identification OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Classification of the : GASES UNDER PRESSURE - Compressed gas substance or mixture GHS label elements Hazard pictograms : Signal word : Warning Hazard statements : Contains gas under pressure; may explode if heated. May displace oxygen and cause rapid suffocation. May increase respiration and heart rate. Precautionary statements General : Read and follow all Safety Data Sheets (SDS’S) before use. Read label before use. Keep out of reach of children. If medical advice is needed, have product container or label at hand. Close valve after each use and when empty. Use equipment rated for cylinder pressure. Do not open valve until connected to equipment prepared for use. Use a back flow preventative device in the piping. Use only equipment of compatible materials of construction. Prevention : Not applicable. Response : Not applicable. Storage : Protect from sunlight. Store in a well-ventilated place. Disposal : Not applicable. Hazards not otherwise : In addition to any other important health or physical hazards, this product may displace classified oxygen and cause rapid suffocation. -
Storing Syngas Lowers the Carbon Price for Profitable Coal Gasification
Carnegie Mellon Electricity Industry Center Working Paper CEIC-07-10 www.cmu.edu/electricity Storing syngas lowers the carbon price for profitable coal gasification ADAM NEWCOMER AND JAY APT Carnegie Mellon Electricity Industry Center, Tepper School of Business, and Department of Engineering and Public Policy, 254 Posner Hall, Carnegie Mellon University, Pittsburgh, Pennsylvania 15213 Integrated gasification combined cycle (IGCC) electric power generation systems with carbon capture and sequestration have desirable environmental qualities, but are not profitable when the carbon dioxide price is less than approximately $50 per metric ton. We examine whether an IGCC facility that operates its gasifier continuously but stores the syngas and produces electricity only when daily prices are high may be profitable at significantly lower CO2 prices. Using a probabilistic analysis, we have calculated the plant-level return on investment (ROI) and the value of syngas storage for IGCC facilities located in the US Midwest using a range of storage configurations. Adding a second turbine to use the stored syngas to generate electricity at peak hours and implementing 12 hours of above ground high pressure syngas storage significantly increases the ROI and net present value. Storage lowers the carbon price at which IGCC enters the US generation mix by approximately 25%. 1 Carnegie Mellon Electricity Industry Center Working Paper CEIC-07-10 www.cmu.edu/electricity Introduction Producing electricity from coal-derived synthesis gas (syngas) in an integrated gasification combined cycle (IGCC) facility can improve criteria pollutant performance over other coal-fueled technologies such as pulverized coal (PC) facilities [1-5] and can be implemented with carbon capture and sequestration. -
Experimental and Analytical Study of Nitric Oxide Formation During Combustion of Propane in a Jet-Stirred Combustor
NASA Technical Paper 1181 I 1 Experimental and Analytical Study of Nitric Oxide Formation During / Combustion of Propane in a Jet-Stirred Combustor , ' N. T. Wakelyn, Casimir J. Jachimowski, and Charles H. Wilson , TECH LIBRARY KAFB, NM 0134538 NASA Technical Paper 1181 Experimental and Analytical Study of Nitric Oxide Formation During Combustion of Propane in a Jet-Stirred Combustor N. T. Wakelyn, Casimir J. Jachimowski, and Charles H. Wilson Langley Research Center Hampton, Virginia National Aeronautics and Space Administration Scientific and Technical Information Otfice 1978 '8' SUMMARY A jet-stirred combustor, constructed of castable zirconia and with an inconel injector, has been used to study nitric oxide formation in propane-air combustion with residence times in the range from 3.2 to 3.3 msec and equiva lence ratios varying from 0.7 to 1.4. The residence time range was character istic of that found in the primary zones of aircraft turbines. Premixed propane-air formulations were subjected to intense and turbulent backmixed combustion within the cavity formed between the injector and the hemispherical inner walls of the zirconia shell. The volume of the combustor cavity was 12.7 cm3 and the mass loading was maintained in the range from 0.053 to 0.055 g/cm3-sec. Measurements were made of combustor operating tem perature and of nitric oxide concentration. Maximum nitric oxide concentrations of the order of 55 ppm were found in the range of equivalence ratio from 1.0 to 1.1. Nitric oxide concentrations were predicted over the range of equivalence ratio by a computer program which employs a perfectly stirred'reactor (PSR) algorithm with finite-rate kinetics. -
Alternatives to High Propane Prices Interest Expense and the Cost of Utilities Are the Two Largest “Out of Pocket” Expenses Facing Most Broiler Growers
ThePoultry Engineering, Economics & Management NEWSLETTER Critical Information for Improved Bird Performance Through Better House and Ventilation System Design, Operation and Management Auburn University, in cooperation with the U.S. Poultry & Egg Association Issue No 29, May 2004 Alternatives to High Propane Prices Interest expense and the cost of utilities are the two largest “out of pocket” expenses facing most broiler growers. There is little a grower can do to reduce interest costs, short of major mortgage refinancing. However, costs associated with utilities are another matter. The topics we have addressed in most past issues of this newsletter have all dealt with housing and ventilation factors which can result in improved flock performance and in reduced levels of energy being used, which directly reduces costs to the grower. Electricity rates are typically fixed and are highly regulated. However, the price of heating fuel, specifically propane (liquefied petroleum gas or LPG), has varied widely up and down in most recent years, depending on the time of year and numerous supply and demand conditions. Growers can choose What growers should be aware of is that there are ways to reduce the from several good risk that they will have to buy propane at one of those times when the alternatives to paying price is highest. This newsletter explains several alternative methods consistently high prices growers can use to get lower and more stable propane costs over time. for propane. Understanding the Basics of Propane Pricing The most fundamental factor in propane pricing is that propane is basically a fossil fuel, being derived from raw natural gas during the oil refining process. -
Safety Data Sheet
SAFETY DATA SHEET 1. Identification Product number 1000007900 Product identifier AUTO GLASS QUICK RELEASE AGENT Company information Sprayway, Inc. 1005 S. Westgate Drive Addison, IL 60101 United States Company phone General Assistance 1-630-628-3000 Emergency telephone US 1-866-836-8855 Emergency telephone outside 1-952-852-4646 US Version # 01 Recommended use Not available. Recommended restrictions None known. 2. Hazard(s) identification Physical hazards Flammable aerosols Category 1 Health hazards Serious eye damage/eye irritation Category 2A Specific target organ toxicity, single exposure Category 3 narcotic effects Aspiration hazard Category 1 Environmental hazards Not classified. OSHA defined hazards Not classified. Label elements Signal word Danger Hazard statement Extremely flammable aerosol. May be fatal if swallowed and enters airways. Causes serious eye irritation. May cause drowsiness or dizziness. Precautionary statement Prevention Keep away from heat/sparks/open flames/hot surfaces. - No smoking. Do not spray on an open flame or other ignition source. Pressurized container: Do not pierce or burn, even after use. Avoid breathing gas. Wash thoroughly after handling. Use only outdoors or in a well-ventilated area. Wear eye/face protection. Response If swallowed: Immediately call a poison center/doctor. If inhaled: Remove person to fresh air and keep comfortable for breathing. If in eyes: Rinse cautiously with water for several minutes. Remove contact lenses, if present and easy to do. Continue rinsing. Call a poison center/doctor if you feel unwell. Do NOT induce vomiting. If eye irritation persists: Get medical advice/attention. Storage Store in a well-ventilated place. Keep container tightly closed. Store locked up. -
Fuel Properties Comparison
Alternative Fuels Data Center Fuel Properties Comparison Compressed Liquefied Low Sulfur Gasoline/E10 Biodiesel Propane (LPG) Natural Gas Natural Gas Ethanol/E100 Methanol Hydrogen Electricity Diesel (CNG) (LNG) Chemical C4 to C12 and C8 to C25 Methyl esters of C3H8 (majority) CH4 (majority), CH4 same as CNG CH3CH2OH CH3OH H2 N/A Structure [1] Ethanol ≤ to C12 to C22 fatty acids and C4H10 C2H6 and inert with inert gasses 10% (minority) gases <0.5% (a) Fuel Material Crude Oil Crude Oil Fats and oils from A by-product of Underground Underground Corn, grains, or Natural gas, coal, Natural gas, Natural gas, coal, (feedstocks) sources such as petroleum reserves and reserves and agricultural waste or woody biomass methanol, and nuclear, wind, soybeans, waste refining or renewable renewable (cellulose) electrolysis of hydro, solar, and cooking oil, animal natural gas biogas biogas water small percentages fats, and rapeseed processing of geothermal and biomass Gasoline or 1 gal = 1.00 1 gal = 1.12 B100 1 gal = 0.74 GGE 1 lb. = 0.18 GGE 1 lb. = 0.19 GGE 1 gal = 0.67 GGE 1 gal = 0.50 GGE 1 lb. = 0.45 1 kWh = 0.030 Diesel Gallon GGE GGE 1 gal = 1.05 GGE 1 gal = 0.66 DGE 1 lb. = 0.16 DGE 1 lb. = 0.17 DGE 1 gal = 0.59 DGE 1 gal = 0.45 DGE GGE GGE Equivalent 1 gal = 0.88 1 gal = 1.00 1 gal = 0.93 DGE 1 lb. = 0.40 1 kWh = 0.027 (GGE or DGE) DGE DGE B20 DGE DGE 1 gal = 1.11 GGE 1 kg = 1 GGE 1 gal = 0.99 DGE 1 kg = 0.9 DGE Energy 1 gallon of 1 gallon of 1 gallon of B100 1 gallon of 5.66 lb., or 5.37 lb. -
Process Technologies and Projects for Biolpg
energies Review Process Technologies and Projects for BioLPG Eric Johnson Atlantic Consulting, 8136 Gattikon, Switzerland; [email protected]; Tel.: +41-44-772-1079 Received: 8 December 2018; Accepted: 9 January 2019; Published: 15 January 2019 Abstract: Liquified petroleum gas (LPG)—currently consumed at some 300 million tonnes per year—consists of propane, butane, or a mixture of the two. Most of the world’s LPG is fossil, but recently, BioLPG has been commercialized as well. This paper reviews all possible synthesis routes to BioLPG: conventional chemical processes, biological processes, advanced chemical processes, and other. Processes are described, and projects are documented as of early 2018. The paper was compiled through an extensive literature review and a series of interviews with participants and stakeholders. Only one process is already commercial: hydrotreatment of bio-oils. Another, fermentation of sugars, has reached demonstration scale. The process with the largest potential for volume is gaseous conversion and synthesis of two feedstocks, cellulosics or organic wastes. In most cases, BioLPG is produced as a byproduct, i.e., a minor output of a multi-product process. BioLPG’s proportion of output varies according to detailed process design: for example, the advanced chemical processes can produce BioLPG at anywhere from 0–10% of output. All these processes and projects will be of interest to researchers, developers and LPG producers/marketers. Keywords: Liquified petroleum gas (LPG); BioLPG; biofuels; process technologies; alternative fuels 1. Introduction Liquified petroleum gas (LPG) is a major fuel for heating and transport, with a current global market of around 300 million tonnes per year. -
Gasification of Woody Biomasses and Forestry Residues
fermentation Article Gasification of Woody Biomasses and Forestry Residues: Simulation, Performance Analysis, and Environmental Impact Sahar Safarian 1,*, Seyed Mohammad Ebrahimi Saryazdi 2, Runar Unnthorsson 1 and Christiaan Richter 1 1 Mechanical Engineering and Computer Science, Faculty of Industrial Engineering, University of Iceland, Hjardarhagi 6, 107 Reykjavik, Iceland; [email protected] (R.U.); [email protected] (C.R.) 2 Department of Energy Systems Engineering, Sharif University of Technologies, Tehran P.O. Box 14597-77611, Iran; [email protected] * Correspondence: [email protected] Abstract: Wood and forestry residues are usually processed as wastes, but they can be recovered to produce electrical and thermal energy through processes of thermochemical conversion of gasification. This study proposes an equilibrium simulation model developed by ASPEN Plus to investigate the performance of 28 woody biomass and forestry residues’ (WB&FR) gasification in a downdraft gasifier linked with a power generation unit. The case study assesses power generation in Iceland from one ton of each feedstock. The results for the WB&FR alternatives show that the net power generated from one ton of input feedstock to the system is in intervals of 0 to 400 kW/ton, that more that 50% of the systems are located in the range of 100 to 200 kW/ton, and that, among them, the gasification system derived by tamarack bark significantly outranks all other systems by producing 363 kW/ton. Moreover, the environmental impact of these systems is assessed based on the impact categories of global warming (GWP), acidification (AP), and eutrophication (EP) potentials and Citation: Safarian, S.; Ebrahimi normalizes the environmental impact. -
The Influence of Residual Sodium on the Catalytic Oxidation of Propane and Toluene Over Co3o4 Catalysts
catalysts Article The Influence of Residual Sodium on the Catalytic Oxidation of Propane and Toluene over Co3O4 Catalysts Guangtao Chai 1,2, Weidong Zhang 1, Yanglong Guo 2,* , Jose Luis Valverde 3 and Anne Giroir-Fendler 1,* 1 Université Claude Bernard Lyon 1, Université de Lyon, CNRS, IRCELYON, 2 Avenue Albert Einstein, F-69622 Villeurbanne, France; [email protected] (G.C.); [email protected] (W.Z.) 2 Key Laboratory for Advanced Materials, Research Institute of Industrial Catalysis, School of Chemistry and Molecular Engineering, East China University of Science and Technology, Shanghai 200237, China 3 Department of Chemical Engineering, University of Castilla La Mancha, Avda. Camilo José Cela 12, 13071 Ciudad Real, Spain; [email protected] * Correspondence: [email protected] (Y.G.); [email protected] (A.G.-F.); Tel.: +86-21-64-25-29-23 (Y.G.); +33-472-431-586 (A.G.-F.) Received: 16 July 2020; Accepted: 30 July 2020; Published: 3 August 2020 Abstract: A series of Co3O4 catalysts with different contents of residual sodium were prepared using a precipitation method with sodium carbonate as a precipitant and tested for the catalytic oxidation 1 1 of 1000 ppm propane and toluene at a weight hourly space velocity of 40,000 mL g− h− , respectively. Several techniques were used to characterize the physicochemical properties of the catalysts. Results showed that residual sodium could be partially inserted into the Co3O4 spinel lattice, inducing distortions and helping to increase the specific surface area of the Co3O4 catalysts. Meanwhile, it could negatively affect the reducibility and the oxygen mobility of the catalysts. -
Harmon of Energ THIRD REVIS Onisation of Definitions Rgy
Harmononisation of Definitions of Energrgy Products and Flows THIRD REVISISION OF THE DEFINITIOIONS Part 1: Flows IEA,A, Paris, 21 December 2009 Table of Contents Page Note by Tim Simmons ............................................................................................................................. 5 Flow Structure ......................................................................................................................................... 7 Definition of National Territory (not in flow classification) ................................................................... 9 Supply .................................................................................................................................................... 11 Production .............................................................................................................................................. 13 Receipts from Other Sources ................................................................................................................. 16 Imports and Exports .............................................................................................................................. 18 International Marine Bunkers ................................................................................................................ 21 International Aviation Bunkers ............................................................................................................. 22 Stocks (not in flow classification) ........................................................................................................ -
Review of Technologies for Gasification of Biomass and Wastes
Review of Technologies for Gasification of Biomass and Wastes Final report NNFCC project 09/008 A project funded by DECC, project managed by NNFCC and conducted by E4Tech June 2009 Review of technology for the gasification of biomass and wastes E4tech, June 2009 Contents 1 Introduction ................................................................................................................... 1 1.1 Background ............................................................................................................................... 1 1.2 Approach ................................................................................................................................... 1 1.3 Introduction to gasification and fuel production ...................................................................... 1 1.4 Introduction to gasifier types .................................................................................................... 3 2 Syngas conversion to liquid fuels .................................................................................... 6 2.1 Introduction .............................................................................................................................. 6 2.2 Fischer-Tropsch synthesis ......................................................................................................... 6 2.3 Methanol synthesis ................................................................................................................... 7 2.4 Mixed alcohols synthesis ......................................................................................................... -
BENZENE Disclaimer
United States Office of Air Quality EPA-454/R-98-011 Environmental Protection Planning And Standards June 1998 Agency Research Triangle Park, NC 27711 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF BENZENE Disclaimer This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and has been approved for publication. Mention of trade names and commercial products does not constitute endorsement or recommendation of use. EPA-454/R-98-011 ii TABLE OF CONTENTS Section Page LIST OF TABLES.....................................................x LIST OF FIGURES.................................................. xvi EXECUTIVE SUMMARY.............................................xx 1.0 PURPOSE OF DOCUMENT .......................................... 1-1 2.0 OVERVIEW OF DOCUMENT CONTENTS.............................. 2-1 3.0 BACKGROUND INFORMATION ...................................... 3-1 3.1 NATURE OF POLLUTANT..................................... 3-1 3.2 OVERVIEW OF PRODUCTION AND USE ......................... 3-4 3.3 OVERVIEW OF EMISSIONS.................................... 3-8 4.0 EMISSIONS FROM BENZENE PRODUCTION ........................... 4-1 4.1 CATALYTIC REFORMING/SEPARATION PROCESS................ 4-7 4.1.1 Process Description for Catalytic Reforming/Separation........... 4-7 4.1.2 Benzene Emissions from Catalytic Reforming/Separation .......... 4-9 4.2 TOLUENE DEALKYLATION AND TOLUENE DISPROPORTIONATION PROCESS ............................ 4-11 4.2.1 Toluene Dealkylation