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Blending Hydrogen Into Natural Gas Pipeline Networks: a Review of Key Issues
Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues M. W. Melaina, O. Antonia, and M. Penev NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. Technical Report NREL/TP-5600-51995 March 2013 Contract No. DE-AC36-08GO28308 Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues M. W. Melaina, O. Antonia, and M. Penev Prepared under Task No. HT12.2010 NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. National Renewable Energy Laboratory Technical Report 15013 Denver West Parkway NREL/TP-5600-51995 Golden, Colorado 80401 March 2013 303-275-3000 • www.nrel.gov Contract No. DE-AC36-08GO28308 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. -
LLNL Underground Coal Gasification: an Overview of Groundwater
David W. Camp Joshua A. White Underground Coal Gasification: An Overview of Groundwater Contamination Hazards and Mitigation Strategies March 2015 Lawrence Livermore National Laboratory LLNL-TR-668633 Disclaimer This document was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor Lawrence Livermore Na- tional Security, LLC, nor any of their employees makes any warranty, expressed or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or useful- ness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or Lawrence Livermore National Security, LLC. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or Lawrence Livermore National Security, LLC, and shall not be used for advertising or product endorsement purposes. v Acknowledgements This work was funded by a 2012 Applied Science Grant from the Office of Surface Mining Reclamation and Enforcement. This work was performed under the auspices of the U.S. Department of Energy by Lawrence Livermore National Laboratory under Contract DE- AC52-07NA27344. The authors wish to thank Duane Matt and other members of the OSM Underground Coal Gasification Working Group for their support and recommendations. We also thank the Clean Air Task Force (CATF) for earlier funding that allowed LLNL to begin investi- gating groundwater contamination issues. -
DRAFT Comparative Assessment of Technology Options for Biogas Clean‐Up
Public Interest Energy Research (PIER) Program DRAFT INTERIM PROJECT REPORT DRAFT Comparative Assessment of Technology Options for Biogas Clean‐up Prepared for: California Energy Commission Prepared by: California Biomass Collaborative University of California, Davis OCTOBER 2014 CEC‐500‐11‐020, TASK 8 Prepared by: Primary Author(s): Matthew D. Ong Robert B. Williams Stephen R. Kaffka California Biomass Collaborative University of California, Davis 1 Shields Avenue Davis, CA 95616 Contract Number: 500-11-020, Task 8 Prepared for: California Energy Commission Michael Sokol Contract Manager Aleecia Gutierrez Office Manager Energy Generation Research Office Laurie ten Hope Deputy Director Energy Research and Development Robert Oglesby Executive Director DISCLAIMER This report was prepared as the result of work sponsored by the California Energy Commission. It does not necessarily represent the views of the Energy Commission, its employees or the State of California. The Energy Commission, the State of California, its employees, contractors and subcontractors make no warrant, express or implied, and assume no legal liability for the information in this report; nor does any party represent that the uses of this information will not infringe upon privately owned rights. This report has not been approved or disapproved by the California Energy Commission nor has the California Energy Commission passed upon the accuracy or adequacy of the information in this report. ACKNOWLEDGEMENTS The author would like to express his gratitude and appreciation to the following individuals for their various contributions to the development of this report: California Biomass Collaborative Robert Williams, Project Supervisor Dr. Stephen Kaffka, Project Manager Dr. Bryan Jenkins, Contract Manager American Biogas Council Bioenergy Association of California. -
Impact of Rising Natural Gas Prices on U.S. Ammonia Supply
A Report from the Economic Research Service United States Department www.ers.usda.gov of Agriculture WRS-0702 August 2007 Impact of Rising Natural Gas Prices on U.S. Ammonia Supply Wen-yuan Huang Abstract The volatile and upward trend in U.S. natural gas prices from 2000-06 has led to a 17- percent decline in the Nation’s annual aggregate supply of ammonia. During the period, U.S. ammonia production declined 44 percent, while U.S. ammonia imports increased Contents 115 percent. Also, the share of U.S.-produced ammonia in the U.S. aggregate supply of ammonia dropped from 80 to 55 percent, while the share from imports increased from Introduction ........................1 15 percent to 42 percent. Meanwhile, ammonia prices paid by farmers increased from $227 per ton in 2000 to $521 per ton in 2006, an increase of 130 percent. Natural gas is Background ........................3 the main input used to produce ammonia. Additional increases in U.S. natural gas prices could lead to a further decline in domestic ammonia production and an even greater rise Impact of Natural Gas Prices on Ammonia in ammonia imports. Prices ................................5 Keywords: Natural gas and ammonia prices, ammonia supply, nitrogen fertilizers Effects of Natural Gas Prices on Ammonia Producers .........................6 Acknowledgments Effects of Rising Natural Gas Prices on Farmers .....................10 The author thanks the Fertilizer Institute, the International Center for Soil Fertility and Future Sources of Agricultural Development, and the National Gas Company of Trinidad and Tobago Ammonia Supply in Limited for providing data used in this study. The author also thanks the following indi- the United States ............12 viduals for their helpful suggestions: Stan Daberkow and Greg Pompelli of USDA’s Economic Research Service and James Duffield of USDA’s Office of Energy Policy Summary and Implications ......................15 and New Uses, and Harry Vroomen, the Fertilizer Institute. -
Single Membrane Reactor Configuration for Separation of Hydrogen, Carbon Dioxide and Hydrogen Sulfide
II.C SeparaTioNS II.C.1 Single Membrane Reactor Configuration for Separation of Hydrogen, Carbon Dioxide and Hydrogen Sulfide overall footprint than can be achieved by utilizing Shain J. Doong separate components for each required unit process/unit Gas Technology Institute (GTI) operation. Specifically, research is sought to perform a 1700 South Mount Prospect Road combination of theoretical and experimental research Des Plaines, IL 60018 to provide a scientific basis needed to develop a novel Phone: (847) 768-0884 “one-box” process to combine synthesis gas cleanup, E-mail: [email protected] water-gas shift reaction, hydrogen separation and carbon dioxide separation. A successful strategy will have the DOE Technology Development Manager: potential to selectively remove pure hydrogen, carbon Dan Cicero dioxide and synthesis gas impurities in a single reactor Phone: (412) 386-4826 configuration that can operate simultaneously at high E-mail: [email protected] temperature and high conversion, possibly without the DOE Project Officer: Elaine Everitt requirement of excess steam. Phone: (304) 285-4491 E-mail: [email protected] Approach Contract Number: DE-FC26-05NT42450 The objective of this research is to develop a Start Date: June 2005 “one-box” approach that can consolidate two or Projected End Date: May 2007 more downstream reaction/separation units of a coal gasification system in a single module for production of a pure stream of hydrogen. The project will evaluate the technical feasibility of using two or three types Objectives of membranes to selectively separate pure hydrogen, carbon dioxide and hydrogen sulfide in a single reactor • Develop a novel membrane process concept configuration that can operate simultaneously at high that would combine hydrogen sulfide removal, temperatures (e.g., 700-900ºC). -
Cool GTL for the Production of Jet Fuel from Biogas
DOE Bioenergy Technologies Office (BETO) 2021 Project Peer Review Cool GTL to Produce Jet Fuel from Biogas March 25, 2021 WBS: 3.5.1.405 Terry Marker Gas Technology Institute This presentation does not contain any proprietary, confidential, or otherwise restricted information 1 Cool GTL for the Production of Jet Fuel from Biogas Project Overview 2 Project Overview Cool GTL to Produce Jet Fuel from Biogas • Goal is to produce 100 gallons of Jet Fuel from Biogas using the Cool GTL Process – GTI will demonstrate a new simple GTL process which converts biogas, CO2, and methane directly to jet, gasoline, and diesel – Show the technology to be significantly lower cost, and more efficient than previous GTL processes- produce jet fuel at < $3/GGE – Also complete modeling, engineering, technoeconomic and LCA for Cool GTL biogas commercial process- advance from TRL 3 to 5 3 3 Cool GTL • Converts CO2-rich methane, ethane and propane to high-quality gasoline, diesel and jet fuel • Works well for any gas containing CO2 or CO • Uses unique CO2/steam reforming catalyst to directly make 2:1 H2/CO synthesis gas • Uses unique combined Fischer-Tropsch and wax-cracking reactor • Simple and compact with unique catalysts in each stage 4 SM Unique Cool GTL Technology Novel Features Beneficial Results • Unique bi-reforming catalyst • Modular, low-cost GTL • Unique wax cracking-FT catalyst • Small footprint • Unique electric reformer design • Great economics • Distributed plant locations Two patents issued Current GTL Cool GTLSM and several others pending 5 SM -
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. -
2020 Stainless Steels in Ammonia Production
STAINLESS STEELS IN AMMONIA PRODUCTION A DESIGNERS’ HANDBOOK SERIES NO 9013 Produced by Distributed by AMERICAN IRON NICKEL AND STEEL INSTITUTE INSTITUTE STAINLESS STEELS IN AMMONIA PRODUCTION A DESIGNERS’ HANDBOOK SERIES NO 9013 Originally, this handbook was published in 1978 by the Committee of Stainless Steel Producers, American Iron and Steel Institute. The Nickel Institute republished the handbook in 2020. Despite the age of this publication the information herein is considered to be generally valid. Material presented in the handbook has been prepared for the general information of the reader and should not be used or relied on for specific applications without first securing competent advice. The Nickel Institute, the American Iron and Steel Institute, their members, staff and consultants do not represent or warrant its suitability for any general or specific use and assume no liability or responsibility of any kind in connection with the information herein. Nickel Institute [email protected] www.nickelinstitute.org CONTENTS INTRODUCTION ............................ 4 PROCESS DESCRIPTION ............ 5 CORROSIVES IN AMMONIA PROCESSES ............... 5 CONSIDERATIONS FOR SELECTING STAINLESS STEELS .......................................... 6 Desulfurization of Natural Gas ....................... 6 Catalytic Steam Reforming of Natural Gas ....................... 6 Carbon Monoxide Shift .............. 8 Removal of Carbon Dioxide . 10 Methanation ............................. 11 Synthesis of Ammonia ............. 11 -
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 ......................................................................................................... -
Proposal for Development of Dry Coking/Coal
Development of Coking/Coal Gasification Concept to Use Indiana Coal for the Production of Metallurgical Coke, Liquid Transportation Fuels, Fertilizer, and Bulk Electric Power Phase II Final Report September 30, 2007 Submitted by Robert Kramer, Ph.D. Director, Energy Efficiency and Reliability Center Purdue University Calumet Table of Contents Page Executive Summary ………………………………………………..…………… 3 List of Figures …………………………………………………………………… 5 List of Tables ……………………………………………………………………. 6 Introduction ……………………………………………………………………… 7 Process Description ……………………………………………………………. 11 Importance to Indiana Coal Use ……………………………………………… 36 Relevance to Previous Studies ………………………………………………. 40 Policy, Scientific and Technical Barriers …………………………………….. 49 Conclusion ………………………………………………………………………. 50 Appendix ………………………………………………………………………… 52 2 Executive Summary Coke is a solid carbon fuel and carbon source produced from coal that is used to melt and reduce iron ore. Although coke is an absolutely essential part of iron making and foundry processes, currently there is a shortfall of 5.5 million tons of coke per year in the United States. The shortfall has resulted in increased imports and drastic increases in coke prices and market volatility. For example, coke delivered FOB to a Chinese port in January 2004 was priced at $60/ton, but rose to $420/ton in March 2004 and in September 2004 was $220/ton. This makes clear the likelihood that prices will remain high. This effort that is the subject of this report has considered the suitability of and potential processes for using Indiana coal for the production of coke in a mine mouth or local coking/gasification-liquefaction process. Such processes involve multiple value streams that reduce technical and economic risk. Initial results indicate that it is possible to use blended coal with up to 40% Indiana coal in a non recovery coke oven to produce pyrolysis gas that can be selectively extracted and used for various purposes including the production of electricity and liquid transportation fuels and possibly fertilizer and hydrogen. -
Wind to Hydrogen to Ammonia Pilot Project
Renewable Energy Storage and Utilization Using Hydrogen and Anhydrous Ammonia MN House Energy and Climate Committee August 27, 2020 Michael Reese, Director - Renewable Energy Dr. Prodromos Daoutidis, Professor UMN West Central Research and Outreach Center UMN Dept. of Chemical Engineering and Morris, MN Material Science Minneapolis, MN Renewable Ammonia for Energy Storage University of Minnesota is a global research leader in this field. NH3 UMM 1.65 MW 131 kW solar PV Wind Turbine and two 10 kW small wind turbines 1.65 MW Vestas V82 Wind Turbine H2 & NH3 Pilot Plant Existing Wind-to-Ammonia Pilot Plant at the UMN WCROC, Morris, MN G. Soloveichik, US Dept. of Energy, 2016 Slide 2 Benefits for using ammonia as regional-scale energy storage •Provides both distribution and transmission-scale energy storage, •Wide range of fuel uses (ICE genset, turbine, fuel cell, and thermal energy) •Seasonal storage capability, •Grid stabilization, •Readily dispatchable generation capacity (Peak load and peak fertilizer months are complementary. High N fertilizer demand is during utility shoulder seasons.), •Enables utilization of excess generation of wind, solar, and nuclear (low and negatively priced power within the Regional Transmission Organization / Independent System Operator), •Provides emergency backup outside of traditional energy sources •Flexibility between renewable and non-renewable generation (allows choice of carbon intensity of fuel between green and brown ammonia) •Significant levels of ammonia storage already in the Midwest (and usually