Industrial Implementation of Carbon Capture in Nordic Industry Sectors

Total Page:16

File Type:pdf, Size:1020Kb

Industrial Implementation of Carbon Capture in Nordic Industry Sectors IndustrialimplementationofCarbon CaptureinNordicindustrysectors KristinOnarheim,StefanìaÒ.Garðarsdòttir, AnetteMathisen,LarsO.Nord,DavidBerstad(eds.) NORDICCSTechnicalReportD4.2.1501/D18 November2015 Summary This report investigates the feasibility of separating CO2 from industrial gas streams for carbon capture and storage (CCS) in the Nordic countries. Detailed case studies were developed for iron and steel production, cement production, pulp and paper production, oil and gas refineries, and geothermal power production. Available technologies for separating CO2 have been reviewed and detailed process simulations on the technologies feasible for implementation for the specific cases have been performed. The work shows it is feasible to apply carbon capture technologies to a broad set of process conditions. However, it is crucial to consider the specific conditions of each case as they strongly affect the performance of the technologies and the choice of technology. Considering process and site specific conditions as well as possible developments of the industrial process simplifies the implementation and increases the efficiency of carbon capture considerably. The specific findings for each case study are summarized below. Iron and steel production The steel mill case study showed that replacing the conventional gas powered steam cycle in the power plant with a low-BTU gas turbine improves process performance. Adding a water-gas shift reactor and a CO2 capture process further increases the top gas fuel value. An additional 70 MW electric output can be achieved from this process configuration with a CO2 reduction of about 80% - 85%. Furthermore, the design allows for a staged deployment of the concept, which minimizes the investment risk and burden of implementation. Cement production The case study on cement production favored a retrofit of the existing process by implementing an amine-based CO2 capture plant. The capture unit can be added without any major updates of the cement plant. The most important installations required are the exhaust gas waste heat recovery unit, which will cover part of the steam needed to separate the CO2, and the installation of exhaust gas cleaning equipment for SOX, NOX, and dust before the capture unit. Oxy-fuel combustion is also a feasible option for the cement case. In general, few modifications of the cement plant are required to implement oxy-fuel technology. To avoid air in-leakages in the cement plant, which has a considerable influence on the energy consumption of the compression and CO2 purification unit, is one of the largest concerns for a retro fit of oxy-fuel combustion. Pulp and paper production The pulp production case considers possibilities with bio-energy with CCS (BECCS) as pulp mills mainly have biogenic CO2 emissions. This work investigated the possibilities of implementing carbon capture to pulp mills using a conventional recovery boiler or black liquor gasification (BLG) technology. The latter scenario using either the Selexol process together with a combined cycle for electricity production or the Rectisol process together with dimethyel ether (DME) biofuel production proved a high performance. The results show that the pulp and paper industry is suitable for BECCS. The combination of BLG technology and CO2 capture would require low additional utility, compared with the conventional post-combustion process. Oil and gas refineries The case study on a refinery highlights the complexity of the refinery process that gives a large variety in size and quality of the many CO2 sources. It is therefore of importance to investigate the sub-processes of the refinery individually. The most favorable CO2 sources is the steam-methane reformer for hydrogen production due to high CO2 content in the flue gas and being the largest point source of CO2. The refinery also includes CO2 sources that are not suitable for CO2 capture, mainly due to their relatively small size, which will have the consequence that the overall capture efficiency of the refinery will be below the 85-90% that is possible to achieve on an individual stream. Geothermal power production The case study on geothermal power in Iceland is a unique example of a CO2 source that is highly suitable for capture. The plant is already required to recover the high amounts of H2S in the gas and there are several technology options for removing the H2S and CO2 from the turbine off-gas. Absorption in water as well as in amines was investigated with promising results. Also cryogenic gas separation would be technically feasible. Furthermore the results show the possibility of achieving a pure hydrogen stream if an extra pressure swing adsorption (PSA) unit is added. Keywords CCS implementation, Nordic industry, CO2 emissions Editors Kristin Onarheim, VTT Technical Research Centre of Finland, Ltd., Finland [email protected] Stefanìa Òsk Garðarsdòttir, Chalmers University of Technology, Sweden [email protected] Anette Mathisen, Tel-Tek, Norway [email protected] Lars O. Nord, NTNU, Norway [email protected] David Berstad, Sintef Energy Research, Norway [email protected] Authors Kristin Onarheim (VTT Technical Research Centre of Finland, Ltd., Finland), Stefanìa Òsk Garðarsdòttir (Chalmers University of Technology, Sweden), Anette Mathisen (Tel- Tek, Norway), Lars O. Nord (NTNU, Norway), David Berstad (Sintef Energy Research, Norway), Fredrik Normann (Chalmers University of Technology, Sweden), Klas Andersson (Chalmers University of Technology, Sweden), Filip Johnsson (Chalmers University of Technology, Sweden), Joakim Hedström (Chalmers University of Technology, Sweden), Antti Arasto (VTT Technical Research Center of Finland, Ltd., Finland), Maria M. Skinnemoen (NTNU, Norway) Date November 2015 About NORDICCS Nordic CCS Competence Centre, NORDICCS, is a networking platform for increased CCS deployment in the Nordic countries. NORDICCS has 10 research partners and six industry partners, is led by SINTEF Energy Research, and is supported by Nordic Innovation through the Top-level Research Initiative. The views presented in this report solely represent those of the authors and do not necessarily reflect those of other members in the NORDICCS consortia, NORDEN, The Top Level Research Initiative or Nordic Innovation. For more information regarding NORDICCS and available reports, please visit http://www.sintef.no/NORDICCS. Contents SUMMARY......................................................................................................................................2 INTRODUCTION...........................................................................................................................8 Nordic industrial CO2 emissions........................................................................................................................ 8 Aim of research .............................................................................................................................................. 10 METHODOLOGY.........................................................................................................................11 CO2 capture technology .................................................................................................................................. 11 Energy supply and integration of CO2 capture ................................................................................................ 15 CARBONCAPTUREINIRONANDSTEELPRODUCTION...................................................16 Process overview ........................................................................................................................................... 16 CO2 capture in iron and steel production........................................................................................................ 17 Case study – Modified blast furnace and power production processes .......................................................... 18 Conclusions .................................................................................................................................................... 25 References ..................................................................................................................................................... 27 CARBONCAPTUREINCEMENTPRODUCTION...................................................................29 Process overview ........................................................................................................................................... 29 CO2 capture in cement production ................................................................................................................. 29 Case study A – Retrofit application of carbon capture .................................................................................... 30 Case study B – Oxy-combustion ..................................................................................................................... 33 Conclusions .................................................................................................................................................... 35 References ..................................................................................................................................................... 37 CARBONCAPTUREINPULPANDPAPERPRODUCTION..................................................38 Process overview ..........................................................................................................................................
Recommended publications
  • Process Simulation of a Dual-Stage Selexol Unit for Pre-Combustion Carbon Capture at an IGCC Power Plant', Energy Procedia, Vol
    Edinburgh Research Explorer Process simulation of a dual-stage Selexol unit for pre- combustion carbon capture at an IGCC power plant Citation for published version: Ahn, H, Kapetaki, Z, Brandani, P & Brandani, S 2014, 'Process simulation of a dual-stage Selexol unit for pre-combustion carbon capture at an IGCC power plant', Energy Procedia, vol. 63, pp. 1751–1755. https://doi.org/10.1016/j.egypro.2014.11.182 Digital Object Identifier (DOI): 10.1016/j.egypro.2014.11.182 Link: Link to publication record in Edinburgh Research Explorer Document Version: Peer reviewed version Published In: Energy Procedia General rights Copyright for the publications made accessible via the Edinburgh Research Explorer is retained by the author(s) and / or other copyright owners and it is a condition of accessing these publications that users recognise and abide by the legal requirements associated with these rights. Take down policy The University of Edinburgh has made every reasonable effort to ensure that Edinburgh Research Explorer content complies with UK legislation. If you believe that the public display of this file breaches copyright please contact [email protected] providing details, and we will remove access to the work immediately and investigate your claim. Download date: 28. Sep. 2021 Available online at www.sciencedirect.com ScienceDirect Energy Procedia 63 ( 2014 ) 1751 – 1755 GHGT-12 Process simulation of a dual-stage Selexol unit for pre-combustion carbon capture at an IGCC power plant Hyungwoong Ahn*, Zoe Kapetaki, Pietro Brandani, Stefano Brandani Scottish Carbon Capture and Storage Centre, School of Engineering, The University of Edinburgh, Edinburgh, EH9 3JL, UK Abstract It is aimed to simulate a dual-stage Selexol process for removing CO2 as well as H2S from the syngas typically found in the IGCC power plant with a dry-coal fed gasifier.
    [Show full text]
  • Hydrogen Sulfide Capture: from Absorption in Polar Liquids to Oxide
    Review pubs.acs.org/CR Hydrogen Sulfide Capture: From Absorption in Polar Liquids to Oxide, Zeolite, and Metal−Organic Framework Adsorbents and Membranes Mansi S. Shah,† Michael Tsapatsis,† and J. Ilja Siepmann*,†,‡ † Department of Chemical Engineering and Materials Science, University of Minnesota, 421 Washington Avenue SE, Minneapolis, Minnesota 55455-0132, United States ‡ Department of Chemistry and Chemical Theory Center, University of Minnesota, 207 Pleasant Street SE, Minneapolis, Minnesota 55455-0431, United States ABSTRACT: Hydrogen sulfide removal is a long-standing economic and environ- mental challenge faced by the oil and gas industries. H2S separation processes using reactive and non-reactive absorption and adsorption, membranes, and cryogenic distillation are reviewed. A detailed discussion is presented on new developments in adsorbents, such as ionic liquids, metal oxides, metals, metal−organic frameworks, zeolites, carbon-based materials, and composite materials; and membrane technologies for H2S removal. This Review attempts to exhaustively compile the existing literature on sour gas sweetening and to identify promising areas for future developments in the field. CONTENTS 4.1. Polymeric Membranes 9785 4.2. Membranes for Gas−Liquid Contact 9786 1. Introduction 9755 4.3. Ceramic Membranes 9789 2. Absorption 9758 4.4. Carbon-Based Membranes 9789 2.1. Alkanolamines 9758 4.5. Composite Membranes 9790 2.2. Methanol 9758 N 5. Cryogenic Distillation 9790 2.3. -Methyl-2-pyrrolidone 9758 6. Outlook and Perspectives 9791 2.4. Poly(ethylene glycol) Dimethyl Ether 9759 Author Information 9792 2.5. Sulfolane and Diisopropanolamine 9759 Corresponding Author 9792 2.6. Ionic Liquids 9759 ORCID 9792 3. Adsorption 9762 Notes 9792 3.1.
    [Show full text]
  • Selexol Process
    PROSIMPLUS APPLICATION EXAMPLE NATURAL GAS DEACIDIFICATION WITH SELEXOL PROCESS EXAMPLE PURPOSE This example illustrates a natural gas deacidification with the Selexol process. Selexol, mixture of polyethylene glycol dimethyl ether, is used as the solvent. The deacidification is done through a contactor and the solvent regeneration needs three successive flashes. The process objective is to highly decrease the CO2 composition of the input gas. Selexol make-up is automatically calculated with simple modules. This example is taken from [RAN76] publication which describes main features of this process. ACCESS Free Internet Restricted to ProSim clients Restricted Confidential CORRESPONDING PROSIMPLUS FILES PSPS_EX_EN-Selexol-Process.pmp3 Reader is reminded that this use case is only an example and should not be used for other purposes. Although this example is based on actual case it may not be considered as typical nor are the data used always the most accurate available. ProSim shall have no responsibility or liability for damages arising out of or related to the use of the results of calculations based on this example. Copyright © 2015 ProSim, Labège, France - All rights reserved www.prosim.net Natural Gas Deacidification with Selexol Process Version: February 2015 Page: 2 / 16 TABLE OF CONTENTS 1. PROCESS MODELING ..................................................................................................... 3 1.1. Process description ............................................................................................................................
    [Show full text]
  • Wear Conduct Investigation of 410 by Cryogenic Process Ch
    SSRG International Journal of Mechanical Engineering (SSRG - IJME) – Volume 4 Issue 11 November 2017 Wear Conduct Investigation of 410 by Cryogenic Process Ch. Vijay Krishna1, Ram Subbaiah2 1PG Student, Department of Mechanical Engineering, GRIET, Hyderabad, India 2Associate Professor, Department of Mechanical Engineering, GRIET, Hyderabad, India Abstract Martensitic stainless steels discover wide zero treatment apart from improved surface applications due to their ideal blend of quality, finish, reduced coefficient of friction at the interface hardness and wear resistance in cryogenic condition. between work piece and tool. AISI 410 martensitic stainless steel, subjected to Cryogenic hardening is a cryogenic treatment cryogenic hardening was considered using pin on disc process where the material is cooled to very low tests took after by metallurgical examinations using temperatures. By utilizing liquid nitrogen, the scanning electron microscopy and energy dispersive temperature can go as low as -190ºC. It can have a spectroscopy. The microstructure includes martensite profound effect on the mechanical properties of with randomly scattered carbides in the matrix. In this certain materials like expelling residual stresses and paper, it is used to enhance the wear conduct improving wear resistance on steels. In addition to investigation of martensitic stainless steel 410 by seeking enhanced stress relief and stabilization, or cryogenic hardening process. wear resistance, cryogenic treatment is also sought for its ability to improve corrosion resistance by Keywords – AISI 410 martensitic stainless steel, precipitating micro fine carbides. Cryogenic hardening, Microstructure, Pin on disc test, Wear resistance Mechanical achievement in refrigeration cycles cross prepared the advancement of cryogenic I. INTRODUCTION treatment systems that were able to carry out effective Stainless steels are present day materials.
    [Show full text]
  • Experimental Wear Behaviour of Cryogenically Treated Aluminium 6063 and 8011 Materials
    © Applied Science Innovations Pvt. Ltd., India Carbon – Sci. Tech. 8/4(2016)28-34 ASI Carbon – Science and Technology ISSN 0974 – 0546 http://www.applied-science-innovations.com RESEARCH ARTICLE Received:10/07/2016, Accepted:24/09/2016 ------------------------------------------------------------------------------------------------------------------------------ Experimental wear behaviour of cryogenically treated aluminium 6063 and 8011 materials K. K. Padmanabhan (1) and R. Bharathbalaji (2) Department of Automobile Engineering, Karpagam University, Coimbatore, Tamilnadu, India. Email: (1) [email protected] , (2) [email protected] Abstract: The aim of this paper is to focus on the effect of cryogenic treatment on the microstructure, mechanical and wear properties of Al 6061 and Al 8011. The first objective was to understand the degree to which wear behaviour has shown improvement with aluminium grades being treated cryogenically on the specimens. To conduct wear test Aluminium experimental investigation has been carried out on aluminium alloys with cryogenic coolants. The cryogenic coolant has increased the wear resistance properties of aluminium upto 25% when compared to wear of non-cryogenically treated aluminium. The cryogenic treatment was carried out under three different timings for three different rpm’s under varying loads. The paper also studies the micro structural changes under these varying conditions. The experimental investigation of the paper concludes that cryogenically treated aluminium shows increase in wear resistance of nearly 25%. Keywords: Cryogenic, Wear, Microstructure. ------------------------------------------------------------------------------------------------------------------------------------------------ 1 Introduction: The word, “Cryogenics” is taken from two Greek words–“kryos” which means ‘frost’ or freezing, and “genic” meaning to ‘produce’ or generated. Technologically, it means the study and use of materials (or other requirements) at very low temperatures.
    [Show full text]
  • Tribology in Industry Effect of Cryogenic Treatment on the Wear
    Vol. 41, No. 1 (2019) 33-42, DOI: 10.24874/ti.2019.41.01.04 Tribology in Industry www.tribology.rs RESEARCH Effect of Cryogenic Treatment on the Wear Behavior of Additive Manufactured 316L Stainless Steel a a M. Sugavaneswaran , A. Kulkarni a School of Mechanical Engineering, Vellore Institute of Technology, Vellore, Tamil Nadu, 632 014, India. Keywords: A B S T R A C T Additive Manufacturing In this research work, an investigation is done to study the effect of Cryogenic Treatment cryogenic treatment on 316L SS fabricated using Direct Metal Laser Direct Metal Laser Sintering Sintering process. Cryogenic treatment is done at -196°C for 24 hours in Microstructure a chamber filled with liquid nitrogen. The post effects of this cryogenic Wear treatment over the properties of the material such as hardness, wear 316L Stainless Steel behaviour and microstructure have been studied. The result showed that the porosity present in additive manufactured 316L SS is greatly reduced Corresponding author: after cryogenic treatment. Tribological properties were analyzed, using M. Sugavaneswaran zirconia pin-on- additive manufactured 316L SS disc, the result showed School of Mechanical Engineering, that the treatment has considerable effect on decreasing coefficient of Vellore Institute of Technology, friction. Wear track surface morphologies shows the evidence for the Vellore 632 014, Tamil Nadu, India. indentation of the abrasives in pores in the untreated AM sample. E-mail: [email protected] Hardness increases significantly due to strain-induced phase change in the sample after cryogenic treatment. © 2019 Published by Faculty of Engineering 1. INTRODUCTION any external fixtures and cutting tools [4].
    [Show full text]
  • Hydrogen Pathways: Updated Cost, Well-To-Wheels Energy Use
    Hydrogen Pathways Updated Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of Ten Hydrogen Production, Delivery, and Distribution Scenarios T. Ramsden, M. Ruth, V. Diakov National Renewable Energy Laboratory M. Laffen, T.A. Timbario Alliance Technical Services, Inc. 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 This report is available at no cost from the National Renewable Energy Laboratory (NREL) at www.nrel.gov/publications. Technical Report NREL/TP-6A10-60528 March 2013 Contract No. DE-AC36-08GO28308 Hydrogen Pathways Updated Cost, Well-to-Wheels Energy Use, and Emissions for the Current Technology Status of 10 Hydrogen Production, Delivery, and Distribution Scenarios T. Ramsden, M. Ruth, V. Diakov National Renewable Energy Laboratory M. Laffen, T.A. Timbario Alliance Technical Services, Inc. Prepared under Task No. HS07.1002 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 This report is available at no cost from the National Renewable Energy Laboratory (NREL) at www.nrel.gov/publications. National Renewable Energy Laboratory Technical Report 15013 Denver West Parkway NREL/TP-6A10-60528 Golden, CO 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.
    [Show full text]
  • Cost and Performance of Some Carbon Capture Technology Options for Producing Different Quality CO2 Product Streams
    Cost and performance of some carbon capture technology options for producing different quality CO2 product streams Richard T.J. Portera,†,*, Michael Fairweatherb, Clea Kolsterc,d, Niall Mac Dowellc,d, Nilay Shahd and Robert M. Woolleyb aEnergy Research Institute, School of Chemical and Process Engineering, University of Leeds, Leeds LS2 9JT, UK. bInstitute of Particle Science and Engineering, School of Chemical and Process Engineering, University of Leeds, Leeds LS2 9JT, UK. cCentre for Environmental Policy, Imperial College London, London SW7 1NA, UK. dCentre for Process Systems Engineering, Department of Chemical Engineering, Imperial College London, London SW7 2AZ, UK. †Current address: Department of Chemical Engineering, University College London, Torrington Place, London WC1E 7JE, UK. * Corresponding author: Tel: +44(0)207 679 3809 Email address: [email protected] (Richard T.J. Porter). Submission of a full-length article to the International Journal of Greenhouse Gas Control, of unpublished material not submitted for publication elsewhere 1 ABSTRACT A techno-economic assessment of power plants with CO2 capture technologies with a focus on process scenarios that deliver different grades of CO2 product purity is presented. The three leading CO2 capture technologies are considered, namely; oxyfuel combustion, pre-combustion and post-combustion capture. The study uses a combination of process simulation of flue gas cleaning processes, modelling with a power plant cost and performance calculator and literature values of key performance criteria in order to evaluate the performance, cost and CO2 product purity of the considered CO2 capture options. For oxyfuel combustion capture plants, three raw CO2 flue gas processing strategies of compression and dehydration only, double flash system purification and distillation purification are considered.
    [Show full text]
  • 2–4 March 2020
    2–4 MARCH 2020 Wyndham Lake Buena Vista Orlando, Fla., USA FOCUS Development and application of alternative ironmaking processes to provide virgin iron units to the electric arc furnace (EAF) sector, hot metal to steelmaking vessels, or to process waste oxides in both blast furnace-based and EAF steel plants. ABOUT THE PROGRAM This is the eighth in a series of symposia covering scrap substitutes and alternative ironmaking, which originated with a highly successful meeting in Myrtle Beach, S.C., USA, in 1993. This meeting was initiated by the Advanced Technology Committee, which belonged to the Process Technology Division of the Iron & Steel Society (an AIST predecessor). This symposium, which is international in scope and participation, is associated with a high level of activity in research, process and project development, plant construction, and start-up of direct reduction and alternative ironmaking processes. This symposium will focus on the following areas: successful projects/processes, the challenges of struggling processes and those still under development including new approaches, and use of products. WHO SHOULD ATTEND Those engaged in the production, sale, and use of direct reduced iron, pig iron and scrap; managers and engineers from electric furnace and blast furnace–based steel companies; suppliers of iron ore, coal and natural gas; and steel company, engineering company, academic and research institute personnel engaged in ironmaking process development. REGISTRATION Registration includes a welcome reception on Monday evening, breakfast and lunch Tuesday and Wednesday, a reception on Tuesday evening, and a seminar workbook or flash drive. AIST MEMBERS NON-MEMBERS US$845 US$945 US$1,090 US$1,190 by 20 January 2020 after 20 January 2020 by 20 January 2020 after 20 January 2020 HOTEL ACCOMMODATIONS A block of rooms has been reserved at the Wyndham Lake Buena Vista Disney Springs Resort Area.
    [Show full text]
  • Decarbonisation Options for the Dutch Steel Industry
    DECARBONISATION OPTIONS FOR THE DUTCH STEEL INDUSTRY A. Keys, M. van Hout, B. Daniëls 21 November 2019 Updated version: 16 September 2021 Manufacturing Industry Decarbonisation Data Exchange Network Decarbonisation options for the Dutch steel industry © PBL Netherlands Environmental Assessment Agency; © ECN part of TNO The Hague, 2019 PBL publication number: 3723 TNO project no. 060.33956 / TNO publication number: TNO 2019 P11483 Authors Keys, A., van Hout, M., Daniëls, B. MIDDEN project coordination and responsibility The MIDDEN project (Manufacturing Industry Decarbonisation Data Exchange Network) was initiated and is also coordinated and funded by PBL and ECN part of TNO. The project aims to support industry, policymakers, analysts, and the energy sector in their common efforts to achieve deep decarbonisation. Correspondence regarding the project may be addressed to: Dick van Dam (PBL) [email protected] and Silvana Gamboa Palacios (TNO) [email protected] Production coordination This publication is a joint publication by PBL and ECN part of TNO and can be downloaded from: www.pbl.nl/en. Parts of this publication may be reproduced, providing the source is stated, in the form: Keys. A, van Hout. M, Daniëls. B (2019), Decarbonisation options for the Dutch Steel Industry. PBL Netherlands Environmental Assessment Agency & ECN part of TNO, The Hague. PBL Netherlands Environmental Assessment Agency is the national institute for strategic policy analysis in the fields of the environment, nature and spatial planning. We contribute to improving the quality of political and administrative decision-making by conducting outlook studies, analyses and evaluations in which an integrated approach is considered paramount. Policy relevance is the prime concern in all of our studies.
    [Show full text]
  • Cryogenic Hardening of EN 19 Alloy Steel
    International Journal of Innovative Technology and Exploring Engineering (IJITEE) ISSN: 2278-3075, Volume-8 Issue-10, August 2019 Cryogenic Hardening of EN 19 Alloy Steel Karthik Pandiyan .G, Prabaharan. T Abstract — This paper includes the study of heat treatment process that we carried out on En 19 steel in cryogenic atmosphere. Cryogenic treatments of alloy steels have been significantly increase wear resistance and toughness. These investigations of warmth treatment cryogenic medicines of amalgam steels have been asserted to altogether expand wear protection and sturdiness. Cryogenic handling is a supplementary procedure to customary warmth treatment process in steels. The cryogenic treatment on apparatus materials builds the life of instruments, gear, parts and materials by boosting elasticity, sturdiness and strength. This cryogenic hardening process is an onetime treatment influencing the whole part — not only the surface. Cryogenic treatment has been broadly embraced as a cost decrease and execution upgrading innovation. Cryogenic treatment is likewise utilized as an empowering innovation, when its pressure alleviating benefits are used to allow the manufacture (or machining) of basic resistance parts. With Figure 1 schematic diagram of Absolute zero temp., regards to great outcomes about the use of profound cryogenic treatment (DCT) on materials, the impact on the microstructure This legitimate separating line, since the ordinary breaking and properties (hardness, strength and the substance of held austenite) are observed to be made strides. Cryogenic treatment points of the alleged lasting gases, (for example, helium, has been distinguished to improve the properties of Tools steels. hydrogen, neon, nitrogen, oxygen, and air) lie underneath It is discovered that cryogenic treatment confers almost 110% −180 °C while the Freon refrigerants, hydrogen sulfide, and change in apparatus life.
    [Show full text]
  • CO2 Management at Exxonmobil’S Labarge Field, Wyoming
    Available online at www.sciencedirect.com Energy Energy Procedia 4 (2011) 5455–5470 Procedia Energy Procedia 00 (2010) 000–000 www.elsevier.com/locate/procedia www.elsevier.com/locate/XXX GHGT-10 CO2 Management at ExxonMobil’s LaBarge Field, Wyoming, USA Michael E. Parker, P.E., ExxonMobil Production Company, Scott Northrop, ExxonMobil Upstream Research Company, Jaime A. Valencia, ExxonMobil Upstream Research Company, Robert E. Foglesong, ExxonMobil Production Company, William T. Duncan, ExxonMobil Production Company Elsevier use only: Received date here; revised date here; accepted date here Abstract Production of natural gas from the LaBarge field in southwest Wyoming began in 1986. This gas contains high concentrations of carbon dioxide (CO2), and from the very beginning, ExxonMobil has successfully implemented several technologies and approaches to effectively manage the substantial volumes of CO2 associated with its production. Many of the technologies and approaches used for managing CO2 at LaBarge are examples of technologies and approaches being proposed for use in carbon capture and storage (CCS) by other industries. The Shute Creek Treating Facility (SCTF) processes the gas produced from the LaBarge field. The SCTF handles the lowest hydrocarbon content natural gas commercially produced in the world. The gas composition entering Shute Creek is 65% CO2, 21% methane, 7% nitrogen, 5% hydrogen sulfide (H2S) and 0.6% helium. The SCTF separates CO2, methane, and helium for sale and removes hydrogen sulfide for disposal. Most of the CO2 captured at Shute Creek is used for enhanced oil recovery (EOR). EOR is consistently cited as one of the most viable early opportunities for large scale implementation of CCS.
    [Show full text]