A NOVEL DESIGN FOR MTPA LNG TRAINS
|
|
- Evan Wright
- 6 years ago
- Views:
Transcription
1 A NOVEL DESIGN FOR MTPA TRAINS Sander Kaart Wiveka Elion Barend Pek Rob Klein Nagelvoort Shell Global Solutions International B.V. P.O. Box 541, 2501 CM The Hague, The Netherlands ABSTRACT Shell believes, along with many others, that the projected growth in markets will translate into a demand for larger train sizes. This is primarily driven by economies of scale in terms of equipment costs, construction costs and project management. In this paper, we present a new design for a large train producing at a rate of about 11 Mtpa. The design is based on Shell s Parallel Mixed Refrigerant process, includes CO2 and sulphur treating, and will be flexible to reach heating values down to typical US specifications. Using large yet fully developed and proven gas turbines, and other key equipment, maximizes economies of scale. Care has been taken to retain multiple sourcing options for all equipment. Steam is used to integrate heat generation and demand plant-wide; this includes the waste heat recovery from the gas-turbine drivers, co-firing, and heat demand of the energy intensive treating train and heat production by the sulphur-recovery unit. The heat recovered is utilized for process heating and to produce mechanical and electrical power. The full utilization of waste heat from the gas-turbine exhausts enables a step-change in plant efficiency and reduces the specific CO 2 emissions considerably, compared to conventional plant design. In this paper, conceptual design choices are presented, followed by a description of the waste heat recovery system, key equipment considerations and a summarizing discussion. Shell Global Solutions is a network of independent technology companies in the Shell Group. In this material the expression 'Shell Global Solutions' is sometimes used for convenience where reference is made to these companies in general, or where no useful purpose is served by identifying a particular company. The information contained in this material is intended to be general in nature and must not be relied on as specific advice in connection with any decisions you may make. Shell Global Solutions is not liable for any action you may take as a result of you relying on such material or for any loss or damage suffered by you as a result of you taking this action. PS2-3.1
2 INTRODUCTION The fast growing world demand for clean and affordable energy translates into a large increase in production capacity in the next decade. At Shell, we see demand for natural gas growing by some 3% a year over the next 15 years, with demand for liquefied natural gas growing by some 8-10% a year [1]. The large number of projects underway has resulted in a constrained contractor market, a worldwide heavy demand for raw materials as well as issues around logistics of work force and products. These challenges call for large trains, particularly where large resources are involved as in the Middle East, Russia, Nigeria and Australia. Shell and others have already increased train sizes in recent decades from 1 Mtpa to 8 Mtpa, primarily driven by the desire to reduce capital expenditure. Application of large trains will also help to use the available contractor capability more effectively. Minimizing the effect of the CO2 emission rates from this increased liquefaction activity will require focus on efficiency of processes and drivers. In addition, novel approaches like CO2 sequestration are being considered. This paper presents a train design for the production of 11 Mtpa. The design is based on Shell s Parallel Mixed Refrigerant Process (PMR) with propane refrigerant in the pre-cool cycle (C3/PMR). A typical Middle East sour gas (Table 1) has been assumed for the concept development. A plant-wide integration of heat generation and demand is provided by steam. The full utilization of waste heat from the gas turbine exhausts enables a step-change in plant efficiency with respect to conventional plant designs and reduces the specific CO 2 emissions considerably. Table 1. Feed gas composition Component Composition [mol%] Methane 84 Ethane 5 Propane 2 Butanes 1 Higher Hydrocarbons 1 Nitrogen 4 Carbon dioxide 2 Hydrogen Sulphide 1 Mercaptans 500 ppm Beyond the design presented in this paper, there will be developments for which a smaller train capacity is more suitable; in particular, where gas reserves are limited, when there is a capital constraint, or when market opportunities are uncertain. The concept described in this paper is fully scalable from 11 to 6 MTPA by changing helper motor size or changing to smaller gas turbines. We are continuously improving our portfolio of processes (Figure 1) including small trains and offshore liquefaction plants [5-8]. The improvement of fuel efficiency by waste heat recovery is applicable to several designs, thus minimizing CO2 emissions. PS2-3.2
3 E- drive 4 x 4 E-drive x E - Drives PMR DMR - 3 x Electrical Drives PMR 3 x identical mechanical drivers DMR 2 x GE F7 or equiv. C3/MR 2 x GE F7 or equiv. Workhorses Capacity [Mtpa] CONCEPTUAL DESIGN CHOICES Figure 1. The Shell portfolio For the liquefaction, Shell s proprietary Parallel Mixed Refrigerant Process [11] has been selected, consisting of a 4 stage propane pre-cooling (C3/PMR), two parallel mixed refrigerant circuits followed by a common nitrogen rejection unit combined with an endflash system (Figure 2). This process conceptually provides higher efficiency than alternative 3 cycle processes, which translates into a higher production for fixed capital costs. Feed From Well CO2 Sulphur Gas Landing Treating & Dehydration Sulphur Recovery Condensate Stabilization GT Fuel Gas Field Condensate NGL Extraction Pre-cool cycle MR cycle End Flash storage ST MR cycle GT Frac. LPG Treating LPG Refrig Plant Condensate Figure 2. Process Block scheme The design presented in this paper is based on air-cooling, as this is well proven even in tropical climates and independent of the marine environment. Dedicated attention to hot air re-circulation and plot plan optimization will provide a robust design. Should cooling LPG PS2-3.3
4 water be available for a once through or re-circulating cooling system, this can be easily incorporated and will further improve fuel efficiency and, depending on cooling water supply complexity, also the specific cost. The design is suited to handle the CO2, H2S and mercaptans present in the feed gas, and it contains front-end LPG extraction, allowing a flexible HHV value down to the Btu/scf often required for US markets. The front-end NGL extraction unit also allows maximum refrigeration power and optimum liquefaction pressure. In an optimization like this, it is important to consider the full interaction of process units, from slug-catcher up to loading facilities. To meet the challenge of a CO2 constrained world as well as rising fuel value, the design was fitted with full waste heat recovery. All turbines, both in power generation and in liquefaction, are fitted with steam generating heat recovery systems (HRSG). The system is then optimized with respect to the use of this steam as process heat as well as for mechanical power and electricity generation. TREATMENT FACILITIES An integrated and optimized solution has been selected to remove acid gas components and mercaptans from the feed gas (Figure 3). Details regarding the optimization process have been described elsewhere [2-4]. Not surprisingly, total CAPEX for the removal of the contaminants is minimized if the acid gas removal unit (AGRU) and the molsieve unit (MSU) for dehydration and mercaptan removal are optimized as a single unit. It appears that Sulfinol-D is a very good solvent for this particular feed gas composition. MSU Treated Gas AGRU Absorber mixed MSU Regen Absorber mixed AGRU Regen. mixed Feed Gas AGEU Regen. aqueous AGEU Absorber aqueous Sulphur SRU Incinerator TGT aqueous Flue Gas Figure 3. Treating scheme The regeneration of the acid gas solvents from the AGRU and acid gas enrichment unit (AGEU) consumes low-pressure steam. The sulphur recovery unit (SRU) produces PS2-3.4
5 medium-pressure steam. Unconverted hydrogen sulphide is removed from the SRU tail gas in the tail gas absorber (TGT). After treating and mercury removal, the dry sweet natural gas is sent to a dedicated NGL extraction unit. NGL EXTRACTION FACILITIES The NGL extraction unit is based on the proprietary Shell Deep LPG extraction process (SHDL). The SHDL process (Figure 4) is a robust and flexible extraction scheme that yields high LPG recoveries for a large variety in feed gas compositions. For this study the SHDL process allows LPG recoveries up to 99% without requiring external refrigeration for the considered feed gas. With these high recoveries, HHV specifications of less than 1070 Btu/scf can easily be met. Booster Compressor Lean Natural Gas Rich Natural Gas External Refrigeration Figure 4. Shell Deep LPG extraction process Light Condensate High pressure treated and dried rich natural gas is first pre-cooled and partially condensed in a series of heat exchangers against lower pressure cold lean natural gas. The heat exchange with external refrigeration is optional in the scheme and is not required for the feed gas conditions discussed in this paper. After separation of the liquid from the partially condensed natural gas stream, the high-pressure vapor is expanded through an expander; this drives the re-compressor of the lean low-pressure natural gas stream. This expansion produces the required refrigeration to obtain the reflux for the de-ethanizer column and pre-cool the rich natural gas stream. The lean natural gas first pre-cools the rich natural gas and is then compressed by the expander driven re-compressor. A separate booster compressor further raises the lean natural gas pressure to the maximum allowed by the 600 lbs piping class. This integration of the NGL and liquefaction units maximizes LPG and production within equipment and power constraints. PS2-3.5
6 LIQUEFACTION Shell developed the Parallel Mixed Refrigerant (PMR) Process [11] to meet the challenge of the industry for larger train sizes. The interim temperature between pre-cooling and liquefaction is an important design parameter. Correct selection of this temperature balances the utilized power between the pre-cooling and the liquefaction cycles to the thermodynamically favored 1:2 ratio for the C3/PMR process. The ability to tune the power balance exactly to the installed mechanical refrigeration capacity in the C3/PMR process is an advantage over the conventional C3/MR process, where power requirement of the cooling cycles cannot be balanced with two equal sized gas turbines. Application of Shell s end flash system with nitrogen rejection [12] and a scheme to recover cold from the end-flash gas using lean natural gas have been integrated in the design. Figure 5 shows a schematic representation of the combined nitrogen rejection and end-flash system. Prior to expanding the high-pressure liquid natural gas over the expanders, it is first further sub-cooled against a liquid fraction of the expanded. The vapor thus produced, is used to strip low boiling point components (i.e. Nitrogen) from the. End Flash Gas Liquefied NG Figure 5. N2 stripper line-up [12] The parallel line-up of the liquefaction cycles improves the on-stream reliability of the train since the production can be designed to continue at 60% of the train capacity when one of the liquefaction cycles trips. Moreover, it allows high production capacity with only two refrigeration cycles in series, compared with the alternative of three cycles in series. This limits pressure drops and the number of cascades between cycles, and thereby again improving efficiency of the PMR process compared with other 3-cycle processes. With a single pre-cooling cycle and two parallel mixed refrigerant cycles, the capacity of the PMR process can be boosted up to 8.5 Mtpa in a tropical climate, when using 3 GE- Fr7 compressor drivers. The process can either use propane or mixed refrigerant in the pre-cool cycle. The well-proven refrigerant cycles can be used and the design can be applied today, without step changes in technology. With larger drivers like GE Fr9 or PS2-3.6
7 Siemens V94.2 gas turbines, capacity can be further increased up to 11 Mtpa, still within normal pressure drop constraints and equipment sizes. FULL, INTEGRATED WASTE HEAT RECOVERY The required process heat will largely depend on the concentration of acid gas contaminants in the feed gas and typically steam at low pressure will be required to provide the heat required for the regeneration of the acid gas solvent. Depending on the exact amount of high-pressure steam generated from gas turbine exhaust and lowpressure steam required by the regeneration process, the high-pressure steam could be utilized in backpressure or condensing steam turbines to generate power, either electrical or mechanical. This choice results from a detailed optimization that also considers other factors such as plot layout, sparing philosophy and the overall number of trains included in the development Low quality heat Heat and Power from Fuel [%] Process Heat Power CST & BPST BPST More Fuel Combined Heat and Power Generation improves overall fuel efficiency Heat to Power Ratio [MWProcessHeat/MWpower] Figure 6. Heat and Power integration The required process heat relative to the power requirement, determines the maximum potential fuel efficiency of the total process. Figure 6 illustrates this for a simple example system, based on the waste heat recovery from a 33% efficient gas turbine. Part of the heat contained in the gas turbine exhaust can be recovered to generate high-pressure steam. The high-pressure steam can subsequently be converted into LP steam and power by expansion through a backpressure steam turbine (BPST). Alternatively, a condensing steam turbine (CST) can be used to produce power and low quality heat that is of no further use to the process. In this simplified example, up to a heat-to-power ratio of 1.2, expanding part of the high-pressure steam through a BPST and the rest through a CST can generate all the required process heat. The exact limit will depend on many factors, like selected pressure levels in the steam system and gas turbine exhaust gas temperature. PS2-3.7
8 At higher required heat to power ratios, the need for heating steam prevents the use of CST s to generate power and only part of the steam can be expanded in a BPST. Another transition point occurs when no further power can be recovered from the steam. In the example of figure 6, this occurs at a heat-to-power ratio of 1.7, a value largely dictated by the gas turbine efficiency and process heat temperature levels. If even more heat is required, additional fuel will be required to generate this. For the case studied in this paper, the required heat to power ratio is below 1 and hence the produced HP steam can generate a significant amount of additional driver power. The propane compressor driver can be replaced by a steam turbine (Figure 7). This option has a distinct availability advantage in comparison with a gas turbine drive. The PMR train can continue to run at about 60 % of capacity while one of the GT-driven MR circuits is out for maintenance or has tripped due to an unscheduled event. Combining this feature with the low maintenance requirements of a steam turbine provides a significant increase in availability for this option. In addition, the variable speed of the steam turbine extends the operating window for the propane compressor. PROCESS E-Power - Fuel M FR9 MR Compr M FR9 MR Compr PR Compr GT Power Generation HPS SRU Booster ST Power Generation MPS LPS AGRU / FRAC. Condensate Figure 7. Example: Plant wide integration of heat and power An alternative would be to keep the three process turbines intact, but use the steam to generate electricity and minimize the helper power generated by the gas turbines. Obviously the start-up needs to be taken into consideration. To handle start-ups, additional boilers or some GT power generation may need to be included. A second alternative is to power smaller drivers by steam, like the booster compressor, the end flash compressor or helper motors. This would require a quite extensive steam infrastructure. In Figure 8, the CO2 emission from fuel of the current air-cooled design is compared with the performance of some base project train designs as published in 2003 [9]. For reference, Figure 8 also includes the result of the conventional air-cooled C3/PMR design PS2-3.8
9 with limited waste heat recovery. Proper optimization of the fuel and the steam balance can achieve a reduction of some 30% in fuel consumption; this results in a very competitive specific fuel CO2 emission from fuel of 0.21 ton CO2 /ton, for the aircooled train in a tropical climate with sour feed gas. The waste heat recovery and steam generated power contributes to environmentally sustainable development, and where fuel has a high value or CO2 trading rates apply, may give good pay-back. The result for the conventional air-cooled PMR process is very similar to the values shown in Figure 8 for the water-cooled base projects in Qatar, operating at similar gas compositions. This clearly illustrates the high efficiency of the PMR process, taking into account that a water-cooled version of the PMR process would show a further efficiency increase of up to 8 percent. Emissions, ton CO2/ton Qatar gas Ras gas Atlantic Nigeria Oman -30% Large Conventional Train Design Figure 8. Specific CO2 emissions compared [9] KEY EQUIPMENT CONSIDERATIONS Economies of scale and reliability call for the use of state of the art gas turbines. When aiming for capacities of around 11 Mtpa, high power output gas turbines should be considered, like the GE Fr9 or Siemens V94.2. Compressors able to absorb the high shaft powers are available from several vendors. It is however essential to define the exact design parameters in discussion with vendors, rotating equipment specialists and process designers. The lower rotational speed (3000 rpm) of the Fr9 and V94.2 machines allows for higher volume flows than the 3600 rpm required in F7 based designs. In addition, we apply the proprietary SplitPropane process [10] that allows higher propane circulation within the volumetric flow constraints of the compressor wheels. PS2-3.9
10 M GT LP MP HP HHP Figure 9. SplitPropane line-up As the PMR process utilizes two parallel mixed refrigerant circuits, pressure drop or cryogenic exchanger limitations are not experienced. The required spiral wound heat exchangers are well within existing manufacturing capabilities. In depth process development work shows that with high but realistic constraints for compressor suction flows and MCHE area, capacities of 11 Mtpa can be realized. The remaining equipment is also proven. CONCLUSION In this paper we have introduced a novel design for a very large train with the following characteristics: Capacity of 11 Mtpa Economies of scale both with respect to capital as well as operational costs Proven equipment High availability, provided by the steam driven propane compressor Fuel consumption some 30 % lower than open cycle based designs The key to achieving this is the ability to assess and utilize the full capabilities of, in particular, rotating and heat exchange equipment. Secondly, a full understanding of the complete process, including treating and LPG extraction, is required to provide optimal heat recovery. The start-up and operation of this large plant is comparable to conventional designs. The designs of the waste heat recovery and electrical system need to be robust against start-up and trip scenarios. While absolute costs are difficult to predict in today s overheated contractor market, we are utilizing full economies of scale for all equipment items. At the same time, care has been taken not to rely on a single vendor for any of the equipment. The high efficiency of the PMR design makes optimal use of expensive turbine power to generate. This design for an 11 Mtpa train represents another major technology step that will meet the world s need for in the coming decades. PS2-3.10
11 REFERENCES CITED [1] Linda Cook, Forging strong Links enabling the global expansion of natural gas, SPE Technical Conference, Dallas 10 th October (2005) [2] J van de Graaf, J. Klinkenbijl, Optimized treating configurations for the combined removal of H2S, CO2 and mercaptans from Natural Gas for and GTL applications, GPA, San Antonio (2004). [3] J. Klinkenbijl, H.F. Grootjans, Best Practices for deep treating sour natural gasses (to and GTL), GasTech, Bilbao (2005). [4] E. Bras, G van der Zwet, J. Klinkenbijl, P. Clinton, Treating Difficult Feed gases to Plants, -15, Barcelona (2005). [5] J. van de Graaf, B. Pek, Large-Capacity Trains The Shell Parallel Mixed Refrigerant Process, Review (2005). [6] B. Pek, A van Driel, E de Jong, R. Klein Nagelvoort, Large Capacity plant Development, -14, Qatar (2004). [7] M. Pesaud, G. Chamberlain, S. Kauffman, Safety drivers in the lay-out of Floating Plants, AIChE New Orleans (2003). [8] C. Groothuis, Fletcher, R. Klein Nagelvoort, Changing the Game, -13, (2001). [9] C. Yost, R. DiNapoli, Benchmarking study compares plant costs, Oil & Gas Journal, April 14 (2003) pg [10] H.F. Grootjans (Shell), Compression Apparatus for gaseous refrigerant, US Patent No. 6,637,238 (2003). [11] R. Klein Nagelvoort (Shell), Plant for Liquefying Natural gas, US Patent No. 6,389,844 (2002). [12] W.E. Elion, R. Klein Nagelvoort, J. Vink, Reducing the amount of components having low boiling point in Liquefied Natural Gas, US Patent 6,014,869 (1998). [13] C. Buijs, W. Dam, E. de Jong (Shell), Method and Apparatus for Liquefaction of a Natural Gas stream, Patent application WO (2006). PS2-3.11
ADVANCED PROCESS CONTROL QATAR GAS ONE YEAR EXPERIENCE
ADVANCED PROCESS CONTROL QATAR GAS ONE YEAR EXPERIENCE Bouchebri El-Hadi Senior Process Engineer Benmouley Abdelkader Head of Process Qatar Liquefied Gas Company Limited. Ras Laffan Industrial Area, Doha,
More informationUNIQUE DESIGN CHALLENGES IN THE AUX SABLE NGL RECOVERY PLANT
UNIQUE DESIGN CHALLENGES IN THE AUX SABLE NGL RECOVERY PLANT Presented at the 81 st Annual Convention of the Gas Processors Association March 11, 2002 Dallas, Texas Joe T. Lynch, P.E. Ortloff Engineers,
More informationMLNG DUA DEBOTTLENECKING PROJECT
MLNG DUA DEBOTTLENECKING PROJECT Yahya Ibrahim Senior General Manager Malaysia LNG Malaysia yahyai@petronas.com.my Tariq Shukri LNG Consultant Foster Wheeler Energy Limited Reading, U.K. Tariq_shukri@fwuk.fwc.com
More informationMOLECULAR GATE TECHNOLOGY FOR (SMALLER SCALE) LNG PRETREATMENT
MOLECULAR GATE TECHNOLOGY FOR (SMALLER SCALE) LNG PRETREATMENT Presented at the 2010 Gas Processors 89 th Annual Convention Austin, TX March, 2010 Michael Mitariten, P.E. Guild Associates, Inc. Dublin,
More informationChemistry of Petrochemical Processes
Chemistry of Petrochemical Processes ChE 464 Instructor: Dr. Ahmed Arafat, PhD Office: building 45 room 106 E-mail: akhamis@kau.edu.sa www.kau.edu.sa.akhamis files Book Chemistry of Petrochemical Processes
More informationLNG UNIT (ENGINEERING DESIGN GUIDELINE)
Page : 1 of 60 Guidelines for Processing Plant www.klmtechgroup.com Rev 01 KLM Technology #03-12 Block Aronia, Jalan Sri Perkasa 2 Taman Tampoi Utama 81200 Johor Bahru Malaysia (ENGINEERING DESIGN GUIDELINE)
More informationINCREASING THE CAPACITY OF NGL RECOVERY TRAINS. Stéphane MESPOULHES XVI CONVENCIÓN INTERNACIONAL DE GAS Caracas de Mayo de 2004
INCREASING THE CAPACITY OF NGL RECOVERY TRAINS Stéphane MESPOULHES XVI CONVENCIÓN INTERNACIONAL DE GAS Caracas WHO IS TECHNIP? 2 World Class Engineering & Construction Group in Oil & Gas Public Company
More informationGT-LPG Max SM. Maximizing LPG Recovery from Fuel Gas Using a Dividing Wall Column. Engineered to Innovate
GTC Technology White Paper GT-LPG Max SM Maximizing LPG Recovery from Fuel Using a Dividing Wall Column Engineered to Innovate GT-LPG Max SM Maximizing LPG Recovery from Fuel Using a Dividing Wall Column
More informationImproving Natural Gas Liquefaction Plant Performance with Process Analyzers
Process Analytics Improving Natural Gas Liquefaction Plant Performance with Process Analyzers LNG is natural gas in its liquid state with high energy density, which makes it useful for storage and transportation
More informationLNG LIQUEFIED NATURAL GAS TECHNOLOGIES
LNG LIQUEFIED NATURAL GAS TECHNOLOGIES Air Liquide Group Air Liquide Engineering & Construction The world leader in gases, technologies and services for Industry and Health Air Liquide is present in 80
More informationGastech Singapore October Capital Cost and Efficiency Data for the ZR-LNG Dual Methane Expander Liquefaction Technology
Gastech Singapore October 2015 Capital Cost and Efficiency Data for the ZR-LNG Dual Methane Expander Liquefaction Technology Authors: GW Howe, GF Skinner, AD Maunder Presenter: GW Howe Introduction LNG
More informationOptimising. the LNG process. The rapidly expanding global LNG industry continues. Projects
Optimising the LNG process John Baguley, Liquefied Natural Gas Ltd, Australia, outlines the benefits of an innovative liquefaction process technology for mid scale LNG projects. The rapidly expanding global
More informationCONVERTING DOMINION COVE POINT LNG INTO BIDIRECTIONAL FACILITY
CONVERTING DOMINION COVE POINT LNG INTO BIDIRECTIONAL FACILITY Pascal Bocherel, Jim Strohman, Juan Martinez Dominion Cove Point LNG, LP Brett Wink, Kamal Shah, John Ray IHI E & C International Corporation
More informationSimple Dew Point Control HYSYS v8.6
Simple Dew Point Control HYSYS v8.6 Steps to set up a simulation in HYSYS v8.6 to model a simple dew point control system consisting of: Gas chiller Flash separator Liquid stabilizer with gas recycle &
More informationFloating LNG Business A breakthrough in offshore gas monetization
Floating LNG Business A breakthrough in offshore gas monetization LNG Malaysia Forum 2013 19-21 March, Kuala Lumpur Allan Magee, Ph.D. R&D Manager, Offshore Product Line and Technologies, Technip Geoproduction
More informationA Comparative Study of Propane Recovery Processes
A Comparative Study of Propane Recovery Processes Kent A. Pennybaker, Scott E. Wolverton, Steven W. Chafin, Thomas R. Ruddy River City Engineering, Inc. Lawrence, Kansas ABSTRACT There are many processes
More informationLNG Plant Overview. Seminar with Supplier Association Murmanshelf Murmansk, 15 May 2012 Jostein Pettersen
LNG Plant Overview Seminar with Supplier Association Murmanshelf Murmansk, 15 May 2012 Jostein Pettersen Table of Content Part 1 : LNG plant overview (Jostein) Part 2 : Main equipment units (Jostein) Part
More informationTechnical Innovation for Floating LNG. Bengt Olav Neeraas & Jostein Pettersen, Statoil ASA
Technical Innovation for Floating LNG Bengt Olav Neeraas & Jostein Pettersen, Statoil ASA Table of contents Relevant know how for FLNG FLNG concept development Technology development & innovation Conclusions
More informationNGL NATURAL GAS LIQUIDS TECHNOLOGIES
NGL NATURAL GAS LIQUIDS TECHNOLOGIES Air Liquide Group Air Liquide Engineering & Construction The world leader in gases, technologies and services for Industry and Health Air Liquide is present in 80 countries
More informationWWT Two-Stage Sour Water Stripping
WWT Two-Stage Sour Water Stripping Improve performance of sulfur recovery units ben efits The Chevron WWT Process is a two-stage stripping process which separates ammonia and hydrogen sulfide from sour
More informationDESIGN AND OPERATING EXPERIENCE FOR ANADARKO S LANCASTER FACILITY
DESIGN AND OPERATING EXPERIENCE FOR ANADARKO S LANCASTER FACILITY Presented at the 95 th Annual Convention of the Processors Association April 11, 2016 New Orleans, Louisiana Joe T. Lynch, P.E. Ortloff
More informationOptions for Removing Methanol from NGL in an Amine Treater Abstract. Submitted to SOGAT 2017 by:
Options for Removing Methanol from NGL in an Amine Treater Abstract Methanol is commonly injected into hydrocarbon fluids to inhibit hydrate formation. Bulk methanol removal from a hydrocarbon fluid often
More informationHYSYS WORKBOOK By: Eng. Ahmed Deyab Fares.
HYSYS WORKBOOK 2013 By: Eng. Ahmed Deyab Fares eng.a.deab@gmail.com adeyab@adeyab.com Mobile: 002-01227549943 - Email: adeyab@adeyab.com 1 Flash Separation We have a stream containing 15% ethane, 20% propane,
More informationModular Oil & Gas Equipment Onshore & Offshore
Modular Oil & Gas Equipment Onshore & Offshore Separators & Desalters AI Energy Solutions onshore and offshore oil process solutions offer innovative technologies packaged with global project management
More informationMagnetically Coupled Submerged Cryogenic Pumps and Expanders for Ammonia Applications
Paper 4d Magnetically Coupled Submerged Cryogenic Pumps and Expanders for Ammonia Applications Liquefied Ammonia, or Liquid NH3, is (like LNG or liquefied natural gas) a cryogenic fluid and production
More informationMITIGATION OF SEASONAL PRODUCTION LOSS FOR THREE PARALLEL 4.7MMTPA
17 th INTERNATIONAL CONFERENCE & EXHIBITION ON LIQUEFIED NATURAL GAS (LNG 17) 17 th INTERNATIONAL CONFERENCE & EXHIBITION MITIGATION OF SEASONAL PRODUCTION LOSS FOR THREE PARALLEL 4.7MMTPA
More informationQualitative Phase Behavior and Vapor Liquid Equilibrium Core
2/22/2017 Qualitative Phase Behavior and Qualitative Phase Behavior Introduction There are three different phases: solid, liquid, and gas (vapor) Energy must be added to melt a solid to form liquid If
More informationKalex Kalina Cycle Power Systems For Use as a Bottoming Cycle for Combined Cycle Applications
Superior Efficiency Reduced Costs Viable Alternative Energy Kalex Kalina Cycle Power Systems For Use as a Bottoming Cycle for Combined Cycle Applications Copyright 2009, 2010, Kalex LLC. Kalex LLC's Kalina
More informationModified Reverse-Brayton Cycles for Efficient Liquefaction of Natural Gas
Modified Reverse-Brayton Cycles for Efficient Liquefaction of Natural Gas H.M. Chang 1, J.H. Park 1, K.S. Cha 2, S. Lee 2 and K.H. Choe 2 1 Hong Ik University, Seoul, Korea 121-791 2 Korea Gas Corporation,
More informationRectisol Wash Units Acid Gas Removal for Polygeneration Concepts downstream Gasification
Rectisol Wash Units Acid Gas Removal for Polygeneration Concepts downstream Gasification Ulvi Kerestecioğlu, Thomas Haberle GTC Conference, Washington DC, USA, November 3rd, 2010 Agenda of the Presentation
More informationNITROGEN REJECTION UNITS NATURAL GAS TREATMENT TECHNOLOGIES
NITROGEN REJECTION UNITS NATURAL GAS TREATMENT TECHNOLOGIES Air Liquide Group Air Liquide Engineering & Construction The world leader in gases, technologies and services for Industry and Health Air Liquide
More informationHeat Recovery Systems and Heat Exchangers in LNG Applications. Landon Tessmer LNG Technical Workshop 2014 Vancouver
Heat Recovery Systems and Heat Exchangers in LNG Applications Landon Tessmer LNG Technical Workshop 2014 Vancouver Presentation Overview LNG plant arrangement with heat recovery (OSMR Process by LNG Limited)
More informationTeknologi Pemrosesan Gas (TKK 564) Instructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi )
Teknologi Pemrosesan Gas (TKK 564) Instructor: Dr. Istadi (http://tekim.undip.ac.id/staf/istadi ) Email: istadi@undip.ac.id id Instructor s t Background BEng. (1995): Universitas Diponegoro Meng. (2000):
More informationYemen LNG Operational feedbacks
Yemen LNG Operational feedbacks APCI Owners Seminar XI September 2013 1 Yemen LNG - Agenda 1. Yemen LNG general presentation 2. Feedback on Plant restarts optimization 3. Other operational feedbacks 2
More informationYour compressor of choice since Integrally geared. siemens.com /compressors
Turbocompressor STC-GV Your compressor of choice since 1948. Integrally geared. siemens.com /compressors 2 A success story since 1948 The integrally geared type compressor operates both as the Main Air
More informationGAS MONETISATION SOLUTIONS
GAS MONETISATION SOLUTIONS Global Flare Reduction programme Bill Spence & Guus Kessler UI CO 2 Shell International Exploration and - The Hague THE ASSOCIATED GAS MONETISATION CHALLENGE Barriers that impede
More informationThe Trinidad LNG Project - Back to the Future
The Trinidad LNG Project - Back to the Future Phil Redding, Atlantic LNG Company of Trinidad and Tobago, Frank Richardson, Bechtel Corporation (USA) In the small Caribbean state of Trinidad and Tobago
More informationChallenges for Processing Oil and Gas from Kazakhstan
Challenges for Processing Oil and Gas from Kazakhstan Paul Roberts, Les Armstrong WorleyParsons Parkview Great West Road Brentford Middlesex, TW8 9AZ, UK ABSTRACT In recent years WorleyParsons has been
More informationPROCESSING NATURAL GAS Leontev A.A. Vladimirskiy State University named after the Stoletov brothers Vladimir, Russia
PROCESSING NATURAL GAS Leontev A.A. Vladimirskiy State University named after the Stoletov brothers Vladimir, Russia ПЕРЕРАБОТКА ПРИРОДНОГО ГАЗА Леонтьев А.А. Владимирский государственный университет имени
More informationCCS Learning from the LNG Sector
CCS Learning from the LNG Sector A Report for the Global CCS Institute 401010-01060 00-PM-REP-0001 12 December 2013 Hydrocarbons Level 12, 333 Collins Street Melbourne VIC 3000 Australia Telephone: +61
More informationGas Processing. Speed. Simplicity. Efficiency Modular Gas Processing Plants
Gas Processing Speed. Simplicity. Efficiency Modular Gas Processing Plants The Golden Age of Gas Over the next decade, global gas use will rise by more than 20% and will account for almost one quarter
More informationGas Processing. Speed. Simplicity. Efficiency Modular Gas Processing Plants
Gas Processing Speed. Simplicity. Efficiency Modular Gas Processing Plants The Golden Age of Gas Over the next decade, global gas use will rise by more than 20% and will account for almost one quarter
More informationFull electrical LNG-plant: Highest availability and energy efficiency trough overall system design
Full electrical LNG-plant: Highest availability and energy efficiency trough overall system design Dr. Edwin Lerch Principal Expert Power System Dynamics Siemens AG Erlangen, Germany edwin.lerch@siemens.com
More informationHIGH PUITY CARBON MONOXIDE FROM A FEED GAS ARNOLD KELLER AND RONALD SCHENDEL KINETICS TECHNOLOGY INTERNATIONAL CORPORATION MONROVIA, CALIFORNIA
THE USE OF COSORB R II TO RECOVER HIGH PUITY CARBON MONOXIDE FROM A FEED GAS BY ARNOLD KELLER AND RONALD SCHENDEL KINETICS TECHNOLOGY INTERNATIONAL CORPORATION MONROVIA, CALIFORNIA PRESENTED AT AICHE SUMMER
More informationDominion Cove Point Export Project Platts 16 th Annual Liquefied Natural Gas February 9, 2017
Dominion Cove Point Export Project Platts 16 th Annual Liquefied Natural Gas February 9, 2017 Note to Investors This presentation contains certain forward-looking statements, including projected future
More informationTransPacific Energy Advantage: Case Studies
TransPacific Energy Advantage: Case Studies Typical Power Plant TPE-ORC 0.60 KWh ORC 2.3 KWh LP steam 0.35 KWh 30% (maximum) 2.05 KWh CHP Typical Power Generated 1.1 KWh Typical Power Wasted 2.31 KWh Typical
More informationSteam balance optimisation strategies
Steam balance optimisation strategies Publicado en Chemical Engineering, Noviembre 2002 Background Optimising a steam balance in a plant with several steam mains pressures is not always a simple intuitive
More informationHigh-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture
High-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture The MIT Faculty has made this article openly available. Please share how this access benefits you. Your
More informationwith Physical Absorption
meinschaft Mitglied der Helmholtz-Gem Pre-Combustion Carbon Capture with Physical Absorption Sebastian Schiebahn, Li Zhao, Marcus Grünewald 5. Juli 2011 IEK-3, Forschungszentrum Jülich, Germany ICEPE Frankfurt
More informationCansolv Technologies Inc. Alberta NOx and SOx Control Technologies Symposium April 9, Rick Birnbaum
A Novel SO 2 Scrubbing Process For Industrial SO 2 Emission Control Alberta NOx and SOx Control Technologies Symposium April 9, 2008 Rick Birnbaum rick.birnbaum@cansolv.com OUTLINE Gas Absorption Solutions
More information10/2/2013. Gas CHEMICAL PLANTS AMMONIA METHANOL UTILITIES TOWN GASS SUPPLIES ENERGY INTENSIVE INDUSTRIES. Power Generation
Gas Burning Feed Stock UTILITIES TOWN GASS SUPPLIES ENERGY INTENSIVE INDUSTRIES Power Generation CHEMICAL PLANTS AMMONIA METHANOL 1 Fundamentals of Natural Gas Processing Natural gas has been formed by
More informationCanada. Iron and Steel Sector - PI Specifics
How can process integration help me? Process integration (PI) is a very efficient approach to improving the energy efficiency of large and complex industrial facilities. PI refers to the application of
More informationProcessing LNG Offshore: Maximizing Reliability, Performance & Safety. By Inga Bettina Waldmann at KANFA Aragon FLNG World Congress 28 th June 2016
Processing LNG Offshore: Maximizing Reliability, Performance & Safety By Inga Bettina Waldmann at KANFA Aragon FLNG World Congress 28 th June 2016 FLNG World Congress 2016 Agenda I. About KANFA Aragon
More informationCOMBINED CYCLE OPPORTUNITIES FOR SMALL GAS TURBINES
19 TH SYMPOSIUM OF THE INDUSTRIAL APPLICATION OF GAS TURBINES COMMITTEE BANFF, ALBERTA, CANADA OCTOBER 17-19, 2011 11-IAGT-204 COMBINED CYCLE OPPORTUNITIES FOR SMALL GAS TURBINES Michael Lucente Found
More informationON LIQUEFIED NATURAL GAS (LNG 17) 17 th INTERNATIONAL CONFERENCE & EXHIBITION ON LIQUEFIED NATURAL GAS (LNG 17)
17 th INTERNATIONAL CONFERENCE & EXHIBITION ON LIQUEFIED NATURAL GAS (LNG 17) 17 th INTERNATIONAL CONFERENCE & EXHIBITION ON LIQUEFIED NATURAL GAS (LNG 17) HOW TO DEVELOP AN ECONOMICAL SMALL CAPACITY FLOATING
More informationNatural Gas. and the Liquefaction Process
Natural Gas and the Liquefaction Process Table of Contents Cameron LNG.................... 2 Liquefied Natural Gas................ 4 LNG Safety...................... 5 Environmental Safety................
More informationBrazed aluminium heat exchangers (BAHXs), also referred to
Brazed aluminium heat exchangers (BAHXs), also referred to as plate fin heat exchangers, are at the heart of many of the processes used for the liquefaction of natural gas. They are deployed across the
More informationAKAKUS OIL OPERATIONS- LIBYA Gas Utilization& Flare Emission Reduction Project
Tripoli, Libya 2010 AKAKUS OIL OPERATIONS- LIBYA Gas Utilization& Flare Emission Reduction Project Presented by: Mohamed Amari Project Location Tripoli, Libya 2010 N Tunisia Tripoli Mediterranean Sea Benghazi
More informationGas Enhanced Membrane Fuel Gas Conditioning Solutions for Compressor Stations with Ultra High BTU Gases in Oil-rich Shale Plays
Gas Enhanced Membrane Fuel Gas Conditioning Solutions for Compressor Stations with Ultra High BTU Gases in Oil-rich Shale Plays Authors: (a) Sachin Joshi, Priyanka Tiwari and Kaaeid Lokhandwala, Membrane
More informationSPE DISTINGUISHED LECTURER SERIES is funded principally through a grant of the SPE FOUNDATION
SPE DISTINGUISHED LECTURER SERIES is funded principally through a grant of the SPE FOUNDATION The Society gratefully acknowledges those companies that support the program by allowing their professionals
More informationHOW TO COMPARE CRYOGENIC PROCESS DESIGN ALTERNATIVES FOR A NEW PROJECT
HOW TO COMPARE CRYOGENIC PROCESS DESIGN ALTERNATIVES FOR A NEW PROJECT Presented at the 86 th Annual Convention of the Gas Processors Association March 12, 2007 San Antonio, Texas Joe T. Lynch, P.E. Ortloff
More informationModelling of CO 2 capture using Aspen Plus for EDF power plant, Krakow, Poland
Modelling of CO 2 capture using Aspen Plus for EDF power plant, Krakow, Poland Vipul Gupta vipul.gupta@tecnico.ulisboa.pt Instituto Superior Técnico,Lisboa, Portugal October 2016 Abstract This work describes
More informationReduce Emissions for Compressor Stations in Condensate-rich Shale Gas Plays by Reducing Heavy Hydrocarbons in Fuel Gas
Reduce Emissions for Compressor Stations in Condensate-rich Shale Gas Plays by Reducing Heavy Hydrocarbons in Fuel Gas Authors: Sachin Joshi and Kaaeid Lokhandwala, Membrane Technology and Research, Inc.
More informationHeat Integration of an Oxy-Combustion Process for Coal- Fired Power Plants with CO 2 Capture by Pinch Analysis
CHEMICAL ENGINEERING TRANSACTIONS Volume 21, 2010 Editor J. J. Klemeš, H. L. Lam, P. S. Varbanov Copyright 2010, AIDIC Servizi S.r.l., ISBN 978-88-95608-05-1 ISSN 1974-9791 DOI: 10.3303/CET1021031 181
More informationSulsim Sulfur Recovery in Aspen HYSYS V9 A Brief Tutorial for Using and Optimizing Your Sulfur Recovery Unit in Aspen HYSYS
Sulsim Sulfur Recovery in Aspen HYSYS V9 A Brief Tutorial for Using and Optimizing Your Sulfur Recovery Unit in Aspen HYSYS Jump Start Guide Chad Mondor, Product Management, Aspen Technology, Inc. Jennifer
More informationGASTECH Achieving Product Specifications for Ethane through to Pentane Plus from NGL Fractionation Plants
GASTECH 2005 Achieving Product Specifications for Ethane through to Pentane Plus from NGL Fractionation Plants ABSTRACT This paper examines the techniques that may be applied in evaluating processing options
More information2015. This manuscript version is made available under the CC-BY-NC-ND 4.0 license
Al-Lagtah NMA, Al-Hasbi S, Onaizi SA. Optimization and performance improvement of Lekhwair natural gas sweetening plant using Aspen HYSYS. Journal of Natural Gas Science and Engineering2015, 26, 367-381.
More informationGGFR. Methane Expo Best practices for evaluating and reducing emissions from oil and gas production An evaluation of Flare Gas Reduction Opportunities
GGFR Methane Expo Best practices for evaluating and reducing emissions from oil and gas production An evaluation of Flare Gas Reduction Opportunities Bent Svensson March 12-15, 2013-1 - Today s presentation
More informationCANSOLV SO2 Scrubbing System - 10 Years of Reliable Operation Integration with SRU Tail Gas Incineration
CANSOLV SO2 Scrubbing System - 1 Years of Reliable Operation Integration with SRU Tail Gas Incineration NICOLAS EDKINS, NANCY MORETON Cansolv Technologies Inc. (an affiliate of Shell Global Solutions BV)
More information50 Years of PSA Technology for H2 Purification
50 Years of PSA Technology for H 2 Purification 1 50 Years of PSA Technology for H2 Purification The first industrial application of Pressure Swing Adsorption (PSA) went on stream in 1966 at a Union Carbide
More informationGrand Composite Curve Module 04 Lecture 12
Module 04: Targeting Lecture 12: Grand Composite Curve While composite curves provide overall energy targets, these do not indicate the amount of energy that should be supplied at different temperature
More informationMicroTurbine CHP Applications for Oil and Gas Industry
MicroTurbine CHP Applications for Oil and Gas Industry January 2008 Lee Richards Director, O&G Sales What is a MicroTurbine? Power generator driven by a small scale gas turbine Electrical efficiency of
More informationPIONEERING GAS SOLUTIONS PROCESS SYSTEMS
PIONEERING GAS SOLUTIONS PROCESS SYSTEMS WHO ARE WE? GENERON is one of the only single source providers of gas solutions in the world. An industry-leading provider, we have the capabilities and customized
More informationGASTECH 2OO2. Jeff Sawchuk, BP Global Gas Technology. Richard Jones, BP Global Gas Technology. Pat Ward, BP Global Gas Technology
PROGRAMME GASTECH 2OO2 Jeff Sawchuk, BP Global Gas Technology Jeff Sawchuk holds a Bachelor of Science in Mechanical Engineering and has been with BP for 22 years. He is currently the LNG Technology Manager
More informationREFRIGERATION CYCLES
REFRIGERATION CYCLES Carnot Cycle We start discussing the well-known Carnot cycle in its refrigeration mode. Figure 2-1: Carnot Cycle In this cycle we define the coefficient of performance as follows:
More informationLarge LNG plant capabilities for capacity >2 MTPA Benefit from economies of scale and proven technology
Large LNG plant capabilities for capacity > MTPA Benefit from economies of scale and proven technology Benefits to our customers: Economical Production Air Products natural gas liquefaction processes and
More informationSulfur Management in Natural Gas Treating Plants: A state-ofthe-art approach for LNG Plants
Page 1 of 18 Sulfur Management in Natural Gas Treating Plants: A state-ofthe-art approach for LNG Plants Peter Hawes, ZEOCHEM AG, Uetikon/ Switzerland Justin Hearn, BASF AG, Ludwigshafen/ Germany Max-Michael
More informationHydrate Formation in Chevron Mabee Unit for NGL Recovery and CO 2 Purification for EOR. Abstract
Hydrate Formation in Chevron Mabee Unit for NGL Recovery and CO 2 Purification for EOR Abstract In the early 199 s, Chevron installed a new process to recover natural gas liquids (NGLs) from recycled CO
More informationBLUE OPTION White space is filled with one or more photos
Driving Innovation Delivering Results BLUE OPTION White space is filled with one or more photos Performance Baseline for Direct-Fired sco 2 Cycles Nathan Weiland, Wally Shelton NETL Chuck White, David
More informationNOVEL SCHEME FOR SMALL SCALE LNG PRODUCTION in POLAND. W.H. Isalski
NOVEL SCHEME FOR SMALL SCALE LNG PRODUCTION in POLAND W.H. Isalski Presentation Overview The history of gas de-nitrogenation in Poland Changes in feed gas Changes in market conditions Expanding market
More informationFloating LNG: The Challenges of production systems and well fluids management By: Frederic MOLLARD, TECHNIP France 04/19/2013
17 th INTERNATIONAL CONFERENCE & EXHIBITION ON LIQUEFIED NATURAL GAS (LNG 17) Floating LNG: The Challenges of production systems and well fluids management By: Frederic MOLLARD, TECHNIP France 04/19/2013
More informationTraining Title GAS PROCESSING, SWEETENING & SULPHUR RECOVERY
Training Title GAS PROCESSING, SWEETENING & SULPHUR RECOVERY Training Duration 5 days Training Venue and Dates Gas Processing, Sweetening & Sulphur Recovery 5 19-23 November, 2017 $4,000 Dubai, UAE Trainings
More informationEvolution of an LNG Terminal: Senboku Terminal of Osaka Gas
23 rd World Gas Conference, Amsterdam 2006 Evolution of an LNG Terminal: Senboku Terminal of Osaka Gas Main author Toshiro Otsuka Japan TABLE OF CONTENTS 1. Abstract 2. Body of Paper 3. List Tables 4.
More informationQatargas is the world s
Acid treatment upgrade for Qatar Upgrading acid treatment at the world s largest LNG facility safeguards the plant s design capacity and its ability to process increasingly sour feeds GAUTHIER PERDU, LAURENT
More informationSULPHUR RECOVERY BY TAIL GAS TREATING TECHNOLOGY (MCRC PROCESS) MAXIMUM CLAUS
International Journal of Science, Environment and Technology, Vol. 3, No 4, 2014, 1609 1613 ISSN 2278-3687 (O) SULPHUR RECOVERY BY TAIL GAS TREATING TECHNOLOGY (MCRC PROCESS) MAXIMUM CLAUS Sulabh Jangra
More informationItem Hydrogen Gas Plant
Item 6530. Hydrogen Gas Plant Hydro-Chem Hydrogen Generating Plant 90,000 scfh @ 200 psig. Purity 99.99% Hydrogen generating plant engineered by Hydro-Chem built in 1980. Design capacity is 90,000 scfh
More informationThermodynamics Optimization of GARRI (1) Combined Cycle Power Plant by Using ASPEN HYSYS Simulation
International Journal on Recent and Innovation Trends in Computing and Communication ISSN: 21-8169 Thermodynamics Optimization of GARRI (1) Combined Cycle Power Plant by Using ASPEN HYSYS Simulation AbdAllah
More informationGASIFICATION TECHNOLOGIES 2003
S.Francisco, California October 12-15, 2003 GASIFICATION TECHNOLOGIES 2003 COAL POWER PLANTS WITH CO2 CAPTURE: THE IGCC OPTION J.Davison - IEA Greenhouse Gas R&D Programme L.Bressan - R.M.Domenichini -
More informationReforming Natural Gas for CO 2 pre-combustion capture in Combined Cycle power plant
Reforming Natural Gas for CO 2 pre-combustion capture in Combined Cycle power plant J.-M. Amann 1, M. Kanniche 2, C. Bouallou 1 1 Centre Énergétique et Procédés (CEP), Ecole Nationale Supérieure des Mines
More informationModeling and simulation of main cryogenic heat exchanger in a base-load liquefied natural gas plant
17 th European Symposium on Computer Aided Process Engineering ESCAPE17 V. Plesu and P.S. Agachi (Editors) 2007 Elsevier B.V. All rights reserved. 1 Modeling and simulation of main cryogenic heat exchanger
More informationThermodynamic analysis on post combustion CO 2 capture of natural gas fired power plant
Thermodynamic analysis on post combustion CO 2 capture of natural gas fired power plant Abstract Zeinab Amrollahi, 1 Ivar S. Ertesvåg, Olav Bolland Department of Energy and Process Engineering, Norwegian
More informationRETROFIT OF THE AMERADA HESS SEA ROBIN PLANT FOR VERY HIGH ETHANE RECOVERY ABSTRACT
RTROFIT OF TH AMRADA HSS SA ROBIN PLANT FOR VRY HIGH THAN RCOVRY Joe T. Lynch, P.. Ortloff ngineers, Ltd. Midland, Texas USA J. Pat McCann and Paul Carmody, P.. Amerada Hess Corporation Houston, Texas
More informationAutothermal Reforming for efficient and versatile syngas production. Esben Sorensen, Haldor Topsoe Inc. GSTC 2017 Syngas Technologies Conference
Autothermal Reforming for efficient and versatile syngas production Esben Sorensen, Haldor Topsoe Inc. GSTC 2017 Syngas Technologies Conference Haldor Topsoe Company Established in 1940 by Dr. Haldor Topsoe.
More informationLurgi s MPG Gasification plus Rectisol Gas Purification Advanced Process Combination for Reliable Syngas Production
Lurgi s MPG Gasification plus Rectisol Gas Purification Advanced Process Combination for Reliable Syngas Production Ulrich Koss, Holger Schlichting Gasification Technologies 2005 San Francisco, 9. 12.
More informationPRISM Membrane Systems for petrochemical applications... tell me more
PRISM Membrane Systems for petrochemical applications... tell me more Air Products PRISM Membrane Systems are found in petrochemical plants around the world operating efficiently and economically. PRISM
More informationA COMPARATIVE STUDY OF ETHANE RECOVERY PROCESSES
A COMPARATIVE STUDY OF ETHANE RECOVERY PROCESSES Kent A. Pennybaker, Scott E. Wolverton, Steven W. Chafin, Thomas R. Ruddy, Christopher W. Pritchard River City Engineering, Inc. Lawrence, Kansas ABSTRACT
More informationIon Transport Membrane (ITM) Technology for Lower-Cost Oxygen Production
Ion Transport Membrane (ITM) Technology for Lower-Cost Oxygen Production Rob Steele EPRI (rsteele@epri.com) Phil Armstrong - Air Products and Chemicals Inc. Arun Bose DOE NETL Gasification Technologies
More informationThomas G. Braga Manager, Research and Development. SulfaTreat, a Business Unit of M I L.L.C. A Smith/Schlumberger Company
Thomas G. Braga Manager, Research and Development SulfaTreat, a Business Unit of M I L.L.C. A Smith/Schlumberger Company Who is SulfaTreat? A World Leader in H 2 S Removal for More than a Decade Today
More informationNathan A. Hatcher and Ralph H. Weiland, Optimized Gas Treating Inc., USA, discuss the fate of ammonia in refinery amine systems.
Special treatment T he corrosion that results from ammonia ingress and accumulation in refinery and biogas amine systems is a problem that may be exacerbated by the increasing utilisation of advantaged
More informationA World of Solutions Visit Product Storage Terminals for Bulk Liquids
A World of Solutions Visit www.cbi.com Product Storage Terminals for Bulk Liquids United Arab Emirates The most global experience of any tank company CB&I has more than eight decades of experience designing
More information