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Relevant bibliographies by topics / Synthesis gas

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Academic literature on the topic 'Synthesis gas'

Author: Grafiati

Published: 4 June 2021

Last updated: 6 September 2023

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Journal articles on the topic "Synthesis gas"

1

JM, Bahig. "Synthesis of Bio-gas Using Squander Cooking Oil." Petroleum & Petrochemical Engineering Journal 5, no. 3 (2021): 1–7. http://dx.doi.org/10.23880/ppej-16000270.

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The point of this examination is to evaluate the performance of both catalytic and thermal cracking processes in the thermochemical conversion of squander cooking oil into biofuel and investigate the impact of ZSM-5 impetus and breaking reactor temperature to items yield, biofuel caloric substance and synthetic arrangement. Several parameters might affect process performance which resulted in different product’s yield and specification. Cracking temperature variation gave appreciable effect on yield and product’s caloric values.

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Encinar, J. M., J. F. González, N. Sánchez, and S. Nogales. "Glycerol Reuse for Obtaining Synthesis Gas through Steam Reforming." International Journal of Chemical Engineering and Applications 10, no. 5 (October 2019): 163–67. http://dx.doi.org/10.18178/ijcea.2019.10.5.762.

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Dac Dien, Nguyen, Luong Huu Phuoc, Do Duc Tho, Nguyen Anh Phuc Duc, Nguyen Duc Chien, and Dang Duc Vuong. "HYDROTHERMAL SYNTHESIS AND NH3 GAS SENSING PROPERTY OFWO3 NANO PARTICLES." Journal of Science, Natural Science 60, no. 7 (2015): 68–74. http://dx.doi.org/10.18173/2354-1059.2015-0034.

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Shalaev, R. V. "Gas-Phase Synthesis of Film Structures of Ni—N System." METALLOFIZIKA I NOVEISHIE TEKHNOLOGII 37, no. 4 (August 17, 2016): 509–19. http://dx.doi.org/10.15407/mfint.37.04.0509.

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Chiche, D., C. Diverchy, A. C. Lucquin, F. Porcheron, and F. Defoort. "Synthesis Gas Purification." Oil & Gas Science and Technology – Revue d’IFP Energies nouvelles 68, no. 4 (July 2013): 707–23. http://dx.doi.org/10.2516/ogst/2013175.

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Zhang, Qianwen, Xiaohong Li, Kenji Asami, Sachio Asaoka, and Kaoru Fujimoto. "Synthesis of LPG from synthesis gas." Fuel Processing Technology 85, no. 8-10 (July 2004): 1139–50. http://dx.doi.org/10.1016/j.fuproc.2003.10.016.

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Betts, Natalie S., Christoph Dockter, Oliver Berkowitz, Helen M. Collins, Michelle Hooi, Qiongxian Lu, Rachel A. Burton, et al. "Transcriptional and biochemical analyses of gibberellin expression and content in germinated barley grain." Journal of Experimental Botany 71, no. 6 (December 10, 2019): 1870–84. http://dx.doi.org/10.1093/jxb/erz546.

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Abstract Mobilization of reserves in germinated cereal grains is critical for early seedling vigour, global crop productivity, and hence food security. Gibberellins (GAs) are central to this process. We have developed a spatio-temporal model that describes the multifaceted mechanisms of GA regulation in germinated barley grain. The model was generated using RNA sequencing transcript data from tissues dissected from intact, germinated grain, which closely match measurements of GA hormones and their metabolites in those tissues. The data show that successful grain germination is underpinned by high concentrations of GA precursors in ungerminated grain, the use of independent metabolic pathways for the synthesis of several bioactive GAs during germination, and a capacity to abort bioactive GA biosynthesis. The most abundant bioactive form is GA1, which is synthesized in the scutellum as a glycosyl conjugate that diffuses to the aleurone, where it stimulates de novo synthesis of a GA3 conjugate and GA4. Synthesis of bioactive GAs in the aleurone provides a mechanism that ensures the hormonal signal is relayed from the scutellum to the distal tip of the grain. The transcript data set of 33 421 genes used to define GA metabolism is available as a resource to analyse other physiological processes in germinated grain.

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Wender, Irving. "Reactions of synthesis gas." Fuel Processing Technology 48, no. 3 (September 1996): 189–297. http://dx.doi.org/10.1016/s0378-3820(96)01048-x.

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Valenti, Michael. "Turbines for Synthesis Gas." Mechanical Engineering 120, no. 08 (August 1, 1998): 72–73. http://dx.doi.org/10.1115/1.1998-aug-6.

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This article reviews on one of the most demanding applications for steam turbines, which are providing the extraction steam for the production of ammonia and methanol synthesis gas, or syngas. Dresser-Rand Energy Systems, Wellsville, NY, designed their Syngas Steam Turbine specifically to meet these requirements. Demand is expected to grow for both ammonia and methanol. Ammonia is the source for most of the nitrogen fertilizer produced globally. The capacity in 1996 was 117 million metric tons, up from 113 million metric tons five years earlier. Dresser-Rand approached the syngas project with more than 30 years’ experience as a leading supplier of compression equipment for ammonia plants. The first Syngas Steam Turbine, and its complete compression train including Dresser-Rand DATUM compressors, was shipped to a methanol plant operated by Qatar Fuel Additives Ltd. in the Mesaieed Industrial Area, Qatar. It is scheduled to begin operation by the middle of next year, producing 610,000 metric tons of methanol annually. Dresser-Rand engineers have also adapted their Syngas Turbine technology for different applications.

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Debabov, V. G. "Bioethanol from synthesis gas." Applied Biochemistry and Microbiology 49, no. 7 (October 22, 2013): 619–28. http://dx.doi.org/10.1134/s000368381307003x.

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Dissertations / Theses on the topic "Synthesis gas"

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Ng, Kok Leong. "Kinetics and modelling of dimethyl ether synthesis from synthesis gas." Thesis, Imperial College London, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.392222.

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Hagey, H. Louis. "Kinetic modelling of synthesis gas into hydrocarbons." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp04/NQ58214.pdf.

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Broberg, Marina. "FTIR method for analysis of synthesis gas." Thesis, Linköpings universitet, Institutionen för fysik, kemi och biologi, 2013. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-94539.

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The research institute ETC in Piteå is working with energy technical research and development. Today, much work revolves around research about renewable sources for fuel. In one project, biomass such as wood pellet is heated up while producing synthesis gas. The synthesis gas is then analyzed using three different GC techniques. ETC wanted to be able to make all their analysis on one instrument and with a faster speed. They contacted the company Rowaco in Linköping for help with developing a method on FTIR for analysis of the synthesis gas and that has been the aim for this thesis. A method has been developed for analysis of water, carbon monoxide, carbon dioxide and methane. The results from this thesis show that the concentrations of the molecules in the synthesis gas are outside the calibration curved that has been made and that the high concentrations give much interference to other molecules. The thesis also shows that many areas in the spectrum from the process are roof absorbers and there is also a contamination of water and carbon dioxide in the system. Suggested improvements are to find the source for the contamination, to develop calibration points with higher concentrations, to reduce the length of the gas cell and to dilute the gas before entering the FTIR.

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Moore, Simon Andrew. "Formation of higher alcohols from synthesis gas." Thesis, University of Glasgow, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.272886.

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Dam, Bidhan Kumar. "Flashback propensity of gas mixtures." To access this resource online via ProQuest Dissertations and Theses @ UTEP, 2009. http://0-proquest.umi.com.lib.utep.edu/login?COPT=REJTPTU0YmImSU5UPTAmVkVSPTI=&clientId=2515.

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Ardha, Vishwanath Reddy. "Laminar burning velocities of gas mixtures." To access this resource online via ProQuest Dissertations and Theses @ UTEP, 2009. http://0-proquest.umi.com.lib.utep.edu/login?COPT=REJTPTU0YmImSU5UPTAmVkVSPTI=&clientId=2515.

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Pryce, Imogen Mary. "Calcium reclamation and synthesis of PCC for acid gas control in flue gas." Connect to resource, 2006. http://hdl.handle.net/1811/6477.

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Thesis (Honors)--Ohio State University, 2006.
Title from first page of PDF file. Document formatted into pages: contains vi, 61 p.; also includes graphics. Includes bibliographical references (p. 59-60). Available online via Ohio State University's Knowledge Bank.

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Olsen, Susanne Kelly. "Catalytic membrane reactors for synthesis gas production from natural gas via partial oxidation." Thesis, Robert Gordon University, 2004. http://hdl.handle.net/10059/626.

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Natural gas obtained during the extraction of liquid hydrocarbons is often undesired due to the lack of infrastructure to transport the natural gas to an onshore location. As a result the natural gas is often flared causing economic waste and environmental concern. It would therefore be desirable to either convert the natural gas into some other substance which can be transported easily, or transport the natural gas in a liquid state. In that way, new field development will be more financially viable through the use of the extensive infrastructure and technology already in place in the offshore industry for transporting liquid hydrocarbons. It is considered that one feasible way of utilising offshore produced natural gas, is to convert it into synthetic gas (syngas) which can in turn be used to produce gases and fluids such as methanol, ammonia or a synthetic crude oil that can be readily pumped through the same pipelines as the produced oil. For the production of synthetic gas, membrane technology presents an attractive advantage improving conversion efficiency by operating as catalyst support, which then also increases the catalyst dispersion, resulting in optimal catalyst load and complete consumption of oxygen and methane in the partial oxidation. In the present investigation, an enhanced catalyst-dispersed ceramic membrane for low-cost synthesis gas production suitable for gas-to-liquids has been prepared, characterised and tested in a self-designed membrane reactor. The effect of temperature and feed flow rates has been studied and a kinetic model has been developed. In the novel membrane reactor, an active porous layer is located on both sides facing the oxygen and methane containing gas, adjacent is a second active porous layer and is supported by layers with increasing pore radii. Here the active porous layer on the bore side enhances the reaction between permeated oxygen and fuel species. In this study, it has also been demonstrated that the oxygen is activated prior to contacting the methane inside the membrane. This often results in 100% oxygen conversion, CO selectivity higher than 96% and syngas ratio (1-1/2 C O) of 2.2 to 1.8. Another advantage of the developed membrane system is that it can be used in high temperatures (> 1273.15K) and high pressure (80bars) processes with no variation on the flow rates, due to the mechanical strength of the ceramic support used.

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Arinan, Ayca. "Direct Synthesis Of Dimethyl Ether (dme) From Synthesis Gas Using Novel Catalysts." Master's thesis, METU, 2010. http://etd.lib.metu.edu.tr/upload/3/12611490/index.pdf.

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Increasing prices of crude oil derived transportation fuels ascended the researches on seeking alternative fuels, in last decades. Moreover, the increasing rate of global warming, because of high greenhouse gas emissions initiated new research for environment-friendly clean alternative fuels. Due to its low NOx emission, good burning characteristics and high cetane number, dimethyl ether (DME) attracted major attention as a transportation fuel alternative. Two possible pathways have been proposed for DME production. One of these pathways is DME synthesis through conventional methanol dehydration. More recently, direct DME synthesis in a single step has attracted significant attention of researchers and fuel producers. Catalysts having two active sites are required for direct DME synthesis from synthesis gas. The aim of this work was to synthesize novel bifunctional direct DME synthesis catalysts and test their activity in a high pressure fixed bed flow reactor. Bifunctional mesoporous catalysts were synthesized by using one-pot hydrothermal synthesis, impregnation and physical mixing methods. These materials were characterized by XRD, EDS, SEM, N2 physisorption and diffuse reflectance FT-IR (DRIFTS) techniques. Characterization results of the catalysts synthesized by one-pot hydrothermal synthesis procedures in basic and acidic routes showed that pH value of the synthesis solution was highly effective on the final physical structure and chemical nature of the catalysts. Increase in the pH value promoted the incorporation of Cu, Zn and Al into the mesoporous MCM-41 structure. Also, effects of Na2CO3 addition on the catalyst structure during the hydrothermal synthesis procedure were investigated. The characterization results showed that metals were incorporated into the catalyst structure successfully. However, surface area results showed that loaded metals blocked the pores of MCM-41 and decreased the surface area of the catalysts. Effects of zirconium (Zr) metal with different weight ratios were also investigated. Results showed that Zr loading increased the surface area of the catalyst. A high pressure fixed bed flow reactor was built and the catalyst testing experiments were performed between the temperature range of 200-400°
C, at 50 bars. The activity results of the catalyst synthesized by impregnation method showed that no DME was formed over this catalyst
however it showed promising results for production of methanol and ethanol. Selectivity values of these alcohols were between 0.35 and 0.2. Formation of methane and CO2 indicated the occurrence of reverse dry reforming reaction. Incorporation of Zr into the catalyst structure at neutral synthesis condition caused significant activity enhancement, giving CO conversion values of about 40% at 400°
C. Product distribution obtained with this catalyst indicated the formation of DME, ethanol, methanol as well as CH4 and CO2. Highest DME selectivity (60%) was observed with the catalyst prepared by physical mixing of commercial methanol reforming catalyst with silicotungstic acid incorporated methanol dehydration catalyst having W/Si ratio of 0.4.

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Rafiq, Muhammad Hamid. "Experimental Studies and Modeling of Synthesis Gas Production and Fischer-Tropsch Synthesis." Doctoral thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-16572.

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Indirect route can be used to convert abundant natural resources such as natural gas (NG), coal and biomass to synthetic fuels (referred to as gas-to-liquid (GTL), coalto- liquid (CTL) and biomass-to-liquid (BTL)). It is currently one of the most effective solutions to the problem of finding suitable substitutes for liquid clean fuels. In this work, an investigation on the production of synthetic fuel from gaseous hydrocarbons (HCs)/bio-HCs and liquid bio-HCs on a small-scale unit has been carried out. The research project consists of two major parts, a modified version of a plasma-assisted catalytic partial oxidation (CPO) gliding arc (GlidArc) reactor and a thermally stable single-tube fixed-bed Fischer−Tropsch (FT) reactor. The potential for the CPO of methane to produce synthesis gas (syngas) was studied both experimentally and thermodynamically at a fixed pressure (1 bar) and electric power (0.3 kW). The investigations were performed in a partially adiabatic plasma-assisted (nonthermal) GlidArc reactor, using a Ni-based catalyst. Two cases were studied: in the first, normal air (molar ratio of O2/N2=21/79) was used, whereas enriched air (O2/N2=40/60) was utilized in the second. The individual effect of the O2/CH4 molar ratio, gas hour space velocity (GHSV) and bed exiting temperature (Texit) was studied for both cases. The main trends of the CH4 conversion, the syngas (H2 and CO) yield and the thermal efficiency of the reactor based on the lower heating value (LHV) were analyzed and compared. A numerical investigation of the CPO of methane to syngas using a GlidArc reactor was also studied. A 2D heterogeneous plug-flow model with radial dispersion and no gradients inside the catalyst pellet are used, including the transport equations for the gas and solid phase and reaction rate equations. The governing equations of this model formed a set of stationary differential algebraic equations coupled with the non-linear algebraic equations, and were solved numerically using in-house MATLAB code. Model results of CPO of methane were compared to previous experimental data with the GlidArc reactor found in the literature. A close match between the calculated and experimental results for temperature, reactant (CH4 and O2) conversion, H2 and CO yields and species molefraction were obtained. The developed model was extended to predict and quantify the influence of the GHSV as well as determine the influence of the reactor energy density (RED), the O2/CH4 molar ratio and the O2/N2 molar ratio. The predicted behaviors for the species mole-fraction, reactants conversion, H2 and CO yields and temperature along the length of the reactor have been analyzed. Furthermore, FT synthesis of a model biosyngas (33% H2, 17% CO and 50% N2) in a single tube fixed-bed FT reactor was investigated. The FT reactor consisted of a shell and tube with high-pressure boiling water circulating throughout the shell. A spherical unpromoted cobalt catalyst was used with the following reaction conditions: a wall temperature of 473 K, a pressure of 20 bars and a GHSV of 37 to 180 NmL/(gcat.h). The performance of the FT reactor was also validated by developing a 2D pseudo-homogeneous model that includes transport equations and reaction rate equations. Good agreement between the model predictions and experimental results were obtained. This developed model was extended to predict and quantify the influence of the FT kinetics as well as determine the influence of the tube diameter and the wall temperature. The predicted behaviors for CO and H2 conversion, productivity of HCs (mainly CH4 and C5 +) and fluid temperature along the axis of the reactor have been analyzed. In addition, the initial tests results are presented for the conversion of waste cookingoil (WCO) to biosyngas by CPO over a granular Ni-based catalyst. Additionally, autothermalreforming (ATR) of propane with water and normal air was also carried out.The investigations were performed in a partially adiabatic plasma-assisted (non-thermal)GlidArc reactor at fixed pressure (1 bar) and electric power (0.3 kW). Detailed axial temperaturedistributions, product concentrations, reactant conversions, H2 and CO yield,H2/CO ratio and thermal efficiency, as a function of the cold and hot WCO flow rate, thewater flow rate and the time on stream were studied. Propane and normal air were usedas oxidizing components to maintain autothermal operation. Finally, an investigation of the influence of process conditions on the production ofsyngas from model biogas (molar ratio of CH4/CO2=60/40) through partial oxidationover a granular Ni-based catalyst was explored. The investigations were performed in apartially adiabatic plasma-assisted (non-thermal) GlidArc reactor in a transitional flowregime at a fixed pressure (1 bar) and electric power (0.3 kW). The emphasis of this investigationwas on an experimental study and a comparative thermodynamic analysis. Theequilibrium compositions were calculated using a Lagrange multiplier and resulted in thedevelopment of systems of non-linear algebraic equations, which were solved numericallyusing the MATLAB function “fmincon”. Two cases were studied: normal air (molar ratioof O2/N2=21/79) and enriched air (O2/N2=40/60). The individual effects of the O2/CH4molar ratio and the Texit were studied in both cases. The main trends of the CH4 conversion,the syngas yield, the H2/CO ratio and the thermal efficiency of the reactor wereanalyzed.

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Books on the topic "Synthesis gas"

1

Yannick, Vallée, ed. Gas phase reactions in organic synthesis. Amsterdam, The Netherlands: Gordon and Breach, 1997.

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Granqvist, Claes, Laszlo Kish, and William Marlow, eds. Gas Phase Nanoparticle Synthesis. Dordrecht: Springer Netherlands, 2004. http://dx.doi.org/10.1007/978-1-4020-2444-3.

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G, Granqvist Claes, Kish Laszlo B, and Marlow W. H, eds. Gas phase nanoparticle synthesis. Dordrecht: Kluwer Academic Publishers, 2004.

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Huttel, Yves, ed. Gas-Phase Synthesis of Nanoparticles. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2017. http://dx.doi.org/10.1002/9783527698417.

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C, Lieuwen Timothy, Yang Vigor, and Yetter Richard A. 1952-, eds. Synthesis gas combustion: Fundamentals and applications. Boca Raton: CRC Press, 2010.

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Adorjan, Kurucz, and Bencik Izsak, eds. Syngas production methods, post treatment, and economics. Hauppauge, NY, USA: Nova Science Publishers, 2009.

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Kurucz, Adorjan. Syngas production methods, post treatment, and economics. Hauppauge, NY, USA: Nova Science Publishers, 2009.

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Geider, Richard J. Algal photo-synthesis. New York: Chapman and Hall, 1992.

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Richards, David Gareth. Synthesis gas conversion to oxygenates using rhodium catalysts. Uxbridge: Brunel University, 1985.

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Albritton, Daniel L. (Daniel Lee), 1936-, Intergovernmental Panel on Climate Change. Working Group I., Intergovernmental Panel on Climate Change. Working Group II, and Intergovernmental Panel on Climate Change. Working Group III, eds. Climate change 2001: Synthesis report. Geneva, Switzerland]: [Intergovernmental Panel on Climate Change], 2001.

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Book chapters on the topic "Synthesis gas"

1

Keim, W. "Synthesis Gas." In ACS Symposium Series, 1–16. Washington, DC: American Chemical Society, 1987. http://dx.doi.org/10.1021/bk-1987-0328.ch001.

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Lloyd, Lawrie. "Synthesis Gas." In Handbook of Industrial Catalysts, 351–95. Boston, MA: Springer US, 2011. http://dx.doi.org/10.1007/978-0-387-49962-8_9.

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Dahmen, N., E. Henrich, and T. Henrich. "Synthesis Gas Biorefinery." In Advances in Biochemical Engineering/Biotechnology, 217–45. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/10_2016_63.

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Winterer, Markus. "Gas Phase Synthesis." In Nanocrystalline Ceramics, 7–33. Berlin, Heidelberg: Springer Berlin Heidelberg, 2002. http://dx.doi.org/10.1007/978-3-662-04976-1_2.

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Sahebdelfar, Saeed, Maryam Takht Ravanchi, and Ashok Kumar Nadda. "Synthesis Gas Chemistry." In C1 Chemistry, 131–64. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/9781003279280-5.

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Tremblay, Alain, Louis Varfalvy, Charlotte Roehm, and Michelle Garneau. "Synthesis." In Greenhouse Gas Emissions — Fluxes and Processes, 637–59. Berlin, Heidelberg: Springer Berlin Heidelberg, 2005. http://dx.doi.org/10.1007/978-3-540-26643-3_27.

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Lutic, Doina, Mehri Sanati, and Anita Lloyd Spetz. "Gas Sensors." In Synthesis, Properties, and Applications of Oxide Nanomaterials, 411–50. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2006. http://dx.doi.org/10.1002/9780470108970.ch15.

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Marlow, William H. "Van der Waals Energies in the Formation and Interaction of Nanoparticle Aggregates." In Gas Phase Nanoparticle Synthesis, 1–27. Dordrecht: Springer Netherlands, 2004. http://dx.doi.org/10.1007/978-1-4020-2444-3_1.

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Naruse, Fumio, Seiichiro Kashu, and Chikara Hayashia. "Effect of Thermoporesis on 10-NM-Diameter Nanoparticles in Gas Flow Inside a Tube." In Gas Phase Nanoparticle Synthesis, 29–42. Dordrecht: Springer Netherlands, 2004. http://dx.doi.org/10.1007/978-1-4020-2444-3_2.

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Altman, Igor S., Peter V. Pikhitsa, and Mansoo Choi. "Key Effects in Nanoparticle Formation by Combustion Techniques." In Gas Phase Nanoparticle Synthesis, 43–67. Dordrecht: Springer Netherlands, 2004. http://dx.doi.org/10.1007/978-1-4020-2444-3_3.

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Conference papers on the topic "Synthesis gas"

1

Aslanov, Sh, A. Buxorov, and N. Fayzullaev. "CATALYTIC SYNTHESIS OF SYNTHESIS GAS FROM METHANE." In MODALITĂȚI CONCEPTUALE DE DEZVOLTARE A ȘTIINȚEI MODERNE. European Scientific Platform, 2020. http://dx.doi.org/10.36074/20.11.2020.v2.02.

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Li, Xiaohong, Kenji Asami, Mengfei Luo, Keisuke Michigi, Kaoru Fujimoto, Noritatsu Tsubaki, and Tokuta Inoue. "Direct synthesis of middle isoparaffins from synthesis gas." In 2003 JSAE/SAE International Spring Fuels and Lubricants Meeting. 400 Commonwealth Drive, Warrendale, PA, United States: SAE International, 2003. http://dx.doi.org/10.4271/2003-01-1941.

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Zhu, Lingjun, Shurong Wang, Yingying Zhu, Xiaolan Ge, Xinbao Li, and Zhongyang Luo. "Synthetic fuels and chemicals production from biomass synthesis gas." In 2010 International Conference on Mechanic Automation and Control Engineering (MACE). IEEE, 2010. http://dx.doi.org/10.1109/mace.2010.5535423.

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Agee, Mark A. "Gas to Liquids (GTL) Conversion: A New Option for Monetizing Natural Gas." In ASME 1997 Turbo Asia Conference. American Society of Mechanical Engineers, 1997. http://dx.doi.org/10.1115/97-aa-055.

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A new process for converting natural gas into liquid fuels and other petroleum products is described, as is the increased market opportunity this technology portends for gas turbine manufacturers. The GTL technology, developed by Syntroleum Corporation, utilizes Autothermal Reforming with air to produce a nitrogen-diluted synthesis gas having a near ideal ratio for converting into synthetic hydrocarbons via Fischer-Tropsch synthesis. A proprietary catalyst system achieves conversion rates comparable to conventional F-T processes without the need for recycling. This results in plant capital costs low enough to make conversion of remote and/or sub-quality gas into synthetic fuels economical at current oil prices. The process is energy self-sufficient and compact enough to be constructed in small sizes for plants in remote areas, including floating or platform facilities to utilize offshore gas reserves. It can also be scaled up for 50,000 BPD or larger applications.

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Sushil Adhikari and Sandun Fernando. "Hydrogen Separation from Synthesis Gas." In 2005 Tampa, FL July 17-20, 2005. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2005. http://dx.doi.org/10.13031/2013.19649.

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Bukhorov, A. Q., Sh Ch Aslanov, and N. I. Fayzullaev. "Kinetic laws of dimethyl ether synthesis in synthesis gas." In 2021 ASIA-PACIFIC CONFERENCE ON APPLIED MATHEMATICS AND STATISTICS. AIP Publishing, 2022. http://dx.doi.org/10.1063/5.0090209.

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Rebrov, A. K. "GAS-PHASE SYNTHESIS OF DIAMOND STRUCTURES." In 8TH INTERNATIONAL SYMPOSIUM ON NONEQUILIBRIUM PROCESSES, PLASMA, COMBUSTION, AND ATMOSPHERIC PHENOMENA. TORUS PRESS, 2020. http://dx.doi.org/10.30826/nepcap2018-2-01.

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The diamond synthesis from vapor (gas) phase is realized under complex influence of nonequilibrium transfer processes in activated gas mixtures by formation of carbon structures on a nascent diamond surface. The microwave plasma generates an active gas mixture and fragments of building material are transported

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Buyantuev, Sergey L., Stanislav Yu Shishulkin, Anatoly D. Alferov, Anatoly S. Kondratenko, and Andrey B. Khmelev. "DESIGNING AIR-GAS TORCHES FOR COMBUSTION OF THE SYNTHESIS GAS." In Innovative technologies in science and education. Buryat State University Publishing Department, 2015. http://dx.doi.org/10.18101/978-5-9793-0803-6-74-78.

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9

Feghali, Elias, Joey Abi Rizk, Layla Dina, and Rachid Klaimi. "Novel Reactor Design Strategies for Synthesis Gas Production from Natural Gas." In 2023 Fifth International Conference on Advances in Computational Tools for Engineering Applications (ACTEA). IEEE, 2023. http://dx.doi.org/10.1109/actea58025.2023.10194038.

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Dossumov, Kusman, Gaukhar Y. Yergaziyeva, Laura K. Myltykbayeva, Naukhan A. Asanov, Moldir M. Telbayeva, and E. M. Tulibayev. "Catalytic Conversion of Biogas to Synthesis Gas." In 10TH International Conference on Sustainable Energy and Environmental Protection. University of Maribor Press, 2017. http://dx.doi.org/10.18690/978-961-286-048-6.27.

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Reports on the topic "Synthesis gas"

1

Kamil Klier, Richard G. Herman, Alessandra Beretta, Maria A. Burcham, Qun Sun, Yeping Cai, and Biswanath Roy. Oxygenates vs. synthesis gas. Office of Scientific and Technical Information (OSTI), April 1999. http://dx.doi.org/10.2172/750374.

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2

Ackerson, M. D., E. C. Clausen, and J. L. Gaddy. Biological conversion of synthesis gas. Office of Scientific and Technical Information (OSTI), January 1993. http://dx.doi.org/10.2172/6728177.

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3

Klasson, K. T., R. Basu, E. R. Johnson, E. C. Clausen, and J. L. Gaddy. Biological conversion of synthesis gas. Office of Scientific and Technical Information (OSTI), March 1992. http://dx.doi.org/10.2172/6744576.

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Ackerson, M. D., E. C. Clausen, and J. L. Gaddy. Biological conversion of synthesis gas. Office of Scientific and Technical Information (OSTI), June 1992. http://dx.doi.org/10.2172/6873481.

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Clausen, E. C. Biological conversion of synthesis gas. Office of Scientific and Technical Information (OSTI), April 1993. http://dx.doi.org/10.2172/6484911.

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6

Steven F. Rice and David P. Mann. Autothermal Reforming of Natural Gas to Synthesis Gas. Office of Scientific and Technical Information (OSTI), April 2007. http://dx.doi.org/10.2172/902090.

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7

Kwang-Bok Yi, Anirban Mukherjee, Elizabeth J. Podlaha, and Douglas P. Harrison. HIGH EFFICIENCY DESULFURIZATION OF SYNTHESIS GAS. Office of Scientific and Technical Information (OSTI), March 2004. http://dx.doi.org/10.2172/833407.

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Kwang-Bok Yi, Elizabeth J. Podlaha, and Douglas P. Harrison. HIGH EFFICIENCY DESULFURIZATION OF SYNTHESIS GAS. Office of Scientific and Technical Information (OSTI), November 2003. http://dx.doi.org/10.2172/823018.

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Anirban Mukherjee, Kwang-Bok Yi, Elizabeth J. Podlaha, and Douglas P. Harrison. HIGH EFFICIENCY DESULFURIZATION OF SYNTHESIS GAS. Office of Scientific and Technical Information (OSTI), November 2001. http://dx.doi.org/10.2172/824753.

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Kwang-Bok Yi, Elizabeth J. Podlaha, and Douglas P. Harrison. HIGH EFFICIENCY DESULFURIZATION OF SYNTHESIS GAS. Office of Scientific and Technical Information (OSTI), November 2002. http://dx.doi.org/10.2172/824758.

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