Partial Oxidation and Autothermal Reforming of Methane for Hydrogen Production Using NiO-CoO/MgO Catalyst

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ISBN 13 :
Total Pages : pages
Book Rating : 4.:/5 (96 download)

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Book Synopsis Partial Oxidation and Autothermal Reforming of Methane for Hydrogen Production Using NiO-CoO/MgO Catalyst by : Tutuk Djoko Kusworo

Download or read book Partial Oxidation and Autothermal Reforming of Methane for Hydrogen Production Using NiO-CoO/MgO Catalyst written by Tutuk Djoko Kusworo and published by . This book was released on 2003 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Optimization of Partial Oxidation of Methane to Hydrogen Production Over NiO-CoO-MgO Solid Solution Catalyst Using Statistical Experimental Design

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ISBN 13 :
Total Pages : pages
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Book Synopsis Optimization of Partial Oxidation of Methane to Hydrogen Production Over NiO-CoO-MgO Solid Solution Catalyst Using Statistical Experimental Design by :

Download or read book Optimization of Partial Oxidation of Methane to Hydrogen Production Over NiO-CoO-MgO Solid Solution Catalyst Using Statistical Experimental Design written by and published by . This book was released on 2003 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Advances in Synthesis Gas: Methods, Technologies and Applications

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Publisher : Elsevier
ISBN 13 : 0323985211
Total Pages : 560 pages
Book Rating : 4.3/5 (239 download)

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Book Synopsis Advances in Synthesis Gas: Methods, Technologies and Applications by : Mohammad Reza Rahimpour

Download or read book Advances in Synthesis Gas: Methods, Technologies and Applications written by Mohammad Reza Rahimpour and published by Elsevier. This book was released on 2022-10-18 with total page 560 pages. Available in PDF, EPUB and Kindle. Book excerpt: Advances in Synthesis Gas: Methods, Technologies and Applications: Syngas Process Modelling and Apparatus Simulation consists of numerical modeling and simulation of different processes and apparatus for producing syngas, purifying it as well as synthesizing different chemical materials or generating heat and energy from syngas. These apparatus and processes include, but are not limited to, reforming, gasification, partial oxidation, swing technologies and membranes. Introduces numerical modeling and the simulation of syngas production processes and apparatus Describes numerical models and simulation procedures utilized for syngas purification processes and equipment Discusses modelling and simulation of processes using syngas as a source for producing chemicals and power

Autothermal Reforming of Methane to Hydrogen Production Over Cobalt-nickel Catalyst Supported MgO Solid Solution

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Total Pages : pages
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Book Synopsis Autothermal Reforming of Methane to Hydrogen Production Over Cobalt-nickel Catalyst Supported MgO Solid Solution by :

Download or read book Autothermal Reforming of Methane to Hydrogen Production Over Cobalt-nickel Catalyst Supported MgO Solid Solution written by and published by . This book was released on 2003 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Methane Conversion by Oxidative Processes

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Publisher : Springer Science & Business Media
ISBN 13 : 9401574499
Total Pages : 556 pages
Book Rating : 4.4/5 (15 download)

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Book Synopsis Methane Conversion by Oxidative Processes by : Wolf

Download or read book Methane Conversion by Oxidative Processes written by Wolf and published by Springer Science & Business Media. This book was released on 2013-11-11 with total page 556 pages. Available in PDF, EPUB and Kindle. Book excerpt: A reasonable case could be made that the scientific interest in catalytic oxidation was the basis for the recognition of the phenomenon of catalysis. Davy, in his attempt in 1817 to understand the science associated with the safety lamp he had invented a few years earlier, undertook a series of studies that led him to make the observation that a jet of gas, primarily methane, would cause a platinum wire to continue to glow even though the flame was extinguished and there was no visible flame. Dobereiner reported in 1823 the results of a similar investigation and observed that spongy platina would cause the ignition of a stream of hydrogen in air. Based on this observation Dobereiner invented the first lighter. His lighter employed hydrogen (generated from zinc and sulfuric acid) which passed over finely divided platinum and which ignited the gas. Thousands of these lighters were used over a number of years. Dobereiner refused to file a patent for his lighter, commenting that "I love science more than money." Davy thought the action of platinum was the result of heat while Dobereiner believed the ~ffect ~as a manifestation of electricity. Faraday became interested in the subject and published a paper on it in 1834; he concluded that the cause for this reaction was similar to other reactions.

Catalytic Partial Oxidation of Methane to Synthesis Gas Over Pt, MgO Catalysts

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Publisher :
ISBN 13 :
Total Pages : 382 pages
Book Rating : 4.:/5 (18 download)

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Book Synopsis Catalytic Partial Oxidation of Methane to Synthesis Gas Over Pt, MgO Catalysts by : Min Yang

Download or read book Catalytic Partial Oxidation of Methane to Synthesis Gas Over Pt, MgO Catalysts written by Min Yang and published by . This book was released on 2006 with total page 382 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Methane Conversion by Oxidative Processes

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Publisher : Springer
ISBN 13 :
Total Pages : 566 pages
Book Rating : 4.3/5 (91 download)

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Book Synopsis Methane Conversion by Oxidative Processes by : Eduardo E. Wolf

Download or read book Methane Conversion by Oxidative Processes written by Eduardo E. Wolf and published by Springer. This book was released on 1992 with total page 566 pages. Available in PDF, EPUB and Kindle. Book excerpt: A reasonable case could be made that the scientific interest in catalytic oxidation was the basis for the recognition of the phenomenon of catalysis. Davy, in his attempt in 1817 to understand the science associated with the safety lamp he had invented a few years earlier, undertook a series of studies that led him to make the observation that a jet of gas, primarily methane, would cause a platinum wire to continue to glow even though the flame was extinguished and there was no visible flame. Dobereiner reported in 1823 the results of a similar investigation and observed that spongy platina would cause the ignition of a stream of hydrogen in air. Based on this observation Dobereiner invented the first lighter. His lighter employed hydrogen (generated from zinc and sulfuric acid) which passed over finely divided platinum and which ignited the gas. Thousands of these lighters were used over a number of years. Dobereiner refused to file a patent for his lighter, commenting that "I love science more than money." Davy thought the action of platinum was the result of heat while Dobereiner believed the ~ffect ~as a manifestation of electricity. Faraday became interested in the subject and published a paper on it in 1834; he concluded that the cause for this reaction was similar to other reactions.

Natural Gas Conversion V

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Publisher : Elsevier
ISBN 13 : 0080537308
Total Pages : 1005 pages
Book Rating : 4.0/5 (85 download)

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Book Synopsis Natural Gas Conversion V by : A. Parmaliana

Download or read book Natural Gas Conversion V written by A. Parmaliana and published by Elsevier. This book was released on 1998-09-17 with total page 1005 pages. Available in PDF, EPUB and Kindle. Book excerpt: On January 1988, the ascertained and economically accessible reserves of Natural Gas (NG) amounted to over 144,000 billion cubic meters worldwide, corresponding to 124 billion tons of oil equivalents (comparable with the liquid oil reserves, which are estimated to be 138 billion TOE). It is hypothesized that the volume of NG reserve will continue to grow at the same rate of the last decade. Forecasts on production indicate a potential increase from about 2,000 billion cubic meters in 1990 to not more than 3,300 billion cubic meters in 2010, even in a high economic development scenario. NG consumption represents only one half of oil: 1.9 billion TOE/y as compared to 3.5 of oil. Consequently, in the future gas will exceed oil as a carbon atom source. In the future the potential for getting energetic vectors or petrochemicals from NG will continue to grow. The topics covered in Natural Gas Conversion V reflect the large global R&D effort to look for new and economic ways of NG exploitation. These range from the direct conversion of methane and light paraffins to the indirect conversion through synthesis gas to fuels and chemicals. Particularly underlined and visible are the technologies already commercially viable. These proceedings prove that mature and technologically feasible processes for natural gas conversion are already available and that new and improved catalytic approaches are currently developing, the validity and feasibility of which will soon be documented. This is an exciting area of modern catalysis, which will certainly open novel and rewarding perspectives for the chemical, energy and petrochemical industries.

Simulation of Millisecond Catalytic Partial Oxidation of Methane

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Publisher : LAP Lambert Academic Publishing
ISBN 13 : 9783659698415
Total Pages : 80 pages
Book Rating : 4.6/5 (984 download)

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Book Synopsis Simulation of Millisecond Catalytic Partial Oxidation of Methane by : Julie Flynn

Download or read book Simulation of Millisecond Catalytic Partial Oxidation of Methane written by Julie Flynn and published by LAP Lambert Academic Publishing. This book was released on 2015-04-21 with total page 80 pages. Available in PDF, EPUB and Kindle. Book excerpt: Hydrogen can be the key solution of all our energy needs in the future and to face climate change while reducing greenhouse gases. Syngas, H2 and CO, is industrially produced by steam reforming of methane. A potential alternative is the catalytic partial oxidation of methane. The process is fast, exothermic and auto-thermal.A dual sequential bed catalyst is used, which makes use of a combustion catalyst followed by a reforming catalyst in order to carry out catalytic partial oxidation in two steps.Numerical simulations using finite elements methods coupled with global kinetics are performed to have a better understanding of the transient process and the solid and gas temperature profiles in a catalyst. The results include temporal and spatial reactant conversion, product selectivity, and temperature profiles in the catalyst. Where possible simulation results are compared to experimental data. The model shows high yields of hydrogen from methane and air which fits the experimental results in most of the cases. It also fits qualitatively the transient results.

Encyclopedia of Chemical Processing and Design

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Publisher : CRC Press
ISBN 13 : 9780824726133
Total Pages : 556 pages
Book Rating : 4.7/5 (261 download)

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Book Synopsis Encyclopedia of Chemical Processing and Design by : John J. McKetta Jr

Download or read book Encyclopedia of Chemical Processing and Design written by John J. McKetta Jr and published by CRC Press. This book was released on 1997-11-11 with total page 556 pages. Available in PDF, EPUB and Kindle. Book excerpt: "Vent Collection System, Design and Safety to Viscosity-Gravity-Contrast, Estimation"

Natural Gas Conversion VI

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Publisher : Elsevier
ISBN 13 : 0080537316
Total Pages : 577 pages
Book Rating : 4.0/5 (85 download)

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Book Synopsis Natural Gas Conversion VI by : T.H. Fleisch

Download or read book Natural Gas Conversion VI written by T.H. Fleisch and published by Elsevier. This book was released on 2001-06-01 with total page 577 pages. Available in PDF, EPUB and Kindle. Book excerpt: This volume contains peer-reviewed manuscripts describing the scientific and technological advances presented at the 6th Natural Gas Conversion Sumposium held in Alaska in June 2001. This symposium continues the tradition of excellence and the status as the premier technical meeting in this area established by previous meetings. The 6th Natural Gas Conversion Symposium is conducted under the overall direction of the Organizing Committee. The Program Committee was responsible for the review, selection, editing of most of the manuscripts included in this volum. A standing International Advisory Board has ensured the effective long-term planning and the continuity and technical excellence of these meetings.

Hydrogen Production and Optimization of Methanol Partial Oxidation and Autothermal Reforming in a Spray Reactor

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ISBN 13 :
Total Pages : 73 pages
Book Rating : 4.:/5 (123 download)

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Book Synopsis Hydrogen Production and Optimization of Methanol Partial Oxidation and Autothermal Reforming in a Spray Reactor by : 蘇郁淇

Download or read book Hydrogen Production and Optimization of Methanol Partial Oxidation and Autothermal Reforming in a Spray Reactor written by 蘇郁淇 and published by . This book was released on 2020 with total page 73 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Catalytic Partial Oxidation of Methane in SCT Reactor with Rh and Ni Based Catalysts for Hydrogen Production

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ISBN 13 :
Total Pages : pages
Book Rating : 4.:/5 (955 download)

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Book Synopsis Catalytic Partial Oxidation of Methane in SCT Reactor with Rh and Ni Based Catalysts for Hydrogen Production by : Luigi Domenico Vella

Download or read book Catalytic Partial Oxidation of Methane in SCT Reactor with Rh and Ni Based Catalysts for Hydrogen Production written by Luigi Domenico Vella and published by . This book was released on 2011 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt:

Modelling and Experimental Study of Methane Catalytic Cracking as a Hydrogen Production Technology

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ISBN 13 :
Total Pages : 249 pages
Book Rating : 4.:/5 (827 download)

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Book Synopsis Modelling and Experimental Study of Methane Catalytic Cracking as a Hydrogen Production Technology by : Ashraf Mukhtar Lotfi Amin

Download or read book Modelling and Experimental Study of Methane Catalytic Cracking as a Hydrogen Production Technology written by Ashraf Mukhtar Lotfi Amin and published by . This book was released on 2011 with total page 249 pages. Available in PDF, EPUB and Kindle. Book excerpt: Production of hydrogen is primarily achieved via catalytic steam reforming, partial oxidation, and auto-thermal reforming of natural gas. Although these processes are mature technologies, they are somewhat complex and CO is formed as a by-product, therefore requiring a separation process if a pure or hydrogen-rich stream is needed. As an alternative method, supported metal catalysts can be used to catalytically decompose hydrocarbons to produce hydrogen. The process is known as catalytic cracking of hydrocarbons. Methane, the hydrocarbon containing the highest percentage of hydrogen, can be used in such a process to produce a hydrogen-rich stream. The decomposition of methane occurs on the surface of the active metal to produce hydrogen and filamentous carbon. As a result, only hydrogen is produced as a gaseous product, which eliminates the need of further separation processes to separate CO2 or CO. Nickel is commonly used in research as a catalyst for methane cracking in the 500-700C temperature range. To conduct methane catalytic cracking in a continuous manner, regeneration of the deactivated catalyst is required and circulation of the catalysts between cracking and regeneration cycles must be achieved. Different reactor designs have been successfully used in cyclic operation, such as a set of parallel fixed-bed reactors alternating between cracking and regeneration, but catalyst agglomeration due to carbon deposition may lead to blockage of the reactor and elevated pressure drop through the fixed bed. Also poor heat transfer in the fixed bed may lead to elevated temperature during the regeneration step when carbon is burned in air, which may cause catalyst sintering. A fluidized bed reactor appears as a viable option for methane catalytic cracking, since it would permit cyclic operation by moving the catalyst between a cracker and a regenerator. In addition, there is the possibility of using fine catalyst particles, which improves catalyst effectiveness. The aims of this project were 1) to develop and characterize a suitable nickel-based catalyst and 2) to develop a model for thermal catalytic decomposition of methane in a fluidized bed.

Biofuels

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Publisher : BoD – Books on Demand
ISBN 13 : 1789233461
Total Pages : 302 pages
Book Rating : 4.7/5 (892 download)

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Book Synopsis Biofuels by : Krzysztof Biernat

Download or read book Biofuels written by Krzysztof Biernat and published by BoD – Books on Demand. This book was released on 2018-07-11 with total page 302 pages. Available in PDF, EPUB and Kindle. Book excerpt: This book offers the current state of knowledge in the field of biofuels, presented by selected research centers from around the world. Biogas from waste production process and areas of application of biomethane were characterized. Also, possibilities of applications of wastes from fruit bunch of oil palm tree and high biomass/bagasse from sorghum and Bermuda grass for second-generation bioethanol were presented. Processes and mechanisms of biodiesel production, including the review of catalytic transesterification process, and careful analysis of kinetics, including bioreactor system for algae breeding, were widely analyzed. Problem of emissivity of NOx from engines fueled by B20 fuel was characterized. The closing chapters deal with the assessment of the potential of biofuels in Turkey, the components of refinery systems for production of biodegradable plastics from biomass. Also, a chapter concerning the environmental conditions of synthesis gas production as a universal raw material for the production of alternative fuels was also added.

Hydrogen Production from CO2 Reforming of Methane Over Cobalt-based Catalysts

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ISBN 13 :
Total Pages : 108 pages
Book Rating : 4.:/5 (953 download)

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Book Synopsis Hydrogen Production from CO2 Reforming of Methane Over Cobalt-based Catalysts by : Ji Siang Tan

Download or read book Hydrogen Production from CO2 Reforming of Methane Over Cobalt-based Catalysts written by Ji Siang Tan and published by . This book was released on 2015 with total page 108 pages. Available in PDF, EPUB and Kindle. Book excerpt: Increased concerns on anthropogenic greenhouse gas emissions have renewed interest in the CO2 (dry) reforming process as an alternative to steam reforming for synthesis gas production from natural gas. For hydrocarbon dry reforming, where the product stream H2:CO ratio is less than 3, synfuel production is more amenable and acceptable for downstream methanol and other oxygenated synthesis. However, dry reforming is highly endothermic, and suffers from carbon-induced catalyst deactivation. This thesis therefore investigates and evaluates the performance of methane dry reforming process at different operation conditions such as reaction temperature and feed composition, and the effects of loaded metals (Mo and Ni) on alumina-supported Co-based catalyst. Runs of the methane dry reforming experiment were conducted in a computer-controlled fixebed reactor at different feed compositions and reaction temperature. Both MoO3 and NiO phases were formed during wetness co-impregnation with a mixture of deionized water and alumina support as measured in X-ray diffraction. Temperature-programmed calcination showed that the transformations from MoO3 to CoMoO4 phase and NiO to NiAl2O4 phase were a 2 step process involving the formation of an oxidation intermediate form. Calcination of co-impregnated catalysts at 500 0C for 5 h appeared to be optimal preparation condition for H2 selectivity. Al2O3 support was the best support to give the highest H2 to CO ratio. Second metal promotion did not alter reaction rate significantly. However the interaction of loaded metal oxides with the surface carbonaceous species resulted in substantially reduced carbon deposition on Co-based catalyst, with Ni providing the greatest coking resistance compared to Mo. A quantitative relationship between activation energy and feed composition of CO2:CH4 ( 1:1, 2:1 and 3:1 ) as well as reaction temperatures (923 K, 953 K and 973 K) was obtained over bimetallic 5%Ni-10%Co/Al2O3 catalyst which gave the highest value of H2/CO ratio in the methane dry reforming process. Methane dry reforming activity was stable with time-on-stream for 4 h.

Environmental Challenges and Greenhouse Gas Control for Fossil Fuel Utilization in the 21st Century

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Publisher : Springer Science & Business Media
ISBN 13 : 9780306473364
Total Pages : 464 pages
Book Rating : 4.4/5 (733 download)

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Book Synopsis Environmental Challenges and Greenhouse Gas Control for Fossil Fuel Utilization in the 21st Century by : M. Mercedes Maroto-Valer

Download or read book Environmental Challenges and Greenhouse Gas Control for Fossil Fuel Utilization in the 21st Century written by M. Mercedes Maroto-Valer and published by Springer Science & Business Media. This book was released on 2002-08-31 with total page 464 pages. Available in PDF, EPUB and Kindle. Book excerpt: As we are moving ahead into the 21st century, our hunger for cost effective and environmentally friendly energy continues to grow. The Energy Information Administration of US has forecasted that only in the first two decades of the 21st century, our energy demand will increase by 60% compared to the levels at the end of the 20th century. Fossil fuels have been traditionally the major primary energy sources worldwide, and their role is expected to continue growing for the forecasted period, due to their inherent cost competitiveness compared to non-fossil fuel energy sources. However, the current fossil energy scenario is undergoing significant transformations, especially to accommodate increasingly stringent environmental challenges of contaminants like sulfur dioxide, nitrogen oxides or mercury, while still providing affordable energy. Furthermore, traditional fossil fuel utilization is inherently plagued with greenhouse gas emissions from combustion, especially carbon dioxide from stationary sources as well as from mobile sources. Should worldwide government policies dictate a reduction of greenhouse gas emissions, such as proposed by the Kyoto Protocol and the implementation of carbon taxes, fossil fuels would lose their significant competitive appeal in favor of nuclear energy and renewable energy sources. However, the current non-fossil fuel energy share of the worldwide energy market is merely below 15%, and therefore, it is more likely that fossil fuel energy producers would adapt to the new requirements by developing and implementing emission control technologies, and emission trades among other strategies.