Relevant bibliographies by topics / Catalytic hydrogenation of CO2̲

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Catalytic hydrogenation of CO2̲'

Author: Grafiati
Published: 4 June 2021
Last updated: 5 February 2022

Create a spot-on reference in APA, MLA, Chicago, Harvard, and other styles

Select a source type:

Consult the lists of relevant articles, books, theses, conference reports, and other scholarly sources on the topic 'Catalytic hydrogenation of CO2̲.'

Next to every source in the list of references, there is an 'Add to bibliography' button. Press on it, and we will generate automatically the bibliographic reference to the chosen work in the citation style you need: APA, MLA, Harvard, Chicago, Vancouver, etc.

You can also download the full text of the academic publication as pdf and read online its abstract whenever available in the metadata.

Journal articles on the topic "Catalytic hydrogenation of CO2̲"

1

Spadaro, Lorenzo, Alessandra Palella, and Francesco Arena. "Totally-green Fuels via CO2 Hydrogenation." Bulletin of Chemical Reaction Engineering & Catalysis 15, no. 2 (April 23, 2020): 390–404. http://dx.doi.org/10.9767/bcrec.15.2.7168.390-404.

Full text
Abstract:
Hydrogen is the cleanest energy vector among any fuels, nevertheless, many aspects related to its distribution and storage still raise serious questions concerning costs, infrastructure and safety. On this account, the chemical storage of renewable-hydrogen by conversion into green-fuels, such as: methanol, via CO2 hydrogenation assumes a role of primary importance, also in the light of a cost-to-benefit analysis. Therefore, this paper investigates the effects of chemical composition on the structural properties, surface reactivity and catalytic pathway of ternary CuO-ZnO-CeO2 systems, shedding light on the structure-activity relationships. Thus, a series of CuZnCeO2 catalysts, at different CuO/CeO2 ratio (i.e. 0.2-1.2) were performed in the CO2 hydrogenation reactions at 20 bar and 200-300 °C, (GHSV of 4800 STP L∙kg∙cat-1∙h-1). Catalysts were characterized by several techniques including X-ray Diffraction (XRD), N2-physisorption, single-pulse N2O titrations, X-ray Photoelectron Spectroscopy (XPS), and Temperature-programmed Reduction with H2 (H2-TPR). Depending on preparation method, the results clearly diagnostics the occurrence of synergistic structural-electronic effects of cerium oxide on copper activity, with an optimal 0.5 copper-to-cerium content. The rise of CuO loading up to 30% drives to a considerable increase of hydrogenation activity: C2Z1-C catalyst obtains the best catalytic performance, reaching methanol yield value of 12% at 300 °C. Catalyst activity proceeds according to volcano-shaped relationships, in agreement with a dual sites mechanism. Copyright © 2020 BCREC Group. All rights reserved
APA, Harvard, Vancouver, ISO, and other styles
2

Tagiyeva, Sh F., and E. H. Ismailov. "HETEROGENEOUS CATALYTIC HYDROGENATION OF CARBON DIOXIDE INTO HYDROCARBONS: ACHIEVEMENTS AND PROSPECTS." Chemical Problems 18, no. 4 (2020): 485–500. http://dx.doi.org/10.32737/2221-8688-2020-4-485-500.

Full text
Abstract:
The works published over the past 10 years on the catalytic hydrogenation of carbon dioxide into methane and C2+ hydrocarbons are considered. The choice of catalysts based on their elemental and phase composition, structural-porous characteristics, grain-size and acidic properties, the reaction mechanism and problems and prospects for the industrial application of heterogeneous catalytic conversion of CO2 to hydrocarbons are discussed.
APA, Harvard, Vancouver, ISO, and other styles
3

Qaderi, Jawed. "A brief review on the reaction mechanisms of CO2 hydrogenation into methanol." International Journal of Innovative Research and Scientific Studies 3, no. 2 (May 11, 2020): 33–40. http://dx.doi.org/10.53894/ijirss.v3i2.31.

Full text
Abstract:
The catalytic reduction of CO2 to methanol is an appealing option to reduce greenhouse gas concentration as well as renewable energy production. In addition, the exhaustion of fossil fuel, increase in earth temperature and sharp increases in fuel prices are the main driving factor for exploring the synthesis of methanol by hydrogenating CO2. Many studies on the catalytic hydrogenation of CO2 to methanol were published in the literature over the last few decades. Many of the studies have presented different catalysts having high stability, higher performance, low cost, and are immediately required to promote conversion. Understanding the mechanisms involved in the conversion of CO2 is essential as the first step towards creating these catalysts. This review briefly summarizes recent theoretical developments in mechanistic studies focused on using density functional theory, kinetic Monte Carlo simulations, and microkinetics modeling. Based on these simulation techniques on different transition metals, metal/metal oxide, and other heterogeneous catalysts surfaces, mainly, three important mechanisms that have been recommended are the formate (HCOO), reverse water–gas shift (RWGS), and trans-COOH mechanisms. Recent experimental and theoretical efforts appear to demonstrate that the formate route in which the main intermediate species is H2CO* in the reaction route, is more favorable in catalytic hydrogenation of CO2 to chemical fuels in various temperature and pressure conditions.
APA, Harvard, Vancouver, ISO, and other styles
4

Srivastava, Vivek. "Hydrotalcite Anchored Ruthenium Catalyst for CO2 Hydrogenation Reaction." Letters in Organic Chemistry 16, no. 5 (April 1, 2019): 396–408. http://dx.doi.org/10.2174/1570178615666180816120058.

Full text
Abstract:
We developed a series of new hydrotalcite functionalized Ru catalytic system to synthesize formic acid via CO2 hydrogenation reaction. Advance analytical procedures like FTIR, N2 physisorption, ICP-OES, XPS, and TEM analysis were applied to understand the physiochemical nature of functionalized hydrotalcite materials. This well-analyzed system was used as catalysts for CO2 hydrogenation reaction (with and without ionic liquid medium). Ru metal containing functionalized hydrotalcite materials were found highly active catalysts for formic acid synthesis via hydrogenation reaction. The concern of catalyst stability was studied via catalysts leaching and recycling experiments. We recycled the ionic liquid mediated functionalized hydrotalcite catalytic system up to 8 runs without any significant loss of catalytic activity. Surprisingly, no sign of catalyst leaching was recorded during the catalyst recycling experiment.
APA, Harvard, Vancouver, ISO, and other styles
5

Jia, Miao Yao, Wen Gui Gao, Hua Wang, and Yu Hao Wang. "Effect of Silica Promoter on Performance of CuO-ZnO-ZrO2 Catalyst for Methanol Synthesis from CO2 Hydrogenation." Applied Mechanics and Materials 556-562 (May 2014): 117–22. http://dx.doi.org/10.4028/www.scientific.net/amm.556-562.117.

Full text
Abstract:
Various CuO-ZnO-ZrO2(CZZ) catalysts for methanol synthesis from CO2 hydrogenation were prepared by co-precipitation method. Small amount of silica was incorporated into CZZ catalyst to produce these modified ternary CZZ catalysts. The effects of silica on physicochemical and catalytic properties were studied by TG-DTG,XRD,BET,N2O chemisorption,H2-TPR,NH3-TPD and CO2-TPD techniques. The results show that the properties of catalysts were strongly influenced by the content of SiO2 used as promoter. The catalytic performance for methanol synthesis from CO2 hydrogenation was evaluated. The test results show that the CZZ catalyst modified with 4 wt.% SiO2 exhibits an optimum catalytic activity. The silica improves the dispersion of CuO and its modified CZZ catalysts exhibits higher specific surface area, which were confirmed to be responsible for excellent performance of the catalysts for methanol synthesis from CO2 hydrogenation.
APA, Harvard, Vancouver, ISO, and other styles
6

Choi, Jonghoon, and Yunho Lee. "Catalytic hydrogenation of CO2 at a structurally rigidified cobalt center." Inorganic Chemistry Frontiers 7, no. 9 (2020): 1845–50. http://dx.doi.org/10.1039/c9qi01431d.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Li, Yong, Zheng Wang, and Qingbin Liu. "Progress in Homogeneous Catalytic Hydrogenation of CO2." Chinese Journal of Organic Chemistry 37, no. 8 (2017): 1978. http://dx.doi.org/10.6023/cjoc201702038.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Stephenson, Phil, Peter Licence, Stephen K. Ross, and Martyn Poliakoff. "Continuous catalytic asymmetric hydrogenation in supercritical CO2." Green Chemistry 6, no. 10 (2004): 521. http://dx.doi.org/10.1039/b411955j.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

ERDOHELYI, A. "Catalytic hydrogenation of CO2 over supported palladium." Journal of Catalysis 98, no. 1 (March 1986): 166–77. http://dx.doi.org/10.1016/0021-9517(86)90306-4.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Kovaleva, Anastasiya. "Selectivity regulation of perovskite-based iron-manganese catalysts for the synthesis of light olefins from CO, CO2 and H2." Farmacevticheskoe delo i tehnologija lekarstv (Pharmacy and Pharmaceutical Technology), no. 2 (April 1, 2020): 8–23. http://dx.doi.org/10.33920/med-13-2002-01.

Full text
Abstract:
There is a solution to prevent global problems caused due to carbon dioxide increase in planet atmosphere – reuse of CO2 in hydrogenation reaction. Literature analysis provides information about catalytic conversion of synthesis gas and carbon dioxide to carbohydrates in modern catalytic systems. Actual investigation of catalytic properties in GdFeO3 and GdMnO3 systems with perovskite structure has been carried out in the joint hydrogenation of carbon mono- and dioxide. Scientific novelty of research is to determine influence of the catalyst composition and reaction medium composition on the selectivity of target products.
APA, Harvard, Vancouver, ISO, and other styles
More sources

Dissertations / Theses on the topic "Catalytic hydrogenation of CO2̲"

1

Namijo, S. N. "Carbon dioxide hydrogenation over supported metal catalysts." Thesis, Brunel University, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.379411.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

ELHUSSIEN, HUSSIEN Eldod. "NON- CATALYTIC TRANSFER HYDROGENATION IN SUPERCRITICAL CO2 FOR COAL LIQUEFACTION." OpenSIUC, 2014. https://opensiuc.lib.siu.edu/theses/1409.

Full text
Abstract:
This thesis presents the results of the investigation on developing and evaluating a low temperature (<150oC) non - catalytic process using a hydrogen transfer agent (instead of molecu-lar hydrogen) for coal dissolution in supercritical CO2. The main idea behind the thesis was that one hydrogen atom from water and one hydrogen atom from the hydrogen transfer agent (HTA) were used to hydrogenate the coal. The products of coal dissolution were non-polar and polar while the supercritical CO2, which enhanced the rates of hydrogenation and dissolution of the non-polar molecules and removal from the reaction site, was non-polar. The polar modifier (PM) for CO2 was added to the freed to aid in the dissolution and removal of the polar components. The addition of a phase transfer agent (PTA) allowed a seamless transport of the ions and by-product between the aqueous and organic phases. DDAB, used as the PTA, is an effective phase transfer catalyst and showed enhancement to the coal dissolution process. COAL + DH- +H2O  COAL.H2 + DHO-- This process has a great feature due to the fact that the chemicals were obtained without requir-ing to first convert coal to CO and H2 units as in indirect coal liquefaction. The experiments were conducted in a unique reactor set up that can be connected through two lines. one line to feed the reactor with supercritical CO2 and the other connected to gas chromatograph. The use of the supercritical CO2 enhanced the solvent option due to the chemical extraction, in addition to the low environmental impact and energy cost. In this thesis the experiment were conducted at five different temperatures from atmos-pheric to 140°C, 3000 - 6000 psi with five component of feed mixture, namely water, HTA, PTA, coal, and PM in semi batch vessels reactor system with a volume of 100 mL. The results show that the chemicals were obtained without requiring to first convert coal to CO and H2 units as in indirect coal liquefaction. The results show that the conversion was found to be 91.8% at opti-mum feed mixtures values of 3, 1.0 and 5.4 for water: PM, HTA: coal, water: coal respectively. With the oil price increase and growing in energy demand, the coal liquefaction remain afforda-ble and available energy alternative.
APA, Harvard, Vancouver, ISO, and other styles
3

Afonso, Joana da Costa Franco. "Catalytic hydrogenation of carbon dioxide to form methanol and methane." Master's thesis, Faculdade de Ciências e Tecnologia, 2013. http://hdl.handle.net/10362/10854.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Gaikwad, Rohit. "Carbon Dioxide To Methanol: Stoichiometric Catalytic Hydrogenation Under High Pressure Conditions." Doctoral thesis, Universitat Rovira i Virgili, 2018. http://hdl.handle.net/10803/586089.

Full text
Abstract:
El CO2 en la atmósfera aumenta a raíz del empleo de combustibles fósiles. La hidrogenación de CO2 ofrece una ruta única para transformar esta molécula en productos químicos o combustibles como el metanol. El uso de alta presión en el ratio CO2:H2 = 1:>3 permite incrementar la cinética de la reacción, alcanzando así la conversión termodinámica como ya se ha reportado. No obstante, el mayor inconveniente del mencionado proceso es el tratamiento del hidrógeno sin reaccionar. Por ello, se evaluaron las ventajas de realizar la reacción a alta presión en condiciones estequiométricas (CO2:H2=1:3) examinando diferentes parámetros. Una vez optimizados, se alcanzó el límite termodinámico y se obtuvo un valor de conversión de CO2 cercano al 90% con una selectividad para metanol > 95% a 280 °C y 442 bar empleando Cu/ZnO/AlO3 como catalizador. Al minimizar las limitaciones de transferencia de masa, el rendimiento fue de 15.6 gMeOH gcat-1 h-1, aproximadamente un orden de magnitud mayor comparado con los de bibliografía. Adicionalmente, los mecanismos de la reacción en condiciones de alta presión se estudiaron mediante análisis espacial de la fase gas por CG y espectroscopía Raman. El estudio mostró que el CO2 se convierte directamente a metanol a baja temperatura, mientras que a alta temperatura la reacción water-gas shift es predominante generando CO, que produce metanol posteriormente. estructura core-shell. Este material mostró un recubrimiento uniforme del ZnO en los cores de Cu, y el espesor del shell se optimizó. Dichos nanomateriales mostraron alta actividad catalítica, útil para comprender la interacción entre Cu y Zn y en concreto, las exclusivas fases de Zn formadas durante la reacción a alta presión mediante operando DRX a alta presión.
Carbon dioxide concentration in the atmosphere is continuously increasing as a consequence of the combustion of fossil fuels. CO2 hydrogenation offers a unique path to transform the chemically stable CO2 to useful chemicals or fuel such as methanol. High-pressure advantages under over-stoichiometric CO2:H2 ratio (1:>3) has been reported previously by drastically increasing the reaction kinetics and even reaching the thermodynamic conversion. However, the major drawback of such processes is the treatment of unreacted hydrogen. Reflecting this background, the advantages of the high pressure approach in stoichiometric CO2:H2 (1:3) ratio were critically evaluated by examining different reaction and process parameters. When optimized, we could reach the thermodynamic limit and obtained about 90% CO2 conversion with >95% methanol selectivity at 280 °C and 442 bar using Cu/ZnO/Al2O3 catalyst. When the mass transfer limitation was minimized, an outstanding weight time yield was achieved with 15.6 gMeOH gcat-1 h-1, which is about one order of magnitude higher than the state-of-the-art values. Furthermore, the reaction mechanisms under high-pressure reaction conditions were studied by spatially-resolved gas phase analysis through the axial direction of the catalytic reactor by GC and Raman spectroscopy.
APA, Harvard, Vancouver, ISO, and other styles
5

Hasan, Tanvir. "NON-CATALYTIC TRANSFER HYDROGENATION IN SUPERCRITICAL CO2 FOR COAL LIQUEFACTION AND GRAPHENE EXTRACTION." OpenSIUC, 2015. https://opensiuc.lib.siu.edu/theses/1742.

Full text
Abstract:
The paper discusses a two-step process for the simultaneous extraction of graphene quantum dots and chemicals. The two steps are sequential structure disruption by supercritical CO2 explosion followed by a low temperature (120oC), non-catalytic transfer hydrogenation in supercritical CO2. The key idea of this research is, one hydrogen atom from hydrogen transfer agent (HTA) one hydrogen atom from water is used to hydrogenate the coal. The use of supercritical CO2 enhances the rate of hydrogenation, helps in dissolution of non-polar molecules and removal from the reaction site. The coal dissolution products are polar and non-polar. A phase transfer agent (PTA) allows seamless transport of the ions and byproduct between the aqueous and organic phases. A polar modifier (PM) for CO2 has been added to aid in the dissolution and removal of the polar components. The effect of feed conditions on the liquefaction process has been investigated. The response metrics considered were the conversion of coal and the yields of various organic classes such as ketones, alkanes, alkenes, aliphatic acids, alcohols, amines, aromatics and aromatic oxygenates. Ketones were found to be the major constituent of the products. Graphene quantum dots were also extracted.
APA, Harvard, Vancouver, ISO, and other styles
6

Bansode, Atul Baban. "Exploiting high pressure advantages in catalytic hydrogenation of carbon dioxide to methanol." Doctoral thesis, Universitat Rovira i Virgili, 2014. http://hdl.handle.net/10803/135008.

Full text
Abstract:
The aim of this thesis was to develop highly efficient CO2 hydrogenation process towards methanol by making use of high pressure approach. A high pressure lab scale plant was developed to conduct CO2 hydrogenation up to 400 bar. High pressure and low temperature were found to be the favourable conditions to excellent catalytic activity. Improved reaction performance towards methanol synthesis and reverse water-gas shift reaction was observed for the Ba and K promoted Cu/Al2O3 catalysts, respectively. Almost complete one-pass conversion of CO2 into methanol was observed under optimized process conditions over coprecipitated Cu/ZnO/Al2O3 catalysts. One-step transformation of CO2 into dimethyl ether was achieved with excellent catalytic activity. Selective formation of alkane or alkene was obtained by varying pressure of the secondary reactor coupled with methanol synthesis reactor. A high pressure, high temperature capillary cell for in-situ XAS was developed having capability for combined XAFS-Raman experiments under high pressure conditions.
El propòsit d’aquesta tesis va ser desenvolupar un procés altament eficient per a la hidrogenació de CO2 a metanol, mitjançant l’ús de micro-reactors d’alta pressió. Una planta d’alta pressió va ser desenvolupada per a dur a terme la hidrogenació de CO2 fins a 400 bar. Una millora en el rendiment de la reacció cap a la síntesis de metanol i cap a la reacció inversa del desplaçament del gas d’aigua va ser observada per als catalitzadors de Cu/Al2O3 promocionats amb Ba i K, respectivament. Conversió, gairebé completa de CO2 a metanol, en una etapa, va ser observada en les condicions de procés optimitzades utilitzant catalitzadors de Cu/ZnO/Al2O3. Transformació de CO2 a dimetil-èter, alcans i alquens en una sola etapa de reacció, tot mantenint la conversió de CO2 elevada. Una cel•la capil•lar d’alta pressió i alta temperatura, per a mesures espectroscòpiques de raig-X in-situ, va ser desenvolupada.
APA, Harvard, Vancouver, ISO, and other styles
7

Parent, John Scott. "Catalytic hydrogenation of butadiene copolymers." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1997. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp04/nq21378.pdf.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Willoughby, Christopher Alan. "Catalytic hydrogenation using titanium complexes." Thesis, Massachusetts Institute of Technology, 1995. http://hdl.handle.net/1721.1/11382.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Yu, Jinquan. "Mechanistic investigation into catalytic hydrogenation." Thesis, University of Cambridge, 2000. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.621759.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Sutherland, Luke Malcolm. "Catalytic mild hydrogenation of pygas." Thesis, University of Glasgow, 2018. http://theses.gla.ac.uk/8687/.

Full text
Abstract:
In the production of ethylene and propylene via steam cracking, one of the major by-products is pygas. This mixture has a high octane number, owing to the large quantity of aromatics, diolefins, and olefins present within this mixture. This stream contains, in particular, a significant quantity of benzene and toluene. This is a waste product, but is currently heavily utilised for the extraction of benzene, mainly in order to produce styrene, cumene, and cyclohexane. While the demand for these compounds will continue to increase, the usage of pygas products will decrease in terms of its other main use, as a petrol additive, due to the increasingly strict regulation regarding the total allowable content of aromatics in fuel. When attempting to refine pygas for use as an aromatic chemical feedstock, the most common method of purification is to perform a hydrocracking reaction. Reactions will usually be carried out in two steps; the first is to hydrogenate the diolefins and styrene over, typically, a Pd-alumina catalyst under mild conditions. The second stage involves hydrogenating olefins, removing sulfur compounds by converting them into H2S, acid-catalysed ring opening of napthenics, and cracking paraffins. The aim of this research was to perform an analysis of the effect of reaction mixture on the retention of benzene when passed over an industrially-used bifunctional metal/zeolite hydrocracking catalyst, and to analyse the carbon laydown and other relevant effects produced by altering the reaction mixture. Previous work looking at pygas has mostly been carried out using only one, or a few, reaction compounds for simplicity of analysis. A number of studies use only styrene as a model for pygas. This is an excessively simplistic model of the reaction, and neglects the interactions between the various components of pygas present in a real reaction setting. Therefore, within this research, a mixture of alkanes, cycloalkanes, and aromatics are used to make a model reaction feed. These were reacted over the hydrocracking metal/zeolite catalyst, and an as-prepared zeolite catalyst. This reaction mixture model is more comprehensive in scope than most research performed, without also including olefins, which would accelerate coking of the catalyst, therefore obscuring the more basic interactions between aromatic and saturated paraffin compounds. The efficacy of each reaction mixture was measured by running a model feed based on common pygas compositions in industry, then running reactions in which a single one of four of the the six feed components was removed from the mixture. When the as-prepared zeolite support was used as a catalyst it was found to crack more of the aromatics, benzene and toluene, along with producing significantly more xylenes due to disproportionation, than the metal/zeolite catalyst. One of the main causes of catalyst deactivation in hydrocracking catalysts is coking, due to carbon deposition. The effect of coking was analysed using thermogravimetric analysis (TGA) ex-situ, which was also verified using CHN analysis. The as-prepared zeolite support was found to produce more carbon laydown than the metal/zeolite catalyst, although it is unclear if the difference would have a significant effect during longer reactions. Within the two groups of catalyst, metal/zeolite and zeolite, the total quantity of coke detected for each reaction mixture was found to show some variation, but would be similar. Some of the reaction mixtures showed a difference in product composition in the offline GC results, although the cause of this is unclear. The results in these reactions cannot, therefore, be anticipated based upon a simple addition-subtraction model in terms of feed components, as there appears to be a complex interdependence between these components that influences the final retention of products observed, that was not assumed to be present before this work was carried out. Analysis of the coke deposit by Raman spectroscopy revealed that the graphite platelets in all reactions were between 10 and 13 nm. Therefore, it appears coke deposition was observed only on the external surface of the catalyst.
APA, Harvard, Vancouver, ISO, and other styles
More sources

Books on the topic "Catalytic hydrogenation of CO2̲"

1

Rinaldi, Roberto, ed. Catalytic Hydrogenation for Biomass Valorization. Cambridge: Royal Society of Chemistry, 2014. http://dx.doi.org/10.1039/9781782620099.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Khan, Zaffer. Catalytic hydrogenation in a cocurrent downflow contactor reactor. Birmingham: University of Birmingham, 1995.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
3

Liu, Zhongyi, Shouchang Liu, and Zhongjun Li. Catalytic Technology for Selective Hydrogenation of Benzene to Cyclohexene. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-6411-6.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Hou, Ruijun. Catalytic and Process Study of the Selective Hydrogenation of Acetylene and 1,3-Butadiene. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-0773-6.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Ebrahimi-Moshkabad, Morteza. A study of a twin screw extruder with catalyst immobilised on the screws for catalytic hydrogenation of highly viscous solutions. Birmingham: University of Birmingham, 1998.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
6

Orchard, Stephen Frederick. Reactive extrusion: The use of a co-rotating, intermeshing twin-screw extruder to perform catalytic hydrogenation of soya bean oil using immobilised and slurry catalysts. Birmingham: University of Birmingham, 1998.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
7

CO2 Hydrogenation Catalysis. Wiley & Sons, Limited, John, 2021.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
8

Himeda, Yuichiro, ed. CO2 Hydrogenation Catalysis. Wiley, 2021. http://dx.doi.org/10.1002/9783527824113.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

L, Červený, ed. Catalytic hydrogenation. Amsterdam: Elsevier, 1986.

Find full text
APA, Harvard, Vancouver, ISO, and other styles
10

Catalytic Hydrogenation. Elsevier, 1986. http://dx.doi.org/10.1016/s0167-2991(08)x6095-1.

Full text
APA, Harvard, Vancouver, ISO, and other styles
More sources

Book chapters on the topic "Catalytic hydrogenation of CO2̲"

1

Yan, Xiuli, and Xinzheng Yang. "Theoretical Studies of Homogeneously Catalytic Hydrogenation of Carbon Dioxide and Bioinspired Computational Design of Base-Metal Catalysts." In CO2 Hydrogenation Catalysis, 113–47. Weinheim, Germany: WILEY-VCH GmbH, 2021. http://dx.doi.org/10.1002/9783527824113.ch5.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Sahebdelfar, Saeed, and Maryam Takht Ravanchi. "Heterogeneous Catalytic Hydrogenation of CO2 to Basic Chemicals and Fuels." In Chemo-Biological Systems for CO2 Utilization, 15–48. First edition. | Boca Raton, FL : CRC Press, 2020.: CRC Press, 2020. http://dx.doi.org/10.1201/9780429317187-2.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Phongprueksathat, Nat, and Atsushi Urakawa. "Heterogeneously Catalyzed CO2 Hydrogenation to Alcohols." In CO2 Hydrogenation Catalysis, 207–36. Weinheim, Germany: WILEY-VCH GmbH, 2021. http://dx.doi.org/10.1002/9783527824113.ch8.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Ohkuma, Takeshi, Masato Kitamura, and Ryoji Noyori. "Asymmetric Hydrogenation." In Catalytic Asymmetric Synthesis, 1–110. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2005. http://dx.doi.org/10.1002/0471721506.ch1.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Hertrich, Maximilian Franz, and Matthias Beller. "Metal-Catalysed Hydrogenation of CO2 into Methanol." In Organometallics for Green Catalysis, 1–16. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/3418_2018_13.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

Holladay, Johnathan E., Todd A. Werpy, and Danielle S. Muzatko. "Catalytic Hydrogenation of Glutamic Acid." In Proceedings of the Twenty-Fifth Symposium on Biotechnology for Fuels and Chemicals Held May 4–7, 2003, in Breckenridge, CO, 857–69. Totowa, NJ: Humana Press, 2004. http://dx.doi.org/10.1007/978-1-59259-837-3_70.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Feldgus, Steven, and Clark R. Landis. "Catalytic Enantioselective Hydrogenation of Alkenes." In Catalysis by Metal Complexes, 107–35. Boston, MA: Springer US, 2002. http://dx.doi.org/10.1007/0-306-47718-1_5.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Panagiotopoulou, Paraskevi, and Xenophon E. Verykios. "Metal–support interactions of Ru-based catalysts under conditions of CO and CO2 hydrogenation." In Catalysis, 1–23. Cambridge: Royal Society of Chemistry, 2020. http://dx.doi.org/10.1039/9781788019477-00001.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Zhang, Ran, and Zhenshan Hou. "Soluble Pd Nanoparticles for Catalytic Hydrogenation." In Nanocatalysis in Ionic Liquids, 83–95. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527693283.ch5.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Meier, Paul F., and Marvin M. Johnson. "Modeling Catalytic Deactivation of Benzene Hydrogenation." In ACS Symposium Series, 428–38. Washington, DC: American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch031.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Conference papers on the topic "Catalytic hydrogenation of CO2̲"

1

Musadi, Maya R. "Catalytic Hydrogenation of CO2 for Sustainable Transport." In 14th Asia Pacific Confederation of Chemical Engineering Congress. Singapore: Research Publishing Services, 2012. http://dx.doi.org/10.3850/978-981-07-1445-1_498.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Zeng, Yuxuan, Li Wang, Ashford Bryony, and Xin Tu. "Co2 Hydrogenation In A Temperature Controlled Plasma-Catalytic Reactor." In 2017 IEEE International Conference on Plasma Science (ICOPS). IEEE, 2017. http://dx.doi.org/10.1109/plasma.2017.8496098.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Sohrabi, Morteza, and Azar Shabani. "Catalytic hydrogenation of carbon dioxide as a key step in continuous CO2 recycle (CCR)." In 2012 International Conference on Green and Ubiquitous Technology (GUT). IEEE, 2012. http://dx.doi.org/10.1109/gut.2012.6344196.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Myrzakhanov, M., R. Sharipov, A. Utelbayeva, and E. Suleimenov. "Storage of hydrogen in the benzene by catalytic hydrogenation." In 6TH INTERNATIONAL CONFERENCE ON ENVIRONMENT (ICENV2018): Empowering Environment and Sustainable Engineering Nexus Through Green Technology. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5117136.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Hocke, E., B. Kommoss, and G. H. Vogel. "Catalytic hydrogenation of carbon dioxide to methanol under supercritical conditions." In 2015 5th International Youth Conference on Energy (IYCE). IEEE, 2015. http://dx.doi.org/10.1109/iyce.2015.7180766.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

Talyzin, A. V. "Comparative study of hydrofullerides C60Hx synthesized by direct and catalytic hydrogenation." In MOLECULAR NANOSTRUCTURES: XVII International Winterschool Euroconference on Electronic Properties of Novel Materials. AIP, 2003. http://dx.doi.org/10.1063/1.1627979.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Hu, Ruijue, Jianli Li, Xiaohong Zhang, and Haiquan Su. "Mesoporous carbon-supported β-Mo2C for catalytic hydrogenation of carbon monoxide to mixed alcohols." In ADVANCES IN ENERGY SCIENCE AND ENVIRONMENT ENGINEERING II: Proceedings of 2nd International Workshop on Advances in Energy Science and Environment Engineering (AESEE 2018). Author(s), 2018. http://dx.doi.org/10.1063/1.5029796.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Mallick, Sujata, Surjyakanta Rana, and K. M. Parida. "Characterization of Nano-Crystalline Nickel Supported Zirconia and its Catalytic Activity of Hydrogenation of Nitrophenol." In 2011 International Conference on Nanoscience, Technology and Societal Implications (NSTSI). IEEE, 2011. http://dx.doi.org/10.1109/nstsi.2011.6111782.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Wong, Farng Hui, Timm Joyce Tiong, Loong Kong Leong, and Yeow Hong Yap. "Role of ZnO in Ni/ZnO/Al2O3 as catalytic materials for hydrogenation of vegetable oil." In 3RD INTERNATIONAL SCIENCES, TECHNOLOGY & ENGINEERING CONFERENCE (ISTEC) 2018 - MATERIAL CHEMISTRY. Author(s), 2018. http://dx.doi.org/10.1063/1.5066959.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Mardhiyah, Fairuz J., Nino Rinaldi, and Sigit Priatmoko. "Catalytic activity of CoMo/Al2O3 on hydrogenation reaction of Rosin oil: Effect addition of MgO." In SolarPACES 2017: International Conference on Concentrating Solar Power and Chemical Energy Systems. Author(s), 2018. http://dx.doi.org/10.1063/1.5064301.

Full text
APA, Harvard, Vancouver, ISO, and other styles

Reports on the topic "Catalytic hydrogenation of CO2̲"

1

Wayland, B. B. Catalytic hydrogenation of carbon monoxide. Office of Scientific and Technical Information (OSTI), December 1992. http://dx.doi.org/10.2172/5260923.

Full text
APA, Harvard, Vancouver, ISO, and other styles
2

Reinaldo M. Machado. Advanced Catalytic Hydrogenation Retrofit Reactor. Office of Scientific and Technical Information (OSTI), August 2002. http://dx.doi.org/10.2172/822407.

Full text
APA, Harvard, Vancouver, ISO, and other styles
3

Lawal, Adeniyi, Woo Lee, Ron Besser, Donald Kientzler, and Luke Achenie. Microchannel Reactor System for Catalytic Hydrogenation. Office of Scientific and Technical Information (OSTI), December 2010. http://dx.doi.org/10.2172/1018952.

Full text
APA, Harvard, Vancouver, ISO, and other styles
4

Rothwell, I. P. Catalytic arene hydrogenation using early transition metal hydride compounds. Office of Scientific and Technical Information (OSTI), March 1993. http://dx.doi.org/10.2172/6443562.

Full text
APA, Harvard, Vancouver, ISO, and other styles
5

Yang, Shiyong, and L. M. Stock. Molecular catalytic hydrogenation of aromatic hydrocarbons and hydrotreating of coal liquids. Office of Scientific and Technical Information (OSTI), May 1996. http://dx.doi.org/10.2172/466864.

Full text
APA, Harvard, Vancouver, ISO, and other styles
6

Rothwell, I. P. Catalytic arene hydrogenation using early transition metal hydride compounds. Progress report. Office of Scientific and Technical Information (OSTI), March 1993. http://dx.doi.org/10.2172/10159596.

Full text
APA, Harvard, Vancouver, ISO, and other styles
7

Wayland, B. B. Catalytic hydrogenation of carbon monoxide. Progress report, December 15, 1991--December 14, 1992. Office of Scientific and Technical Information (OSTI), December 1992. http://dx.doi.org/10.2172/10148116.

Full text
APA, Harvard, Vancouver, ISO, and other styles
8

Wayland, B. B. Catalytic hydrogenation of carbon monoxide. Technical research progress report, December 15, 1992--December 14, 1993. Office of Scientific and Technical Information (OSTI), December 1993. http://dx.doi.org/10.2172/10184412.

Full text
APA, Harvard, Vancouver, ISO, and other styles
9

Patmore, D. J., W. H. Dawson, and T. J. W. de Bruijn. Catalytic effect of iron based additives on hydrogenation and coke inhibition during hydrocracking of heavy oils. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/304339.

Full text
APA, Harvard, Vancouver, ISO, and other styles
10

Wayland, B. B. Final Technical Report "Catalytic Hydrogenation of Carbon Monoxide and Olefin Oxidation" Grant number : DE-FG02-86ER13615. Office of Scientific and Technical Information (OSTI), August 2009. http://dx.doi.org/10.2172/946685.

Full text
APA, Harvard, Vancouver, ISO, and other styles
You might also be interested in the extended bibliographies on the topic 'Catalytic hydrogenation of CO2̲' for particular source types:
Journal articles Dissertations / Theses Books
We offer discounts on all premium plans for authors whose works are included in thematic literature selections. Contact us to get a unique promo code!

To the bibliography