Relevant bibliographies by topics / Co-hydroprocessing

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Academic literature on the topic 'Co-hydroprocessing'

Author: Grafiati
Published: 5 June 2025
Last updated: 1 August 2025

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Journal articles on the topic "Co-hydroprocessing"

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Treusch, Klara, Anna Huber, Samir Reiter, et al. "Refinery integration of lignocellulose for automotive fuel production via the bioCRACK process and two-step co-hydrotreating of liquid phase pyrolysis oil and heavy gas oil." Reaction Chemistry & Engineering 5, no. 3 (2020): 519–30. http://dx.doi.org/10.1039/c9re00352e.

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Dagonikou, Vasiliki, Stella Bezergianni, and Dimitrios Karonis. "Co-hydroprocessing of Light Cycle Oil with Waste Cooking Oil." Materials Today: Proceedings 5, no. 14 (2018): 27369–76. http://dx.doi.org/10.1016/j.matpr.2018.09.053.

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Templis, Ch, A. Vonortas, I. Sebos, and N. Papayannakos. "Vegetable oil effect on gasoil HDS in their catalytic co-hydroprocessing." Applied Catalysis B: Environmental 104, no. 3-4 (2011): 324–29. http://dx.doi.org/10.1016/j.apcatb.2011.03.012.

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Sokolova, Yulia V., and Anton N. Chepikov. "OXIDATIVE ROASTING OF INDUSTRIAL SPENT CATALYSTS CO-Mo/Al2O3 HYDROPROCESSING WITH LIM." IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 63, no. 11 (2020): 57–64. http://dx.doi.org/10.6060/ivkkt.20206311.6256.

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The oxidative roasting of industrial spent catalyst Co-Mo/Al2O3 for the hydrotreatment of diesel fuel with lime in an air atmosphere was studied. Using the data of DTA, TG and X-ray phase analysis, it was found that during roasting, the sulfur and carbon oxides forms CaSO4 and CaCO3, and Mo is converted to calcium molybdate. Using the filtering fixed bed of reagents, the kinetics of roasting was studied. It was found that in the temperature range of 550 – 600 °C with air, supply rate of 3 l/min the process ends in 38 - 44 min for ground and non-ground catalyst. The optimal parameters (lime con
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Du, Kun, Yufeng Zeng, and Ronghuan Qin. "Coliquefaction of coal-plastic mixtures by two-stage methods." Europub Journal of Exact and Engineering Research 3, no. 1 (2022): 107–15. http://dx.doi.org/10.54749/ejeerv3n1-003.

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The two-stage co-processing of coal with medium-density polyethylene (MDPE) was investigated using ammonium tetrathiomolybdate (ATTM) as a catalyst. The first-stage plastic pyrolysis carried out at 420 °C, 6.0 MPa hydrogen pressure and HZSM-5 as catalyst. The second-stage coal and MDPE co-liquefaction had been performed in a hydroprocessing unit at 430 °C and 6.0 MPa hydrogen pressure with ATTM catalyst. A competitive experiment was performed by the way of one stage co-liquefaction of coal with MDPE using ATTM as catalyst and tetraline as solvent. The aim of the experiments was to determine th
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Yunusov, M. P., Sh M. Saidaxmedov, Sh B. Djalаlova, et al. "Synthesis and Study of Ni-Mo-Co Catalysts for Hydroprocessing of Oil Fractions." Catalysis for Sustainable Energy 2, no. 1 (2015): 43–56. http://dx.doi.org/10.1515/cse-2015-0003.

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AbstractThe problems of synthesis of Ni-Mo, Ni-Mo Co and Co-Mo oxide catalysts for hydrodesulfurization and hydrogenation of aromatic hydrocarbons in the composition of kerosene, diesel and oil fractions are discussed. The influence of spent adsorbent and kaolin as the additives on the physical-chemical and catalytic properties of bimetallic and trimetallic catalysts is established.
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Dimitriadis, Athanasios, and Stella Bezergianni. "Towards Bio-Crude Refinery Integration: Hydrodeoxygenation and Co-Hydroprocessing with Light Cycle Oil." Energies 17, no. 23 (2024): 6032. https://doi.org/10.3390/en17236032.

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Hydrothermal liquefaction of solid waste has been gaining more and more attention over the last few years. However, the properties of the HTL product, i.e., biocrude, are limiting its direct utilization. As a result, HTL biocrude upgrading is essential to improve its quality. The main objective of the current research is to study the hydrotreatment stabilization of HTL biocrude, produced from spent coffee grounds, utilizing commercial hydrotreated catalysts, and also to investigate the integration of the stabilized biocrude into a light cycle oil (LCO) hydrotreatment plant for coprocessing to
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Grimblot, J. "Genesis, architecture and nature of sites of Co(Ni)–MoS2 supported hydroprocessing catalysts." Catalysis Today 41, no. 1-3 (1998): 111–28. http://dx.doi.org/10.1016/s0920-5861(98)00042-x.

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Chen, Jinwen, Hena Farooqi, and Craig Fairbridge. "Experimental Study on Co-hydroprocessing Canola Oil and Heavy Vacuum Gas Oil Blends." Energy & Fuels 27, no. 6 (2013): 3306–15. http://dx.doi.org/10.1021/ef4005835.

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Xing, Tingyong, Anton Alvarez-Majmutov, Rafal Gieleciak, and Jinwen Chen. "Co-hydroprocessing HTL Biocrude from Waste Biomass with Bitumen-Derived Vacuum Gas Oil." Energy & Fuels 33, no. 11 (2019): 11135–44. http://dx.doi.org/10.1021/acs.energyfuels.9b02711.

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Book chapters on the topic "Co-hydroprocessing"

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Ansari, Khursheed B., Shakeelur Rahman A. R., Mohd Shariq Khan, Saleem Akhtar Farooqui, Mohd Yusuf Ansari, and Mohammad Danish. "Conversion of Biomass to Green Gasoline: Feedstocks, Technological Advances and Commercial Scope." In Green Gasoline. Royal Society of Chemistry, 2023. http://dx.doi.org/10.1039/bk9781837670079-00124.

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Biomass-driven energy has attracted considerable attention in recent decades as an alternative to petroleum fuel, particularly diesel and gasoline. Green gasoline production through the hydroprocessing of biomass/plant materials is one innovative approach that has brought biorefinery facilities to the forefront. Several biomass-based feedstocks, including wood chips, bagasse, vegetable oils and blends of bio-oil and petroleum oil, are being investigated for green gasoline production. Of these, vegetable oils produce kerosene and diesel-range hydrocarbons (C15–C20) along with gasoline, and the
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van Gestel, J., J. Leglise, and J. C. Duchet. "Effect of H2S on the Functionalities of a Co/Mo/A12O3 Hydrotreating Catalyst." In Catalytic Hydroprocessing of Petroleum and Distillates. CRC Press, 2020. http://dx.doi.org/10.1201/9781003067306-19.

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Conference papers on the topic "Co-hydroprocessing"

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Sutton, Nathaniel, and Ken Kirkham. "Converting Hydroprocessing Equipment to Produce Renewable Diesel from Soybean and Corn Oil: Corrosion and Materials Considerations." In CONFERENCE 2022. AMPP, 2022. https://doi.org/10.5006/c2022-17989.

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Abstract Around the globe, refiners are seeking to convert an increasing portion of existing Hydroprocessing capacity to process renewable feedstocks. Facilities face economic pressure to bring renewables production online quickly, in order to take advantage of the current government incentives (credits) for renewable fuels. Simultaneously, however, materials and corrosion engineers face a lack of data-based guidance regarding the appropriate materials selection and expected damage mechanisms for renewables processing units. This paper discusses many of the major damage mechanisms which are co
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Srinivasan, Sridhar, and Gerrit Buchheim. "High Temperature Corrosion Quantification in Renewable Diesel and Sustainable Aviation Fuel Applications." In MECC 2023. AMPP, 2023. https://doi.org/10.5006/mecc2023-20056.

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Abstract Production of Renewable Diesel (RD) and Sustainable Aviation Fuels (SAF) from biological sources (natural oils) has seen exponential growth in recent years, stemming from worldwide government mandated climate change initiatives alongside the need for carbon capture and sequestration. Significant, rapid investments have occurred in retrofitting / adapting existing refinery hydroprocessing infrastructure to process natural oils or coprocess natural oils blended with crudes to produce RD and SAF. This stems from the fact that natural oils have the hydrocarbon (HC) structures to fit withi
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Srinivasan, Sridhar, Winston Robbins, and Gerrit Buchheim. "Quantifying High Temperature Corrosion in Renewable Diesel and Sustainable Aviation Fuel Production." In CONFERENCE 2023. AMPP, 2023. https://doi.org/10.5006/c2023-19457.

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Abstract Production of Renewable Diesel (RD) and Sustainable Aviation Fuels (SAF) from bio / natural oils has seen tremendous interest and investment in recent years, stemming from worldwide government mandated need to reduce fossil fuel CO2 emissions. Significant, rapid investments have occurred in retrofitting / adapting existing refinery hydroprocessing infrastructure to process natural oils or coprocess natural oils blended with crudes to produce RD and SAF. This stems from the fact that natural oils have the hydrocarbon (HC) structures to fit within the mid-distillate fuel product such as
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Reports on the topic "Co-hydroprocessing"

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Minja, R. J. A., and M. Ternan. Effect of H-mordenite zeolite as a component in Co-Mo-Al203 hydroprocessing catalysts used for the conversion of Boscan heavy oil. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1989. http://dx.doi.org/10.4095/304445.

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Journal articles
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