Download e-book for iPad: Handbook of Spent Hydroprocessing Catalysts: Regeneration, by Meena Marafi, Anthony Stanislaus, Edward Furimsky

By Meena Marafi, Anthony Stanislaus, Edward Furimsky

ISBN-10: 044453556X

ISBN-13: 9780444535566

This guide serves scientists and researchers drawn to any point of spent hydroprocessing catalysts. Its objective is to aid within the research and evaluate of refined catalyst byproducts and processing ideas, to figure out even if spent catalysts may be processed into effective assets. For non-regenerable spent catalysts, the book takes into account either security and ecological implications of using landfill and different waste recommendations. offers entire tips and tips to these making judgements at the destiny of spent catalysts, significantly bettering strategic concepts for refining firms bargains suggestions that maximize procedural, regulatory, defense, and preparedness benefitsContains certain details on harmful features of spent and regenerated catalysts with deployment options, and acts as a benchmark record for setting up threshold limits of regulated species in addition to for constructing techniques for dealing with spent catalysts to make sure environmental reputation

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Extra resources for Handbook of Spent Hydroprocessing Catalysts: Regeneration, Rejuvenation, Reclamation, Environment and Safety

Sample text

3 [120]. The features of these reactors indicate the importance of the proper selection of catalysts, the size and shape of the catalyst particles in particular, to ensure an efficient and continuous operation. In addition, the properties of feeds must be taken into consideration to achieve the optimal matching of catalysts with reactor. 3: Operating conditions during hydroprocessing of heavy feeds in different reactors [From ref. 120. Reprinted with permission]. 4–2 CO: continuous operation; RCC: relative catalyst consumption for the same feed for one year; LHSV: Liquid hourly space velocity.

40 Chapter 3 generally observed that the coke build-up in fixed bed reactors increased from the inlet towards the outlet, whereas metal deposition usually exhibits opposite trend. The H2 S/H2 ratio increased in the same direction [27]. Consequently, the variable structure of spent catalyst between the inlet and outlet of the reactor should be expected. , either dense loading or sock loading [124]. In the latter case, many catalyst particles will reach the loading surface together, having little time to attain a favorable resting position.

6: Yields and properties of products from different reactors [From ref. 120. Reprinted with permission]. 7 11000 26 50 tons per day of the catalytically active solid. , aluminium production) generating low-cost solids would enhance the viability of slurry bed reactors The safety aspects of hydroprocessing operations deserve attention. Decades of the experience using heavy feeds varying widely in properties shows that it is quite easy and safe to operate fixed bed reactors. The additional high-pressure equipment upstream and downstream of the moving bed and ebullated bed reactors adds to the complexity of the operation.

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Handbook of Spent Hydroprocessing Catalysts: Regeneration, Rejuvenation, Reclamation, Environment and Safety by Meena Marafi, Anthony Stanislaus, Edward Furimsky


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