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公开(公告)号:US09873096B2
公开(公告)日:2018-01-23
申请号:US13519140
申请日:2010-12-03
申请人: Bidyut De , Pankaj Kumar Kasliwal , Debasis Bhattacharyya , Venkatachalam Krishnan , Santanam Rajagopal
发明人: Bidyut De , Pankaj Kumar Kasliwal , Debasis Bhattacharyya , Venkatachalam Krishnan , Santanam Rajagopal
CPC分类号: B01F5/0256 , B01J4/002
摘要: The present subject matter relates to a feed nozzle assembly 100 for atomizing a heavy hydrocarbon feed by mixing the hydrocarbon feed with a diluent and an atomizing media. The feed nozzle assembly 100 includes at least one primary mixing chambers 101 for receiving the liquid hydrocarbon feed and the diluent to create a primary mixture. The primary mixture is than forwarded to a secondary mixing chamber 102. The secondary mixing chamber extends to a tertiary mixing chamber 103. A steam inlet 110 is provided to inject streams of steam to the secondary mixing chamber 102 and to the tertiary mixing chamber 103 through a first opening and a second opening, respectively, located within the steam inlet 110.
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公开(公告)号:US20120024748A1
公开(公告)日:2012-02-02
申请号:US13260919
申请日:2010-03-29
申请人: Saravanan Subramani , Debasis Bhattacharyya , Karthikeyani Arumugam Velayutham , Pankaj Kumar Kasliwal , Krishnan Venkatachalam
发明人: Saravanan Subramani , Debasis Bhattacharyya , Karthikeyani Arumugam Velayutham , Pankaj Kumar Kasliwal , Krishnan Venkatachalam
CPC分类号: C10G11/187 , B01J29/084 , B01J29/40 , B01J29/80 , B01J35/0006 , B01J2229/42 , C10G2300/202 , C10G2300/305 , C10G2300/701 , C10G2400/02
摘要: The present invention relates to a fluidized catalytic cracking process for cracking hydrocarbon feed having organo-sulfur compound as an impurity, said process comprising: adding a heavy metal poisoned spent catalyst to an equilibrium catalyst to obtain a composite circulating catalyst, wherein the heavy metal poisoned spent catalyst is added in an amount to maintain the activity of the circulating catalyst; and obtaining a fluidized catalytic cracked product.The present invention further relates to fluidized catalytic cracked product obtained by the process of the present invention. The sulfur content of the fluidized catalytic cracked product mainly gasoline which is boiling in the range of C5-250° C. reduced by more than 20% (wt/wt). And Research Octane number of the fluidized catalytic cracked product is increased by more than 1 unit.
摘要翻译: 本发明涉及一种用于裂化具有有机硫化合物作为杂质的烃进料的流化催化裂化方法,所述方法包括:向沉淀催化剂中加入重金属中毒废催化剂以得到复合循环催化剂,其中重金属中毒 添加废催化剂以维持循环催化剂的活性; 得到流化催化裂化产物。 本发明还涉及通过本发明的方法获得的流化催化裂化产物。 主要是在C5-250℃范围内沸腾的汽油的流化催化裂化产物的硫含量降低了20%(wt / wt)。 研究表明,流化催化裂化产物的辛烷值增加了1个以上。
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