公开(公告)号：US20150267130A1

公开(公告)日：2015-09-24

申请号：US14658036

申请日：2015-03-13

Applicant: INDIAN OIL CORPORATION LTD.

Inventor： Ganesh Vitthalrao BUTLEY ,  Mainak SARKAR ,  Yamini GUPTA ,  Arangarasu ARUN ,  Madhusudan SAU ,  Vatsala SUGUMARAN ,  Vivekanand KAGDIYAL ,  Paramasivam SAKTHIVEL ,  Brijesh KUMAR ,  Biswapriya DAS

IPC: C10G65/12 ,  C07C45/39 ,  C07C29/50 ,  C10L1/06 ,  C10L1/02

CPC classification number: C10G65/12 ,  C07C2602/10 ,  C10G65/08 ,  C10G2300/305 ,  C10G2300/307 ,  C10G2400/02 ,  C10G2400/04 ,  C10L1/026 ,  C10L1/06 ,  C10L2270/023 ,  C10L2270/026

Abstract: An integrated process for production of ultra low sulfur products of high octane gasoline, high aromatic naphtha and high Cetane Diesel from high aromatic middle distillate range streams from any cracker units such as Light Cycle Oil (LCO) stream of Fluid catalytic cracking (FCC) units and comprising of subjecting the feed boiling between 200 to 400° C. and having at least 30 wt % multi-ring aromatics content subjected to hydrotreating for removal of heteroatoms like sulfur and nitrogen and at a pressure sufficient only for saturation of one ring of multi-ring aromatics. The effluent from hydrotreating is subjected to hydrocracking at same pressure of hydrotreating step above for selective opening of saturated ring of multi-ring aromatics. The effluent from hydrocracking is separated in CUT-1 boiling between 35 to 70° C., CUT-2 boiling between 70 to 200° C. in which the monoaromatics and alkylated monoaromatics are concentrated and CUT-3 boiling above 200° C. in which concentration of saturates i.e. paraffins and naphthenes significantly increased. The CUT-3 is selectively oxidized in selective oxidation step in presence of catalyst, an oxidizing agent and operating conditions such that it results in diesel product with more enhanced Cetane.

Abstract translation: 来自高芳烃中间馏分的高辛烷值汽油，高芳烃石脑油和高十六烷值柴油的超低硫产品的综合方法来自任何裂解装置，例如流化催化裂化（FCC）装置的轻循环油（LCO）流 并且包括使进料沸腾在200-400℃之间并具有至少30重量％的多环芳烃含量进行加氢处理以除去杂原子如硫和氮，并且在足以仅饱和一个多环的压力 环芳烃。 来自加氢处理的流出物在上述加氢处理步骤的相同压力下进行加氢裂化，以选择性地打开饱和环多环芳族化合物。 来自加氢裂化的流出物在CUT-1沸腾温度为35-70℃之间，CUT-2在70至200℃之间沸腾，其中单芳族化合物和烷基化单芳烃浓缩，CUT-3沸点高于200℃ 饱和物的浓度即石蜡和环烷烃显着增加。 在催化剂，氧化剂和操作条件的存在下，在选择性氧化步骤中选择性地氧化CUT-3，使得其产生具有更多增强的十六烷的柴油产品。

公开(公告)号：US20150275084A1

公开(公告)日：2015-10-01

申请号：US14668446

申请日：2015-03-25

Applicant: INDIAN OIL CORPORATION LTD.

Inventor： Satyen Kumar DAS ,  Ponoly Ramachandran PRADEEP ,  Terapalli Hari Venkata Devi PRASAD ,  Jagdev Kumar DIXIT ,  Gautam THAPA ,  Ram Mohan THAKUR ,  Vinod Kumar SHARMA ,  Debasis BHATTACHARYYA ,  Suresh Kumar PURI ,  Anurag Ateet GUPTA ,  Brijesh KUMAR ,  Biswapriya DAS ,  Ravinder Kumar MALHOTRA

IPC: C09K15/28 ,  C10G9/00

CPC classification number: C09K15/28 ,  C10G9/00 ,  C10G9/005 ,  C10G75/04 ,  C10G2300/1033 ,  C10G2300/107

Abstract: The present invention relates to a liquid phase additive comprising an alkyl nitrate; a petroleum sulphonates; an aliphatic, aromatic, cyclohexylamines or hetroalkylated lower amines; a hindered phenol based compounds; a phosphate esters and an aliphatic alcohols for use in delayed coking process with decreased coke yield and increased yield of liquid and/or gaseous product and a process for preparing the liquid phase additive. The present invention also relates to a process for thermal cracking of petroleum residue producing petroleum coke and lighter hydrocarbon products by using liquid phase additive.

Abstract translation: 本发明涉及包含硝酸烷基酯的液相添加剂; 石油磺酸盐; 脂族，芳族，环己胺或氢化烷基化的低级胺; 受阻酚基化合物; 用于延迟焦化工艺中的磷酸酯和脂族醇，其具有降低的焦炭产率和提高液体和/或气体产物的产率以及制备液相添加剂的方法。 本发明还涉及通过使用液相添加剂对生产石油焦油和轻烃产物进行热裂解的方法。

公开(公告)号：US20180264430A1

公开(公告)日：2018-09-20

申请号：US15988909

申请日：2018-05-24

Applicant: INDIAN OIL CORPORATION LTD.

Inventor： Mukthiyar SADHULLAH ,  Satheesh Vetterkunnel KUMARAN ,  Debasis BHATTACHARYYA ,  Gadari SAIDULU ,  Somnath KUKADE ,  Brijesh KUMAR ,  Santanam RAJAGOPAL

IPC: B01J19/24 ,  C10G11/10 ,  B01J8/26 ,  C10G11/18 ,  B01J8/38

CPC classification number: B01J19/24 ,  B01J8/26 ,  B01J8/386 ,  B01J2208/0084 ,  C10G11/10 ,  C10G11/18

Abstract: An apparatus which is an integral hardware consisting of an annular downer reactor and a concentric upflow riser regenerator for catalytic cracking of hydrocarbon feed to is disclosed. The annular downer reactor terminates in annular stripper which is also concentric with the regenerator. The regenerator, reactor and stripper are in fluid connection with each other. The apparatus is highly compact and provides efficient contact between circulating catalyst and hydrocarbon feed. The proposed hardware includes a novel radial distributor for providing improved control and radial distribution of catalyst inside the downflow reactor. The radial distributor has equal numbers of stationary and movable parts placed one after another to cover the entire annular opening at the bottom of the regenerated catalyst vessel. The radial distributor is concentric with regenerator and located between the catalyst holding vessel and the reactor. A process for catalytic cracking using the invented apparatus is also disclosed.