TR201903230T4 - Çok aşamalı parçalama için fcc katalizörünün yukarı akış rejenerasyonu. - Google Patents

Çok aşamalı parçalama için fcc katalizörünün yukarı akış rejenerasyonu. Download PDF

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Publication number
TR201903230T4
TR201903230T4 TR2019/03230T TR201903230T TR201903230T4 TR 201903230 T4 TR201903230 T4 TR 201903230T4 TR 2019/03230 T TR2019/03230 T TR 2019/03230T TR 201903230 T TR201903230 T TR 201903230T TR 201903230 T4 TR201903230 T4 TR 201903230T4
Authority
TR
Turkey
Prior art keywords
catalyst
coke
regeneration
fcc catalyst
spent
Prior art date
Application number
TR2019/03230T
Other languages
English (en)
Inventor
Mukthiyar S
R Pradeep P
Bhattacharyya Debasis
K Satheesh V
Saidulu G
Original Assignee
Indian Oil Corp Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Indian Oil Corp Ltd filed Critical Indian Oil Corp Ltd
Publication of TR201903230T4 publication Critical patent/TR201903230T4/tr

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/0025—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor by an ascending fluid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00—Regeneration or reactivation of catalysts, in general
    • B01J38/04—Gas or vapour treating; Treating by using liquids vaporisable upon contacting spent catalyst
    • B01J38/12—Treating with free oxygen-containing gas
    • B01J38/30—Treating with free oxygen-containing gas in gaseous suspension, e.g. fluidised bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • B01J8/28—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations the one above the other
    • B01J8/30—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations the one above the other the edge of a lower bed projecting beyond the edge of the superjacent bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C10G11/182—Regeneration
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel stages only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/70—Catalyst aspects
    • C10G2300/708—Coking aspect, coke content and composition of deposits

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Bu buluş harcanan FCC katalizörünün harcanan katalizöre ilişkin geniş kok varyasyonu ile sonuçlanacak şekilde çoklu reaktörler operasyonu kullanarak rejenerasyonu için bir proses ve bir aparat ile ilgilidir. Bu proses kendi etkin rejenerasyonuna ve indirgenmiş hidrotermal deaktivasyonuna yönelik kalma süresini kontrol etmek için bunların kok içeriğine bağlı olarak harcanan katalizörün bölünmüş enjeksiyonuna sahip bir yukarı akışlı rejeneratör kullanmaktadır. Bu sistem kendi tam rejenerasyonu için katalizörde saklanan yüksek kokun gerekli süreye ve düşük koklu katalizörün yüksek sıcaklığa maruz kalmasını muhtemel mimimum süreye minimize etme avantajına sahiptir.
TR2019/03230T 2010-07-08 2011-07-04 Çok aşamalı parçalama için fcc katalizörünün yukarı akış rejenerasyonu. TR201903230T4 (tr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IN747KO2010 2010-07-08

Publications (1)

Publication Number Publication Date
TR201903230T4 true TR201903230T4 (tr) 2019-03-21

Family

ID=44629865

Family Applications (1)

Application Number Title Priority Date Filing Date
TR2019/03230T TR201903230T4 (tr) 2010-07-08 2011-07-04 Çok aşamalı parçalama için fcc katalizörünün yukarı akış rejenerasyonu.

Country Status (4)

Country Link
US (1) US20130172173A1 (tr)
EP (1) EP2591071B1 (tr)
TR (1) TR201903230T4 (tr)
WO (1) WO2012004805A1 (tr)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8888899B2 (en) * 2012-04-12 2014-11-18 Kellogg Brown & Root Llc Transfer line for the primary cyclone of a gasifier
EP2909289B1 (en) * 2012-10-19 2018-05-16 Saudi Arabian Oil Company Process for high severity catalytic cracking of crude oil
CN103509596B (zh) * 2013-09-29 2015-08-26 中国石油大学(北京) 一种加工劣质重油的方法
CN105268381B (zh) * 2014-07-03 2017-09-15 中国石油化工股份有限公司 用于甲醇制烯烃的下行床反应‑再生装置及其反应方法
CN105561895B (zh) * 2014-10-14 2018-05-11 中国石油化工股份有限公司 带催化剂混合器的甲醇制烯烃装置及反应方法
CN105566023B (zh) * 2014-10-14 2017-11-21 中国石油化工股份有限公司 高效混合的甲醇制烯烃反应‑再生装置及其反应方法
EP3448960B1 (en) * 2016-04-29 2023-02-08 BASF Corporation New cyclic metal deactivation unit design for fcc catalyst deactivation
US10781377B2 (en) * 2017-11-30 2020-09-22 Uop Llc Process and apparatus for cracking hydrocarbons to lighter hydrocarbons
CN114426877B (zh) * 2020-10-29 2023-07-14 中国石油化工股份有限公司 一种原油催化裂解生产低碳烯烃和btx的方法
CN116212971B (zh) * 2021-12-03 2024-10-11 中国石油化工股份有限公司 一种催化剂再生设备以及再生方法
US20230183582A1 (en) 2021-12-14 2023-06-15 Anellotech, Inc. Process for converting solid hydrocarbonaceous materials to chemicals and fuels

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3433733A (en) 1966-12-01 1969-03-18 Texaco Inc Method and apparatus for fluid catalytic cracking
US4448753A (en) 1982-02-12 1984-05-15 Mobil Oil Corporation Apparatus for regenerating cracking catalyst
US4424116A (en) * 1982-03-25 1984-01-03 Ashland Oil, Inc. Converting and stripping heavy hydrocarbons in two stages of riser conversion with regenerated catalyst
US4514285A (en) 1983-03-23 1985-04-30 Texaco Inc. Catalytic cracking system
US4814068A (en) 1986-09-03 1989-03-21 Mobil Oil Corporation Fluid catalytic cracking process and apparatus for more effective regeneration of zeolite catalyst
US5009769A (en) 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
US5435906A (en) 1992-08-20 1995-07-25 Stone & Webster Engineering Corporation Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components
CN1089641A (zh) 1992-08-20 1994-07-20 史东及韦伯斯特工程公司 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法
US5582712A (en) 1994-04-29 1996-12-10 Uop Downflow FCC reaction arrangement with upflow regeneration
US5824208A (en) 1994-05-27 1998-10-20 Exxon Research & Engineering Company Short contact time catalytic cracking process
US6267873B1 (en) * 1997-04-11 2001-07-31 Indian Oil Corporation, Ltd. Fluidized catalytic cracking process
US6658615B2 (en) 1998-06-30 2003-12-02 Texas Instruments Incorporated IC with IP core and user-added scan register
US5944982A (en) 1998-10-05 1999-08-31 Uop Llc Method for high severity cracking
FR2785907B1 (fr) 1998-11-13 2001-01-05 Inst Francais Du Petrole Procede et dispositif de craquage catalytique comprenant des reacteurs a ecoulements descendant et ascendant
FR2802211B1 (fr) 1999-12-14 2002-02-01 Inst Francais Du Petrole Procede et dispositif de craquage catalytique comprenant en parallele au moins un reacteur a ecoulement ascendant et au moins un reacteur a ecoulement descendant
EP1190019A1 (en) 2000-02-16 2002-03-27 Indian Oil Corporation Limited A multi stage selective catalytic cracking process and a system for producing high yield of middle distillate products from heavy hydrocarbon feedstocks
CN1118539C (zh) * 2000-12-13 2003-08-20 中国石油天然气股份有限公司 两段提升管催化裂化新技术
CA2496037C (en) * 2002-08-21 2010-04-27 Fluor Corporation Methods and configurations for catalyst regeneration
CN1438296A (zh) * 2003-03-13 2003-08-27 中国石油天然气股份有限公司 三段提升管催化裂化新工艺
KR20080080302A (ko) 2005-12-20 2008-09-03 쉘 인터내셔날 리써취 마트샤피지 비.브이. 폐 ｆｃｃ 촉매를 재생하는 방법 및 장치
US20080011645A1 (en) 2006-07-13 2008-01-17 Dean Christopher F Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations
US7491315B2 (en) 2006-08-11 2009-02-17 Kellogg Brown & Root Llc Dual riser FCC reactor process with light and mixed light/heavy feeds

Also Published As

Publication number Publication date
WO2012004805A1 (en) 2012-01-12
EP2591071A1 (en) 2013-05-15
US20130172173A1 (en) 2013-07-04
EP2591071B1 (en) 2018-12-12

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