JPS55151086A - Fluidized catalytic cracking of heavy petroleum containing distillation residue - Google Patents

Fluidized catalytic cracking of heavy petroleum containing distillation residue

Info

Publication number
JPS55151086A
JPS55151086A JP5818379A JP5818379A JPS55151086A JP S55151086 A JPS55151086 A JP S55151086A JP 5818379 A JP5818379 A JP 5818379A JP 5818379 A JP5818379 A JP 5818379A JP S55151086 A JPS55151086 A JP S55151086A
Authority
JP
Japan
Prior art keywords
line
catalyst
distillation residue
fed
catalytic cracking
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
JP5818379A
Other languages
Japanese (ja)
Inventor
Shinji Takase
Yasuyuki Ooishi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eneos Corp
Original Assignee
Nippon Oil Corp
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 Nippon Oil Corp filed Critical Nippon Oil Corp
Priority to JP5818379A priority Critical patent/JPS55151086A/en
Publication of JPS55151086A publication Critical patent/JPS55151086A/en
Pending legal-status Critical Current

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

PURPOSE: To improve the fluidity of heavy oil, to avoid the local heating and contact, and to increase the liquid yield, by subjecting a mixture of a small amount of naphtha having a specific boiling point with a feedstock oil consisting of the heavy oil containing a distillation residue to catalytic cracking.
CONSTITUTION: Heavy oil containing a distillation residue is fed from the line 3a; 1W10vol% of naphtha boiling at 20W220°C, from the line 3b. Both are fed from the line 3 to the bottom of the riser reactor 1; and the high-temperature catalyst regenerated in the zone 5 is taken out and partly fed from the line 8 to the bottom, preferably at a level less than 1/10 of the total height, of the reactor 1 and mixed with the preheated oil from the line 3. The rest of the catalyst is partly blown into a point after the contact position in the reactor 1 to crack the feedstock oil. The cracked product is separated from the catalyst in the separation zone 2 to recover a hydrocarbon vapor and to regenerate the catalyst in the zone 5.
COPYRIGHT: (C)1980,JPO&Japio
JP5818379A 1979-05-12 1979-05-12 Fluidized catalytic cracking of heavy petroleum containing distillation residue Pending JPS55151086A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5818379A JPS55151086A (en) 1979-05-12 1979-05-12 Fluidized catalytic cracking of heavy petroleum containing distillation residue

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5818379A JPS55151086A (en) 1979-05-12 1979-05-12 Fluidized catalytic cracking of heavy petroleum containing distillation residue

Publications (1)

Publication Number Publication Date
JPS55151086A true JPS55151086A (en) 1980-11-25

Family

ID=13076888

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5818379A Pending JPS55151086A (en) 1979-05-12 1979-05-12 Fluidized catalytic cracking of heavy petroleum containing distillation residue

Country Status (1)

Country Link
JP (1) JPS55151086A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63159492A (en) * 1986-09-03 1988-07-02 モービル・オイル・コーポレイション Fluidized catalytic cracking method
JP2017019962A (en) * 2015-07-14 2017-01-26 出光興産株式会社 Catalytic cracking method for raw oil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63159492A (en) * 1986-09-03 1988-07-02 モービル・オイル・コーポレイション Fluidized catalytic cracking method
JP2017019962A (en) * 2015-07-14 2017-01-26 出光興産株式会社 Catalytic cracking method for raw oil

Similar Documents

Publication Publication Date Title
US4331533A (en) Method and apparatus for cracking residual oils
US3679576A (en) Fluidized catalytic cracking apparatus and process
US4336160A (en) Method and apparatus for cracking residual oils
US2543884A (en) Process for cracking and coking heavy hydryocarbons
US2358888A (en) Catalytic conversion of hydrocarbons
US3424672A (en) Fluid catalytic stripping
US3812029A (en) Device for injecting easily coked fluids into a high temperature vessel
US3303123A (en) Catalytic cracking of residuum oils containing metal contaminants in several stages
US3751359A (en) Conversion of hydrocarbons
US2450724A (en) Conversion of sulfur containing hydrocarbons
JPS5848597B2 (en) Method of converting hydrocarbons into gasoline and fuel oil
US3065166A (en) Catalytic cracking process with the production of high octane gasoline
US3042196A (en) Catalytic conversion of hydrocarbon oils with the use of different types of feed oils
US2247126A (en) Clean circuit powdered catalyst cracking
US2616836A (en) Products from catalytic cracking
US2700017A (en) Method of coking residual hydrocarbons
US2902430A (en) Removal of metal contaminants from catalytic cracking feed stocks with sulfuric acid
JPS55151086A (en) Fluidized catalytic cracking of heavy petroleum containing distillation residue
US3190828A (en) Catalytic process for cracking oils containing metallic contaminants
US2322019A (en) Art of treating hydrocarbons
US2734021A (en) Preparation of catalytic feed stocks
US2305004A (en) Chemical process
GB548134A (en) An improved process for the catalytic treatment of hydrocarbon oils
US2432277A (en) Catalytic cracking of hydrocarbon oils
US2737475A (en) Conversion of hydrocarbons