ES386940A1 - Catalytic cracking of hydrocarbons - Google Patents

Catalytic cracking of hydrocarbons

Info

Publication number
ES386940A1
ES386940A1 ES386940A ES386940A ES386940A1 ES 386940 A1 ES386940 A1 ES 386940A1 ES 386940 A ES386940 A ES 386940A ES 386940 A ES386940 A ES 386940A ES 386940 A1 ES386940 A1 ES 386940A1
Authority
ES
Spain
Prior art keywords
catalyst
reactor
boiling range
elongated reaction
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.)
Expired
Application number
ES386940A
Other languages
Spanish (es)
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.)
Texaco Development Corp
Original Assignee
Texaco Development 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 Texaco Development Corp filed Critical Texaco Development Corp
Publication of ES386940A1 publication Critical patent/ES386940A1/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • 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

Landscapes

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

Abstract

Improvements made to a process for catalytic cracking of a multiplicity of virgin gas-oils with a zeolitic cracking catalyst in a fluid catalytic cracking unit, comprising a reactor, a regenerator and a multiplicity of elongated reaction zones, in which said reactor contains a dense phase and a diluted phase of said catalyst and the mentioned elongated reaction zones end in said reactor and in which the mixtures of said gas-oils and catalyst are passed through said elongated reaction zones in catalytic cracking conditions to said reactor, characterized by said improvements consisting of: (a) passing through at least one elongated reaction zone a virgin gas oil with a boiling range of between 500º and 1050ºF (260 and 550ºC), (b) passing through at least one other elongated reaction zone a virgin gas oil with a boiling range of between 450º and 750ºF (221º and 399ºC), said gas oil from step (a) having a boiling range higher than that of the diesel oil in step (b) and (c) discharging the effluent from said elongated reaction zones in a catalyst phase contained in said reactor, said effluent being constituted by a vaporized reaction mixture, and the catalyst, with the conversion of gas oil to a boiling range being more high 0-30% lower in volume than lower boiling range diesel oil. (Machine-translation by Google Translate, not legally binding)
ES386940A 1969-12-31 1970-12-30 Catalytic cracking of hydrocarbons Expired ES386940A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US88949469A 1969-12-31 1969-12-31

Publications (1)

Publication Number Publication Date
ES386940A1 true ES386940A1 (en) 1973-04-16

Family

ID=25395223

Family Applications (1)

Application Number Title Priority Date Filing Date
ES386940A Expired ES386940A1 (en) 1969-12-31 1970-12-30 Catalytic cracking of hydrocarbons

Country Status (15)

Country Link
BE (1) BE761079A (en)
BR (1) BR7025028D0 (en)
CA (1) CA941324A (en)
CH (1) CH552048A (en)
DE (1) DE2064142C3 (en)
EG (1) EG10560A (en)
ES (1) ES386940A1 (en)
FI (1) FI50796C (en)
FR (1) FR2072150B1 (en)
GB (1) GB1317927A (en)
IE (1) IE34854B1 (en)
NL (1) NL157644B (en)
NO (1) NO128661B (en)
SE (1) SE364721B (en)
ZA (1) ZA708607B (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL9385C (en) * 1900-01-01
US3617496A (en) * 1969-06-25 1971-11-02 Gulf Research Development Co Fluid catalytic cracking process with a segregated feed charged to separate reactors

Also Published As

Publication number Publication date
CH552048A (en) 1974-07-31
DE2064142C3 (en) 1973-11-29
BE761079A (en) 1971-06-30
DE2064142A1 (en) 1971-07-08
ZA708607B (en) 1972-04-26
NL7019049A (en) 1971-07-02
SE364721B (en) 1974-03-04
GB1317927A (en) 1973-05-23
FI50796C (en) 1976-07-12
IE34854B1 (en) 1975-09-03
FI50796B (en) 1976-03-31
NO128661B (en) 1973-12-27
IE34854L (en) 1971-06-30
FR2072150A1 (en) 1971-09-24
BR7025028D0 (en) 1973-04-17
DE2064142B2 (en) 1973-04-26
CA941324A (en) 1974-02-05
NL157644B (en) 1978-08-15
EG10560A (en) 1976-04-30
FR2072150B1 (en) 1973-12-07

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