FI64900B - Krackningskatalysatorkomposition och foerfarande foer krackning av ett kolvaete-inmatningsmaterial - Google Patents

Krackningskatalysatorkomposition och foerfarande foer krackning av ett kolvaete-inmatningsmaterial Download PDF

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Publication number
FI64900B
FI64900B FI783204A FI783204A FI64900B FI 64900 B FI64900 B FI 64900B FI 783204 A FI783204 A FI 783204A FI 783204 A FI783204 A FI 783204A FI 64900 B FI64900 B FI 64900B
Authority
FI
Finland
Prior art keywords
catalyst
antimony
tin
cracking
weight
Prior art date
Application number
FI783204A
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English (en)
Finnish (fi)
Other versions
FI64900C (fi
FI783204A (fi
Inventor
Brent Joseph Bertus
Dwight Lamar Mckay
Original Assignee
Phillips Petroleum Co
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
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First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=27126560&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=FI64900(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority claimed from US05/941,896 external-priority patent/US4255287A/en
Application filed by Phillips Petroleum Co filed Critical Phillips Petroleum Co
Publication of FI783204A publication Critical patent/FI783204A/fi
Priority to FI824525A priority Critical patent/FI66128C/fi
Publication of FI64900B publication Critical patent/FI64900B/fi
Application granted granted Critical
Publication of FI64900C publication Critical patent/FI64900C/fi

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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
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/90—Regeneration or reactivation
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/20—Regeneration or reactivation
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56—Platinum group metals
    • B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/644—Arsenic, antimony or bismuth
    • B01J23/6445—Antimony
    • 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
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides

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

Claims (14)

1. Krackningskatalysatorkomposition innehällande en med zeolit modifierad krackningskatalysator av kiseldioxid-aluminiumoxid och (A) elementärt antimon och/eller en antimonförening, k ä n n e -tecknad av att den ytterligare innehäller (B) elementärt tenn och/eller en tennförening, varvid komponenterna (A) och (B) föreligger i en mängd som ger en antimonmängd av 0,0001-8 vikt-procent och en tennmängd av 0,0001-8 viktprocent, vilka mängder baserar sig pä vikten av krackningskatalysatorn fore tillsatsen av komponenterna (A) och (B).
2. Komposition enligt patentkravet 1, kännetecknad av att krackningskatalysatorn är en använd krackningskatalysator pä vilken en deaktiverande mängd nickel, järn och/eller vanadinium avsatts.
3. Komposition enligt patentkravet 1, kännetecknad av att komponenterna (A) och (B) föreligger i en mängd av 0,005-8 viktprocent.
4. Komposition enligt patentkravet 1, kännetecknad av att mängden antimon är 0,01-1 viktprocent och mängden tenn är cirka 0,001-1 viktprocent.
5. Komposition enligt patentkravet 1, kännetecknad av att viktförhällandet mellan antimon och tenn är 5:1 - 15:1.
6. Komposition enligt nägot av patentkraven 1-5, kännetecknad av att antimonföreningen är antimon-tris(0,0-di-propyl-fosforditioat).
7. Komposition enligt nägot av patentkraven 1-6, kännetecknad av att tennföreningen är dibutyltennoxid.
8. Komposition enligt nägot av patentkraven 1-6, kännetecknad av att tennföreningen är dibutyltenn-bis(iso-oktyl-merkaptoacetat).
9. Komposition enligt nägot av patentkraven L-6, kännetecknad av att tennföreningen är tonn(IV)- eller tenn (II)-0,0-dipropy Lfosforditioat.
FI783204A 1977-10-25 1978-10-20 Krackningskatalysatorkomposition och foerfarande foer krackning av ett kolvaete-inmatningsmaterial FI64900C (fi)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FI824525A FI66128C (fi) 1977-10-25 1982-12-30 Passiveringsmedel och foerfarande foer passivering av kontaminerande metaller pao en krackningskatalysator

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US84518477A 1977-10-25 1977-10-25
US84518477 1977-10-25
US94189678 1978-09-12
US05/941,896 US4255287A (en) 1978-09-12 1978-09-12 Cracking catalyst

Publications (3)

Publication Number Publication Date
FI783204A FI783204A (fi) 1979-04-26
FI64900B true FI64900B (fi) 1983-10-31
FI64900C FI64900C (fi) 1984-02-10

Family

ID=27126560

Family Applications (1)

Application Number Title Priority Date Filing Date
FI783204A FI64900C (fi) 1977-10-25 1978-10-20 Krackningskatalysatorkomposition och foerfarande foer krackning av ett kolvaete-inmatningsmaterial

Country Status (19)

Country Link
EP (1) EP0001642B1 (sv)
JP (1) JPS5935259B2 (sv)
AT (1) AT374488B (sv)
AU (1) AU511282B2 (sv)
BR (1) BR7806981A (sv)
CA (1) CA1225074A (sv)
DE (1) DE2862431D1 (sv)
DK (1) DK160995C (sv)
ES (1) ES474430A1 (sv)
FI (1) FI64900C (sv)
IT (1) IT1192587B (sv)
MX (1) MX150887A (sv)
NO (1) NO156948C (sv)
PH (1) PH14374A (sv)
PL (1) PL124764B1 (sv)
PT (1) PT68688A (sv)
RO (1) RO77416A2 (sv)
TR (1) TR20304A (sv)
YU (1) YU41124B (sv)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4218337A (en) * 1978-03-13 1980-08-19 Phillips Petroleum Company Passivating metals on cracking catalysts with tellurium
US4169042A (en) * 1978-03-13 1979-09-25 Phillips Petroleum Company Cracking process and catalyst for same containing tellurium
EP0051689A1 (en) * 1980-11-10 1982-05-19 Phillips Petroleum Company Method for passivating contaminant metals on a cracking catalyst and cracking process
US4488984A (en) * 1983-07-05 1984-12-18 Nalco Chemical Company Self-dispersing antimony oxide sols
US4504381A (en) * 1983-12-09 1985-03-12 Exxon Research And Engineering Co. Passivation of cracking catalysts with cadmium and tin
CA1240946A (en) * 1983-12-09 1988-08-23 Carl F. Bertsch Passivation of cracking catalyst
JPS60258288A (ja) * 1984-06-01 1985-12-20 ガルフ・リサ−チ・エンド・デベロツプメント・コンパニ− 接触分解方法
US4889617A (en) * 1986-03-24 1989-12-26 Chevron Research Company Method of suppressing sodium poisoning of cracking catalysts during fluid catalytic cracking
US4939109A (en) * 1986-09-15 1990-07-03 Phillips Petroleum Company Passivation of metal contaminated cracking catalysts
US5401384A (en) * 1993-12-17 1995-03-28 Inteven, S.A. Antimony and tin containing compound, use of such a compound as a passivating agent, and process for preparing such a compound
JP3534405B1 (ja) 2002-11-28 2004-06-07 鐘淵化学工業株式会社 耐熱性フレキシブル積層板の製造方法およびこれにより製造される耐熱性フレキシブル積層板
RU2603964C2 (ru) * 2011-11-21 2016-12-10 Басф Корпорейшн Усовершенствованный пассиватор/ловушка металла для процессов кфк

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2934548A (en) * 1954-08-25 1960-04-26 Heyden Newport Chemical Corp Bimetallic organic compounds and compositions containing same
BE566528A (sv) * 1958-04-05
IT795163A (sv) * 1962-12-08
US3152170A (en) * 1959-07-01 1964-10-06 Distillers Co Yeast Ltd Production of unsaturated aliphatic nitriles
US3287210A (en) * 1962-12-26 1966-11-22 M & T Chemicals Inc Antimony compounds and compositions and method for protecting against microorganisms
CA818485A (en) * 1964-03-21 1969-07-22 J. Gasson Edward Oxidation catalysts
US3445521A (en) * 1966-11-17 1969-05-20 Standard Oil Co Promoted antimony-iron oxidation catalyst
US3530158A (en) * 1966-11-25 1970-09-22 M & T Chemicals Inc Organo antimony mercaptides and the preparation thereof
US3625867A (en) * 1967-06-02 1971-12-07 Takachika Yoshino Process for production of metal oxide-antimony oxide catalysts
GB1236949A (en) * 1968-10-09 1971-06-23 Ici Ltd Catalytic process for making polyesters
BE741001A (sv) * 1968-11-02 1970-04-01
US3711422A (en) * 1970-09-08 1973-01-16 Phillips Petroleum Co Cracking catalyst restoration with antimony compounds
US4025458A (en) * 1975-02-18 1977-05-24 Phillips Petroleum Company Passivating metals on cracking catalysts
US4040945A (en) * 1976-01-02 1977-08-09 Gulf Research & Development Company Hydrocarbon catalytic cracking process
US4101417A (en) * 1976-10-04 1978-07-18 Gulf Research & Development Company Method of negating the effects of metals poisoning on zeolitic cracking catalysts

Also Published As

Publication number Publication date
EP0001642A3 (en) 1979-05-16
AU511282B2 (en) 1980-08-07
DK160995B (da) 1991-05-13
ES474430A1 (es) 1980-01-16
MX150887A (es) 1984-08-09
DE2862431D1 (en) 1984-08-30
PL124764B1 (en) 1983-02-28
EP0001642B1 (en) 1984-07-25
JPS5935259B2 (ja) 1984-08-28
AT374488B (de) 1984-04-25
IT7829062A0 (it) 1978-10-24
BR7806981A (pt) 1979-05-08
YU248178A (en) 1983-02-28
DK160995C (da) 1991-11-04
PH14374A (en) 1981-06-17
RO77416A2 (ro) 1982-06-25
NO156948B (no) 1987-09-14
FI64900C (fi) 1984-02-10
NO783576L (no) 1979-04-26
TR20304A (tr) 1981-01-07
JPS54106093A (en) 1979-08-20
FI783204A (fi) 1979-04-26
AU4072578A (en) 1980-04-24
PT68688A (fr) 1978-11-01
ATA763778A (de) 1983-09-15
CA1225074A (en) 1987-08-04
NO156948C (no) 1987-12-23
IT1192587B (it) 1988-04-20
DK447778A (da) 1979-04-26
PL210499A1 (pl) 1979-07-30
YU41124B (en) 1986-12-31
EP0001642A2 (en) 1979-05-02

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Owner name: PHILLIPS PETROLEUM COMPANY