CA729167A - Conversion process - Google Patents
Conversion processInfo
- Publication number
- CA729167A CA729167A CA729167A CA729167DA CA729167A CA 729167 A CA729167 A CA 729167A CA 729167 A CA729167 A CA 729167A CA 729167D A CA729167D A CA 729167DA CA 729167 A CA729167 A CA 729167A
- Authority
- CA
- Canada
- Prior art keywords
- conversion process
- conversion
- 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
Links
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA729167T |
Publications (1)
Publication Number | Publication Date |
---|---|
CA729167A true CA729167A (en) | 1966-03-01 |
Family
ID=36068082
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA729167A Expired CA729167A (en) | Conversion process |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA729167A (en) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4263130A (en) * | 1978-07-25 | 1981-04-21 | Phillips Petroleum Company | Process for cracking hydrocarbons with a catalyst passivated with an antimony tris (hydrocarbyl sulfide) |
US4279735A (en) * | 1978-07-25 | 1981-07-21 | Phillips Petroleum Company | Passivation of metals contaminating a used cracking catalyst with certain antimony carbonates and their thio analogues |
US4280896A (en) * | 1979-12-31 | 1981-07-28 | Exxon Research & Engineering Co. | Passivation of cracking catalysts |
US4280895A (en) * | 1979-12-31 | 1981-07-28 | Exxon Research & Engineering Co. | Passivation of cracking catalysts |
US4324648A (en) * | 1980-03-24 | 1982-04-13 | Phillips Petroleum Company | Cracking catalyst poisons passivated with tin compounds plus both sulfur and phosphorus |
EP0066018A1 (en) * | 1981-06-01 | 1982-12-08 | Exxon Research And Engineering Company | Method of reducing coke formation in heavy hydrocarbon feed catalytic cracking |
US4372841A (en) * | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
US4372840A (en) | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
US4397767A (en) * | 1982-02-12 | 1983-08-09 | Phillips Petroleum Company | Catalyst poisons passivated with tin compounds plus both sulfur and phosphorus |
US4432864A (en) * | 1979-11-14 | 1984-02-21 | Ashland Oil, Inc. | Carbo-metallic oil conversion with liquid water containing H2 S |
US4584283A (en) * | 1980-08-05 | 1986-04-22 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
US4664779A (en) * | 1980-08-05 | 1987-05-12 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
US4728629A (en) * | 1980-08-05 | 1988-03-01 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
US4986896A (en) * | 1989-04-13 | 1991-01-22 | Mobil Oil Corp. | Method for passivating metals on an FCC catalyst |
US5007999A (en) * | 1989-04-13 | 1991-04-16 | Mobil Oil Corporation | Method for reducing sulfur oxide emission during an FCC operation |
USRE37789E1 (en) | 1980-11-17 | 2002-07-16 | Phillips Petroleum Company | Regenerating zeolitic cracking catalyst |
-
0
- CA CA729167A patent/CA729167A/en not_active Expired
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4279735A (en) * | 1978-07-25 | 1981-07-21 | Phillips Petroleum Company | Passivation of metals contaminating a used cracking catalyst with certain antimony carbonates and their thio analogues |
US4263130A (en) * | 1978-07-25 | 1981-04-21 | Phillips Petroleum Company | Process for cracking hydrocarbons with a catalyst passivated with an antimony tris (hydrocarbyl sulfide) |
US4432864A (en) * | 1979-11-14 | 1984-02-21 | Ashland Oil, Inc. | Carbo-metallic oil conversion with liquid water containing H2 S |
US4280896A (en) * | 1979-12-31 | 1981-07-28 | Exxon Research & Engineering Co. | Passivation of cracking catalysts |
US4280895A (en) * | 1979-12-31 | 1981-07-28 | Exxon Research & Engineering Co. | Passivation of cracking catalysts |
US4372841A (en) * | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
US4372840A (en) | 1979-12-31 | 1983-02-08 | Exxon Research And Engineering Co. | Process for reducing coke formation in heavy feed catalytic cracking |
US4324648A (en) * | 1980-03-24 | 1982-04-13 | Phillips Petroleum Company | Cracking catalyst poisons passivated with tin compounds plus both sulfur and phosphorus |
US4728629A (en) * | 1980-08-05 | 1988-03-01 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
US4584283A (en) * | 1980-08-05 | 1986-04-22 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
US4664779A (en) * | 1980-08-05 | 1987-05-12 | Phillips Petroleum Company | Cracking catalyst restoration with aluminum compounds |
USRE37789E1 (en) | 1980-11-17 | 2002-07-16 | Phillips Petroleum Company | Regenerating zeolitic cracking catalyst |
USRE37842E1 (en) | 1980-11-17 | 2002-09-17 | Phillips Petroleum Company | Regenerating zeolitic cracking catalyst |
EP0066018A1 (en) * | 1981-06-01 | 1982-12-08 | Exxon Research And Engineering Company | Method of reducing coke formation in heavy hydrocarbon feed catalytic cracking |
US4397767A (en) * | 1982-02-12 | 1983-08-09 | Phillips Petroleum Company | Catalyst poisons passivated with tin compounds plus both sulfur and phosphorus |
US4986896A (en) * | 1989-04-13 | 1991-01-22 | Mobil Oil Corp. | Method for passivating metals on an FCC catalyst |
US5007999A (en) * | 1989-04-13 | 1991-04-16 | Mobil Oil Corporation | Method for reducing sulfur oxide emission during an FCC operation |
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