JPS5648250A - Regeneration of catalyst used for contact decomposition of heavy oil containing high-sulfur - Google Patents
Regeneration of catalyst used for contact decomposition of heavy oil containing high-sulfurInfo
- Publication number
- JPS5648250A JPS5648250A JP12473479A JP12473479A JPS5648250A JP S5648250 A JPS5648250 A JP S5648250A JP 12473479 A JP12473479 A JP 12473479A JP 12473479 A JP12473479 A JP 12473479A JP S5648250 A JPS5648250 A JP S5648250A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- tower
- sulfide
- coke
- sulfur
- 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
Links
- 239000003054 catalyst Substances 0.000 title abstract 12
- 229910052717 sulfur Inorganic materials 0.000 title abstract 3
- 239000011593 sulfur Substances 0.000 title abstract 3
- 238000000354 decomposition reaction Methods 0.000 title abstract 2
- 230000008929 regeneration Effects 0.000 title abstract 2
- 238000011069 regeneration method Methods 0.000 title abstract 2
- 239000000295 fuel oil Substances 0.000 title 1
- 239000000571 coke Substances 0.000 abstract 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 abstract 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 abstract 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract 2
- 239000012530 fluid Substances 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 abstract 2
- 229910052742 iron Inorganic materials 0.000 abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 238000002309 gasification Methods 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 150000004763 sulfides Chemical class 0.000 abstract 1
- 150000003464 sulfur compounds Chemical class 0.000 abstract 1
Landscapes
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
PURPOSE:To realize a highly profitable regeneration of the titled catalyst without exhausting any sulfur dioxide by fixing the sulfur deposited on the catalyst along with the coke onto the catalyst which is reduced via a partial burning under the reduction state of the coke and in the form of a sulfide and then decomposing the sulfide into the hydrogen sulfide. CONSTITUTION:The raw oil is supplied to the tower 1 through the inlet 2, and thus the fluid floor 3 of the catalyst particle is formed within the tower to perform the contact decomposition. The light-duty oil thus obtained is gathered through the top part 4 along with the gas for formation of the fluid floor. In that case, the coke containing the sulfur is deposited on the catalyst. This catalyst is supplied to the tower 6 through the tube 11, and then the oxygen content gas such as the air or the like is introduced through the supply mouth 7 to give a partial burning to the coke in the state of reduction. Thus the iron in the catalyst is reduced, and the sulfur compound produced due to gasification of the coke is fixed on the catalyst under the reducing state as a sulfide. A part of the catalyst reduced through the tower 6 is circulated to the tower 1 through the tube 5 for a purpose of heat supply. The reduced catalyst with the sulfide fixed is then supplied to the tower 9 via the tube 8 and then given a contact to the steam. Thus the sulfide is decomposed into the hydrogen sulfide to turn the iron into an oxide. In this way, the catalyst can be regenerated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12473479A JPS5648250A (en) | 1979-09-29 | 1979-09-29 | Regeneration of catalyst used for contact decomposition of heavy oil containing high-sulfur |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12473479A JPS5648250A (en) | 1979-09-29 | 1979-09-29 | Regeneration of catalyst used for contact decomposition of heavy oil containing high-sulfur |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5648250A true JPS5648250A (en) | 1981-05-01 |
Family
ID=14892781
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12473479A Pending JPS5648250A (en) | 1979-09-29 | 1979-09-29 | Regeneration of catalyst used for contact decomposition of heavy oil containing high-sulfur |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5648250A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107126976A (en) * | 2017-04-25 | 2017-09-05 | 广东新华粤树脂科技有限公司 | Crack the hydrogenation catalyst steam blowing hydrogen heat air lift combining and regenerating method of carbon nine |
-
1979
- 1979-09-29 JP JP12473479A patent/JPS5648250A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107126976A (en) * | 2017-04-25 | 2017-09-05 | 广东新华粤树脂科技有限公司 | Crack the hydrogenation catalyst steam blowing hydrogen heat air lift combining and regenerating method of carbon nine |
CN107126976B (en) * | 2017-04-25 | 2021-11-16 | 广东新华粤树脂科技有限公司 | Steam purging-hydrogen hot gas stripping combined regeneration method for cracking carbon nine hydrogenation catalyst |
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