GB1387127A - Fluidized catalytic cracking process - Google Patents
Fluidized catalytic cracking processInfo
- Publication number
- GB1387127A GB1387127A GB2034072A GB2034072A GB1387127A GB 1387127 A GB1387127 A GB 1387127A GB 2034072 A GB2034072 A GB 2034072A GB 2034072 A GB2034072 A GB 2034072A GB 1387127 A GB1387127 A GB 1387127A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- riser
- separation zone
- regenerated
- passing
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/321—Catalytic processes
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
1387127 Chemical contact apparatus UNIVERSAL OIL PRODUCTS CO 2 May 1972 [3 May 1971] 20340/72 Heading B1F [Also in Division C5] A catalytic cracking in which both regenerated and unregenerated catalyst are recycled to the reactor riser (b) process comprises (a) cracking a feed stream (1) in contact with a mixture of regenerated catalyst and recycled used catalyst in a riser (6), (b) passing used catalyst, cracked products and any uncracked feed into a separation zone (8), (c) passing part of the used catalyst from the separation zone to a regeneration zone (9) where coke is removed from the catalyst, (d) passing regenerated catalyst from the regeneration zone to the riser (by line 18) to provide the regenerated catalyst for step (a), and (e) passing part of the used catalyst from the separation zone to the riser (by line 5) to provide the recycled used catalyst for a step (a), without mixing of the two catalyst streams outside the riser. As shown, the separation zone 8 includes a fluidized dense bed 16 in which further cracking takes place; both catalyst streams are stripped by gases from lines 19 and 20; and cracked products and spent regeneration gases are taken off by lines 10 and 11 through cyclone separators 12 and 13. Suitable catalysts are zirconia, silica, silica-alumina and zeolite.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13943371A | 1971-05-03 | 1971-05-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1387127A true GB1387127A (en) | 1975-03-12 |
Family
ID=22486628
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2034072A Expired GB1387127A (en) | 1971-05-03 | 1972-05-02 | Fluidized catalytic cracking process |
Country Status (21)
Country | Link |
---|---|
JP (1) | JPS525032B1 (en) |
AR (1) | AR192444A1 (en) |
AU (1) | AU459793B2 (en) |
BE (1) | BE782612A (en) |
BR (1) | BR7202712D0 (en) |
CA (1) | CA967498A (en) |
DD (1) | DD97138A5 (en) |
DE (1) | DE2221618A1 (en) |
DK (1) | DK143988C (en) |
EG (1) | EG10866A (en) |
ES (1) | ES402306A1 (en) |
FI (1) | FI55860C (en) |
FR (1) | FR2135237B1 (en) |
GB (1) | GB1387127A (en) |
HU (1) | HU166038B (en) |
IT (1) | IT957690B (en) |
NL (1) | NL173482C (en) |
SE (1) | SE396087B (en) |
SU (1) | SU854267A3 (en) |
TR (1) | TR17454A (en) |
ZA (1) | ZA722959B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8815166B2 (en) | 2012-03-20 | 2014-08-26 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8936758B2 (en) | 2012-03-20 | 2015-01-20 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5548206B2 (en) * | 2008-09-30 | 2014-07-16 | ユーオーピー エルエルシー | Apparatus and method for mixing regenerated catalyst and carbonized catalyst |
US8815082B2 (en) * | 2011-12-12 | 2014-08-26 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8747657B2 (en) * | 2011-12-12 | 2014-06-10 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2377935A (en) * | 1941-04-24 | 1945-06-12 | Standard Oil Co | Catalytic hydrocarbon conversion system |
-
1972
- 1972-04-25 BE BE782612A patent/BE782612A/en unknown
- 1972-05-02 HU HUUI191A patent/HU166038B/hu unknown
- 1972-05-02 ZA ZA722959A patent/ZA722959B/en unknown
- 1972-05-02 GB GB2034072A patent/GB1387127A/en not_active Expired
- 1972-05-02 EG EG181/72A patent/EG10866A/en active
- 1972-05-02 ES ES402306A patent/ES402306A1/en not_active Expired
- 1972-05-02 BR BR2712/72A patent/BR7202712D0/en unknown
- 1972-05-02 FI FI1238/72A patent/FI55860C/en active
- 1972-05-02 SE SE7205775A patent/SE396087B/en unknown
- 1972-05-02 CA CA141,084A patent/CA967498A/en not_active Expired
- 1972-05-02 DK DK218172A patent/DK143988C/en active
- 1972-05-02 IT IT4999972A patent/IT957690B/en active
- 1972-05-03 TR TR17454A patent/TR17454A/en unknown
- 1972-05-03 NL NLAANVRAGE7205939,A patent/NL173482C/en not_active IP Right Cessation
- 1972-05-03 AU AU41834/72A patent/AU459793B2/en not_active Expired
- 1972-05-03 DE DE19722221618 patent/DE2221618A1/en active Pending
- 1972-05-03 DD DD162719A patent/DD97138A5/xx unknown
- 1972-05-03 FR FR7215630A patent/FR2135237B1/fr not_active Expired
- 1972-05-03 AR AR241776A patent/AR192444A1/en active
- 1972-05-03 SU SU721780734A patent/SU854267A3/en active
- 1972-05-04 JP JP47044518A patent/JPS525032B1/ja active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8815166B2 (en) | 2012-03-20 | 2014-08-26 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
US8936758B2 (en) | 2012-03-20 | 2015-01-20 | Uop Llc | Process and apparatus for mixing two streams of catalyst |
Also Published As
Publication number | Publication date |
---|---|
EG10866A (en) | 1976-08-31 |
DK143988C (en) | 1982-05-03 |
ZA722959B (en) | 1973-02-28 |
ES402306A1 (en) | 1975-04-01 |
AU459793B2 (en) | 1975-04-10 |
BE782612A (en) | 1972-10-25 |
TR17454A (en) | 1975-07-23 |
DE2221618A1 (en) | 1972-11-23 |
SU854267A3 (en) | 1981-08-07 |
CA967498A (en) | 1975-05-13 |
FR2135237B1 (en) | 1975-08-29 |
AR192444A1 (en) | 1973-02-21 |
DK143988B (en) | 1981-11-09 |
HU166038B (en) | 1974-12-28 |
AU4183472A (en) | 1973-11-08 |
JPS525032B1 (en) | 1977-02-09 |
NL173482B (en) | 1983-09-01 |
NL173482C (en) | 1984-02-01 |
FI55860B (en) | 1979-06-29 |
SE396087B (en) | 1977-09-05 |
FR2135237A1 (en) | 1972-12-15 |
IT957690B (en) | 1973-10-20 |
FI55860C (en) | 1979-10-10 |
BR7202712D0 (en) | 1973-06-21 |
NL7205939A (en) | 1972-11-07 |
DD97138A5 (en) | 1973-04-20 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |