NO132675B - - Google Patents
Download PDFInfo
- Publication number
- NO132675B NO132675B NO4201/72A NO420172A NO132675B NO 132675 B NO132675 B NO 132675B NO 4201/72 A NO4201/72 A NO 4201/72A NO 420172 A NO420172 A NO 420172A NO 132675 B NO132675 B NO 132675B
- Authority
- NO
- Norway
- Prior art keywords
- catalyst
- collection
- flow
- hydrocarbon
- line
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 claims abstract description 141
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 25
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 25
- 239000007787 solid Substances 0.000 claims abstract description 21
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 15
- 239000002245 particle Substances 0.000 claims abstract description 10
- 239000007789 gas Substances 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 13
- 229910052739 hydrogen Inorganic materials 0.000 claims description 13
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 12
- 239000004020 conductor Substances 0.000 claims 1
- 239000006166 lysate Substances 0.000 claims 1
- 238000002407 reforming Methods 0.000 description 13
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 4
- 238000001833 catalytic reforming Methods 0.000 description 3
- 238000004891 communication Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000011949 solid catalyst Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 101150021515 Nin gene Proteins 0.000 description 1
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- GIGQFSYNIXPBCE-UHFFFAOYSA-N alumane;platinum Chemical compound [AlH3].[Pt] GIGQFSYNIXPBCE-UHFFFAOYSA-N 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000004517 catalytic hydrocracking Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000011874 heated mixture Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
- B01J8/0214—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical annular shaped bed
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/0035—Periodical feeding or evacuation
-
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
- B01J8/125—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/10—Catalytic reforming with moving catalysts
- C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US20012371A | 1971-11-18 | 1971-11-18 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NO132675B true NO132675B (da) | 1975-09-08 |
| NO132675C NO132675C (da) | 1975-12-17 |
Family
ID=22740435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO4201/72A NO132675C (da) | 1971-11-18 | 1972-11-17 |
Country Status (23)
| Country | Link |
|---|---|
| US (1) | US3785963A (da) |
| JP (1) | JPS5543380B2 (da) |
| AR (1) | AR200719A1 (da) |
| AT (1) | AT323869B (da) |
| AU (1) | AU471231B2 (da) |
| BG (1) | BG26818A3 (da) |
| BR (1) | BR7208064D0 (da) |
| CA (1) | CA969326A (da) |
| DD (1) | DD105249A5 (da) |
| DK (1) | DK142485B (da) |
| EG (1) | EG10903A (da) |
| ES (1) | ES408700A1 (da) |
| FR (1) | FR2160432B1 (da) |
| GB (1) | GB1408007A (da) |
| IE (1) | IE36843B1 (da) |
| IT (1) | IT974834B (da) |
| MY (1) | MY7600257A (da) |
| NL (1) | NL173144C (da) |
| NO (1) | NO132675C (da) |
| PL (1) | PL85025B1 (da) |
| SE (1) | SE381993B (da) |
| SU (1) | SU735157A3 (da) |
| ZA (1) | ZA727920B (da) |
Families Citing this family (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3856662A (en) * | 1973-04-02 | 1974-12-24 | Universal Oil Prod Co | Method for solids-withdrawal and transport from a superatmospheric pressure system |
| US3873441A (en) * | 1973-09-06 | 1975-03-25 | Universal Oil Prod Co | Catalyst transfer method for moving-bed reactors |
| US3978150A (en) * | 1975-03-03 | 1976-08-31 | Universal Oil Products Company | Continuous paraffin dehydrogenation process |
| US4110081A (en) * | 1977-06-09 | 1978-08-29 | Uop Inc. | Moving-bed radial flow solids-fluid contacting apparatus |
| FR2434648A1 (fr) * | 1978-08-30 | 1980-03-28 | Uop Inc | Chambre de reaction catalytique |
| FR2460990A1 (fr) * | 1979-07-09 | 1981-01-30 | Inst Francais Du Petrole | Procede et appareil de conversion catalytique d'hydrocarbures |
| US4403909A (en) * | 1980-03-24 | 1983-09-13 | Uop Inc. | Method for discharging catalyst particles from a moving bed system at a substantially steady flow rate |
| US4478793A (en) * | 1982-09-22 | 1984-10-23 | Uop Inc. | Radial flow reactor with operating temperature profile |
| US4968409A (en) * | 1984-03-21 | 1990-11-06 | Chevron Research Company | Hydrocarbon processing of gas containing feed in a countercurrent moving catalyst bed |
| US4925632A (en) * | 1988-01-29 | 1990-05-15 | Thacker Milton B | Low profile fluid catalytic cracking apparatus |
| AU1933088A (en) * | 1988-01-29 | 1989-08-25 | John M. Limburg | Low profile fluid catalytic cracking apparatus and method |
| US5516422A (en) * | 1994-05-06 | 1996-05-14 | Uop | Interreactor particle transfer process and arrangement |
| JP2002273199A (ja) * | 2001-03-15 | 2002-09-24 | Idemitsu Petrochem Co Ltd | ガス状流体の抜き出し方法 |
| US9006123B2 (en) * | 2008-12-23 | 2015-04-14 | Uop Llc | Catalytic reformer catalyst collector including purge gas stream |
| RU2708613C2 (ru) | 2015-03-31 | 2019-12-10 | Юоп Ллк | Способы и устройства для интегрированного процесса изомеризации и платформинга |
| FR3090007B1 (fr) * | 2018-12-18 | 2020-12-25 | Ifp Energies Now | Procede de conversion d’hydrocarbures avec recyclage des effluents de reduction |
-
1971
- 1971-11-18 US US00200123A patent/US3785963A/en not_active Expired - Lifetime
-
1972
- 1972-11-06 CA CA155,657A patent/CA969326A/en not_active Expired
- 1972-11-08 ZA ZA727920A patent/ZA727920B/xx unknown
- 1972-11-09 AU AU48645/72A patent/AU471231B2/en not_active Expired
- 1972-11-14 FR FR7240283A patent/FR2160432B1/fr not_active Expired
- 1972-11-14 AT AT968072A patent/AT323869B/de not_active IP Right Cessation
- 1972-11-16 NL NLAANVRAGE7215502,A patent/NL173144C/xx not_active IP Right Cessation
- 1972-11-16 PL PL1972158884A patent/PL85025B1/pl unknown
- 1972-11-16 IT IT54092/72A patent/IT974834B/it active
- 1972-11-16 EG EG470/72A patent/EG10903A/xx active
- 1972-11-16 BR BR008064/72A patent/BR7208064D0/pt unknown
- 1972-11-17 IE IE1590/72A patent/IE36843B1/xx unknown
- 1972-11-17 DK DK576172AA patent/DK142485B/da unknown
- 1972-11-17 SE SE7214996A patent/SE381993B/xx unknown
- 1972-11-17 SU SU721851052A patent/SU735157A3/ru active
- 1972-11-17 GB GB5313872A patent/GB1408007A/en not_active Expired
- 1972-11-17 ES ES408700A patent/ES408700A1/es not_active Expired
- 1972-11-17 NO NO4201/72A patent/NO132675C/no unknown
- 1972-11-17 DD DD166919A patent/DD105249A5/xx unknown
- 1972-11-18 BG BG7221901A patent/BG26818A3/xx unknown
- 1972-11-18 JP JP11611872A patent/JPS5543380B2/ja not_active Expired
- 1972-11-20 AR AR245203A patent/AR200719A1/es active
-
1976
- 1976-12-30 MY MY257/76A patent/MY7600257A/xx unknown
Also Published As
| Publication number | Publication date |
|---|---|
| AU4864572A (en) | 1974-05-09 |
| CA969326A (en) | 1975-06-17 |
| AR200719A1 (es) | 1974-12-13 |
| BR7208064D0 (pt) | 1973-08-23 |
| SU735157A3 (ru) | 1980-05-15 |
| AU471231B2 (en) | 1976-04-15 |
| FR2160432B1 (da) | 1977-08-26 |
| SE381993B (sv) | 1976-01-12 |
| IE36843L (en) | 1973-05-18 |
| DE2255408B2 (de) | 1975-09-11 |
| JPS5543380B2 (da) | 1980-11-06 |
| US3785963A (en) | 1974-01-15 |
| ZA727920B (en) | 1973-07-25 |
| DK142485C (da) | 1981-07-06 |
| BG26818A3 (da) | 1979-06-12 |
| FR2160432A1 (da) | 1973-06-29 |
| NL173144B (nl) | 1983-07-18 |
| MY7600257A (en) | 1976-12-31 |
| JPS4862673A (da) | 1973-09-01 |
| IE36843B1 (en) | 1977-03-02 |
| ES408700A1 (es) | 1976-03-01 |
| EG10903A (en) | 1976-08-31 |
| GB1408007A (en) | 1975-10-01 |
| DK142485B (da) | 1980-11-10 |
| NL173144C (nl) | 1983-12-16 |
| AT323869B (de) | 1975-08-11 |
| NO132675C (da) | 1975-12-17 |
| IT974834B (it) | 1974-07-10 |
| PL85025B1 (da) | 1976-04-30 |
| DD105249A5 (da) | 1974-04-12 |
| DE2255408A1 (de) | 1973-05-30 |
| NL7215502A (da) | 1973-05-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| NO132675B (da) | ||
| US5879537A (en) | Hydrocarbon conversion process using staggered bypassing of reaction zones | |
| US5211838A (en) | Fixed-bed/moving-bed two stage catalytic reforming with interstage aromatics removal | |
| US4119526A (en) | Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles | |
| US5354451A (en) | Fixed-bed/moving-bed two stage catalytic reforming | |
| US9708551B2 (en) | Regenerator for catalysts | |
| US5221463A (en) | Fixed-bed/moving-bed two stage catalytic reforming with recycle of hydrogen-rich stream to both stages | |
| US5196110A (en) | Hydrogen recycle between stages of two stage fixed-bed/moving-bed unit | |
| US4478793A (en) | Radial flow reactor with operating temperature profile | |
| US5190638A (en) | Moving bed/fixed bed two stage catalytic reforming | |
| US5073352A (en) | Apparatus for the low pressure reforming of gasolines with heating by smoke gases | |
| JPH0260993A (ja) | 複数の中空内部空間における熱移送液の流通による接触リホーミング法 | |
| US2730488A (en) | Liquid bath continuous conversion coking process and apparatus | |
| US4498973A (en) | Multiple-stage catalytic reforming with gravity-flowing dissimilar catalyst particles | |
| US4325807A (en) | Multiple stage hydrocarbon conversion with gravity flowing catalyst particles | |
| US4325806A (en) | Multiple stage hydrocarbon conversion with gravity flowing catalyst particles | |
| US9708552B2 (en) | Regenerator for regenerating catalysts under different operating conditions | |
| US5190639A (en) | Multiple fixed-bed reforming units sharing common moving bed reactor | |
| US4411869A (en) | Multiple stage reactor system | |
| US10557091B2 (en) | Process for increasing hydrocarbon yield from catalytic reformer | |
| US2905633A (en) | Method and apparatus for hydrocarbon conversion employing hydrocarbon reactant and recycle gas containing solid particles | |
| US2594289A (en) | Method and apparatus for processes employing fluent solids | |
| US2902436A (en) | Hydrogenative conversion of hydrocarbons | |
| US2772216A (en) | Reforming at a plurality of severities with constant recycle gas of optimum hydrogenconcentration to all zones | |
| CN108473878A (zh) | 催化反应方法中的催化剂分级 |