CN101921610B - 循环至少一部分来自催化剂还原阶段的流出物的汽油的预再生重整方法 - Google Patents
循环至少一部分来自催化剂还原阶段的流出物的汽油的预再生重整方法 Download PDFInfo
- Publication number
- CN101921610B CN101921610B CN201010228949.9A CN201010228949A CN101921610B CN 101921610 B CN101921610 B CN 101921610B CN 201010228949 A CN201010228949 A CN 201010228949A CN 101921610 B CN101921610 B CN 101921610B
- Authority
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- China
- Prior art keywords
- effluent
- reactor
- catalyst
- reactors
- hydrogen
- 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.)
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Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 66
- 230000009467 reduction Effects 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 25
- 230000008569 process Effects 0.000 title claims abstract description 15
- 238000011069 regeneration method Methods 0.000 title claims description 21
- 239000003502 gasoline Substances 0.000 title claims description 13
- 238000004064 recycling Methods 0.000 title abstract description 9
- 238000002407 reforming Methods 0.000 title abstract description 7
- 239000001257 hydrogen Substances 0.000 claims abstract description 38
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 38
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 230000008929 regeneration Effects 0.000 claims description 20
- 238000001833 catalytic reforming Methods 0.000 claims description 19
- 238000000926 separation method Methods 0.000 claims description 4
- 238000004821 distillation Methods 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 23
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000001172 regenerating effect Effects 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 29
- 239000007789 gas Substances 0.000 description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 11
- 239000000460 chlorine Substances 0.000 description 11
- 229910052801 chlorine Inorganic materials 0.000 description 11
- 238000010586 diagram Methods 0.000 description 10
- 239000002994 raw material Substances 0.000 description 9
- 238000000746 purification Methods 0.000 description 8
- 239000000571 coke Substances 0.000 description 7
- 230000007423 decrease Effects 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000001491 aromatic compounds Chemical class 0.000 description 2
- 238000010531 catalytic reduction reaction Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000006356 dehydrogenation reaction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000006057 reforming reaction Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- 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
- C10G11/16—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "moving bed" method
-
- 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
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR09/02802 | 2009-06-10 | ||
| FR0902802A FR2946660B1 (fr) | 2009-06-10 | 2009-06-10 | Procede de reformage pregeneratif des essences comportant le recyclage d'au moins une partie de l'effluent de la phase de reduction du catalyseur. |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101921610A CN101921610A (zh) | 2010-12-22 |
| CN101921610B true CN101921610B (zh) | 2014-11-19 |
Family
ID=41590950
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201010228949.9A Active CN101921610B (zh) | 2009-06-10 | 2010-06-10 | 循环至少一部分来自催化剂还原阶段的流出物的汽油的预再生重整方法 |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US9163184B2 (enExample) |
| JP (1) | JP5662062B2 (enExample) |
| KR (1) | KR101814200B1 (enExample) |
| CN (1) | CN101921610B (enExample) |
| BR (1) | BRPI1001927B1 (enExample) |
| FR (1) | FR2946660B1 (enExample) |
| TW (1) | TWI495718B (enExample) |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2769291B1 (en) | 2011-10-18 | 2021-04-28 | Carnegie Mellon University | Method and apparatus for classifying touch events on a touch sensitive surface |
| KR20140114766A (ko) | 2013-03-19 | 2014-09-29 | 퀵소 코 | 터치 입력을 감지하기 위한 방법 및 장치 |
| US9612689B2 (en) | 2015-02-02 | 2017-04-04 | Qeexo, Co. | Method and apparatus for classifying a touch event on a touchscreen as related to one of multiple function generating interaction layers and activating a function in the selected interaction layer |
| US9013452B2 (en) | 2013-03-25 | 2015-04-21 | Qeexo, Co. | Method and system for activating different interactive functions using different types of finger contacts |
| US20150035759A1 (en) * | 2013-08-02 | 2015-02-05 | Qeexo, Co. | Capture of Vibro-Acoustic Data Used to Determine Touch Types |
| US9138738B1 (en) | 2014-04-14 | 2015-09-22 | Uop Llc | Processes for the continuous regeneration of a catalyst |
| FR3025438B1 (fr) * | 2014-09-10 | 2018-05-11 | IFP Energies Nouvelles | Regenerateur de catalyseurs. |
| US9329715B2 (en) | 2014-09-11 | 2016-05-03 | Qeexo, Co. | Method and apparatus for differentiating touch screen users based on touch event analysis |
| US11619983B2 (en) | 2014-09-15 | 2023-04-04 | Qeexo, Co. | Method and apparatus for resolving touch screen ambiguities |
| US10606417B2 (en) | 2014-09-24 | 2020-03-31 | Qeexo, Co. | Method for improving accuracy of touch screen event analysis by use of spatiotemporal touch patterns |
| US10282024B2 (en) | 2014-09-25 | 2019-05-07 | Qeexo, Co. | Classifying contacts or associations with a touch sensitive device |
| US10642404B2 (en) | 2015-08-24 | 2020-05-05 | Qeexo, Co. | Touch sensitive device with multi-sensor stream synchronized data |
| KR101974003B1 (ko) * | 2017-11-09 | 2019-04-30 | 한국남동발전 주식회사 | 우회배관이 구비된 탈황설비의 재열기 |
| US11009989B2 (en) | 2018-08-21 | 2021-05-18 | Qeexo, Co. | Recognizing and rejecting unintentional touch events associated with a touch sensitive device |
| FR3090007B1 (fr) | 2018-12-18 | 2020-12-25 | Ifp Energies Now | Procede de conversion d’hydrocarbures avec recyclage des effluents de reduction |
| US10942603B2 (en) | 2019-05-06 | 2021-03-09 | Qeexo, Co. | Managing activity states of an application processor in relation to touch or hover interactions with a touch sensitive device |
| US11231815B2 (en) | 2019-06-28 | 2022-01-25 | Qeexo, Co. | Detecting object proximity using touch sensitive surface sensing and ultrasonic sensing |
| US11028328B2 (en) * | 2019-10-07 | 2021-06-08 | Saudi Arabian Oil Company | Systems and processes for catalytic reforming of a hydrocarbon feed stock |
| US11592423B2 (en) | 2020-01-29 | 2023-02-28 | Qeexo, Co. | Adaptive ultrasonic sensing techniques and systems to mitigate interference |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3516924A (en) * | 1968-04-19 | 1970-06-23 | Universal Oil Prod Co | Catalytic reforming process |
| CN1045411A (zh) * | 1989-01-13 | 1990-09-19 | 法国石油公司 | 芳香烃制备或重整催化剂的再生方法 |
| US5203988A (en) * | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3761390A (en) * | 1969-09-25 | 1973-09-25 | Universal Oil Prod Co | Continuous reforming regeneration process |
| FR2160269A1 (en) * | 1971-11-16 | 1973-06-29 | Inst Francais Du Petrole | Catalytic conversion of hydrocarbons - using multiple zones in series with continuous circulation and regeneration of catal |
| FR2213335B1 (enExample) * | 1973-01-10 | 1976-04-23 | Inst Francais Du Petrole | |
| FR2378846A1 (fr) * | 1977-01-31 | 1978-08-25 | Inst Francais Du Petrole | Procede catalytique de reformage ou de production d'hydrocarbures aromatiques |
| PT67978B (en) * | 1977-05-09 | 1979-10-22 | Uop Inc | Multiple-stage hydrocarbon conversion with gravity-flowingcatalyst particles |
| US4613423A (en) * | 1985-05-02 | 1986-09-23 | Exxon Research And Engineering Co. | Catalytic reforming process |
| US5073250A (en) * | 1990-03-02 | 1991-12-17 | Chevron Research & Technology Company | Staged catalyst reforming to produce optimum octane barrel per calendar day reformate production |
| US5043057A (en) * | 1990-06-25 | 1991-08-27 | Exxon Research And Engineering Company | Removal of sulfur from recycle gas streams in catalytic reforming |
| US6458266B1 (en) | 1999-11-24 | 2002-10-01 | Phillips Petroleum Company | Catalytic reforming process with inhibition of catalyst deactivation |
| FR2801604B1 (fr) | 1999-11-30 | 2002-04-26 | Inst Francais Du Petrole | Procede pour la production d'aromatiques en lit mobile incluant une reduction du catalyseur |
| FR2801605B1 (fr) * | 1999-11-30 | 2002-02-01 | Inst Francais Du Petrole | Procede et dispositif pour la production d'aromatiques incluant une reduction du catalyseur |
| FR2835201B1 (fr) * | 2002-01-25 | 2004-04-09 | Inst Francais Du Petrole | Integration de la reduction du catalyseur d'un procede de conversion catalytique et de la regeneration des masses adsorbantes intervenant dans la purification de l'hydrogene necessaire a la reduction |
-
2009
- 2009-06-10 FR FR0902802A patent/FR2946660B1/fr not_active Expired - Fee Related
-
2010
- 2010-06-07 KR KR1020100053435A patent/KR101814200B1/ko active Active
- 2010-06-07 TW TW099118446A patent/TWI495718B/zh active
- 2010-06-09 BR BRPI1001927A patent/BRPI1001927B1/pt not_active IP Right Cessation
- 2010-06-09 US US12/796,712 patent/US9163184B2/en active Active
- 2010-06-10 CN CN201010228949.9A patent/CN101921610B/zh active Active
- 2010-06-10 JP JP2010132714A patent/JP5662062B2/ja active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3516924A (en) * | 1968-04-19 | 1970-06-23 | Universal Oil Prod Co | Catalytic reforming process |
| CN1045411A (zh) * | 1989-01-13 | 1990-09-19 | 法国石油公司 | 芳香烃制备或重整催化剂的再生方法 |
| US5203988A (en) * | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2010285618A (ja) | 2010-12-24 |
| TW201114884A (en) | 2011-05-01 |
| TWI495718B (zh) | 2015-08-11 |
| CN101921610A (zh) | 2010-12-22 |
| KR20100132912A (ko) | 2010-12-20 |
| FR2946660B1 (fr) | 2011-07-22 |
| FR2946660A1 (fr) | 2010-12-17 |
| US9163184B2 (en) | 2015-10-20 |
| BRPI1001927B1 (pt) | 2019-10-22 |
| KR101814200B1 (ko) | 2018-01-02 |
| BRPI1001927A2 (pt) | 2014-02-04 |
| JP5662062B2 (ja) | 2015-01-28 |
| US20100314288A1 (en) | 2010-12-16 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |