CN1386560A - Reactive distilling apparatus - Google Patents
Reactive distilling apparatus Download PDFInfo
- Publication number
- CN1386560A CN1386560A CN 01114953 CN01114953A CN1386560A CN 1386560 A CN1386560 A CN 1386560A CN 01114953 CN01114953 CN 01114953 CN 01114953 A CN01114953 A CN 01114953A CN 1386560 A CN1386560 A CN 1386560A
- Authority
- CN
- China
- Prior art keywords
- lifting tube
- steam lifting
- liquid phase
- phase material
- tower
- 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.)
- Granted
Links
- 238000006243 chemical reaction Methods 0.000 claims abstract description 76
- 239000000463 material Substances 0.000 claims abstract description 62
- 239000003054 catalyst Substances 0.000 claims abstract description 48
- 239000007791 liquid phase Substances 0.000 claims abstract description 44
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 21
- 239000012071 phase Substances 0.000 claims abstract description 11
- 238000004821 distillation Methods 0.000 claims description 56
- 239000012808 vapor phase Substances 0.000 claims description 15
- 238000011049 filling Methods 0.000 claims description 14
- 230000005540 biological transmission Effects 0.000 claims description 13
- 230000000694 effects Effects 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 7
- 150000001336 alkenes Chemical group 0.000 claims description 4
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 2
- 150000001345 alkine derivatives Chemical class 0.000 claims description 2
- 238000005804 alkylation reaction Methods 0.000 claims description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 2
- 150000001993 dienes Chemical class 0.000 claims description 2
- 230000032050 esterification Effects 0.000 claims description 2
- 238000005886 esterification reaction Methods 0.000 claims description 2
- 150000002191 fatty alcohols Chemical class 0.000 claims description 2
- 238000006703 hydration reaction Methods 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- 238000005984 hydrogenation reaction Methods 0.000 claims description 2
- 238000006317 isomerization reaction Methods 0.000 claims description 2
- 239000003209 petroleum derivative Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 description 43
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 26
- 239000000047 product Substances 0.000 description 22
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- 239000000376 reactant Substances 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 9
- 238000000926 separation method Methods 0.000 description 9
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 8
- BKOOMYPCSUNDGP-UHFFFAOYSA-N 2-methylbut-2-ene Chemical group CC=C(C)C BKOOMYPCSUNDGP-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000011068 loading method Methods 0.000 description 6
- 238000000066 reactive distillation Methods 0.000 description 6
- 241000282326 Felis catus Species 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 238000012856 packing Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000011949 solid catalyst Substances 0.000 description 2
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 101000809257 Homo sapiens Ubiquitin carboxyl-terminal hydrolase 4 Proteins 0.000 description 1
- 102100038463 Ubiquitin carboxyl-terminal hydrolase 4 Human genes 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010523 cascade reaction Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000007127 saponification reaction Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- HVZJRWJGKQPSFL-UHFFFAOYSA-N tert-Amyl methyl ether Chemical compound CCC(C)(C)OC HVZJRWJGKQPSFL-UHFFFAOYSA-N 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB011149531A CN1170609C (en) | 2001-05-18 | 2001-05-18 | Reactive distilling apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB011149531A CN1170609C (en) | 2001-05-18 | 2001-05-18 | Reactive distilling apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1386560A true CN1386560A (en) | 2002-12-25 |
CN1170609C CN1170609C (en) | 2004-10-13 |
Family
ID=4661553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB011149531A Expired - Fee Related CN1170609C (en) | 2001-05-18 | 2001-05-18 | Reactive distilling apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1170609C (en) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102462971A (en) * | 2010-11-11 | 2012-05-23 | 中国石油化工股份有限公司 | Mobile catalytic distillation equipment and its application |
CN103436286A (en) * | 2013-07-18 | 2013-12-11 | 济南开发区星火科学技术研究院 | Catalytic rectification hydrogenation desulfurization process of gasoline heavy distillate |
CN104342202A (en) * | 2013-08-06 | 2015-02-11 | 中国石油大学(北京) | Lubricating oil base oil raw material deacidification device and method |
CN105561617A (en) * | 2014-10-09 | 2016-05-11 | 中国石油化工股份有限公司 | Efficient catalysis rectification apparatus and applications thereof |
CN105561615A (en) * | 2014-10-09 | 2016-05-11 | 中国石油化工股份有限公司 | Catalysis rectification apparatus and applications thereof |
CN105561887A (en) * | 2014-10-10 | 2016-05-11 | 天津汇康源科技有限公司 | Catalytic reaction structure of chemical reactor |
CN110776952A (en) * | 2019-10-31 | 2020-02-11 | 中国石油天然气集团有限公司 | Superposed oil hydrogenation device and method capable of producing isooctane |
CN112174809A (en) * | 2019-07-05 | 2021-01-05 | 中国石油化工股份有限公司 | Continuous preparation device of homogeneous organic molybdenum compound |
CN114011341A (en) * | 2021-11-15 | 2022-02-08 | 丹东明珠特种树脂有限公司 | Catalytic distillation tower and high-purity MTBE preparation system for deeply removing isobutene |
WO2022083688A1 (en) * | 2020-10-21 | 2022-04-28 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation column |
CN114432971A (en) * | 2020-10-21 | 2022-05-06 | 中国石油化工股份有限公司 | Catalytic reactor and distillation tower using same |
CN114452900A (en) * | 2020-10-21 | 2022-05-10 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation tower |
RU2815368C1 (en) * | 2020-10-21 | 2024-03-13 | Чайна Петролиум энд Кемикал Корпорейшн | Catalytic reaction unit and reaction distillation column |
-
2001
- 2001-05-18 CN CNB011149531A patent/CN1170609C/en not_active Expired - Fee Related
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102462971B (en) * | 2010-11-11 | 2014-08-20 | 中国石油化工股份有限公司 | Mobile catalytic distillation equipment and its application |
CN102462971A (en) * | 2010-11-11 | 2012-05-23 | 中国石油化工股份有限公司 | Mobile catalytic distillation equipment and its application |
CN103436286A (en) * | 2013-07-18 | 2013-12-11 | 济南开发区星火科学技术研究院 | Catalytic rectification hydrogenation desulfurization process of gasoline heavy distillate |
CN103436286B (en) * | 2013-07-18 | 2015-05-27 | 济南开发区星火科学技术研究院 | Catalytic rectification hydrogenation desulfurization process of gasoline heavy distillate |
CN104342202A (en) * | 2013-08-06 | 2015-02-11 | 中国石油大学(北京) | Lubricating oil base oil raw material deacidification device and method |
CN104342202B (en) * | 2013-08-06 | 2016-08-10 | 中国石油大学(北京) | A kind of Lube basic oil material feedstocks deacidifying device and method |
CN105561617A (en) * | 2014-10-09 | 2016-05-11 | 中国石油化工股份有限公司 | Efficient catalysis rectification apparatus and applications thereof |
CN105561615A (en) * | 2014-10-09 | 2016-05-11 | 中国石油化工股份有限公司 | Catalysis rectification apparatus and applications thereof |
CN105561615B (en) * | 2014-10-09 | 2018-05-04 | 中国石油化工股份有限公司 | catalytic distillation device and application |
CN105561887A (en) * | 2014-10-10 | 2016-05-11 | 天津汇康源科技有限公司 | Catalytic reaction structure of chemical reactor |
CN112174809B (en) * | 2019-07-05 | 2022-10-21 | 中国石油化工股份有限公司 | Continuous preparation device of homogeneous organic molybdenum compound |
CN112174809A (en) * | 2019-07-05 | 2021-01-05 | 中国石油化工股份有限公司 | Continuous preparation device of homogeneous organic molybdenum compound |
CN110776952A (en) * | 2019-10-31 | 2020-02-11 | 中国石油天然气集团有限公司 | Superposed oil hydrogenation device and method capable of producing isooctane |
WO2022083688A1 (en) * | 2020-10-21 | 2022-04-28 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation column |
CN114432971A (en) * | 2020-10-21 | 2022-05-06 | 中国石油化工股份有限公司 | Catalytic reactor and distillation tower using same |
CN114452900A (en) * | 2020-10-21 | 2022-05-10 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation tower |
CN114452901A (en) * | 2020-10-21 | 2022-05-10 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation column |
CN114452901B (en) * | 2020-10-21 | 2023-03-07 | 中国石油化工股份有限公司 | Catalytic reaction unit and reactive distillation column |
CN114432971B (en) * | 2020-10-21 | 2023-04-07 | 中国石油化工股份有限公司 | Catalytic reactor and distillation tower using same |
TWI800045B (en) * | 2020-10-21 | 2023-04-21 | 大陸商中國石油化工科技開發有限公司 | Catalytic reaction unit and reactive distillation column |
RU2815368C1 (en) * | 2020-10-21 | 2024-03-13 | Чайна Петролиум энд Кемикал Корпорейшн | Catalytic reaction unit and reaction distillation column |
CN114011341A (en) * | 2021-11-15 | 2022-02-08 | 丹东明珠特种树脂有限公司 | Catalytic distillation tower and high-purity MTBE preparation system for deeply removing isobutene |
Also Published As
Publication number | Publication date |
---|---|
CN1170609C (en) | 2004-10-13 |
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Legal Events
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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 | ||
ASS | Succession or assignment of patent right |
Owner name: CHINA PETROLEUM & CHEMICAL CORPORATION; QILU PETR Free format text: FORMER OWNER: QILU PETROCHEMICAL GROUP CO., CHINA PETROCHEMICAL CORP. Effective date: 20070608 |
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C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20070608 Address after: 100029, No. 6, Xin Xin Street East, Beijing, Chaoyang District Co-patentee after: Qilu Petrochemical Co., China Petrochemical Group Corp. Patentee after: Sinopec Corp. Address before: 124 mailbox 255408, Shandong City, Zibo Province Patentee before: Qilu Petrochemical Co., China Petrochemical Group Corp. |
|
ASS | Succession or assignment of patent right |
Owner name: CHINA PETROLEUM & CHEMICAL CORPORATION Free format text: FORMER OWNER: CHINA PETROLEUM + CHEMICAL CORPORATION; QILU PETROCHEMICAL GROUP CO., CHINA PETROCHEMICAL CORP. Effective date: 20071228 |
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C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20071228 Address after: 6, Xin Xin Dong Street, Beijing, Chaoyang District, China: 100029 Patentee after: Sinopec Corp. Address before: 6, Xin Xin Dong Street, Beijing, Chaoyang District, China: 100029 Co-patentee before: Qilu Petrochemical Co., China Petrochemical Group Corp. Patentee before: China Petroleum Chemical Co |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20041013 Termination date: 20200518 |
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CF01 | Termination of patent right due to non-payment of annual fee |