EA201692125A1 - Способ получения циклогексана из бензола и метилциклопентана с предварительным гидрированием бензола - Google Patents
Способ получения циклогексана из бензола и метилциклопентана с предварительным гидрированием бензолаInfo
- Publication number
- EA201692125A1 EA201692125A1 EA201692125A EA201692125A EA201692125A1 EA 201692125 A1 EA201692125 A1 EA 201692125A1 EA 201692125 A EA201692125 A EA 201692125A EA 201692125 A EA201692125 A EA 201692125A EA 201692125 A1 EA201692125 A1 EA 201692125A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- cyclohexane
- benzene
- dmp
- necessary
- mcp
- Prior art date
Links
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 title abstract 18
- GDOPTJXRTPNYNR-UHFFFAOYSA-N methylcyclopentane Chemical compound CC1CCCC1 GDOPTJXRTPNYNR-UHFFFAOYSA-N 0.000 title abstract 14
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 title abstract 11
- 238000005984 hydrogenation reaction Methods 0.000 title abstract 4
- 238000000034 method Methods 0.000 title 1
- 239000000203 mixture Substances 0.000 abstract 6
- 239000004215 Carbon black (E152) Substances 0.000 abstract 5
- 238000009835 boiling Methods 0.000 abstract 5
- 229930195733 hydrocarbon Natural products 0.000 abstract 5
- 150000002430 hydrocarbons Chemical class 0.000 abstract 5
- 238000006317 isomerization reaction Methods 0.000 abstract 5
- 238000000926 separation method Methods 0.000 abstract 5
- AEXMKKGTQYQZCS-UHFFFAOYSA-N 3,3-dimethylpentane Chemical class CCC(C)(C)CC AEXMKKGTQYQZCS-UHFFFAOYSA-N 0.000 abstract 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 2
- GXDHCNNESPLIKD-UHFFFAOYSA-N 2-methylhexane Natural products CCCCC(C)C GXDHCNNESPLIKD-UHFFFAOYSA-N 0.000 abstract 1
- 239000011831 acidic ionic liquid Substances 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 150000001934 cyclohexanes Chemical class 0.000 abstract 1
- DMEGYFMYUHOHGS-UHFFFAOYSA-N heptamethylene Natural products C1CCCCCC1 DMEGYFMYUHOHGS-UHFFFAOYSA-N 0.000 abstract 1
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
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/10—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of aromatic six-membered rings
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C13/00—Cyclic hydrocarbons containing rings other than, or in addition to, six-membered aromatic rings
- C07C13/02—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof
- C07C13/16—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with a six-membered ring
- C07C13/18—Monocyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with a six-membered ring with a cyclohexane ring
-
- 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
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
-
- 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
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/29—Rearrangement of carbon atoms in the hydrocarbon skeleton changing the number of carbon atoms in a ring while maintaining the number of rings
-
- 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
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/31—Rearrangement of carbon atoms in the hydrocarbon skeleton changing the number of rings
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/04—Purification; Separation; Use of additives by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- C07C2521/08—Silica
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
- C07C2523/46—Ruthenium, rhodium, osmium or iridium
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/745—Iron
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/75—Cobalt
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/755—Nickel
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/08—Halides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/08—Halides
- C07C2527/10—Chlorides
- C07C2527/11—Hydrogen chloride
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/08—Halides
- C07C2527/12—Fluorides
- C07C2527/1213—Boron fluoride
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/125—Compounds comprising a halogen and scandium, yttrium, aluminium, gallium, indium or thallium
- C07C2527/126—Aluminium chloride
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/135—Compounds comprising a halogen and titanum, zirconium, hafnium, germanium, tin or lead
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/14—The ring being saturated
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
Настоящее изобретение касается способа получения циклогексана из метилциклопентана (МЦП) и бензола. В рамках данного изобретения МЦП и бензол являются компонентами углеводородной смеси (УС1), которая, кроме того, содержит диметилпентаны (ДМП), при необходимости, циклогексан и, при необходимости, по меньшей мере одно соединение (низкокипящий компонент), выбранное из нециклических C-C-алканов и циклопентана. Сначала бензол на этапе гидрирования превращают в (содержащийся в углеводородной смеси (УС2)) циклогексан, в то время как МЦП в присутствии катализатора, предпочтительно кислотной ионной жидкости, изомеризуют в циклогексан. После гидрирования, но перед изомеризацией осуществляют отделение диметилпентана (ДМП), причем содержащийся в углеводородной смеси (УС2) циклогексан сначала удаляют вместе с ДМП Этот уже имеющийся перед изомеризацией циклогексан может быть снова отделен от ДМП на последующем этапе ректификации и выделен и/или возвращен в способ получения циклогексана. Если углеводородная смесь (УС1) содержит низкокипящие компоненты, их отделение, при необходимости, может быть осуществлено между отделением ДМП и изомеризацией МЦП. После изомеризации осуществляют выделение циклогексана, при необходимости, с возвратом неизомеризованного МЦП и, при необходимости, низкокипящих компонентов. Предпочтительно углеводородная смесь (УС1) содержит циклогексан и/или низкокипящие компоненты, и, таким образом, отделение низкокипящих компонентов предпочтительно осуществляют между отделением ДМП перед изомеризацией. Также предпочтительным является дополнительное отделение ДМП от циклогексана, т.е. компонент циклогексана, который образуется при гидрировании бензола, а также, при необходимости, содержится в исходной смеси (УС1), выделяют и таким образом восстанавливают.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14165503 | 2014-04-22 | ||
PCT/EP2015/058526 WO2015162097A1 (de) | 2014-04-22 | 2015-04-20 | Verfahren zur herstellung von cyclohexan aus benzol und methylcyclopentan mit vorgeschalteter benzolhydrierung |
Publications (2)
Publication Number | Publication Date |
---|---|
EA201692125A1 true EA201692125A1 (ru) | 2017-05-31 |
EA032895B1 EA032895B1 (ru) | 2019-07-31 |
Family
ID=50677938
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA201692125A EA032895B1 (ru) | 2014-04-22 | 2015-04-20 | Способ получения циклогексана из бензола и метилциклопентана с предварительным гидрированием бензола |
Country Status (10)
Country | Link |
---|---|
US (1) | US9873646B2 (ru) |
EP (1) | EP3134376B1 (ru) |
JP (1) | JP6359119B2 (ru) |
KR (1) | KR102355201B1 (ru) |
CN (1) | CN106232558B (ru) |
EA (1) | EA032895B1 (ru) |
ES (1) | ES2671148T3 (ru) |
MY (1) | MY189176A (ru) |
SA (1) | SA516380068B1 (ru) |
WO (1) | WO2015162097A1 (ru) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109704906B (zh) * | 2017-10-26 | 2021-11-30 | 中国石油化工股份有限公司 | 利用抽余油生产己烷的工艺方法 |
CN109293465A (zh) * | 2018-10-12 | 2019-02-01 | 青岛科技大学 | 一种单塔热泵精馏分离甲基环戊烷和环己烷的工艺 |
CN111592617B (zh) * | 2020-05-18 | 2021-04-02 | 恒河材料科技股份有限公司 | 一种高芳烃氢化树脂的制备方法 |
CN111848324A (zh) * | 2020-08-07 | 2020-10-30 | 黄河三角洲京博化工研究院有限公司 | 一种油品中分离环己烷的方法 |
Family Cites Families (45)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2846485A (en) * | 1955-06-16 | 1958-08-05 | Exxon Research Engineering Co | Production of high purity cyclohexane concentrate |
US3233001A (en) * | 1963-01-25 | 1966-02-01 | Phillips Petroleum Co | Process for producing cyclohexane |
US3311667A (en) * | 1963-05-06 | 1967-03-28 | Phillips Petroleum Co | Process for the preparation of cyclohexane |
US3309411A (en) * | 1964-12-14 | 1967-03-14 | Phillips Petroleum Co | Process for the production of high purity cyclohexane |
US3406217A (en) | 1966-03-31 | 1968-10-15 | Phillips Petroleum Co | Production of cyclohexane from naphtha |
JPS48102802A (ru) | 1972-03-13 | 1973-12-24 | ||
ES423004A2 (es) * | 1973-02-07 | 1976-07-01 | Ici Ltd | Procedimiento para la produccion de una mezcla de hidrocar-buros olefinicos adecuada para la copolimerizacion c |
US4053369A (en) | 1974-05-30 | 1977-10-11 | Phillips Petroleum Company | Extractive distillation |
JPH0629199B2 (ja) | 1985-05-17 | 1994-04-20 | 軽質留分新用途開発技術研究組合 | 炭化水素類の異性化方法 |
US4955468A (en) | 1989-09-08 | 1990-09-11 | Phillips Petroleum Company | Separation of hydrocarbon mixtures |
JPH0649660B2 (ja) | 1990-04-03 | 1994-06-29 | 旭化成工業株式会社 | シクロヘキサンの精製方法 |
JP3481672B2 (ja) | 1994-04-14 | 2003-12-22 | 新日本石油株式会社 | 高オクタン価ガソリン材源用ベンゼン含有炭化水素油の水素化異性化方法 |
JPH1036295A (ja) | 1996-07-25 | 1998-02-10 | Japan Energy Corp | メチルシクロペンテン含有炭化水素の製造方法 |
JP3890513B2 (ja) | 1997-04-03 | 2007-03-07 | 株式会社ジャパンエナジー | メチルシクロペンタン含有炭化水素の製造方法 |
US6140547A (en) * | 1998-12-01 | 2000-10-31 | Phillips Petroleum Company | Isomerization of hydrocarbons |
US6133496A (en) | 1999-03-09 | 2000-10-17 | Phillips Petroleum Company | Two-stage isomerization of saturated C.sub. 6 hydrocarbons |
DE10008634A1 (de) | 2000-02-24 | 2001-08-30 | Basf Ag | Trennwandkolonne zur Auftrennung eines Vielstoffgemisches |
US6392115B1 (en) | 2000-09-18 | 2002-05-21 | Phillips Petroleum Company | Separation of hydrocarbons by extractive distillation |
RU2001130402A (ru) * | 2001-11-13 | 2003-08-20 | Хальдор Топсеэ А/С (DK) | Способ изомеризации С5-С8 парафинового углеводородного сырья |
US6855853B2 (en) * | 2002-09-18 | 2005-02-15 | Catalytic Distillation Technologies | Process for the production of low benzene gasoline |
EP1403236A1 (en) | 2002-09-25 | 2004-03-31 | Haldor Topsoe A/S | Process of paraffin hydrocarbon isomerisation catalysed by an ionic liquid in the presence of a cyclic hydrocarbon additive |
CN101205163B (zh) * | 2006-12-22 | 2010-07-21 | 中国石油化工股份有限公司 | 一种制备环己烷的方法 |
CA2628361C (en) | 2007-05-18 | 2012-08-07 | Uop Llc | Isomerization of benzene-containing feedstocks |
CA2625905C (en) * | 2007-05-18 | 2012-06-12 | Uop Llc | Isomerization of benzene-containing feedstocks |
US8026402B2 (en) * | 2007-06-27 | 2011-09-27 | H R D Corporation | High shear process for cyclohexane production |
US9315741B2 (en) | 2008-09-08 | 2016-04-19 | Catalytic Distillation Technologies | Process for ultra low benzene reformate using catalytic distillation |
CN102666448B (zh) | 2009-12-07 | 2014-12-10 | 巴斯夫欧洲公司 | 异构化饱和、支化和环状烃的方法 |
US20110137098A1 (en) | 2009-12-07 | 2011-06-09 | Basf Se | Process for isomerizing a saturated hydrocarbon |
US20140018590A1 (en) | 2012-07-11 | 2014-01-16 | Basf Se | Performance of a hydrocarbon conversion or processing of a hydrocarbon conversion in apparatuses with surfaces made from nonmetallic materials |
US20140018597A1 (en) | 2012-07-11 | 2014-01-16 | Basf Se | Process for treating an output from a hydrocarbon conversion by washing with an aqueous medium |
US20140018595A1 (en) | 2012-07-11 | 2014-01-16 | Basf Se | Process for removing hydrogen halides in a rectifying column with a partial condenser |
US20140018588A1 (en) | 2012-07-11 | 2014-01-16 | Basf Se | Isomerization process for hydrocarbons with recycling of hydrogen halides |
US10815168B2 (en) | 2012-07-11 | 2020-10-27 | Basf Se | Chemical conversion process in a dispersion |
US20140024875A1 (en) | 2012-07-11 | 2014-01-23 | Basf Se | Process for treating an output from a hydrocarbon conversion with removal of hydrogen halides and subsequent wash |
US9409839B2 (en) | 2012-07-11 | 2016-08-09 | Basf Se | Removal of ionic liquids by means of a knitted fabric |
US9095789B2 (en) | 2012-07-11 | 2015-08-04 | Basf Se | Removal of ionic liquids by means of coalescing filters made from acrylic/phenolic resin |
US10207201B2 (en) | 2012-07-11 | 2019-02-19 | Basf Se | Phase separation process by inversion of the direction of dispersion |
US10081580B2 (en) | 2012-10-18 | 2018-09-25 | Basf Se | Process for preparing cyclohexane with starting materials originating from a steamcracking process |
US20140114103A1 (en) | 2012-10-18 | 2014-04-24 | Basf Se | Process for preparing cyclohexane comprising a prior removal of dimethylpentanes |
US20140128648A1 (en) | 2012-10-18 | 2014-05-08 | Basf Se | Hydrocarbon conversion process in the presence of an acidic ionic liquid with upstream hydrogenation |
US20140114100A1 (en) | 2012-10-18 | 2014-04-24 | Basf Se | Novel process for preparing cyclohexane from methylcyclopentane and benzene |
US20140257003A1 (en) | 2013-03-07 | 2014-09-11 | Basf Se | Chemical reaction process with addition of metal halides |
US20140257007A1 (en) | 2013-03-07 | 2014-09-11 | Basf Se | Chemical reaction process at constant hydrogen halide partial pressure |
WO2015082388A1 (de) | 2013-12-02 | 2015-06-11 | Basf Se | Abtrennung von ionischen flüssigkeiten in koalesziervorrichtungen |
DE102013226428A1 (de) | 2013-12-18 | 2015-06-18 | Basf Se | Extraktionskolonne und Verfahren zum Extrahieren eines Bestandteils aus einem Fluid |
-
2015
- 2015-04-20 CN CN201580021048.3A patent/CN106232558B/zh active Active
- 2015-04-20 EP EP15716549.9A patent/EP3134376B1/de active Active
- 2015-04-20 MY MYPI2016001873A patent/MY189176A/en unknown
- 2015-04-20 JP JP2016563957A patent/JP6359119B2/ja active Active
- 2015-04-20 EA EA201692125A patent/EA032895B1/ru not_active IP Right Cessation
- 2015-04-20 US US15/305,111 patent/US9873646B2/en active Active
- 2015-04-20 KR KR1020167032186A patent/KR102355201B1/ko active IP Right Grant
- 2015-04-20 WO PCT/EP2015/058526 patent/WO2015162097A1/de active Application Filing
- 2015-04-20 ES ES15716549.9T patent/ES2671148T3/es active Active
-
2016
- 2016-10-13 SA SA516380068A patent/SA516380068B1/ar unknown
Also Published As
Publication number | Publication date |
---|---|
MY189176A (en) | 2022-01-31 |
EA032895B1 (ru) | 2019-07-31 |
JP2017517495A (ja) | 2017-06-29 |
EP3134376B1 (de) | 2018-02-28 |
SA516380068B1 (ar) | 2020-06-18 |
US20170121240A1 (en) | 2017-05-04 |
JP6359119B2 (ja) | 2018-07-18 |
KR20160148598A (ko) | 2016-12-26 |
CN106232558B (zh) | 2019-08-09 |
WO2015162097A1 (de) | 2015-10-29 |
EP3134376A1 (de) | 2017-03-01 |
CN106232558A (zh) | 2016-12-14 |
ES2671148T3 (es) | 2018-06-05 |
US9873646B2 (en) | 2018-01-23 |
KR102355201B1 (ko) | 2022-01-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EA201692125A1 (ru) | Способ получения циклогексана из бензола и метилциклопентана с предварительным гидрированием бензола | |
EA201790247A1 (ru) | Платформа для очистки биспецифичных антител | |
BR112018015531A2 (pt) | processo para a preparação de uma mistura de alcoóis terpenos e uso de um éster de ácido carboxílico | |
EA201691713A1 (ru) | Комбинированный способ гидрокрекинга | |
EA202090153A1 (ru) | Объединенный способ термического крекинга и дегидрирования для получения олефинов | |
CU24505B1 (es) | Variantes de polipéptidos que dividen toxinas de fusarium, aditivo que contiene estas variantes y procedimientos para la división de toxinas de fusarium | |
GEP20227382B (en) | Anti-coagulation factor xi antibodies | |
BR112016025217A2 (pt) | método e sistema para produzir mistura de grãos de aveia de glúten reduzido | |
EA201892515A1 (ru) | Стероидные 6,7-бета-эпоксиды в качестве интермедиатов | |
EA201691834A1 (ru) | Новый способ очистки гонадотропина | |
MX2019005999A (es) | Precipitacion de la fraccion i-iv-1 de inmunoglobulinas plasmaticas. | |
MY180010A (en) | Method and device for distillative separation of a three-or multi-component mixture | |
BR112016006082A2 (pt) | método para a limpeza de uma corrente de gás craqueado em uma coluna de lavagem de óleo | |
EA201692403A1 (ru) | Способ выделения углеводородов и применения расплавленной соли | |
AR103712A1 (es) | Procedimiento para separar el 2-cloro-1,1-difluoroetano y el trans-dicloroetileno | |
BR112017000225A2 (pt) | processo de alquilação com o auxílio de um catalisador que compreende zeólitos os quais contêm terras-raras ricas em cério e um metal de hidrogenação | |
IN2013CH05455A (ru) | ||
AR102116A1 (es) | Proceso de separación para mezcla de compuestos aromáticos de c₈ | |
EA201691717A1 (ru) | Способ конверсии углеводородов в олефины | |
CR20160428A (es) | Pizazinas moduladoras de gpr6 | |
WO2015017177A8 (en) | Method for producing an alkyl 3-hydroxybutyrate | |
EA201500662A1 (ru) | Применение смесей e/z-изомеров для количественного получения определенных продуктов сочетанием асимметрической гидрогенизации и изомеризации | |
EA201390236A1 (ru) | Способ разделения | |
PH12018501326A1 (en) | Process for producing a creamer | |
MY194657A (en) | Demulsification additive composition, use thereof, and method of demulsification |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): AM AZ BY KZ KG TJ TM |