DE60029132T2 - Herstellung von phenol mittels reaktiver destillation - Google Patents
Herstellung von phenol mittels reaktiver destillation Download PDFInfo
- Publication number
- DE60029132T2 DE60029132T2 DE60029132T DE60029132T DE60029132T2 DE 60029132 T2 DE60029132 T2 DE 60029132T2 DE 60029132 T DE60029132 T DE 60029132T DE 60029132 T DE60029132 T DE 60029132T DE 60029132 T2 DE60029132 T2 DE 60029132T2
- Authority
- DE
- Germany
- Prior art keywords
- cumene hydroperoxide
- distillation column
- acetone
- catalyst bed
- column
- 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 - Lifetime
Links
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000000066 reactive distillation Methods 0.000 title claims abstract description 16
- 238000002360 preparation method Methods 0.000 title claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 139
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 claims abstract description 94
- 239000003054 catalyst Substances 0.000 claims abstract description 84
- 238000004821 distillation Methods 0.000 claims abstract description 63
- 238000000034 method Methods 0.000 claims abstract description 50
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 14
- 238000007865 diluting Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 238000009835 boiling Methods 0.000 claims description 18
- 238000010992 reflux Methods 0.000 claims description 16
- 238000010790 dilution Methods 0.000 claims description 9
- 239000012895 dilution Substances 0.000 claims description 9
- 238000011144 upstream manufacturing Methods 0.000 claims description 9
- 230000015572 biosynthetic process Effects 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 7
- 230000002378 acidificating effect Effects 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 5
- 239000002638 heterogeneous catalyst Substances 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 2
- 239000000376 reactant Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 5
- 239000000047 product Substances 0.000 description 45
- 239000010457 zeolite Substances 0.000 description 19
- 229910021536 Zeolite Inorganic materials 0.000 description 17
- 238000006243 chemical reaction Methods 0.000 description 17
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 17
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 16
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 10
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 8
- 238000003776 cleavage reaction Methods 0.000 description 8
- 238000012856 packing Methods 0.000 description 7
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 230000007017 scission Effects 0.000 description 6
- 239000000377 silicon dioxide Substances 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 229920001429 chelating resin Polymers 0.000 description 5
- YQHLDYVWEZKEOX-UHFFFAOYSA-N cumene hydroperoxide Chemical compound OOC(C)(C)C1=CC=CC=C1 YQHLDYVWEZKEOX-UHFFFAOYSA-N 0.000 description 5
- 239000003085 diluting agent Substances 0.000 description 5
- 229920003303 ion-exchange polymer Polymers 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- -1 ALPO-5 Chemical class 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 239000002131 composite material Substances 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 229910044991 metal oxide Inorganic materials 0.000 description 4
- 150000004706 metal oxides Chemical class 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 239000011973 solid acid Substances 0.000 description 4
- 239000011949 solid catalyst Substances 0.000 description 4
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 3
- 239000012013 faujasite Substances 0.000 description 3
- 239000003456 ion exchange resin Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 125000000542 sulfonic acid group Chemical group 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000005804 alkylation reaction Methods 0.000 description 2
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical class O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000003729 cation exchange resin Substances 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000006384 oligomerization reaction Methods 0.000 description 2
- BCTWNMTZAXVEJL-UHFFFAOYSA-N phosphane;tungsten;tetracontahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.P.[W].[W].[W].[W].[W].[W].[W].[W].[W].[W].[W].[W] BCTWNMTZAXVEJL-UHFFFAOYSA-N 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- ZOKCNEIWFQCSCM-UHFFFAOYSA-N (2-methyl-4-phenylpent-4-en-2-yl)benzene Chemical compound C=1C=CC=CC=1C(C)(C)CC(=C)C1=CC=CC=C1 ZOKCNEIWFQCSCM-UHFFFAOYSA-N 0.000 description 1
- YZUPZGFPHUVJKC-UHFFFAOYSA-N 1-bromo-2-methoxyethane Chemical compound COCCBr YZUPZGFPHUVJKC-UHFFFAOYSA-N 0.000 description 1
- BDCFWIDZNLCTMF-UHFFFAOYSA-N 2-phenylpropan-2-ol Chemical compound CC(C)(O)C1=CC=CC=C1 BDCFWIDZNLCTMF-UHFFFAOYSA-N 0.000 description 1
- YHZQOKUDQQISEW-UHFFFAOYSA-N 4-Cumylphenol Natural products C1=CC(C(C)C)=CC=C1C1=CC=C(O)C=C1 YHZQOKUDQQISEW-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- 239000002841 Lewis acid Substances 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002152 alkylating effect Effects 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- GHTGICGKYCGOSY-UHFFFAOYSA-K aluminum silicon(4+) phosphate Chemical class [Al+3].P(=O)([O-])([O-])[O-].[Si+4] GHTGICGKYCGOSY-UHFFFAOYSA-K 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 229940106691 bisphenol a Drugs 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 229940023913 cation exchange resins Drugs 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000010543 cumene process Methods 0.000 description 1
- UFRQQBZAYHXOKS-UHFFFAOYSA-N cumene;phenol Chemical compound OC1=CC=CC=C1.CC(C)C1=CC=CC=C1 UFRQQBZAYHXOKS-UHFFFAOYSA-N 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 238000006471 dimerization reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000011964 heteropoly acid Substances 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000007517 lewis acids Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052680 mordenite Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- QBDSZLJBMIMQRS-UHFFFAOYSA-N p-Cumylphenol Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=CC=C1 QBDSZLJBMIMQRS-UHFFFAOYSA-N 0.000 description 1
- 238000005502 peroxidation Methods 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000012048 reactive intermediate Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229910021647 smectite Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 229910000314 transition metal oxide Inorganic materials 0.000 description 1
- PBYZMCDFOULPGH-UHFFFAOYSA-N tungstate Chemical compound [O-][W]([O-])(=O)=O PBYZMCDFOULPGH-UHFFFAOYSA-N 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/08—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by decomposition of hydroperoxides, e.g. cumene hydroperoxide
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/51—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
- C07C45/53—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition of hydroperoxides
-
- 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
- Y02P20/10—Process efficiency
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S203/00—Distillation: processes, separatory
- Y10S203/06—Reactor-distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US09/468,465 US6410804B1 (en) | 1999-12-21 | 1999-12-21 | Production of phenol using reactive distillation |
| US468465 | 1999-12-21 | ||
| PCT/US2000/034843 WO2001046102A1 (en) | 1999-12-21 | 2000-12-20 | Production of phenol using reactive distillation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| DE60029132D1 DE60029132D1 (de) | 2006-08-10 |
| DE60029132T2 true DE60029132T2 (de) | 2006-12-21 |
Family
ID=23859932
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE60029132T Expired - Lifetime DE60029132T2 (de) | 1999-12-21 | 2000-12-20 | Herstellung von phenol mittels reaktiver destillation |
Country Status (8)
| Country | Link |
|---|---|
| US (2) | US6410804B1 (enExample) |
| EP (1) | EP1242348B1 (enExample) |
| JP (1) | JP5041354B2 (enExample) |
| AT (1) | ATE331702T1 (enExample) |
| AU (1) | AU2447701A (enExample) |
| DE (1) | DE60029132T2 (enExample) |
| ES (1) | ES2267600T3 (enExample) |
| WO (1) | WO2001046102A1 (enExample) |
Families Citing this family (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10036959A1 (de) * | 2000-07-28 | 2002-02-07 | Basf Ag | Verfahren zur Herstellung von tert.-Butylestern aliphatischer C1-C4-Carbonsäuren |
| US7663004B2 (en) | 2002-04-22 | 2010-02-16 | The Curators Of The University Of Missouri | Method of producing lower alcohols from glycerol |
| US8252961B2 (en) | 2002-04-22 | 2012-08-28 | The Curators Of The University Of Missouri | Method of producing lower alcohols from glycerol |
| US8017816B2 (en) | 2002-04-22 | 2011-09-13 | The Curators Of The University Of Missouri | Method of producing lower alcohols from glycerol |
| US6984761B2 (en) * | 2002-12-16 | 2006-01-10 | Exxonmobil Chemical Patents Inc. | Co-production of phenol, acetone, α-methylstyrene and propylene oxide, and catalyst therefor |
| US20040249229A1 (en) * | 2003-06-06 | 2004-12-09 | Gee Jeffery C. | Isomerization of olefins with carboxylic acid |
| WO2005095536A2 (en) * | 2004-03-25 | 2005-10-13 | Suppes Galen J | Method of producing lower alcohols from glycerol |
| EP1732869A1 (en) | 2004-03-31 | 2006-12-20 | General Electric Company A Corporation of the State of New York | Process for producing phenol |
| TWI376361B (en) * | 2004-08-13 | 2012-11-11 | Exxonmobil Chem Patents Inc | Process for producing phenol and methyl ethyl ketone |
| JP2007099746A (ja) * | 2005-09-06 | 2007-04-19 | Ube Ind Ltd | フェノールおよびシクロアルカノンの製造方法 |
| US7326815B2 (en) * | 2005-12-27 | 2008-02-05 | Exxonmobil Chemical Patents Inc. | Selective oxidation of alkylbenzenes |
| US8026398B2 (en) * | 2006-05-16 | 2011-09-27 | Narayana Mysore | Catalysts comprising a combination of oxidized metals and a method for cleaving phenylalkyl hydroperoxides using the catalysts |
| WO2007137020A2 (en) * | 2006-05-16 | 2007-11-29 | Shell Oil Company | Method for decomposing di(phenylalkyl)peroxides to produce hydroxybenzenes and phenylalkenes using solid catalysts |
| US20080116053A1 (en) * | 2006-11-20 | 2008-05-22 | Abb Lummus Global Inc. | Non-refluxing reactor stripper |
| US7888537B2 (en) * | 2006-12-29 | 2011-02-15 | Uop Llc | Solid acid catalyst and process for decomposition of cumene hydroperoxide |
| US7417003B2 (en) * | 2006-12-29 | 2008-08-26 | Uop Llc | Solid acid catalyst and process for decomposition of cumene hydroperoxide |
| WO2009024242A1 (en) * | 2007-08-22 | 2009-02-26 | Exxonmobil Chemical Patents Inc. | Process for producing sec-butylbenzene |
| EP2098498A1 (en) | 2008-03-04 | 2009-09-09 | ExxonMobil Chemical Patents Inc. | Selective oligomerization of isobutene |
| CN102076648A (zh) * | 2008-08-26 | 2011-05-25 | 埃克森美孚化学专利公司 | 用于生产烷基苯氢过氧化物的方法 |
| CN102177126A (zh) | 2008-10-10 | 2011-09-07 | 埃克森美孚化学专利公司 | 制备苯酚和甲乙酮的方法 |
| US8440864B2 (en) * | 2008-10-10 | 2013-05-14 | Exxonmobil Chemical Patents Inc. | Process for producing sec-butylbenzene |
| KR20140015548A (ko) | 2008-12-15 | 2014-02-06 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | 알킬방향족 화합물의 산화 |
| CN102161616A (zh) * | 2011-03-11 | 2011-08-24 | 北京化工大学 | 一种过氧化氢烷基苯分解制备酚和酮的方法 |
| KR101732771B1 (ko) | 2014-06-16 | 2017-05-04 | 주식회사 엘지화학 | 탈거 장치 |
| CN106866379B (zh) * | 2017-03-23 | 2020-11-10 | 中石化上海工程有限公司 | 反应精馏分解chp制备苯酚丙酮的方法 |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55153730A (en) * | 1979-04-20 | 1980-11-29 | Ici Ltd | Manufacture of phenol and acetone |
| EP0018159B1 (en) | 1979-04-20 | 1983-05-11 | Imperial Chemical Industries Plc | Process for the production of phenol, acetone and alpha methylstyrene |
| US5055627A (en) * | 1985-01-07 | 1991-10-08 | Chemical Research & Licensing Company | Process for the preparation of cumene |
| US4935577A (en) * | 1988-07-15 | 1990-06-19 | Mobil Oil Corp. | Hydrocarbon processes comprised of catalytic distillation using Lewis acid promoted inorganic oxide catalyst systems |
| US4870217A (en) * | 1988-10-24 | 1989-09-26 | Texaco Chemical Company | Method for production of phenol/acetone from cumene hydroperoxide |
| EP0367408A3 (en) * | 1988-10-24 | 1991-06-12 | Texaco Development Corporation | Method for production of phenol/acetone from cumene hydroperoxide |
| US5118872A (en) * | 1989-03-10 | 1992-06-02 | Chemical Research & Licensing Company | Process for conducting heterogeneous chemical reactions |
| DE4322712A1 (de) * | 1993-07-08 | 1995-01-12 | Huels Chemische Werke Ag | Verfahren zur Durchführung chemischer Reaktionen in Reaktionsdestillationskolonnen |
| JPH08119892A (ja) * | 1994-10-26 | 1996-05-14 | Mitsui Petrochem Ind Ltd | ヒドロキシ芳香族化合物の製造方法 |
| US5463136A (en) | 1994-12-22 | 1995-10-31 | Shell Oil Company | Cumene hydroperoxide cleavage process |
| US5705711A (en) * | 1995-08-17 | 1998-01-06 | Huntsman Specialty Chemicals Corporation | Manufacture of methyl tertiary butyl ether in reactive distillation column |
| US5905178A (en) * | 1998-04-20 | 1999-05-18 | Catalytic Distillation Technologies | Removal of α-methyl styrene from cumene |
-
1999
- 1999-12-21 US US09/468,465 patent/US6410804B1/en not_active Expired - Fee Related
-
2000
- 2000-12-20 EP EP00988249A patent/EP1242348B1/en not_active Expired - Lifetime
- 2000-12-20 AT AT00988249T patent/ATE331702T1/de not_active IP Right Cessation
- 2000-12-20 DE DE60029132T patent/DE60029132T2/de not_active Expired - Lifetime
- 2000-12-20 JP JP2001546616A patent/JP5041354B2/ja not_active Expired - Fee Related
- 2000-12-20 AU AU24477/01A patent/AU2447701A/en not_active Abandoned
- 2000-12-20 WO PCT/US2000/034843 patent/WO2001046102A1/en not_active Ceased
- 2000-12-20 ES ES00988249T patent/ES2267600T3/es not_active Expired - Lifetime
-
2001
- 2001-11-14 US US09/991,831 patent/US6441252B1/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| DE60029132D1 (de) | 2006-08-10 |
| ATE331702T1 (de) | 2006-07-15 |
| US6441252B1 (en) | 2002-08-27 |
| ES2267600T3 (es) | 2007-03-16 |
| WO2001046102A1 (en) | 2001-06-28 |
| JP5041354B2 (ja) | 2012-10-03 |
| US20020058845A1 (en) | 2002-05-16 |
| EP1242348A1 (en) | 2002-09-25 |
| JP2003518047A (ja) | 2003-06-03 |
| AU2447701A (en) | 2001-07-03 |
| EP1242348B1 (en) | 2006-06-28 |
| US6410804B1 (en) | 2002-06-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE60029132T2 (de) | Herstellung von phenol mittels reaktiver destillation | |
| DE69301579T2 (de) | Verbessertes Verfahren zur Gleichzeitigen Herstellung von Propylenoxid und Styrolmonomer | |
| DE69711918T2 (de) | Herstellung von organischen carbonsäureestern | |
| EP1900712B1 (de) | Verfahren zur Spaltung von Methyl-tertiär-butylether | |
| DE69907653T2 (de) | Verfahren und einrichtung zum herstellen von butylacetat und isobutylacetat | |
| DE2853769C3 (de) | Verfahren zur gleichzeitigen Herstellung von reinem Methyl-tert.-butylether und einem C↓4↓-Kohlenwasserstoffgemisch, das wesentlich weniger als 1% Isobuten enthält | |
| EP1360160A1 (de) | Verfahren zur herstellung von hochreinem diisobuten | |
| EP1894908A1 (de) | Verfahren zur Spaltung von Methyl-tertiär-butylether | |
| EP1900713A1 (de) | Verfahren zur Spaltung von Methyl-tertiär-butylether | |
| DD301736A7 (de) | Verfahren zur herstellung von phenol | |
| EP0162362A1 (de) | Verfahren zur kontinulierlichen Herstellung von Alkoholen | |
| EP2991973B1 (de) | Verfahren zur herstellung von 2-substituierten 4-hydroxy-4-methyl-tetrahydropyranen mit rückführung | |
| DE3149738A1 (de) | Verfahren zum abtrennen von buten-1 aus butan-buten-fraktionen | |
| DE3879150T2 (de) | Verfahren zur katalytischen Hydratation von Olefinen. | |
| EP1824807A1 (de) | Verfahren zur herstellung von acetalen | |
| EP1431264A1 (de) | Verfahren zur Herstellung von tert.-Butanol | |
| DE3118954A1 (de) | Verfahren zur herstellung von olefinen | |
| DE69510087T2 (de) | Verfahren zur herstellung von 5-chlor-2,3-dihydro-1h-inden-1-on | |
| DD263978A5 (de) | Verfahren zur herstellung von isopropylalkohol und tertiaeren c tief 4- bis c tief 5- alkoholen | |
| EP0137433B1 (de) | Verfahren zur kontinuierlichen Herstellung von Alkoholen | |
| DE69516098T2 (de) | Verfahren zur Herstellung von Isopropylalkohol durch Hydratisierung von Propylen | |
| DE69616232T2 (de) | Verfahren zur Herstellung von Bisphenol-Verbindungen mit gleichzeitiger Entwässerung | |
| DE69801654T2 (de) | Verfahren zum herstellen von methacrylatestern | |
| EP0753498B1 (de) | Verfahren zur Herstellung von Diarylethanen | |
| DE3509292A1 (de) | Verfahren zur herstellung von reinen tertiaeren olefinen |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 8364 | No opposition during term of opposition |