UST892018I4 - Process for preparing high purity dihydroisophorone - Google Patents
Process for preparing high purity dihydroisophorone Download PDFInfo
- Publication number
- UST892018I4 UST892018I4 US892018DH UST892018I4 US T892018 I4 UST892018 I4 US T892018I4 US 892018D H US892018D H US 892018DH US T892018 I4 UST892018 I4 US T892018I4
- Authority
- US
- United States
- Prior art keywords
- zone
- dihydroisophorone
- isophorone
- distillate
- hydrogenation
- 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.)
- Pending
Links
Images
Classifications
-
- 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
- C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
- C07C45/67—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
-
- 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
- C07C45/61—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
- C07C45/62—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by hydrogenation of carbon-to-carbon double or triple bonds
-
- 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
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/81—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
- C07C45/82—Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
-
- 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
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
- C07C45/85—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to a chemical modification
Definitions
- the hydrogenation reaction product recovered from the reaction zone is distilled to obtain substantially pure dihydroisophorone.
- the hydrogenation reaction product is distilled in a first zone to separate the distillate comprising dihydroisophorone and B-isophorone from the residue comprising a-iSO- phorone.
- the distillate withdrawn from the first zone is then passed to a second zone wherein said distillate is heated at a temperature sufi'lcient to substantially isomerize B-isophorone to a-isophorone without causing pyrolysis of the remainder of said distillate.
- the eifiuent from said second zone is then passed to a third zone to separate the distillate comprising dihydroisophorone from the residue comprising a-isophorone.
Abstract
IN THE HYDROGENATION OF ISOPHORONE TO DIHYDROISOPHORONE, MAINTAINING THE REACTION ZONE AT ELEVATED PRESSURES UNDER MILD TEMPERATURE CONDITIONS SIGNIFICANTLY IMPROVES THE SELECTIVITY TO DIHYDROISOPHORONE AT HIGH CONVERSION LEVELS. ISOPHORONE IS CONTACTED WITH HDYROGEN IN THE PRESENCE OF A HYDROGENATION CATALYST IN A HYDROGENATION ZONE WHEREIN THE HYDROGEN PRESSURE IN SAID ZONE IS MAINTAINED BETWEEN ABOUT 10-200 P.S.I.G. AND THE TEMPERATURE IN SAID ZONE RANGES FROM ABOUT 25* TO LESS THAN 175*.C THE HYDROGENATION REACTION PRODUCT RECOVERED FROM THE REACTION ZONE IS DISTILLED TO OBTAIN SUBSTANTIALLY PURE DIHYDROISOPHORONE. IN A PREFERRED EMBODIMENT, THE HYDROGENATION REACTION PRODUCT IS DISTILLED IN A FIRST ZONE TO SEPARATE THE DISTILLATE COMPRISING DIHYDROISOPHORONE AND B-ISOPHRONE FROM THE RESIDUE COMPRISING A-ISOPHORONE. THE DISTILLATE WITHDRAWN FROM THE FIRST ZONE IS THEN PASSED TO A SECOND ZONE WHEREIN SAID DISTILLATE IS HEATED AT A TEMPERATURE SUFFICIENT TO SUBSTANTIALLY ISOMERIZE B-ISOPHORONE TO A-ISOPHORONE WITHOUT CAUSING PYROLYSIS OF THE REMAINDER OF SAID DISTILLATE. THE EFFLUENT FROM SAID SECOND ZONE IS THEN PASSED TO A THIRD ZONE TO SEPARATE THE DISTILLATE COMPRISING DIHYDROISOPHORONE FROM THE RESIDUE COMPRISING A-ISOPHORONE.
Description
EFENSTVE UBLTGATIUN UNITED STATES PATENT OFFICE Published at the request of the applicant or owner in accordance with the Notice of Dec. 16, 1969, 869 O.G. 687. The abstracts of Defensive Publication applications are identified by distinctly numbered series and are arranged chronologically. The heading of each abstract indicates the number of pages of specification, including claims and sheets of drawings contained in the application as originally filed. The files of these applications are available to the public for inspection and reproduction may be purchased for 30 cents a sheet.
Defensive Publication applications have not been examined as to the merits of alleged invention. The Patent Office makes no assertion as to the novelty of the disclosed subject matter.
PUBLISHED NOVEMBER 30, 1971 T892,018 PROCESS FOR PREPARING HIGH PURITY DIHYDROISOPHORONE William E. Wellman, 24 Cambridge Road, Edison, NJ.
08817; Paul E. Burton, 761 Austin St., Westfield, NJ.
07090; and William D. Diana, 1001 Shadow Oak Lane,
Somerville, NJ. 08876 Filed Sept. 10, 1968, Ser. No. 758,839 Int. Cl. C07c 45/00, 49/30 US. Cl. 260-586 R 1 Sheet Drawing. 28 Pages Specification In the hydrogenation of isophorone to dihydroisophorone, maintaining the reaction zone at elevated pressures under mild temperature conditions significantly improves the selectivity to dihydroisophorone at high conversion levels. Isophorone is contacted with hydrogen in the presence of a hydrogenation catalyst in a hydrogenation zone wherein the hydrogen pressure in said zone is maintained between about 10 to 200 p.s.i.g. and the temperature in said zone ranges from about 25 to less than 175 C. The hydrogenation reaction product recovered from the reaction zone is distilled to obtain substantially pure dihydroisophorone. In a preferred embodiment, the hydrogenation reaction product is distilled in a first zone to separate the distillate comprising dihydroisophorone and B-isophorone from the residue comprising a-iSO- phorone. The distillate withdrawn from the first zone is then passed to a second zone wherein said distillate is heated at a temperature sufi'lcient to substantially isomerize B-isophorone to a-isophorone without causing pyrolysis of the remainder of said distillate. The eifiuent from said second zone is then passed to a third zone to separate the distillate comprising dihydroisophorone from the residue comprising a-isophorone.
av. 30,, 1971 w. E. WELLMAN ETAL 1 PROCESS FOR PREPARING HIGH PURITY DIHYDROISOPHORONE Filed Sept. 10. 1968 I I HHMOJ.
NOLLVT'ILLSIG AHorney
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US75883968A | 1968-09-10 | 1968-09-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
UST892018I4 true UST892018I4 (en) | 1971-11-30 |
Family
ID=25053311
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US892018D Pending UST892018I4 (en) | 1968-09-10 | 1968-09-10 | Process for preparing high purity dihydroisophorone |
Country Status (1)
Country | Link |
---|---|
US (1) | UST892018I4 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5728891A (en) * | 1990-07-08 | 1998-03-17 | Huels Aktiengesellschaft | Process for the preparation of 3,3,5-trimethylcyclohexanone |
-
1968
- 1968-09-10 US US892018D patent/UST892018I4/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5728891A (en) * | 1990-07-08 | 1998-03-17 | Huels Aktiengesellschaft | Process for the preparation of 3,3,5-trimethylcyclohexanone |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2514961A (en) | Recovery of aldehydes | |
US2614128A (en) | Controlled distillation of oxo alcohols containing high-boiling impurities | |
UST892018I4 (en) | Process for preparing high purity dihydroisophorone | |
US2433008A (en) | 4, 6-di-tertiary-butyl-3-methylcyclo-hexanol | |
US3515763A (en) | Production of styrene | |
US3022349A (en) | Production of amines | |
US2359212A (en) | Process for depolymerizing polystyrene | |
ES372921A1 (en) | Conversion and desulfurization of hydrocarbonaceous black oils | |
US2636909A (en) | Production of akomatic | |
US3211797A (en) | Process for producing benzene and cyclohexane | |
US2013873A (en) | Production of aromatic amines of the benzene series | |
US3428668A (en) | Process for the preparation of 1,4-cyclohexane dicarboxylic acid dialkyl esters | |
US3755482A (en) | Multistage production of styrene | |
US2508922A (en) | Separation of dienes | |
GB923595A (en) | Improvements in and relating to the production of acrylic esters | |
US2265165A (en) | Process for reacting ketene with a vinyl ketone | |
US3527815A (en) | Olefinic alcohols | |
US3082273A (en) | Process for the production of unsaturated hydrocarbons with three carbon atoms | |
US2505817A (en) | Hydrogenated polyalkylated phenols | |
UST896030I4 (en) | Apparatus for the continuous transesteripication op aromatic dicarboxylic acids with diols | |
US2385555A (en) | Cyclohexene production | |
US3330878A (en) | Process for producing styrene | |
GB799396A (en) | Improvements in or relating to methods of hydrogenation | |
US2804483A (en) | Production of alpha, alpha, alpha, 2, 3, 4-hexachlorotoluene | |
US1877203A (en) | Method of simultaneous hydrogenation and dehydrogenation |