UST892018I4 - Process for preparing high purity dihydroisophorone - Google Patents

Process for preparing high purity dihydroisophorone Download PDF

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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
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zone
dihydroisophorone
isophorone
distillate
hydrogenation
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation 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
    • C07C45/67Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation 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
    • C07C45/62Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/78Separation; Purification; Stabilisation; Use of additives
    • C07C45/81Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation
    • C07C45/82Separation; Purification; Stabilisation; Use of additives by change in the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/78Separation; Purification; Stabilisation; Use of additives
    • C07C45/85Separation; 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
US892018D 1968-09-10 1968-09-10 Process for preparing high purity dihydroisophorone Pending UST892018I4 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US75883968A 1968-09-10 1968-09-10

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UST892018I4 true UST892018I4 (en) 1971-11-30

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US892018D Pending UST892018I4 (en) 1968-09-10 1968-09-10 Process for preparing high purity dihydroisophorone

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Cited By (1)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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

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