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US4062900A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing butanediol and/or butenediol

Assignee: Mitsubishi Chemical Corp
•
Filing: 1976-07-15
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Granted: 1977-12-13
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Expires: 1996-07-15
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Abstract

Abstract Butanediol and/or butenediol are prepared by hydrolyzing diacetoxybutane and/or diacetoxybutene in the presence of a cation-exchange resin and recovered by fractional distillation. By the treatment of the hydrolyzed product with an anion exchange resin at any stage before the butanediol and/or butenediol are fractionated, butanediol and/or butenediol are recovered in high yield.

Inventors

  • 👤 Yasuo Tanabe
  • 👤 Jun Toriya
  • 👤 Masato Sato
  • 👤 Ken Shiraga

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 10:46
CPC Classifications
C; C07; C07C; C07C31/00; C07C31/18

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 85 words
In a process for preparing butanediol or butenediol by hydrolyzing diacetoxybutane or diacetoxybutene in the presence of a cation-exchange resin having at least one sulfo group as a functional group, and recovering butanediol or butenediol from the hydrolyzed product by distillation, the improvement which comprises treating the hydrolyzed product containing butanediol or butenediol with a weak anion-exchange resin which has a primary, secondary or tertiary amine groups at a temperature of 20° to 100° C at any stage before the butanediol or butenediol are fractionated.
Claim 2
Dependent Claim 85 words
In a process for preparing butanediol or butenediol by hydrolyzing diacetoxybutane or diacetoxybutene in the presence of a cation-exchange resin having at least one sulfo group as a functional group, and recovering butanediol or butenediol from the hydrolyzed product by distillation, the improvement which comprises treating the hydrolyzed product containing butanediol or butenediol with a weak anion-exchange resin which has a primary, secondary or tertiary amine groups at a temperature of 20° to 100° C at any stage before the butanediol or butenediol are fractionated.
Claim 3
Dependent Claim 19 words
A process for preparing butanediol or butenediol according to claim 1 wherein butanediol or butenediol is 1,4-butanediol or 1,4-butenediol.
Claim 4
Dependent Claim 22 words
A process for preparing butanediol or butenediol according to claim 1 wherein the weak anion-exchange resin has primary or secondary amine groups.
Claim 5
Dependent Claim 14 words
A process according to claim 1 wherein said temperature is 50° to 80° C.
Claim 6
Dependent Claim 37 words
A process for preparing butanediol or butenediol according to claim 1 wherein the anion-exchange resin is used in an amount from 0.0001 to 1 part by weight per one part by weight of the acid cation-exchange resin.
Claim 7
Dependent Claim 38 words
A process for preparing butanediol or butenediol according to claim 1 wherein the treatment is carried out by introducing the hydrolyzed product at a space velocity of 1000 to 0.1 hr -1 to a bed of anion-exchange resin.
Claim 8
Dependent Claim 37 words
A process for preparing butanediol or butenediol according to claim 1 wherein the distillation and the fractionation are carried out in a distillation column, the bottom of which is maintained within the range 150° to 220° C.
Claim 9
Dependent Claim 21 words
A process according to claim 7 wherein the space velocity is from 100 to 1 hr. to the exponent -1 .

References Cited (Backward Citations)

CA470663A Cited
US2868832A Cited
US3647892A Cited
US3891511A Cited
US3852164A Cited
US3917720A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-12-12 1981-06-13 1981-12-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-12-12 1985-06-13 1985-12-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-12-12 1989-06-13 1989-12-13 $7700.00 Window Closed / Lapsed

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