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US3950442A Expired / Lapsed US ⏱️ 0.0 years remaining

Manufacture of t-butanol

Assignee: BASF SE
•
Filing: 1975-06-13
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Granted: 1976-04-13
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Expires: 1995-06-13
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Abstract

Abstract Process for the manufacture of t-butanol by hydration of isobutylene by reaction of isobutylene or isobutylene-containing C 4 -hydrocarbon mixtures at moderately elevated temperature with aqueous sulfuric acid and isolation of the t-butanol from the resulting solution of t-butanol in water and sulfuric acid, wherein the reaction is carried out at temperatures of from 20° to 45°C using 20-48% w/w aqueous sulfuric acid, the t-butanol being separated from the t-butanol solution in water and sulfuric acid by extraction, at temperatures of from 0° to 50°C, with saturated or mono-olefinically or di-olefinically unsaturated aliphatic or cycloaliphatic hydrocarbons containing at least 3 carbon atoms or with aromatic hydrocarbons of from 6 to 10 carbon atoms or with a mixture of said hydrocarbons, whereupon the t-butanol is isolated from the extracted mixture of t-butanol and hydrocarbon or hydrocarbon mixture.

Inventors

  • 👤 Hans-Henning Vogel
  • 👤 Hans-Martin Weitz
  • 👤 Toni Pfeiffer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 00:00
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/03; C07C29/04; C07C29/05; C07C29/06

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 232 words
A process for the manufacture of t-butanol by hydration of isobutylene comprising a. contacting in a hydrating stage an isobutylene-containing C 4 -hydrocarbon mixture at temperatures of 20° to 45°C and at a pressure from 1 to 10 atmospheres gauge with a mixture of aqueous sulfuric acid and t-butanol, the concentration of the aqueous sulfuric acid being 25 to 45% w/w at the beginning of the reaction and the concentration of the t-butanol in the mixture of aqueous sulfuric acid and t-butanol being from 10 to 35% w/w at the beginning of the reaction, b. passing the mixture obtained in the hydrating stage to a separation stage to obtain an essentially isobutylene-free and t-butanol containing C 4 -hydrocarbon mixture and a t-butanol/aqueous sulfuric acid mixture, c. introducing the essentially isobutylene-free and t-butanol containing C 4 -hydrocarbon mixture and the t-butanol/aqueous sulfuric acid mixture of step (b) at separate points into an extraction stage and adding essentially isobutylene-free and t-butanol-free C 4 -hydrocarbon mixture to the extraction stage to obtain an extracted mixture of t-butanol and C 4 -hydrocarbon and a t-butanol/aqueous sulfuric acid mixture having a reduced content of t-butanol, said extraction stage being at 0° to 50° C, and d. recycling the t-butanol/aqueous sulfuric acid mixture having a reduced content of t-butanol to the hydrating stage and isolating the t-butanol from the extracted mixture of t-butanol and C 4 -hydrocarbon mixture.
Claim 2
Dependent Claim 232 words
A process for the manufacture of t-butanol by hydration of isobutylene comprising a. contacting in a hydrating stage an isobutylene-containing C 4 -hydrocarbon mixture at temperatures of 20° to 45°C and at a pressure from 1 to 10 atmospheres gauge with a mixture of aqueous sulfuric acid and t-butanol, the concentration of the aqueous sulfuric acid being 25 to 45% w/w at the beginning of the reaction and the concentration of the t-butanol in the mixture of aqueous sulfuric acid and t-butanol being from 10 to 35% w/w at the beginning of the reaction, b. passing the mixture obtained in the hydrating stage to a separation stage to obtain an essentially isobutylene-free and t-butanol containing C 4 -hydrocarbon mixture and a t-butanol/aqueous sulfuric acid mixture, c. introducing the essentially isobutylene-free and t-butanol containing C 4 -hydrocarbon mixture and the t-butanol/aqueous sulfuric acid mixture of step (b) at separate points into an extraction stage and adding essentially isobutylene-free and t-butanol-free C 4 -hydrocarbon mixture to the extraction stage to obtain an extracted mixture of t-butanol and C 4 -hydrocarbon and a t-butanol/aqueous sulfuric acid mixture having a reduced content of t-butanol, said extraction stage being at 0° to 50° C, and d. recycling the t-butanol/aqueous sulfuric acid mixture having a reduced content of t-butanol to the hydrating stage and isolating the t-butanol from the extracted mixture of t-butanol and C 4 -hydrocarbon mixture.
Claim 3
Dependent Claim 19 words
A process as claimed in claim 1 wherein step (a) is carried out at temperatures of 25° to 40°C.
Claim 4
Dependent Claim 20 words
A process as claimed in claim 1 wherein the hydration and the extraction are carried out at the same temperature.

References Cited (Backward Citations)

US2042212A Cited
US2221955A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-04-13 1979-10-13 1980-04-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-04-13 1983-10-13 1984-04-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-04-13 1987-10-13 1988-04-13 $7700.00 Window Closed / Lapsed

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