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US4045295A Expired / Lapsed US ⏱️ 0.0 years remaining

Purification of sulfuric acid containing acetic acid

Assignee: Hoechst AG
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Filing: 1976-06-10
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Granted: 1977-08-30
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Expires: 1996-06-10
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Abstract

Abstract Dilute sulfuric acid contaminated with acetic acid and hydrogen chloride is purified with the resultant formation of concentrated sulfuric acid and acetic acid. To this end, the contaminated sulfuric acid is heated in a first step to at most 60° C under 25-30 mm Hg so as to expel all of the hydrogen chloride together with minor proportions of acetic acid and water. In a second step, the sulfuric acid is heated to at most 165° C under 20-25 mm Hg so as to distil off the bulk of acetic acid together with water. In a third step, the sulfuric acid is cooled down to 60°-90° C, diluted with 10-30 wieght % of water with agitation and while cooling is continued. Following this, the sulfuric acid is heated to 160°-165° C under 20-25 mm Hg and thereby freed from the water and residual acetic acid.

Inventors

  • 👤 Stefan Schafer
  • 👤 Alexander Ohorodnik
  • 👤 Klaus Gehrmann
  • 👤 Albert Mainski

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 17:06
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/69; C01B17/90; C07; C07C; C07C51/00; C07C51/42; C07C51/43; C07C51/44

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 251 words
A process for purifying dilute sulfuric acid contaminated with acetic acid and hydrogen chloride with the resultant formation of concentrated sulfuric acid of about 94-96 % strength and acetic acid, the sulfuric acid to be purified forming part of a mixture consisting substantially of about 30-60 weight % of concentrated sulfuric acid, about 20-50 weight % of acetic acid, about 10-40 weight % of water, and about 2-10 weight % of hydrogen chloride, which process comprises: heating, in a first step, the contaminated sulfuric acid to a temperature of at most about 60° C under a pressure of about 25-30 mm Hg and thereby expelling all of the hydrogen chloride together with minor proportions of acetic acid and water; heating, in a second step, the sulfuric acid to a temperature of at most 165° C under a pressure of about 20-25 mm Hg and thereby distilling off the bulk of acetic acid together with water with the resultant formation of (a) sulfuric acid containing at most 1.3 up to 1.6 weight % of residual acetic acid and (b) of acetic acid of about 70-80 weight % strength; cooling, in a third step, the sulfuric acid down to a temperature of about 60°-90° C, diluting it with about 10-30 weight % of water with agitation and while cooling is continued, and then heating the sulfuric acid to a temperature of about 160°-165° C under a pressure of about 20-25 mm Hg and thereby freeing it from the water and residual acetic acid.
Claim 2
Dependent Claim 251 words
A process for purifying dilute sulfuric acid contaminated with acetic acid and hydrogen chloride with the resultant formation of concentrated sulfuric acid of about 94-96 % strength and acetic acid, the sulfuric acid to be purified forming part of a mixture consisting substantially of about 30-60 weight % of concentrated sulfuric acid, about 20-50 weight % of acetic acid, about 10-40 weight % of water, and about 2-10 weight % of hydrogen chloride, which process comprises: heating, in a first step, the contaminated sulfuric acid to a temperature of at most about 60° C under a pressure of about 25-30 mm Hg and thereby expelling all of the hydrogen chloride together with minor proportions of acetic acid and water; heating, in a second step, the sulfuric acid to a temperature of at most 165° C under a pressure of about 20-25 mm Hg and thereby distilling off the bulk of acetic acid together with water with the resultant formation of (a) sulfuric acid containing at most 1.3 up to 1.6 weight % of residual acetic acid and (b) of acetic acid of about 70-80 weight % strength; cooling, in a third step, the sulfuric acid down to a temperature of about 60°-90° C, diluting it with about 10-30 weight % of water with agitation and while cooling is continued, and then heating the sulfuric acid to a temperature of about 160°-165° C under a pressure of about 20-25 mm Hg and thereby freeing it from the water and residual acetic acid.
Claim 3
Dependent Claim 25 words
The process as claimed in claim 1, wherein the sulfuric acid is heated in the first step to a temperature of 55° to 60° C.
Claim 4
Dependent Claim 23 words
The process as claimed in claim 1, wherein the temperature used in the second step is maintained at 163° up to 165° C.
Claim 5
Dependent Claim 35 words
The process as claimed in claim 1, wherein the sulfuric acid is freed in the second step from all of the acetic acid contained therein, except for a residual content of about 1.5 weight %.
Claim 6
Dependent Claim 21 words
The process as claimed in claim 1, wherein the sulfuric acid is cooled in the third step down to 70° C.
Claim 7
Dependent Claim 36 words
The process as claimed in claim 1, wherein the sulfuric acid is heated to a temperature of 165° C under a pressure of 20 mm Hg and thereby freed from water and residual acetic acid therein.

References Cited (Backward Citations)

SU320447A1 Cited
DE2027018A1 Cited
US3635664A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-08-29 1981-02-28 1981-08-30 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-08-29 1985-02-28 1985-08-30 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-08-29 1989-02-28 1989-08-30 $7700.00 Window Closed / Lapsed

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