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US4374070A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of acetic anhydride

Assignee: Eastman Chemical Co
•
Filing: 1980-11-21
•
Granted: 1983-02-15
•
Expires: 2000-11-21
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Abstract

Abstract The preparation of acetic anhydride by the carbonylation of methyl acetate in the presence of rhodium, an iodine compound and lithium at elevated temperatures and pressures is improved by the inclusion of about 2 to 7 volume percent hydrogen in the gas fed to the carbonylation reactor. The presence of hydrogen suppresses tar formation and increases reaction rate.

Inventors

  • 👤 Thomas H. Larkins
  • 👤 Stanley W. Polichnowski
  • 👤 Gerald C. Tustin
  • 👤 David A. Young

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 20:13
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/54; C07C51/56

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 61 words
In a process for the preparation of acetic anhydride by the carbonylation of methyl acetate in the presence of rhodium and an iodine compound at elevated pressure and temperature, the improvement comprising the presence of about 2 to 7 volume percent hydrogen in the gas fed to the carbonylation reactor and the carbonylation is carried out in the presence of lithium.
Claim 2
Dependent Claim 61 words
In a process for the preparation of acetic anhydride by the carbonylation of methyl acetate in the presence of rhodium and an iodine compound at elevated pressure and temperature, the improvement comprising the presence of about 2 to 7 volume percent hydrogen in the gas fed to the carbonylation reactor and the carbonylation is carried out in the presence of lithium.
Claim 3
Dependent Claim 16 words
The process of claim 1 wherein about 3 to 6% hydrogen is present in the gas.
Claim 4
Dependent Claim 63 words
Process for the preparation of acetic anhydride which comprises carbonylating in the liquid phase methyl acetate in the presence of about 250 to 1300 ppm. rhodium, about 175 to 5000 ppm. lithium and methyl iodide at a temperature of about 160° to 220° C. and about 300 to 1200 psig wherein about 2 to 7 volume percent of the gas fed is hydrogen.
Claim 5
Dependent Claim 63 words
Process for the preparation of acetic anhydride which comprises carbonylating in the liquid phase methyl acetate in the presence of about 250 to 1300 ppm. rhodium, about 175 to 5000 ppm. lithium and methyl iodide at a temperature of about 160° to 220° C. and about 300 to 1200 psig wherein about 2 to 7 volume percent of the gas fed is hydrogen.
Claim 6
Dependent Claim 126 words
Process for the preparation of acetic anhydride by the liquid phase carbonylation of methyl acetate in the presence of rhodium, methyl iodide and lithium at a temperature of about 160° to 220° C. and about 300 to 1200 psig wherein a feed mixture containing methyl acetate is continuously fed to a carbonylation reactor and a reaction mixture containing acetic anhydride is continuously removed, the feed to the reactor is such as to maintain within the reaction mixture (1) about 500 to 1000 ppm. rhodium, (2) about 1500 to 3700 ppm. lithium, (3) about 7 to 35 weight percent methyl iodide and (4) about 5 to 40 weight percent acetic acid; wherein about 3 to 6 volume percent of the gas fed to the reactor is hydrogen.
Claim 7
Dependent Claim 126 words
Process for the preparation of acetic anhydride by the liquid phase carbonylation of methyl acetate in the presence of rhodium, methyl iodide and lithium at a temperature of about 160° to 220° C. and about 300 to 1200 psig wherein a feed mixture containing methyl acetate is continuously fed to a carbonylation reactor and a reaction mixture containing acetic anhydride is continuously removed, the feed to the reactor is such as to maintain within the reaction mixture (1) about 500 to 1000 ppm. rhodium, (2) about 1500 to 3700 ppm. lithium, (3) about 7 to 35 weight percent methyl iodide and (4) about 5 to 40 weight percent acetic acid; wherein about 3 to 6 volume percent of the gas fed to the reactor is hydrogen.

References Cited (Backward Citations)

US3579566A Cited
JPS5047922A Cited
JPS5047921A Cited
BE819455A Cited
US4046807A Cited
ZA761482B Cited
GB2013184B Cited
US4252741A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-02-14 1986-08-16 1987-02-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-02-14 1990-08-16 1991-02-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-02-14 1994-08-16 1995-02-15 $7700.00 Window Closed / Lapsed

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