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US3933888A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of unsaturated acids, esters and nitriles, and catalyst therefor

Assignee: Rohm and Haas Co
•
Filing: 1972-10-06
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Granted: 1976-01-20
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Expires: 1992-10-06
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Abstract

Abstract Alkanoic acids, esters of such acids, and alkyl nitriles are reacted with formaldehyde in the presence of a basic catalyst comprising pyrogenic silica to form alpha , beta -unsaturated acids, the esters of such unsaturated acids or alpha , beta -unsaturated nitriles. The pyrogenic silica is especially effective when treated with activating agents which provide basic sites on the pyrogenic silica catalyst support, such as organic bases, inorganic bases of Groups IIA and IIIA metals, and precursors of such bases.

Inventors

  • 👤 Francis W. Schlaefer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 10:49
CPC Classifications
C; C07; C07C; C07C255/00; B; B01; B01J; B01J23/00; B01J23/02; B01J23/04; C07C51/00; C07C51/347; C07C51/353

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 180 words
A process for the production of α,β-ethylenically unsaturated acids, esters of said acids having 4 to 15 carbon atoms and nitriles which comprises reacting formaldehyde with an alkanoic acid, an ester of said acid having 3 to 14 carbon atoms, or an alkyl nitrile in the presence of a catalyst consisting of pyrogenic silica, with a total surface area of 150 to 300 square meters per gram, a total porosity volume of 3 to 15 cubic centimeters per gram and a pore size distribution such that pores having a diameter in excess of 100,000 A. and pores between 100,000 and 10,000 A. total at least 50% of the total pore content and less than 30% total pore content is of pores having a diameter of less than 1,000 A., with the remainder of pores in the range of 10,000 to 1,000 A., calcined with a base activating agent and where the reaction is carried out at a temperature of 330° to 390°C. with an alkanoic acid, ester or alkyl nitrile to formaldehyde molar concentration in the range of about 0.3-3.0:1.
Claim 2
Dependent Claim 180 words
A process for the production of α,β-ethylenically unsaturated acids, esters of said acids having 4 to 15 carbon atoms and nitriles which comprises reacting formaldehyde with an alkanoic acid, an ester of said acid having 3 to 14 carbon atoms, or an alkyl nitrile in the presence of a catalyst consisting of pyrogenic silica, with a total surface area of 150 to 300 square meters per gram, a total porosity volume of 3 to 15 cubic centimeters per gram and a pore size distribution such that pores having a diameter in excess of 100,000 A. and pores between 100,000 and 10,000 A. total at least 50% of the total pore content and less than 30% total pore content is of pores having a diameter of less than 1,000 A., with the remainder of pores in the range of 10,000 to 1,000 A., calcined with a base activating agent and where the reaction is carried out at a temperature of 330° to 390°C. with an alkanoic acid, ester or alkyl nitrile to formaldehyde molar concentration in the range of about 0.3-3.0:1.
Claim 3
Dependent Claim 24 words
The process of claim 1 wherein alkanoic acids are reacted with formaldehyde and said acids contain between 2 and 9 carbon atoms per molecule.
Claim 4
Dependent Claim 12 words
The process of claim 2 wherein said alkanoic acid is propionic acid.
Claim 5
Dependent Claim 38 words
The process of claim 1, wherein said catalyst contains as a base activating agent a compound selected from the group consisting of hydroxides, oxides, superoxides, or amides and salts of a metal of Group IA, IIA or IIIB.
Claim 6
Dependent Claim 15 words
The process of claim 4 wherein said base activating agent is an alkali metal hydroxide.
Claim 7
Dependent Claim 16 words
The process of claim 5 wherein said alkali metal hydroxide is potassium hydroxide or cesium hydroxide.
Claim 8
Dependent Claim 24 words
The process of claim 1 wherein said pyrogenic silica has a total porosity of between about 6 and about 10 cubic centimeters per gram.
Claim 9
Dependent Claim 11 words
The process of claim 1 wherein said ester is methyl propionate.
Claim 10
Dependent Claim 21 words
The process of claim 1 wherein alkyl nitriles containing two to about nine carbon atoms per molecule are reacted with formaldehyde.
Claim 11
Dependent Claim 11 words
The process of claim 9 wherein said alkyl nitrile is propionitrile.
Claim 12
Dependent Claim 23 words
The process of claim 1 wherein said process is conducted at a temperature in the range of between about 340° and about 370°C.
Claim 13
Dependent Claim 23 words
The process of claim 1 wherein between about one and about 10 percent by weight of zirconia is admixed with said pyrogenic silica.

References Cited (Backward Citations)

US3247248A Cited
US3578702A Cited
US3535371A Cited
US3574703A Cited
US3840587A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-01-19 1979-07-21 1980-01-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-01-19 1983-07-21 1984-01-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-01-19 1987-07-21 1988-01-20 $7700.00 Window Closed / Lapsed

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