US4039581A
Expired / Lapsed
US
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Process for the preparation of di(amino phenyl)methanes
Assignee: Pharmacia and Upjohn Co
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Filing: 1975-06-27
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Granted: 1977-08-02
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Expires: 1995-06-27
Abstract
Abstract Aniline and formaldehyde are condensed (2-10 moles aniline per mole of formaldehyde) at ambient temperature in the absence of acid catalysts to give a mixture of aminals (anilinoacetals) and aniline from which the water is removed. The anhydrous aminals are contacted with a solid catalyst (clays, zeolites, diatomaceous earth) using either batch or continuous operation initially at 20° C to 55° C until benzylamine formation is substantially complete, then at 50° C to 65° C until benzylamine conversion to methylene polyphenyl polyamines is 75 - 90% complete and finally at 80° C to 100° C. A polyamine mixture is obtained in which diaminodiphenylmethane is the major (order of 90 percent by weight or higher) component, the bulk of the higher oligomeric polyamines being triamine. The diaminodiphenylmethane component contains of the order of 85 percent of 4,4'-isomer, the rest being 2,4'-isomer except for very small amounts (order of 2 percent or less) of 2,2'-isomer. Advantages of the process include high yield of diaminodiphenylmethane with relatively high 4,4'-isomer content, low oligomeric polyamine content, low temperature operation (energy consumption lower), no acidic reactants to cause corrosion of equipment, and rapid rates of conversion.
Inventors
- 👤 Floro F. Frulla
- 👤 Adnan A. R. Sayigh
- 👤 Henri Ulrich
- 👤 Peter J. Whitman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 10:03
CPC Classifications
C; C08; C08G; C08G73/00; C08G73/02; C07; C07C; C07C209/00; C07C209/24; C07C209/54; C07C263/00; C07C263/10; C08G12/00; C08G12/02; C08G12/04; C08G12/06; C08G12/08
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
209 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 2 moles to 10 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water, with a solid catalyst selected from the class consisting of diatomaceous earth, clay, and zeolite at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80% to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to about 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C. to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 2
Dependent Claim
209 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 2 moles to 10 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water, with a solid catalyst selected from the class consisting of diatomaceous earth, clay, and zeolite at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80% to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to about 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C. to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 3
Dependent Claim
24 words
The process of claim 1 wherein the molar proportion of aniline to formaldehyde employed is within the range of about 4:1 to about 6:1.
Claim 4
Dependent Claim
54 words
The process of claim 1 wherein the removal of water from the mixture of aminals in step (b) is completed by distillation of said water from said mixture of aminals under reduced pressure at a temperature not exceeding 55° C. until the water content of said aminal is not greater than 0.15% by weight.
Claim 5
Dependent Claim
11 words
The process of claim 1 wherein the catalyst is attapulgus clay.
Claim 6
Dependent Claim
11 words
The process of claim 1 wherein the catalyst is a zeolite.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein the catalyst is diatomaceous earth.
Claim 8
Dependent Claim
32 words
A process according to claim 1 wherein the solid catalyst has been subjected to drying by heating at a temperature in the range of 100° C. to 500° C. prior to use.
Claim 9
Dependent Claim
198 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight, which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 4 moles to 6 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water, with a diatomaceous earth catalyst at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80 to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C. to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 10
Dependent Claim
198 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight, which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 4 moles to 6 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water, with a diatomaceous earth catalyst at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80 to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C. to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 11
Dependent Claim
32 words
A process according to claim 8 wherein the diatomaceous earth has been subjected to drying by heating at a temperature in the range of 100° C. to 500° C. prior to use.
Claim 12
Dependent Claim
55 words
A process according to claim 8 wherein the removal of water from the mixture of aminals in step (b) is completed by distillation of said water from said mixture of aminals under reduced pressure at a temperature not exceeding 55° C. until the water content of said aminal is not greater than 0.15% by weight.
Claim 13
Dependent Claim
198 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight, which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 4 moles to 6 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water with an attapulgus clay catalyst at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80 to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 14
Dependent Claim
198 words
A process for the preparation of a mixture of di(aminophenyl)methane and oligomeric polymethylene polyphenyl polyamines wherein the diamine content is of the order of 90 percent by weight and wherein the p,p'-isomer content of said diamine is of the order of 85 percent by weight, which process comprises the steps of a. reacting aniline and formaldehyde in a proportion within the range of 4 moles to 6 moles of aniline per mole of formaldehyde at a temperature of 10° C. to 55° C. and in the absence of acid catalyst to form a mixture of aminals; b. separating the water from said aminals; c. contacting said aminals, free from water with an attapulgus clay catalyst at a temperature of 20° C. to 55° C. until the reaction mixture contains from about 80 to 100% by weight of the corresponding benzylamines; d. thereafter adjusting the temperature of the reaction mixture to 55° C. to 65° C. until from about 75% to 90% by weight of said benzylamines have been converted to methylene polyphenyl polyamines; and e. thereupon finally raising the temperature of the reaction mixture to 80° C to 100° C. until conversion to methylene polyphenyl polyamines is complete.
Claim 15
Dependent Claim
32 words
A process according to claim 11 wherein the attapulgus clay has been subjected to drying by heating at a temperature in the range of 100° C. to 500° C. prior to use.
Claim 16
Dependent Claim
55 words
A process according to claim 11 wherein the removal of water from the mixture of aminals in step (b) is completed by distillation of said water from said mixture of aminals under reduced pressure at a temperature not exceeding 55° C. until the water content of said aminal is not greater than 0.15% by weight.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-08-01 | 1981-01-31 | 1981-08-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-01 | 1985-01-31 | 1985-08-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-01 | 1989-01-31 | 1989-08-02 | $7700.00 | Window Closed / Lapsed |