Claims
- 1. A method of preparing linear polyethylenepolyamines from ethylenediamine and monoethanolamine which comprises:
- mixing and reacting ethylenediamine with monoethanolamine at a temperature of about 200.degree. to about 400.degree. C. and a pressure of about 700 to about 1400 psig in the presence of a catalytically effective amount of an aluminum phosphate catalyst;
- said catalyst prepared by mixing and reacting alumina with phosphoric acid, adding water to the reaction mixture, adding ammonium hydroxide to form a precipitate, continuing the addition of ammonium hydroxide until precipitate formation ceases, and separating the precipitate catalyst from the reaction mixture; and
- recovering a polyethylenepolyamine product characterized by a relatively large percentage of linear, non-cyclic polyethylenepolyamines.
- 2. The method of claim 1, wherein about one-half mole to about 5 moles of ethylenediamine per mole of monoethanolamine are mixed and reacted with said monoethanolamine.
- 3. The method of claim 1, wherein the ethylenediamine and monoethanolamine are mixed and reacted in the presence of from about 5.0 to about 15.0 weight percent of said aluminum phosphate catalyst, based on the amount of monoethanolamine present.
- 4. The method of claim 1, wherein about 5 moles to about 10 moles of 85% by weight phosphoric acid per mole of alumina are mixed and reacted with said alumina.
- 5. The method of claim 1, wherein water is added to the phosphoric acid and alumina reaction mixture until the mixture reaches a pH of about 2 to about 3.
- 6. The method of claim 1, wherein the ethylenediamine and monoethanolamine are mixed and reacted in the presence of said catalyst at a temperature of about 300.degree. to about 350.degree. C.
- 7. A method of preparing linear polyethylenepolyamines from ethylenediamine and monoethanolamine which comprises:
- mixing and reacting about one mole to about two moles of ethylenediamine per mole of monoethanolamine with monoethanolamine at a temperature of about 300.degree. C. to about 350.degree. C. and a pressure of about 700 to about 1400 psig in the presence of from about 5.0 to about 15.0 weight percent aluminum phosphate catalyst, based on the amount of monoethanolamine present;
- said catalyst prepared by (a) mixing and reacting 85 wt. % phosphoric acid with hydrated alumina in a molar ratio of about six moles of phosphoric acid per mole of alumina, (b) adding sufficient water to the phosphoric acid and alumina reaction mixture to yield a pH of about 2 to 3 for the mixture, (c) adding a 30% ammonium hydroxide solution to the mixture to form a precipitate and continuing addition of the ammonium hydroxide solution until precipitate formation ceases and the pH of the mixture is about 5 to 6, (d) separating the precipitate from the reaction mixture, isolating and drying the precipitate; and
- recovering a polyethylenepolyamine product characterized by a relatively large percentage of linear, non-cyclic polyethylenepolyamines.
- 8. The method of claim 7, wherein the precipitate from the catalyst reaction mixture is calcined in an oven for about 4 to about 25 hours at about 200.degree. C. to about 750.degree. C. after the precipitate is dried.
TECHNICAL FIELD OF THE INVENTION
This is a continuation-in-part of U.S. patent application Ser. No. 283,713, filed July 16, 1981, now abandoned.
US Referenced Citations (7)
Foreign Referenced Citations (1)
Number |
Date |
Country |
528987 |
Nov 1940 |
GBX |
Continuation in Parts (1)
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Number |
Date |
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Parent |
283713 |
Jul 1981 |
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