Process for the manufacture of diethylenetriamine
A continuously generated alkyleneamines producers composition comprising, based on 100% of the moles of the composition and exclusive of any MEA and water present, a) about 20 to about 40 mole % DETA, b) about 15 to about 60 mole % EDA (net generated), c) about 5 to about 18 mole % AEEA, d) about 3...
Saved in:
Main Authors | , , |
---|---|
Format | Patent |
Language | English |
Published |
13.04.1993
|
Subjects | |
Online Access | Get full text |
Cover
Loading…
Summary: | A continuously generated alkyleneamines producers composition comprising, based on 100% of the moles of the composition and exclusive of any MEA and water present, a) about 20 to about 40 mole % DETA, b) about 15 to about 60 mole % EDA (net generated), c) about 5 to about 18 mole % AEEA, d) about 3 to about 25 mole % of the combination of PIP, AEP and HEP, e) less than about 1 to about 5 mole % of one or more of TETAs and TEPAs, f) less than about 1 mole % of other polyalkylene polyamines, g) a DETA to AEEA mole ratio greater than about 1.35, and h) an EDA to DETA mole ratio less than 2.60, and the process of manufacturing it which comprises feeding hydrogen, ammonia, MEA and EDA, preferably provided from a recycle stream, to a reaction zone containing a fixed bed of a reductive amination catalyst in a tubular reactor, wherein the hydrogen comprises about 1 to about 30 mole percent of the feed in the reaction zone, the mole ratio of EDA to MEA is greater than 0.25 and the mole ratio of ammonia to MEA is about 1 to about 15, the temperature of the reaction zone is about 120 DEG C. to about 300 DEG C., the pressure of the reaction zone is about 1800 to about 2500 psig., the conversion of MEA is about 20 to about 60 weight percent, and recovering said producers composition from the reaction zone. |
---|---|
Bibliography: | Application Number: US19900528554 |