Abstract:
A continuous process for preparing a polyamide by reacting at least one aminonitrile with water comprises: (1) reacting at least one aminonitrile with water at a temperature from 90 to 400° C. and a pressure from 0.1 to 35×106 Pa in a flow tube containing a Brönsted acid catalyst selected from a beta-zeolite catalyst, a sheet-silicate catalyst or a titanium dioxide catalyst comprising from 70 to 100% by weight of anatase and from 0 to 30% by weight of rutile and in which up to 40% by weight of the titanium dioxide may be replaced by tungsten oxide to obtain a reaction mixture, (2) further reacting the reaction mixture at a temperature from 150 to 400° C. and a pressure which is lower than the pressure in step 1, in the presence of a Brönsted acid catalyst as in (1), the temperature and pressure being selected so as to obtain a first gas phase and a first liquid or a first solid phase or a mixture of first solid and first liquid phase, and the first gas phase is separated from the first liquid or the first solid phase or from the mixture of first liquid and first solid phase, and (3) admixing the first liquid or the first solid phase or the mixture of first liquid and first solid phase with a gaseous or liquid phase comprising water at a temperature from 150 to 370° C. and a pressure from 0.1 to 30×106 Pa to obtain a product mixture.
Abstract:
The disclosure is a process for preparing cyclic lactams of the formula I: where R1 is hydrogen, alkyl, cycloalkyl or aryl, and A is C3-C12-alkylene unsubstituted or substituted by 1, 2, 3, 4, 5 or 6 substituents selected independently of one another from the group consisting of alkyl, cycloalkyl and aryl, by conversion of an &ohgr;-aminocarbonitrile of the formula II: HR1N—A—CN (II) where R1 and A are each as defined above, in the presence of at least one catalyst, which comprises converting said nitrile II into an oligomer mixture, and treating with superheated steam.
Abstract:
A process for preparing carboxylic acid derivatives of the formula I ##STR1## where X is OR.sup.2 or NH.sub.2,R.sup.1 is C.sub.1 -C.sub.20 -alkyl, C.sub.l -C.sub.20 -hydroxyalkyl, C.sub.3 -C.sub.12 -cycloalkyl, C.sub.4 -C.sub.12 -alkylcycloalkyl, C.sub.4 -C.sub.12 -cycloalkylalkyl, C.sub.5 -C.sub.20 -alkylcycloalkylalkyl, aryl, C.sub.7 -C.sub.20 -aralkyl, C.sub.7 -C.sub.20 -alkylaryl, a heteroaliphatic or heteroaromatic ring with 5 to 8 carbon atoms andR.sup.2 is C.sub.1 -C.sub.20 -alkyl,from carbonitriles of the formula IIR.sup.1 --C.tbd.N (II),where R.sup.1 has the abovementioned meanings, and alcohols of the formula IIIR.sup.2 --OH (III),where R.sup.2 has the abovementioned meanings, at from 50 to 300.degree. C. under from 0.1 to 350 bar in the presence of a heterogeneous catalyst, wherein the reaction is carried out in liquid phase.
Abstract:
A process for preparing amines of the general formula (I)X(--CH.sub.2 --NR.sup.1 R.sup.2).sub.n (I)whereR.sup.1 and R.sup.2 are preferably methyl, X is preferably 1,4-butylene and n is preferably 2, comprises reacting nitriles of the general formula (II)(R.sup.1 R.sup.2 N--CH.sub.2 --).sub.n-m X(--CN).sub.m (II)where R.sup.1, R.sup.2 and X are each as defined above and m is an integer from 1 to n,with secondary amines of the general formula (III)HNR.sup.1 R.sup.2 (III)where R.sup.1 and R.sup.2 are each as defined above,and hydrogen at from 50 to 250.degree. C. and from 5 to 350 bar in the presence of a palladium catalyst comprising, based on the total weight of the catalyst, from 0.1 to 10% by weight of Pd and from 0.01 to 10% by weight of at least one further metal selected from groups IB and VII of the Periodic Table, cerium and lanthanum on a support.
Abstract:
Process for the preparation of diamines of the general formula I ##STR1## in which A denotes a C.sub.1 -C.sub.20 alkylene chain optionally mono- to penta-substituted by C.sub.1 -C.sub.4 alkyl,R.sup.1, R.sup.2 denote C.sub.1 -C.sub.20 alkyl, C.sub.1 -C.sub.20 hydroxyalkyl, C.sub.3 -C.sub.8 cycloalkyl, C.sub.4 -C.sub.20 alkylcycloalkyl, C.sub.4 -C.sub.20 cycloalkylalkyl, phenyl, C.sub.7 -C.sub.20 phenylalkyl, C.sub.1 -C.sub.20 alkoxyalkyl, C.sub.7 -C.sub.20 phenoxyalkyl or together a saturated or unsaturated C.sub.2 -C.sub.6 alkylene chain optionally monosubstituted, disubstituted, or trisubstituted by C.sub.1 -C.sub.4 alkyl and optionally interrupted by oxygen or nitrogen,by the reaction of dinitriles of the general formula IINC--A--CN (II),in which A has the aforementioned meaning,with secondary amines of the general formula II ##STR2## in which R.sup.1 and R.sup.2 have the aforementioned meanings, with hydrogen at temperatures ranging from 50.degree. to 200.degree. C. and pressures ranging from 5 to 300 bar in the presence of a hydrogenation catalyst, in which a palladium catalyst on an oxidic support is used as hydrogenation catalyst.
Abstract:
Caprolactam is prepared by reacting a solution of 6-aminocapronitrile with water in the liquid phase at elevated temperatures by a process in which(a) an aqueous solution of 6-aminocapronitrile in the liquid phase is heated without the addition of a catalyst in a reactor A to give a mixture I consisting essentially of water, caprolactam and a high-boiling fraction (high boiler), then(b) the water is removed from the resulting mixture I to give a mixture II consisting essentially of caprolactam and the high boilers, then(c) the caprolactam and the high boilers from mixture II are separated from one another by distillation, and then either(d1) the high boilers from stage (c) are fed into the reactor A of stage (a) or(d2) the high boilers are heated similarly to stage (a) in a further reactor B and then worked up similarly to stages (b) and (c) to give further caprolactam, or(d3) the high boilers are heated under reduced pressure in the presence of a base in a reactor C and the reacted mixture is worked up by distillation to give caprolactam.
Abstract:
A process for the purification of tertiary amines in a crude mixture contaminated with undesirable primary and secondary amines which may have only a slight variance in boiling point with respect to the tertiary amine, wherein the crude mixture of the tertiary amine is treated at temperatures which may range from 0.degree. to 200.degree. C. but preferably from 20 to 150.degree. C. and at pressures of from 1 to 200 bar but most preferably under atmospheric pressure with a carboxylate of the formula ##STR1## in which R.sup.4 and R.sup.5 are selected from the group consisting of C.sub.1 -C.sub.20 -alkyl, C.sub.3 -C.sub.12 -cycloalkyl, C.sub.4 -C.sub.20 -cycloalkylalkyl, and aryl or C.sub.7 -C.sub.20 -aralkyl, both optionally mono- to penta- substituted by C.sub.1 -C.sub.8 -alkyl, C.sub.3 -C.sub.8 -cycloalkyl, or C.sub.4 -C.sub.12 -cycloalkylalkyl, and R.sup.4 may also represent hydrogen,to selectively form the alkylamides of the primary and secondary amine contaminants; and then separating the alkylamides from the tertiary amine by distillation.
Abstract:
A process for the preparation of caprolactam is provided, wherein a) a mixture (I) containing 6-aminocapronitrile and water is reacted in the gas phase, in the presence of a catalyst, to give a mixture (II) containing caprolactam, ammonia, water, high-boiling components and low-boiling components, b) ammonia is then removed from the mixture (II) to give a mixture (III) containing caprolactam, water, high-boiling components and low-boiling components, c) water is then removed from the mixture (III) to give a mixture (IV) containing caprolactam, high-boiling components and low-boiling components, and d) a solid (V) containing caprolactam is then obtained from the mixture (IV) by crystallization, the proportion by weight of caprolactam in the solid (V) being greater than in the mixture (IV).
Abstract:
A process for the preparation of caprolactam is provided, wherein a) a mixture (I) containing 6-aminocapronitrile and water is reacted in the liquid phase, in the presence of a catalyst, to give a mixture (II) containing caprolactam, ammonia, water, high-boiling components and low-boiling components, b) ammonia is then removed from the mixture (II) to give a mixture (III) containing caprolactam, water, high-boiling components and low-boiling components, c) water is then removed from the mixture (III) to give a mixture (IV) containing caprolactam, high-boiling components and low-boiling components, and d) a solid (V) containing caprolactam is then obtained from the mixture (IV) by crystallization, the proportion by weight of caprolactam in the solid (V) being greater than in the mixture (IV).