Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
117 words
A process for producing a bis-(morpholino-N-alkyl) ether compound from the corresponding N-(hydroxyalkyl)-morpholine compound, said N-(hydroxyalkyl)morpholine compound having the formula: ##STR2## wherein R is a straight claim or a branched chain alkyl radical of from 2 to about 10 carbon atoms, R' is a lower alkyl radical, and n is an integer from 0 to 4 comprising the steps of: contacting said N-(hydroxyalkyl)morpholine compound with a catalytically effective amount of silica-alumina having an alumina content of from about 5 to about 50 wt. % at a temperature of from about 200° C. to about 300° C. under a pressure sufficient to maintain the mixture substantially in liquid phase; and recovering said bis-(morpholino-N-alkyl) ether compound from the reaction mixture.
Claim 2
Dependent Claim
26 words
The process according to claim 1 wherein said silica-alumina has a surface area of from about 50 m 2 /g to about 700 m 2 /g.
Claim 3
Dependent Claim
24 words
The process according to claim 2 wherein said contacting is carried out at a temperature of from about 240° C. to about 280° C.
Claim 4
Dependent Claim
22 words
The process according to claim 3 wherein R and R' are, independently, alkyl radicals having from 2 to about 4 carbon atoms.
Claim 5
Dependent Claim
23 words
The process according to claim 4 wherein the silica-alumina catalyst has an alumina content of from about 10 to about 40 wt. %.
Claim 6
Dependent Claim
43 words
The process according to claim 5 wherein said contacting is effected at a pressure of from about 10 to about 100 psig and wherein water is continuously removed from the reaction zone as a vapor as it is formed in the condensation reaction.
Claim 7
Dependent Claim
24 words
The process according to claim 6 wherein said contacting is carried out at a temperature of from about 255° C. to about 265° C.
Claim 8
Dependent Claim
22 words
The process according to claim 7 wherein said N-(hydroxyalkyl)morpholine is selected from the group consisting of N-(2-hydroxyethyl)-2,6-dimethylmorpholine, N-(2-hydroxyethyl)morpholine, N-(2-hydroxypropyl)morpholine, N-(3-hydroxypropyl)morpholine, N-(2-hydroxyethyl)-2-methyl morpholine.
Claim 9
Dependent Claim
150 words
A continuous process for preparing a bis-(morpholino-N-alkyl) ether compound from the corresponding N-(hydroxyalkyl) morpholine compound, said N-(hydroxyalkyl)morpholine compound having the formula: ##STR3## wherein R is a straight chain or a branched chain alkyl radical of from 2 to about 10 carbon atoms, R' is a lower alkyl radical, and n is an integer from 0 to 4, said continuous process comprising: feeding said N-(hydroxyalkyl)morpholine compound to a fixed bed reactor at weight hourly space velocity of from about 0.1 to about 5.0 g/ml catalyst/hr at temperatures of from about 240° C. to 280° C. at a reactor pressure of about 50 psig wherein said fixed bed is of silica-alumina containing from about 5 to about 50 wt. % alumina and having a surface area of from about 50 m 2 /g to about 700 m 2 /g; and, recovering the bis-(morpholino-N-alkyl) ether compound from the effluent issuing from said reactor.
Claim 10
Dependent Claim
150 words
A continuous process for preparing a bis-(morpholino-N-alkyl) ether compound from the corresponding N-(hydroxyalkyl) morpholine compound, said N-(hydroxyalkyl)morpholine compound having the formula: ##STR3## wherein R is a straight chain or a branched chain alkyl radical of from 2 to about 10 carbon atoms, R' is a lower alkyl radical, and n is an integer from 0 to 4, said continuous process comprising: feeding said N-(hydroxyalkyl)morpholine compound to a fixed bed reactor at weight hourly space velocity of from about 0.1 to about 5.0 g/ml catalyst/hr at temperatures of from about 240° C. to 280° C. at a reactor pressure of about 50 psig wherein said fixed bed is of silica-alumina containing from about 5 to about 50 wt. % alumina and having a surface area of from about 50 m 2 /g to about 700 m 2 /g; and, recovering the bis-(morpholino-N-alkyl) ether compound from the effluent issuing from said reactor.
Claim 11
Dependent Claim
32 words
The pressure of claim 9 wherein said weight hourly space velocity is about 0.2 to about 2.0 g/ml catalyst/hr and said alumina content is from about 10 to about 40 wt. %.
Claim 12
Dependent Claim
41 words
The process of claim 10 comprising the further step of vacuum stripping the crude reaction product under conditions of from about 760 mm Hg/225° C. to 1.0 mm Hg/60° C. to effect removal of unreacted reagent and residual water of reaction.
Claim 13
Dependent Claim
19 words
The process of claim 9 wherein R contains from 2 to about 4 carbon atoms and n is 0.
Claim 14
Dependent Claim
19 words
The process of claim 9 wherein said N-(hydroxyalkyl)morpholine compound is selected from N-(2-hydroxyethyl)morpholine, N-(3-hydroxypropyl)morpholine, N-(2-hydroxypropyl)morpholine, N-(2-hydroxyethyl)-2-ethyl morpholine, and N-(2-hydroxyethyl)-2,6-dimethylmorpholine.
Claim 15
Dependent Claim
103 words
A process for producing a bis-(morpholino-alkyl) ether compound from the corresponding N-(hydroxyalkyl)-morpholine compound wherein said N-(hydroxyalkyl) morpholine compound is selected from the group consisting of N-(2-hydroxy-ethyl)-2,6-dimethyl morpholine, N-(2-hydroxyethyl) morpholine and N-(2-hydroxypropyl) morpholine comprising the steps of: contacting said N-(hydroxyalkyl)morpholine compound with a catalytically effective amount of silica alumina at a temperature of from about 255° C. to about 265° C at a pressure from about 10 to about 100 psig, wherein said silica alumina has an alumina content of from about 5 to about 50 wt. %; a surface area of from about 50 m 2 /g to about 700 m 2 g.
Claim 16
Dependent Claim
103 words
A process for producing a bis-(morpholino-alkyl) ether compound from the corresponding N-(hydroxyalkyl)-morpholine compound wherein said N-(hydroxyalkyl) morpholine compound is selected from the group consisting of N-(2-hydroxy-ethyl)-2,6-dimethyl morpholine, N-(2-hydroxyethyl) morpholine and N-(2-hydroxypropyl) morpholine comprising the steps of: contacting said N-(hydroxyalkyl)morpholine compound with a catalytically effective amount of silica alumina at a temperature of from about 255° C. to about 265° C at a pressure from about 10 to about 100 psig, wherein said silica alumina has an alumina content of from about 5 to about 50 wt. %; a surface area of from about 50 m 2 /g to about 700 m 2 g.