Process for preparing modified poly(alkylene carbonate) polyahls

Claim 2

A process for modifying a poly(alkylene carbonate)polyahl which comprises: contacting the poly(alkylene carbonate)polyahl with at least one modifier including at least one active hydrogen moiety or a cyclic anhydride moiety selected from the group consisting of polyahls and cyclic anhydrides, containing two or more functional groups and reacting an active moiety of said poly(alkylene carbonate)polyahl and said reactive moiety of said modifier to form a modified poly(alkylene carbonate)polyahl wherein the modifier is chemically bonded to the poly(alkylene carbonate)polyahl; the reaction conditions and the proportion of the modifier to the polyahl being sufficient to provide a modified product weight of the poly(alkylene carbonate)polyahl.

Claim 3

The process of claim 1, wherein the contacting step is conducted at a temperature between about 80° C. and about 300° C.

Claim 4

The process of claim 1, wherein the poly(alkylene carbonate)polyahl is a random polymer which corresponds to the formula: ##STR6## wherein R 1 is separately in each occurrence an n-valent hydrocarbon radical or hydrocarbon radical which can contain one or more heteroatoms of O, N or S; R 2 is separately in each occurrence hydrogen, halogen, a nitrogen group, a cyano group, a C 1-20 hydrocarbyl group or a C 1-20 hydrocarbyl group substituted with one or more of the following: a halo, cyano, nitro, thioalkyl, tert-amino, alkoxy, aryloxy, aralkoxy, carbonyldioxyalkyl, carbonyldioxyaryl, carbonyldioxyaralkyl, alkoxycarbonyl, aryloxycarbonyl, aralkoxycarbonyl, alkylcarbonyl, arylcarbonyl, aralkylcarbonyl, alkylsulfinyl, arylsulfinyl, aralkylsulfinyl, alkylsulfonyl, arylsulfonyl, or aralkylsulfonyl group; X is separately in each occurrence S, O, NH, ##STR7## A is separately in each occurrence ##STR8## combinations thereof or a covalent bond; Q is separately in each occurrence O, S or NH provided that all carbonate moieties are internal because terminal carbonate moieties are unstable and form OH moieties by the elimination of CO 2 ; n is separately in each occurrence an integer of from 1 to 25; x is separately in each occurrence an integer of from 1 to 40; y is separately in eafh occurrence an integer of from 1 to 120; and z is separately in each occurrence an integer of from 0 to 5.

Claim 5

The process of claim 3 wherein x is oxygen, x is separately in each occurrence an interger from 2 to 10, y is separately in each occurrence an interger from 5 to 15, and z is an interger from 0 to 2, provided that the ratio of y to x is from 1:1 to 3:1.

Claim 6

The process of claim 4 wherein R 1 is aliphatic or cycloaliphatic hydrocarbon containing one or more oxygen, nitrogen, or sulfur moieties; R 2 is hydrogen, C 1-20 alkyl, C 1-20 haloalkyl, C 1-20 alkenyl or phenyl; X is S, O, or NH; and n is an integer from 1 to 10.

Claim 7

The process of claim 5, wherein R 1 is an n valent alkane or cycloalkane, or an n valent alkane or cycloalkane containing one or more oxygen, nitrogen, or sulfur moieties; R 2 is hydrogen, methyl or ethyl; X is O; and n is an integer from 1 to 5.

Claim 8

The process of claim 6 wherein R 1 is an n valent C 1-10 alkane or an n valent C 1-10 alkane substituted with one or more oxygen moieties; R 2 is hydrogen or methyl; and n is 1 or 2.

Claim 9

The process of claim 7 wherein R 2 is hydrogen.

Claim 10

The process of claim 1 wherein said modifier is an aliphatic polyahl.

Claim 11

The process of claim 1 wherein said modifier is a poly(propylene glycol).

Claim 12

The process of claim 1 wherein said modifier is a polyether polyol or a polyester polyol.

Claim 13

The process of claim 1 wherein said modifier is a poly(ethylene glycol).

Claim 14

The process of claim 1 wherein said modifier is triethylene glycol.

Claim 15

The process of claim 1 wherein said modifier is a poly(alkylene carbonate)polyahl.

Claim 16

The process of claim 1 wherein said modifier is tripropylene glycol or 1,6-hexanediol.

Claim 17

The process of claim 1 wherein said modifier is an aminated poly(propylene glycol).

Claim 18

The process of claim 1, wherein said modifier is an amine.

Claim 19

The process of claim 1, wherein said modifier is a poly(amine).

Claim 20

The process of claim 1, wherein said modifier is triethylene tetramine.

Claim 21

The process of claim 1, wherein said modifier is a cyclic anhydride.

Claim 22

The process of claim 1, wherein said modifier is succinic anhydride, phthalic anhydride or maleic anhydride.

Claim 23

The process of claim 1, wherein said modifier is a polyhydric alcohol.

Claim 24

The process of claim 1, wherein said modifier is poly(caprolactone)diol.

Claim 25

The process of claim 1, wherein said modifier is poly(1,2-butylene glycol).

Claim 26

The process of claim 1, wherein said poly(alkylene carbonate)polyahl to be modified is poly(ethylene carbonate)polyol.

Claim 27

The process of claim 1, wherein said modifier is a hydroxy-functional tertiary amine.

Claim 28

The process of claim 1, wherein said modifier is a phenolic.

Claim 29

The process of claim 1, wherein said contacting step is conducted in the presence of a catalyst selected from the group consisting of sodium stannate trihydrate, titanium isopropoxide and potassium carbonate.

Claim 30

The process of claim 1, wherein said polyahl and said modifier are contacted at a temperature between about the transesterification temperature of the polyahl and the lowest decomposition temperature of the polyahl, the modifier or the modified polyahl or the temperature at which the modifier is volatilized.

Claim 31

The process of claim 1, wherein the proportion of the modifier to the polyahl is up to about stoichiometric.

Claim 32

The process of claim 1, further comprising adding a catalytic amount of a catalyst for the reaction of an active moiety of the poly(alkylene carbonate)polyahl with a reactive moiety of the modifier; said catalyst selected from the group consisting of alkali metal hydroxides, alkaline earth metal hydroxides, alkali metal carbonates, alkaline earth metal carbonates, ammonium hydroxide, and ammonium carbonate.

Claim 33

The process of claim 1, wherein said contacting step is conducted in the presence of a catalyst selected from the group consisting of metal hydroxides and metal alkoxides of a metal selected from the group consisting of lithium, sodium, potassium, rubidium, cesium, magnesium, calcium, strontium, barium, zinc, aluminum, titanium, cobalt, germanium, tin, lead, antimony, arsenic and cerium, carbonates selected from the group consisting of alkali metal carbonates, alkaline earth metal carbonates, lead carbonate and ammonium carbonate, borates selected from the group consisting of alkali metal borates, alkaline earth metal borates, zinc borate, lead borate, and ammonium borates, hydrocarbyloxy titanates, lead silicate, lead arsenate, litharge, oxides selected from the group consisting of antimony trioxide, zinc oxide, germanium dioxide, cerium trioxide, aluminum isopropoxide, and salts of organic acids selected from the group consisting of magnesium, calcium, cerium, barium, zinc and titanium salts, and stannates selected from the group consisting of alkali metal stannates, alkaline earth metal stannates, and ammonium stannates.

Claim 34

The process of claim 32, wherein the borate catalysts are selected from the group consisting of sodium meta-borate, sodium meta-borate tetrahydrate, sodium meta-borate dihydrate, sodium pentaborate pentahydrate, sodium tetraborate decahydrate, sodium tetraborate pentahydrate, diammonium tetraborate tetrahydrate, ammonium hydrogen tetraborate tetrahydrate, lithium ortho-dihydroborate, lithium meta-borate, lithium tetraborate, lithium pentaborate pentahydrate, potassium meta-borate, potassium tetraborate tetrahydrate, potassium tetraborate pentahydrate, potassium pentaborate tetrahydrate, magnesium meta-borate trihydrate, magnesium diborate, magnesium orthoborate, calcium meta-borate, calcium tetraborate, and strontium tetraborate tetrahydrate.

Claim 35

The process of claim 32, wherein the stannate catalysts are selected from the group consisting of sodium stannate trihydrate, potassium stannate trihydrate, potassium stannate monohydrate, barium stannate trihydrate, and magnesium stannate trihydrate.

Claim 36

The process of claim 31, wherein the catalyst is present in an amount between about 0.01% and 5% by weight based upon the reactants.

Claim 37

Th process of claim 35, wherein the catalyst is present in an amount between about 0.01% and about 1% by weight based on the reactants.

Claim 38

The process of claim 1, further comprising a solvent selected from the group consisting of inert organic solvents which are more volatile than the modified polyahl product.