Process for producing organic acid esters of cellulose

Claim 2

A process for forming organic acid esters of cellulose, in an efficient and rapid manner, which includes a controlled esterification reaction comprising confricating cellulose, at high consistency, in the presence of esterification chemicals, to form a confricated cellulose ester product, said confrication step including high energy, frictional interaction of said cellulose and esterification chemicals, respectively, which are maintained in relatively intimate contact one with the other, and furnishing the predominant means for providing penetration of said esterification chemicals for distribution throughout the cellulose, without substantial degradation of the confricated cellulose ester product formed.

Claim 3

The process of claim 1, wherein said cellulose is chemicaly combined with an organic acid anhydride reactant, said anhydride substantially penetrating, and being distributed throughout, said cellulose.

Claim 4

The process of claim 2, wherein superatmospheric pressure is maintained during said confrication step.

Claim 5

The process of claim 3, wherein the temperature is maintained above the boiling point of said organic acid reagent during said confrication step.

Claim 6

The process of claim 2, wherein the time required to efficiently and rapidly form said organic acid esters of cellulose is less than about 0.5 hour.

Claim 7

The process of claim 5, wherein the formation time is less than about 0.1 hour.

Claim 8

The process of claim 2, wherein the organic acid anhydride reactant is acetic anhydride.

Claim 9

The process of claim 1, wherein said organic acid anhydride is present during said confrication step, said anhydride reactant substantially penetrating, and being distributed throughout, the cellulose.

Claim 10

The process of claim 8, wherein said confricated cellulose product formed during said confrication step is further reacted with an organic acid anhydride reactant.

Claim 11

The process of claim 1, wherein said esterification chemicals comprise an organic acid reagent and esterification catalyst.

Claim 12

The process of claim 10, wherein the organic acid reagent is acetic acid and the esterification catalyst is sulfuric acid.

Claim 13

The process of claim 1, wherein said high consistency confrication step is conducted in a disc refiner.

Claim 14

The process of claim 12, wherein said high consistency is from about 15 to about 35% based on the dry weight of fibers in the feed.

Claim 15

The process of claim 12, wherein the amount of energy imparted to the high consistency cellulose sufficient to provide confrication is from about 8 HPD/T pulp up to an upper energy level of about 40 HPD/T.

Claim 16

The process of claim 14, wherein the amount of energy is from about 15 HPD/T to about 25 HPD/T.

Claim 17

The process of claim 1, wherein the organic acid ester of cellulose formed is cellulose triacetate.

Claim 18

The process of claim 12, wherein the organic acid ester of cellulose formed is cellulose triacetate.

Claim 19

A process for rapidly forming organic acid esters of cellulose which comprises the steps of: a. introducing cellulose, at high consistency, and esterification chemicals into an area formed within a high energy reactor, said area including means for confricating said high-consustency cellulose in the presence of said esterification chemicals; and b. confricating said cellulose and esterification chemicals, respectively, said configuration step including the high energy, frictional interaction of said cellulose and esterification chemicals which are maintained at relatively intimate contact one with the other, said resultant confricated product being characterized in that said esterification chemicals have substantially penetrated, and are uniformly distributed throughout, said cellulose.

Claim 20

A process for rapidly forming organic acid esters of cellulose which comprises the steps of: a. introducing cellulose, at high consistency, and esterification chemicals into an area formed within a high energy reactor, said area including means for confricating said high-consustency cellulose in the presence of said esterification chemicals; and b. confricating said cellulose and esterification chemicals, respectively, said configuration step including the high energy, frictional interaction of said cellulose and esterification chemicals which are maintained at relatively intimate contact one with the other, said resultant confricated product being characterized in that said esterification chemicals have substantially penetrated, and are uniformly distributed throughout, said cellulose.

Claim 21

The process of claim 18, wherein said confricating means comprises a pair of opposed surfaces forming a work space therebetween, said opposed surfaces being capable of imparting the requisite amount of confrication energy to said cellulose passing within the confines of said work space.

Claim 22

The process of claim 19, wherein said high consistency confrication step is conducted in a disc refiner.

Claim 23

The process of claim 20, wherein said high consistency is from about 15 to about 35% by weight based on the dry weight of fibers in the feed.

Claim 24

The process of claim 20, wherein the amount of energy imparted to the high consistency cellulose sufficient to provide confrication is from about 8 HPD/T up to an upper energy level of about 40 HPD/T.

Claim 25

The process of claim 22, wherein the amount of energy is from about 15 HPD/T to about 25 HPD/T.