Process for the manufacture of aliphatic phosphonic acids

Claim 2

In a process for the manufacture of an aliphatic phosphonic acid of the formula: ##STR7## of the type wherein a diester of the aliphatic phosphonic acid of the general formula: ##STR8## is reacted with anhydrous hydrogen halide selected from the group consisting of hydrogen chloride, hydrogen bromide, hydrogen iodide and hydrogen fluoride to produce a reaction product containing the corresponding aliphatic phosphonic acid and the corresponding aliphatic halides, wherein R 1 , R 2 and R 3 are each independently selected from the group consisting of substituted and unsubstituted aryl, alkyl, alkenyl, halo-substituted alkyl and halosubstituted alkenyl, having from 1 to 6 carbon atoms, wherein the improvement comprises a. reacting the diester and the anhydrous hydrogen halide at a first temperature of at least 100° C, at a low pressure and for a first period of time to form a first reaction product; b. subsequently reacting the first reaction product and the anhydrous hydrogen halide at a second temperature of at least 100° C, at a high pressure, said high pressure higher than said low pressure, and for a second period of time to form a second reaction product; and c. removing the aliphatic halides from at least one reaction product.

Claim 3

The process of claim 1, wherein the step of removing aliphatic halides is continuous and the aliphatic halides are removed from the first and second reaction products.

Claim 4

The process of claim 1, wherein R 1 , R 2 and R 3 are the same.

Claim 5

The process of claim 1, wherein R 1 , R 2 and R 3 are the same halo-substituted alkyl.

Claim 6

The process of claim 1, wherein the aliphatic phosphonic acid is 2-chloroethylphosphonic acid.

Claim 7

The process of claim 5, wherein the diester is bis(2-chloroethyl)-2-chloroethyl phosphonate.

Claim 8

The process of claim 1, wherein the anhydrous hydrogen halide is anhydrous hydrogen chloride.

Claim 9

The process of claim 7, wherein the aliphatic halides are ethylene dichloride.

Claim 10

The process of claim 1, wherein a. the aliphatic phosphonic acid is 2-chloroethylphosphonic acid; b. the diester is bis(2-chloroethyl)-2-chloroethyl phosphonate; c. the anhydrous hydrogen halide is anhydrous hydrogen chloride; and d. the aliphatic halides are ethylene dichloride.

Claim 11

The process of claim 9, wherein the first and second temperatures are from about 140° C to about 160° C.

Claim 12

The process of claim 9, wherein the first and second temperature are no greater than about 200° C.

Claim 13

The process of claim 9, wherein the step of removing ethylene dichloride is continuous and the ethylene dichloride is removed from the first and second reaction products; and wherein the steps of: (a) reacting the diester of the anhydrous hydrogen chloride, (b) reacting the first reaction product and the anhydrous hydrogen chloride, and (c) removing aliphatic halides, is accomplished by i. introducing continuously into the first and second reaction products an entrance stream comprised of anhydrous hydrogen chloride; and ii. removing continuously from the first and second reaction products an exit stream comprised of unreacted anhydrous hydrogen chloride and ethylene dichloride.

Claim 14

The process of claim 12, wherein the unreacted anhydrous hydrogen chloride is separated from the exit stream and introduced into the entrance stream.

Claim 15

The process of claim 9, wherein the low pressure is at least about 14 psia and the high pressure is at least about 30 psia.

Claim 16

The process of claim 9, wherein the low pressure is from about 14 psia to about 30 psia, and the high pressure is from about 30 psia to about 50 psia.

Claim 17

The process of claim 9, wherein the first period of time is until the first reaction product contains at least about 70% by weight of 2-chloroethylphosphonic acid.

Claim 18

The process of claim 9, wherein the first period of time is at least about 25 hours.

Claim 19

The process of claim 9, wherein the first period of time is from about 25 to about 35 hours.

Claim 20

The process of claim 9, wherein the second period of time until the second reaction product contains a required concentration of at least about 80% by weight of 2-chloroethylphosphonic acid.

Claim 21

The process of claim 9, wherein the second period of time is at least about 10 hours.

Claim 22

The process of claim 9, wherein the second period of time is from about 10 hours to about 16 hours.

Claim 23

The process of claim 12, wherein the exit stream flowrate during the first period of time is greater than the exit stream flowrate during the second period of time.

Claim 24

The process of claim 22, wherein the weight ratio of the exit stream flowrates is about (3 to 6): 1.

Claim 25

In a process for the manufacture of 2-chloroethylphosphonic acid of the type wherein bis(2-chloroethyl)-2-chloroethyl phosphonate is reacted with anhydrous hydrogen chloride to produce a reaction product containing 2-chloroethylphosphonic acid and ethylene dichloride, wherein the improvement comprises: a. reacting bis(2-chloroethyl)-2-chloroethyl phosphonate and anhydrous hydrogen chloride at a first temperature of at least 100° C, at a low pressure of at least about 14 psia for a first period of time to form a first reaction product, said first period of time is until the first reaction product contains at least about 70% by weight of 2-chloroethylphosphonic acid; b. subsequently reacting the first reaction product and the anhydrous hydrogen chloride at a second temperature of at least 100° C, at a high pressure of at least about 30 psia, said high pressure higher than said low pressure, and for a second period of time to form a second reaction product, said second period of time is until the second reaction product contains a required concentration of at least about 80% by weight of 2-chloroethylphosphonic acid; c. continuously removing ethylene dichloride from the first and second reaction product, wherein the steps of (a) reacting bis(2-chloroethyl)-2-chloroethylphosphonate and anhydrous hydrogen chloride, (b) reacting the first reaction product and anhydrous hydrogen chloride, and (c) removing ethylene dichloride are accomplished by: i. introducing continuously into the first and second reaction products an entrance stream comprised of anhydrous hydrogen chloride; and ii. removing continuously from the first and second reaction products an exit stream comprised of unreacted anhydrous hydrogen chloride and ethylene dichloride.

Claim 26

In a process for the manufacture of 2-chloroethylphosphonic acid of the type wherein bis(2-chloroethyl)-2-chloroethyl phosphonate is reacted with anhydrous hydrogen chloride to produce a reaction product containing 2-chloroethylphosphonic acid and ethylene dichloride, wherein the improvement comprises: a. reacting bis(2-chloroethyl)-2-chloroethyl phosphonate and anhydrous hydrogen chloride at a first temperature of at least 100° C, at a low pressure of at least about 14 psia for a first period of time to form a first reaction product, said first period of time is until the first reaction product contains at least about 70% by weight of 2-chloroethylphosphonic acid; b. subsequently reacting the first reaction product and the anhydrous hydrogen chloride at a second temperature of at least 100° C, at a high pressure of at least about 30 psia, said high pressure higher than said low pressure, and for a second period of time to form a second reaction product, said second period of time is until the second reaction product contains a required concentration of at least about 80% by weight of 2-chloroethylphosphonic acid; c. continuously removing ethylene dichloride from the first and second reaction product, wherein the steps of (a) reacting bis(2-chloroethyl)-2-chloroethylphosphonate and anhydrous hydrogen chloride, (b) reacting the first reaction product and anhydrous hydrogen chloride, and (c) removing ethylene dichloride are accomplished by: i. introducing continuously into the first and second reaction products an entrance stream comprised of anhydrous hydrogen chloride; and ii. removing continuously from the first and second reaction products an exit stream comprised of unreacted anhydrous hydrogen chloride and ethylene dichloride.

Claim 27

The process of claim 24, wherein the unreacted anhydrous hydrogen chloride is separated from the exit stream and introduced into the entrance stream.

Claim 28

The procss of claim 24, wherein the first and second temperatures are from about 140° C to about 160° C.

Claim 29

The process of claim 24, wherein the first and second temperatures are no greater than about 200° C.

Claim 30

The process of claim 24, wherein the low pressure is from about 14 psia to about 30 psia.

Claim 31

The process of claim 24, wherein the high pressure is from about 30 psia to about 50 psia.

Claim 32

The process of claim 24, wherein the first period of time is at least 25 hours.

Claim 33

The process of claim 24, wherein the first period of time is from about 25 to about 35 hours.

Claim 34

The process of claim 24, wherein the second period of time is at least 10 hours.

Claim 35

The process of claim 24, wherein the second period of time is from about 10 hours to about 16 hours.

Claim 36

The process of claim 24, wherein the exit stream flowrate during the first period of time is greater than the exit stream flowrate during the second period of time.

Claim 37

The process of claim 34, wherein the weight ratio of the exit stream flowrate is about (3 to 6) : 1.