Chemical process

Claim 2

A process for preparing a mixture of the alkali metal salts of 1-hydroxy-3-oxa-1,2,4,5-pentane tetracarboxylic acid and 3,6-dioxa-1,2,4,5,7,8-octane hexacarboxylic acid by means of a calcium ion catalyzed reaction which comprises: a. reacting the salts of maleic and D,L-tartaric acids in alkaline medium; b. reducing the calcium content of said reaction product mixture to the extent that the molar ratio of calcium to the D,L-tartrate succinate reaction products is less than about 1:10 by precipitation of calcium carbonate; c. recovering the calcium carbonate removed in step (b) and recycling it to step (a) to prepare additional amounts of reaction product, and d. recovering and purifying the remainder of the reaction product from step (b).

Claim 3

A process of claim 1 wherein the calcium is removed from the reaction product in step b at a temperature of from about 85° C. to about 105° C.

Claim 4

A process of claim 1 wherein the calcium carbonate is formed in the reaction mixture by reaction with an alkali metal carbonate.

Claim 5

A process of claim 2 wherein the calcium carbonate is formed by reaction with an alkali metal bicarbonate.

Claim 6

A process of claim 3 wherein the alkali metal is sodium.

Claim 7

A process of claim 4 wherein the alkali metal is sodium.

Claim 8

A process of claim 1 further including the step of reacting the calcium carbonate recovered in step (c) with maleic acid to form a salt before recycle to step (a).

Claim 9

A process of claim 7 wherein the calcium maleate is added to the reaction mixtures of step (a) in the form of an aqueous slurry.

Claim 10

A process of claim 7 wherein the calcium carbonate is formed by reaction of calcium ions with carbon dioxide.

Claim 11

A process of claim 1 wherein the reaction medium of step (b) is maintained at a pH in the range of from about 10 to about 12.

Claim 12

A process of claim 1 wherein the mole ratio of carbonate to calcium in step (b) is 1.3:1.

Claim 13

A process of claim 1 wherein the solids content of the reaction mixture of step (a) is in the range of from 55% to about 60% by weight.

Claim 14

A process for preparing a mixture of the alkali metal of 1-hydroxy-3-oxa-1,2,4,5-pentane tetracarboxylic acid and 3,6-dioxa-1,2,4,5,7,8-octane hexacarboxylic acid which comprises the steps of: a. forming an aqueous reaction mixture comprising from about 20% to 60% by weight of both calcium and monovalent cation salts of maleic acid and D,L-tartaric acid, said mixture corresponding to the over-neutralized mixture which is formed by combining: (i) maleic and D,L-tartaric acids in a maleic to D,L-tartaric molar ratio of from about 0.5:1 to about 8:1; (ii) a source of calcium cations in an amount such that the molar ratio of calcium to D,L-tartaric acid ranges from about 0.1:1 to 2.0:1 with the ratio of moles of calcium to total moles of maleic and D,L-tartaric acid being less than 1; and (III) a neutralizing agent comprising an hydroxide of a monovalent cation in an amount such that the ratio of moles of monovalent cation to moles of maleic acid plus moles of D,L-tartaric acid minus moles of calcium ranges from about 2.1:1 to 3.8:1; (b) maintaining said aqueous reaction mixture at a temperature of from about 20° C. to 120° C. for a time period sufficient to form a reaction product mixture of said 1-hydroxy-3-oxa-1,2,4,5-pentane tetracarboxylic acid salts and 3,6-dioxa-1,2,4,5,7,8-octane hexacarboxylic acid salts; (c) treating the filtrate from step (b) with a carbonate whereby calcium carbonate precipitates; (d) removing the calcium carbonate from the filtrate and recycling it to step (a) to prepare additional amounts of reaction product and (e) recovering and purifying the filtrate from step (d).

Claim 15

A process for preparing a mixture of the alkali metal of 1-hydroxy-3-oxa-1,2,4,5-pentane tetracarboxylic acid and 3,6-dioxa-1,2,4,5,7,8-octane hexacarboxylic acid which comprises the steps of: a. forming an aqueous reaction mixture comprising from about 20% to 60% by weight of both calcium and monovalent cation salts of maleic acid and D,L-tartaric acid, said mixture corresponding to the over-neutralized mixture which is formed by combining: (i) maleic and D,L-tartaric acids in a maleic to D,L-tartaric molar ratio of from about 0.5:1 to about 8:1; (ii) a source of calcium cations in an amount such that the molar ratio of calcium to D,L-tartaric acid ranges from about 0.1:1 to 2.0:1 with the ratio of moles of calcium to total moles of maleic and D,L-tartaric acid being less than 1; and (III) a neutralizing agent comprising an hydroxide of a monovalent cation in an amount such that the ratio of moles of monovalent cation to moles of maleic acid plus moles of D,L-tartaric acid minus moles of calcium ranges from about 2.1:1 to 3.8:1; (b) maintaining said aqueous reaction mixture at a temperature of from about 20° C. to 120° C. for a time period sufficient to form a reaction product mixture of said 1-hydroxy-3-oxa-1,2,4,5-pentane tetracarboxylic acid salts and 3,6-dioxa-1,2,4,5,7,8-octane hexacarboxylic acid salts; (c) treating the filtrate from step (b) with a carbonate whereby calcium carbonate precipitates; (d) removing the calcium carbonate from the filtrate and recycling it to step (a) to prepare additional amounts of reaction product and (e) recovering and purifying the filtrate from step (d).

Claim 16

A process of claim 13 further including the step of reacting the calcium carbonate recovered in step (d) with maleic acid prior to recycle to step (a) to form calcium maleate.

Claim 17

A process of claim 13 wherein the carbonate is sodium bicarbonate.

Claim 18

A process of claim 14 wherein the mole ratio of carbonate to calcium in step (c) is 1.3:1.

Claim 19

A process of claim 13 wherein the neutralizing agent is sodium hydroxide.