Purification of sugarcane juice

Claim 2

A process of purifying sugarcane juices, comprising the steps of first contacting the sugarcane juices to be purified with a hydrophobic adsorbent and next with a supported strong anion exchange material, then contacting the juices, in any order, with an anion exchange resin and a cation exchange resin, and finally eluting aconitic acid retained by the anion exchange resin of the then contacting step with a solution of acid pH or a solution of basic pH, thereby obtaining aconitic acid or aconitate, wherein the juices to be purified are obtained by crushing and pressing cane, adding a flocculating agent to the juices obtained, and centrifuging and filtrating the resulting mixture so that it has a concentration of sugars of 10° to 25° Brix, and wherein the hydrophobic adsorbent is selected from the group consisting of a cross-linked vinyl aromatic polymer and a mineral support of alumina or silica coated with an amount of less than 15 mg/m 2 of a film of cross-linked vinyl aromatic polymer, said adsorbent having a particle size of 50 to 5000 μm, a specific surface of 5 to 600 m 2 /g, a pore diameter of 60 to 3000 Å, and a pore volume of 0.2 to 4 ml/g.

Claim 3

A process according to claim 1, wherein the supported strong anion exchange material is formed of a mineral support of alumina or silica coated with an amount of less than 15 mg/m 2 of a cross-linked polymer film obtained from epoxy compounds, formaldehyde, and vinyl monomers, said polymer containing or bearing quaternary ammonium salt exchange groups, said exchange material having a particle size of 4 to 5000 μm, a specific surface of 5 to 150 m 2 /g, a pore diameter of 60 to 3000 Å, a pore volume of 0.2 to 4 ml/g, and an ion capacity of less than 2 meq/g.

Claim 4

A process according to any of claims 1 or 2, wherein the anion exchange resin is formed of a cross-linked vinyl polymer containing or bearing primary, secondary, or tertiary amine exchange groups or quaternary ammonium salts and has a particle size of 100 to 5000 μm and an ion capacity of 0.5 to 4 meq/ml.

Claim 5

A process according to any of claims 1 or 2, wherein the cation exchange resin is formed of a cross-linked vinyl polymer containing or bearing carboxylic or sulfonic acid exchange groups and has a particle size of 100 to 5000 μm and an ion capacity of 0.5 to 4 meq/ml.

Claim 6

A process according to any of claims 1 or 2, wherein the process is carried out with juices having a pH of between 5 and 12 and at temperatures of between 15° and 80° C.

Claim 7

A process according to any of claims 1 or 2, wherein the amounts used of hydrophobic adsorbent, supported anion exchange material, anion exchange resin and cation exchange resin are between 10 and 350 g liter of cane juice.

Claim 8

The process of claim 1 further comprising as the last step the step of concentrating the sugarcane juice, thereby obtaining sugar syrup.

Claim 9

The process of claim 7 further comprising as the last step the step of crystallizing the syrup, thereby obtaining sucrose.

Claim 10

A process for the purification of low-grade sugar solutions comprising the steps of first contacting the low-grade sugar solutions with a hydrophobic adsorbent, next contacting the low-grade sugar solutions with a supported strong anion exchange material, then contacting the low-grade sugar solutions, in any order, with an anion exchange resin and a cation exchange resin, and finally eluting aconitic acid retained by the anion exchange resin of the then contacting step with a solution of acid pH or a solution of basic pH, thereby obtaining aconitic acid or aconitate, wherein the low-grade sugar solution is obtained from sugarcane juice by clarification,, evaporation, crystallization and redissolution, said sugarcane juices being obtained by crushing and pressing cane, adding a flocculating agent to the juices obtained, and centrifuging and filtrating the resulting mixture so that it has a concentration of sugars of 10° to 25° Brix, and wherein the hydrophobic adsorbent is selected from the group consisting of a cross-linked vinyl aromatic polymer and a mineral support of alumina or silica coated with an amount of less than 15 mg/m 2 of a film of cross-linked vinyl aromatic polymer, said adsorbent having a particle size of 50 to 5000 μm, a specific surface of 5 to 600 m 2 /g, a pore diameter of 60 to 3000 Å, and a pore volume of 0.2 to 4 ml/g.

Claim 11

A process for the purification of low-grade sugar solutions comprising the steps of first contacting the low-grade sugar solutions with a hydrophobic adsorbent, next contacting the low-grade sugar solutions with a supported strong anion exchange material, then contacting the low-grade sugar solutions, in any order, with an anion exchange resin and a cation exchange resin, and finally eluting aconitic acid retained by the anion exchange resin of the then contacting step with a solution of acid pH or a solution of basic pH, thereby obtaining aconitic acid or aconitate, wherein the low-grade sugar solution is obtained from sugarcane juice by clarification,, evaporation, crystallization and redissolution, said sugarcane juices being obtained by crushing and pressing cane, adding a flocculating agent to the juices obtained, and centrifuging and filtrating the resulting mixture so that it has a concentration of sugars of 10° to 25° Brix, and wherein the hydrophobic adsorbent is selected from the group consisting of a cross-linked vinyl aromatic polymer and a mineral support of alumina or silica coated with an amount of less than 15 mg/m 2 of a film of cross-linked vinyl aromatic polymer, said adsorbent having a particle size of 50 to 5000 μm, a specific surface of 5 to 600 m 2 /g, a pore diameter of 60 to 3000 Å, and a pore volume of 0.2 to 4 ml/g.

Claim 12

A process according to claim 9, wherein the minimum amounts used of hydrophobic adsorbent and supported anion exchange material are 5 g/liter of low-grade sugar solution.

Claim 13

The process of claim 9 or 10 further comprising as the last two steps the steps of concentrating and then crystallizing the low-grade sugar solution purified, thereby obtaining sucrose.

Claim 14

The process of claim 9 or 10 further comprising as the last step of concentrating the low-grade sugar solutions purified, thereby obtaining sucrose syrup.

Claim 15

The process of any one of claims 1 or 9 further comprising the step of eluting amino acids retained by the cation exchange resin with a solution of acid pH, thereby obtaining fractions enriched in amino acids.