Process for the continuous isomerization of dextrose

Claim 2

A process for the continuous isomerization of dextrose to levulose comprising: passing a solution containing dextrose, at a pH of from about 7.0 to about 8.5, through a bed of immobilized dextrose isomerase prepared by bringing a solution of dextrose isomerase into contact with a porous or macroreticulated strongly basic anion exchange resin having -N-(CH 3 ) 3 -X as the ion exchange group; removing a levulose-bearing solution from the bed until a decrease in enzyme activity occurs, then passing additional dextrose isomerase through the bed to reactivate said bed, continuing to pass the solution containing dextrose through the reactivated bed, and recovering additional levulose-bearing solution therefrom.

Claim 3

A process in accordance wth claim 1 wherein the fresh dextrose isomerase is brought into contact with the particulate resin while mixed in the solution containing dextrose that is being brought into contact with the composite.

Claim 4

A continuous process for preparing a levulose-bearing product comprising: continuously passing a solution containing dextrose at a pH in the range from about 7.0 to about 8.5 through a bed of an immobilized dextrose isomerase composite wherein the dextrose isomerase is immobilized on a particulate strongly basic anion exchange resin having --N--(CH 3 ) 3 --X as the ion exchange group that is characterized by the presence throughout its polymeric matrix of a network of pores that provide an adsorptive surface area; continuously removing from the bed a levulose-bearing product until a decrease in activity of the original composite occurs; adding fresh dextrose isomerase to the feed stream of the solution containing dextrose and passing the mixture thereby obtained through said bed into contact with the composite to enhance the activity of the composite without interrupting isomerization, and continuously thereafter recovering additional levulose-bearing product from the bed.

Claim 5

A continuous process for preparing a levulose-bearing product comprising: continuously passing a solution containing dextrose at a pH in the range from about 7.0 to about 8.5 through a bed of an immobilized dextrose isomerase composite wherein the dextrose isomerase is immobilized on a particulate strongly basic anion exchange resin having --N--(CH 3 ) 3 --X as the ion exchange group that is characterized by the presence throughout its polymeric matrix of a network of pores that provide an adsorptive surface area; continuously removing from the bed a levulose-bearing product until a decrease in activity of the original composite occurs; adding fresh dextrose isomerase to the feed stream of the solution containing dextrose and passing the mixture thereby obtained through said bed into contact with the composite to enhance the activity of the composite without interrupting isomerization, and continuously thereafter recovering additional levulose-bearing product from the bed.

Claim 6

A process in accordance with claim 3 wherein the pH is about 8.0.

Claim 7

A process in accordance with claim 3 wherein the particulate resin is a macroreticular, strongly basic anion exchange resin.

Claim 8

A continuous process for the enzymatic production of a levulose-bearing product, comprising: continuously passing a dextrose-containing solution at a pH from about 6 to about 9, at a temperature in the range from about 20°C. to about 80°C. and having a dextrose concentration in the range of between 30% and 70%, d.s., at a flow rate of from 1 to about 5 SV, wherein "SV" is the substrate velocity of the dextrose-containing solution measured in bed volumes per hour, through a bed containing an immobilized dextrose isomerase composite, wherein the immobilized dextrose isomerase composite comprises dextrose isomerase immobilized onto a macroreticular synthetic strongly basic anion exchange resin having -N-(CH 3 ) 3 -X as the ion exchange group in the form of granules or beads having a particle size in the range from about 16 mesh to about 100 mesh (U.S. Standard Screen) and characterized by the presence, throughout the polymeric matrix of its particles, of a network of pores that provide an adsorptive surface area up to about 2,000 square meters per gram, continuously removing a substantially colorless, levulose-bearing product from the bed, and maintaining the isomerase activity of said immobilized dextrose isomerase by adding a solution containing from 10 to about 50 units per gram of isomerase activity per wet gram of resin to said dextrose-containing solution.

Claim 9

A continuous process for the enzymatic production of a levulose-bearing product, comprising: continuously passing a dextrose-containing solution at a pH from about 6 to about 9, at a temperature in the range from about 20°C. to about 80°C. and having a dextrose concentration in the range of between 30% and 70%, d.s., at a flow rate of from 1 to about 5 SV, wherein "SV" is the substrate velocity of the dextrose-containing solution measured in bed volumes per hour, through a bed containing an immobilized dextrose isomerase composite, wherein the immobilized dextrose isomerase composite comprises dextrose isomerase immobilized onto a macroreticular synthetic strongly basic anion exchange resin having -N-(CH 3 ) 3 -X as the ion exchange group in the form of granules or beads having a particle size in the range from about 16 mesh to about 100 mesh (U.S. Standard Screen) and characterized by the presence, throughout the polymeric matrix of its particles, of a network of pores that provide an adsorptive surface area up to about 2,000 square meters per gram, continuously removing a substantially colorless, levulose-bearing product from the bed, and maintaining the isomerase activity of said immobilized dextrose isomerase by adding a solution containing from 10 to about 50 units per gram of isomerase activity per wet gram of resin to said dextrose-containing solution.