Preparation of water-insoluble enzyme compositions

Claim 2

A process for preparing a water-insoluble enzyme composition wherein an enzyme is covalently bonded to an inorganic support material whereby a maximum activity of the insoluble enzyme composition is achieved with the lowest possible amount of enzyme, said process comprising the steps of: (a) selecting an inorganic support material having the most frequent pore-diameter which produces an enzyme composition having the highest absolute activity when a plurality of inorganic support materials having different most frequent pore-diameters are each individually contacted with an enzyme solution containing a given concentration of enzyme, said most frequent pore-diameter producing the highest absolute activity being independent of the enzyme concentration in the solution; (b) selecting an aqueous enzyme solution containing the concentration of enzyme which produces a composition that has a relative activity of substantially 100% when the support material of step (a) is contacted with a plurality of enzyme solutions having different concentrations of enzyme; (c) contacting the support material of step (a) with the enzyme solution of step (b) whereby a portion of the enzyme from the solution is taken up by the support material to produce a water-insoluble enzyme composition; and (d) separating the resulting water-insoluble enzyme composition from the remaining solution.

Claim 3

The process as defined in claim 1 which further comprises the step of bonding a coupling agent to an inorganic carrier material to obtain an inorganic support material which is capable of covalently bonding the enzyme.

Claim 4

The process as defined in claim 2, wherein the inorganic carrier material comprises a hydroxy-group-containing oxide of at least one element selected from the group consisting of silicon, aluminum, nickel, iron, titanium, zirconium, or mixtures thereof.

Claim 5

The process as defined in claim 2, wherein the inorganic support material which is capable of covalently bonding the enzyme is a silanized silicon oxide gel.

Claim 6

The process as defined in claim 1, wherein the inorganic support material comprises a silicon dioxide-gel.

Claim 7

The process as defined in claim 5 which further comprises the step of preparing a silicon dioxide-gel by adjusting the alkali content expressed as % by weight of Na 2 O to from about 0.1 to about 0.5% by weight, drying the gel, and calcining the dried gel at a temperature of from about 400° to about 850° C. in a flow of water-vapor-containing air during a period of from about 5 to about 10 hours.

Claim 8

The process as defined in claim 6, wherein the calcining temperature is from about 570° to about 750° C.

Claim 9

The process as defined in claim 6, wherein the drying is effected at a temperature of between about 180° C. and about 200° C. under water-vapor-saturated air.

Claim 10

The process as defined in claim 6, wherein the calcining is effected in a flow of air having a relative humidity of between about 40 and about 80%.

Claim 11

The process as defined in claim 1, wherein the enzyme is selected from the group consisting of hydrolytic enzymes, redox enzymes, isomerases, and transferase enzymes.

Claim 12

The process as defined in claim 10, wherein the hydrolytic enzymes are selected from the group consisting of amylases, glycosidases, and proteases.

Claim 13

The process as defined in claim 11, wherein the enzyme is amyloglucosidase.

Claim 14

The process as defined in claim 11, wherein the enzyme solution contains from about 25 to about 75 mg of amyloglucosidase per 1 g of support material.

Claim 15

The process as defined in claim 13, wherein the amount of amyloglucosidase is about 50 mg per 1 g of support material.

Claim 16

The process as defined in claim 13, wherein the amyloglucosidase exhibits a specific activity in the free state of from about 10 to about 15 units/mg.

Claim 17

The process as defined in claim 13, wherein the support material comprises a silicon dioxide-gel having a most frequent pore-diameter of from about 300 to about 400 A.

Claim 18

The process as defined in claim 10, wherein the enzyme is glucose-isomerase.

Claim 19

The process as defined in claim 17, wherein the enzyme solution contains from about 20 to about 50 mg of glucose-isomerase per 1 g of support material.

Claim 20

The process as defined in claim 18, wherein the amount of glucose-isomerase is about 25 mg per 1 g of support material.

Claim 21

The process as defined in claim 18, wherein the glucose-isomerase exhibits a specific activity in the free state of from about 50 to from about 70 units/mg.

Claim 22

The process as defined in claim 18, wherein the support material comprises a silicon dioxide-gel having a most frequent pore-diameter of from about 300 to about 400 A.

Claim 23

The process as defined in claim 2, wherein the inorganic support material which is capable of covalently bonding the enzyme is a silicon oxide gel, which is treated with glutardialdehyde.

Claim 24

A process according to claim 1, wherein the inorganic support material is selected by: (a1) contacting a plurality of individual inorganic support materials having different most frequent pore-diameters with at least one enzyme solution to produce insolubilized enzyme compositions; (a2) measuring the absolute activity of each of the resulting insolubilized enzyme compositions; (a3) comparing the measured values for the different support materials; and (a4) selecting the support material having the most frequent pore-diameter which produces the enzyme composition having the highest absolute activity.

Claim 25

A process according to claim 1, wherein the enzyme solution is selected by: (b1) contacting the support material of step (a) with a plurality of enzyme solutions containing different concentrations of enzyme to produce insolubilized enzyme compositions; (b2) measuring the amount of enzyme taken up by each of the support materials and determining the specific activity of each of the insolubilized enzyme compositions; (b3) determining the relative activity of the enzyme in each of the enzyme compositions from the specific activity of the insolubilized enzyme compositions and the specific activity of the enzyme in the free state in the enzyme solutions; and (b4) determining the enzyme solution which produces an insolubilized enzyme composition having a relative activity of substantially 100%.

Claim 26

Process according to claim 1, wherein the water-insoluble enzyme composition from step d) has the highest enzyme activity per weight unit of the composition which is obtainable at the concentration of enzyme contained in said composition.

Claim 27

Process according to claim 24, wherein the enzyme solution of step (b4) produces an insolubilized enzyme composition having the highest activity per weight unit of composition which is obtainable at that enzyme concentration.

Claim 28

A process of producing a water-insoluble enzyme composition wherein an enzyme is covalently bonded to an inorganic support material whereby maximum activity of the insoluble enzyme composition is achieved with the lowest possible amount of enzyme comprising the steps of: (a') contacting at least 2 different inorganic support materials capable of covalently bonding the enzyme, each having a different most frequent pore-diameter, each with at least two different solutions of the enzyme, each having a different enzyme content to form a water-insoluble enzyme composition; (b') determining the enzymatic activity per weight unit of the enzyme compositions obtained in step (a'); (c') comparing enzymatic activities of the enzyme compositions determined in step (b') and determining the inorganic support material having the most frequent pore-diameter that yields the enzyme composition having the highest enzymatic activity for the at least two different solutions of enzyme; (d') contacting the inorganic support material having the most frequent pore-diameter determined in step (c') with a plurality of solutions containing different amounts of the enzyme to form a plurality of water-insoluble enzyme compositions; (e') determining the specific activity of each of the plurality of enzyme compositions obtained in step (d'); (f') comparing the specific activity of each water-insoluble enzyme composition determined in step (e') with the specific activity of the enzyme in the free state contained in each of said plurality of enzyme solutions to determine the relative activity of each water-insoluble enzyme composition; (g') determining from the different amounts of enzyme in the enzyme solutions the amount which yields a water-insoluble enzyme composition having a relative activity of substantially 100%; (h') contacting the inorganic support material having the most frequent pore-diameter as determined in step (c') with a solution containing the amount of enzyme as determined in step (g') to form a water-insoluble enzyme composition; and (i') separating the water-insoluble enzyme composition from the remaining solution.

Claim 29

A process of producing a water-insoluble enzyme composition wherein an enzyme is covalently bonded to an inorganic support material whereby maximum activity of the insoluble enzyme composition is achieved with the lowest possible amount of enzyme comprising the steps of: (a') contacting at least 2 different inorganic support materials capable of covalently bonding the enzyme, each having a different most frequent pore-diameter, each with at least two different solutions of the enzyme, each having a different enzyme content to form a water-insoluble enzyme composition; (b') determining the enzymatic activity per weight unit of the enzyme compositions obtained in step (a'); (c') comparing enzymatic activities of the enzyme compositions determined in step (b') and determining the inorganic support material having the most frequent pore-diameter that yields the enzyme composition having the highest enzymatic activity for the at least two different solutions of enzyme; (d') contacting the inorganic support material having the most frequent pore-diameter determined in step (c') with a plurality of solutions containing different amounts of the enzyme to form a plurality of water-insoluble enzyme compositions; (e') determining the specific activity of each of the plurality of enzyme compositions obtained in step (d'); (f') comparing the specific activity of each water-insoluble enzyme composition determined in step (e') with the specific activity of the enzyme in the free state contained in each of said plurality of enzyme solutions to determine the relative activity of each water-insoluble enzyme composition; (g') determining from the different amounts of enzyme in the enzyme solutions the amount which yields a water-insoluble enzyme composition having a relative activity of substantially 100%; (h') contacting the inorganic support material having the most frequent pore-diameter as determined in step (c') with a solution containing the amount of enzyme as determined in step (g') to form a water-insoluble enzyme composition; and (i') separating the water-insoluble enzyme composition from the remaining solution.