Production of crystalline sugar

Claim 2

A process for the crystallisation of sugar from a supersaturated sugar syrup, in which the syrup is subjected in a nucleation zone to a shear force having a velocity gradient of at least 5000 cm/sec/cm to induce catastrophic homogeneous nucleation of sugar, the syrup is discharged from said nucleation zone before substantial crystallization has taken place, and the syrup is thereafter crystallised to produce crystalline sugar.

Claim 3

A process as claimed in claim 1, wherein said velocity gradient is at least 10,000 cm/sec/cm.

Claim 4

A process as claimed in claim 1, wherein the velocity gradient is at least 20,000 cm/sec/cm.

Claim 5

A process as claimed in claim 1, wherein the shear force is applied by a colloid mill.

Claim 6

A process as claimed in claim 4, wherein said velocity gradient is at least 20,000 cm/sec/cm.

Claim 7

A process as claimed in claim 1, wherein the shear force is applied by means of a homogeniser.

Claim 8

A process as claimed in claim 6, wherein the shear force has a velocity gradient of at least 20,000 cm/sec/cm.

Claim 9

A process for the crystallisation of sugar from a supersaturated sugar syrup, in which the syrup is subjected, in high shear equipment, to a shear force having a velocity gradient of at least 5000 cm/sec/cm to induce catastrophic homogeneous necleation of sugar and the syrup is immediately thereafter discharged from the equipment before substantial crystallization has taken place and allowed to crystallise.

Claim 10

A process for the crystallisation of sugar from a supersaturated sugar syrup, in which the syrup is subjected, in high shear equipment, to a shear force having a velocity gradient of at least 5000 cm/sec/cm to induce catastrophic homogeneous necleation of sugar and the syrup is immediately thereafter discharged from the equipment before substantial crystallization has taken place and allowed to crystallise.

Claim 11

A process as claimed in claim 8, wherein the nucleated syrup is discharged from the equipment onto a moving belt conveyor.

Claim 12

A process as claimed in claim 8, wherein the velocity gradient is at least 20,000 cm/sec/cm.

Claim 13

A process as claimed in claim 8, wherein the syrup contains less than 15% by weight impurities.

Claim 14

A process as claimed in claim 8, wherein the supersaturated sugar syrup has a temperature of at least 123°C and a sugar concentration of at least 90°Bx.

Claim 15

A process as claimed in claim 8, wherein the residence time of said sugar syrup in said high shear equipment is less than about 1 second.

Claim 16

A process for the crystallization of sugar from a supersaturated sugar syrup, in which the syrup is passed through a colloid mill to induce catastrophic homogeneous nucleation of sugar, the syrup is discharged from the mill before substantial crystallization has taken place and the syrup is thereafter crystallized to produce crystalline sugar.

Claim 17

A process for the crystallization of sugar from a supersaturated sugar syrup, in which the syrup is passed through a colloid mill to induce catastrophic homogeneous nucleation of sugar, the syrup is discharged from the mill before substantial crystallization has taken place and the syrup is thereafter crystallized to produce crystalline sugar.

Claim 18

In a process for the refining of sugar, the steps of: concentrating a non-concentrated sugar solution to form a supersaturated sugar syrup; subjecting in a nucleation zone the supersaturated sugar syrup to a shear force having a velocity gradient of at least 5000 cm/sec/cm to induce catastrophic homogeneous nucleation of sugar; discharging the syrup from said zone before substantial crystallization has taken place; and thereafter crystallizing the sugar from the nucleated syrup.

Claim 19

In a process for the refining of sugar, the steps of: concentrating a non-concentrated sugar solution to form a supersaturated sugar syrup; subjecting in a nucleation zone the supersaturated sugar syrup to a shear force having a velocity gradient of at least 5000 cm/sec/cm to induce catastrophic homogeneous nucleation of sugar; discharging the syrup from said zone before substantial crystallization has taken place; and thereafter crystallizing the sugar from the nucleated syrup.

Claim 20

A process as claimed in claim 1 wherein the residence time of said sugar syrup in said nucleation zone is less than about one second.

Claim 21

A process as claimed in claim 4 wherein the residence time in said nucleation zone is from 0.05 to 0.5 second.

Claim 22

A process as claimed in claim 6 wherein the residence time in said nucleation zone is from 0.0001 to 0.001 second.

Claim 23

A process as claimed in claim 14 wherein the residence time of said sugar syrup in said colloid mill is from 0.05 to 0.5 second.

Claim 24

A process as claimed in claim 15 wherein the residence time of said sugar syrup in said nucleation zone is less than about one second.