Process for controlling the rate of growth of particulate masses

Claim 2

A process for controlling the rate of growth of a particulate mass within a zone which contains a liquid medium within which is charged a material suitable for sustaining, and increasing the rate of growth of said particulate mass comprising withdrawing liquid from said zone, and splitting same into two separate streams for determining the total concentration of particulates therein, (a) a first stream wherein the liquid is separated from the particulates and directly analyzed to determine the amount of solids contained therein, (b) a second stream wherein the size of the particulates is measured, and determination made of the number of particles contained in a unit of volume of the liquid, and having directly determined the rate of change in the total concentration of particulates within the liquid, controlling other process variables to establish the desired rate of change of total particulate concentration, and then discharging the contents from the zone when said zone contains the desired amount of particulates.

Claim 3

In a process for the operation of a vacuum pan by controlling the rate of growth of sucrose crystals in a supersaturated syrup, or massecuite, containing nuclei or granules of sucrose crystals, wherein charges of syrup are fed into the vacuum pan and water evaporated therefrom at reduced temperature and pressure, the improvement comprising withdrawing syrup, or massecuite, from the vacuum pan, and splitting same into two separate streams for determining the total concentration of sucrose within the syrup, or massecuite, (a) a first stream wherein the mother liquor is separated from the sucrose crystals and directly analyzed to determine the amount of sucrose dissolved therein, (b) a second stream wherein the size of the crystals of sucrose is measured, and determination made of the number of crystals contained in a unit of volume of the syrup, or massecuite, and having directly determined the rate of change in the total concentration of sucrose within the syrup, or massecuite, controlling temperature or pressure, or both, to establish the desired rate of change of total sucrose concentration, and then discharging the contents of the pan when the pan has been filled with massecuite.

Claim 4

In a process for the operation of a vacuum pan by controlling the rate of growth of sucrose crystals in a supersaturated syrup, or massecuite, containing nuclei or granules of sucrose crystals, wherein charges of syrup are fed into the vacuum pan and water evaporated therefrom at reduced temperature and pressure, the improvement comprising withdrawing syrup, or massecuite, from the vacuum pan, and splitting same into two separate streams for determining the total concentration of sucrose within the syrup, or massecuite, (a) a first stream wherein the mother liquor is separated from the sucrose crystals and directly analyzed to determine the amount of sucrose dissolved therein, (b) a second stream wherein the size of the crystals of sucrose is measured, and determination made of the number of crystals contained in a unit of volume of the syrup, or massecuite, and having directly determined the rate of change in the total concentration of sucrose within the syrup, or massecuite, controlling temperature or pressure, or both, to establish the desired rate of change of total sucrose concentration, and then discharging the contents of the pan when the pan has been filled with massecuite.

Claim 5

The process of claim 2 wherein the syrup, or massecuite, is withdrawn from the vacuum pan and split into two separate streams for analysis of the total sucrose concentration, (a) a first stream wherein the mother liquor is separated from the sucrose crystals and directly analyzed to determine the amount of sucrose dissolved therein, (b) a second stream wherein the size of the crystals of sucrose is measured, and determination made of the number of crystals contained in a unit of volume of the syrup, or massecuite.

Claim 6

The process of claim 3 wherein, in the analysis of said first stream, the concentration of sucrose contained in the mother liquor is determined by use of a polarimeter.

Claim 7

The process of claim 3 wherein, in the analysis of said first stream, the concentration of sucrose contained in the mother liquor is determined by use of a polarimeter, and the polarimeter reading is corrected for error caused by impurities in the syrup, or massecuite.

Claim 8

The process of claim 5 wherein, in the analysis of said first stream, the amount of impurities in the mother liquor is determined by means of a densitometer, the polarimeter reading being taken in connection with said densiometer reading to make the determination feasible.

Claim 9

The process of claim 6 wherein the polarimeter and densitometer are connected in series.

Claim 10

The process of claim 3 wherein, in the analysis of said second stream, an electronic counter is used to measure the number of crystals of sucrose per unit volume, and to measure sucrose crystal size.

Claim 11

The process of claim 8 wherein, in the analysis of said second stream, the second stream is diluted with mother liquor from said first stream in known amount in the determination of sucrose crystal count.

Claim 12

The process of claim 3 wherein, in the analysis of said second stream, an electronic counter is used to measure the number and size of the sucrose crystals, the liquid fed into the electronic counter for analysis having been diluted in predetermined known concentration in a dilution device.

Claim 13

In a process for the operation of a vacuum pan by controlling the rate of growth of sucrose crystals in a supersaturated syrup, or massecuite, containing nuclei or granules of sucrose crystals, wherein charges of syrup are fed into the vacuum pan and water evaporated therefrom at reduced temperature and pressure, the improvement comprising withdrawing syrup, or massecuite, from the vacuum pan and splitting the withdrawn syrup, or massecuite, into two separate streams for analysis of the total sucrose concentration contained in said syrup, or massecuite, (i) a first stream wherein the mother liquor is separated from the sucrose crystals and directly analyzed via use of both a polarimeter and densitometer to determine the amount of sucrose dissolved therein, (ii) a second stream which is directly analyzed via use of a counter to determine the number of sucrose crystals contained in a unit of volume of the syrup, or massecuite, and the size of the sucrose crystals, and having determined the total concentration of sucrose in said syrup, or massecuite, relating the total concentration of sucrose in said syrup, or massecuite, to set the temperature or pressure, or both, to obtain with consistency a full pan of sucrose at the time the pan is struck.

Claim 14

In a process for the operation of a vacuum pan by controlling the rate of growth of sucrose crystals in a supersaturated syrup, or massecuite, containing nuclei or granules of sucrose crystals, wherein charges of syrup are fed into the vacuum pan and water evaporated therefrom at reduced temperature and pressure, the improvement comprising withdrawing syrup, or massecuite, from the vacuum pan and splitting the withdrawn syrup, or massecuite, into two separate streams for analysis of the total sucrose concentration contained in said syrup, or massecuite, (i) a first stream wherein the mother liquor is separated from the sucrose crystals and directly analyzed via use of both a polarimeter and densitometer to determine the amount of sucrose dissolved therein, (ii) a second stream which is directly analyzed via use of a counter to determine the number of sucrose crystals contained in a unit of volume of the syrup, or massecuite, and the size of the sucrose crystals, and having determined the total concentration of sucrose in said syrup, or massecuite, relating the total concentration of sucrose in said syrup, or massecuite, to set the temperature or pressure, or both, to obtain with consistency a full pan of sucrose at the time the pan is struck.