Drying co-mingled carbohydrate solution and recycled product by dielectric heating

Claim 2

A process for drying a carbohydrate solution to form a stable, solid, substantially anhydrous particulate product therefrom comprising: (a) co-mingling said carbohydrate solution with recycled dry product solid to form a particulate admixture dryable in a dielectrically heated drying zone; (b) drying said particulate admixture in said dielectrically heated drying zone at a particle temperature below the melting point of said particulate admixture to form said stable, solid, substantially anhydrous product; (c) removing said stable, solid, substantially anhydrous product from the drying zone and dividing it into a first portion and a second portion; (d) recycling said first portion; and (e) recovering said second portion.

Claim 3

The process of claim 1 in which the carbohydrate is fructose.

Claim 4

A process for drying a carbohydrate solution to form a stable, solid, substantially anhydrous particulate product therefrom comprising: (a) co-mingling said carbohydrate solution with about 5 to 20 parts of recycled dry product solids per part of solids in said solution in a co-mingling zone to form a particulate admixture dryable in a dielectrically heated drying zone and having a water content of not more than about 4% by weight; (b) drying said particulate admixture at a particle temperature below the melting point of said particulate admixture, in a gas stream in said dielectrically heated drying zone to form said stable, solid, substantially anhydrous product; (c) discharging said stable, solid, substantially anhydrous product from the drying zone and dividing it into a first portion and a second portion; (d) recycling said first portion to the co-mingling zone; and (e) recovering said second portion.

Claim 5

A process for drying a carbohydrate solution to form a stable, solid, substantially anhydrous particulate product therefrom comprising: (a) co-mingling said carbohydrate solution with about 5 to 20 parts of recycled dry product solids per part of solids in said solution in a co-mingling zone to form a particulate admixture dryable in a dielectrically heated drying zone and having a water content of not more than about 4% by weight; (b) drying said particulate admixture at a particle temperature below the melting point of said particulate admixture, in a gas stream in said dielectrically heated drying zone to form said stable, solid, substantially anhydrous product; (c) discharging said stable, solid, substantially anhydrous product from the drying zone and dividing it into a first portion and a second portion; (d) recycling said first portion to the co-mingling zone; and (e) recovering said second portion.

Claim 6

The process of claim 3 in which the carbohydrate is fructose.

Claim 7

The process of claim 3 in which the gas stream has a temperature and a flow rate effective for maintaining the temperature of solid particles within the dielectrically heated drying zone below their melting point.

Claim 8

The process of claim 3 in which the particle size of the particles of said first portion is adjusted to about 50-500 microns before they are recycled to the co-mingling zone.

Claim 9

The process of claim 3 in which the dielectrically heated zone for drying the particulate admixture comprises an elongated enclosed waveguide having a low loss gas-porous membrane dividing said waveguide into two portions, means for directing a fluidizing gas into the bottom portion of said waveguide through said membrane, so as to establish a fluidized bed with said particulate admixture and a dielectric energy source adapted to propagate dielectric energy through said waveguide.

Claim 10

The process of claim 3 in which the dielectrically heated drying zone is a fluidized bed operating under reduced pressure.

Claim 11

The process of claim 3 in which the co-mingled carbohydrate solution and recycled product solids is belt-conveyed under vacuum through (i) the dielectrically heated drying zone, and (ii) a cooling zone before discharging.

Claim 12

The process of any one of claims 3, 5, 6, 7 or 8 in which the carbohydrate solution comprises water and at least one member selected from the group consisting of fructose, dextrose, sucrose, total sugars from sugar cane, total sugars from sugar beets, sugar cane molasses and sugar beet molasses.

Claim 13

A process for drying a carbohydrate solution to form a stable, solid, substantially anhydrous particulate product therefrom comprising: (a) co-mingling, in a co-mingling zone, said carbohydrate solution with an amount of recycled dry product solids effective for forming a particulate admixture dryable in a dielectrically heated drying zone and having a water content of not more than about 4% by weight; (b) drying said particulate admixture in a gas stream in said dielectrically heated drying zone to form said stable, solid, substantially anhydrous product; (c) discharging said stable, solid, substantially anhydrous product from the drying zone and dividing it into a first portion and a second portion; (d) recycling said first portion to the co-mingling zone; and (e) recovering said second portion.

Claim 14

A process for drying a carbohydrate solution to form a stable, solid, substantially anhydrous particulate product therefrom comprising: (a) co-mingling, in a co-mingling zone, said carbohydrate solution with an amount of recycled dry product solids effective for forming a particulate admixture dryable in a dielectrically heated drying zone and having a water content of not more than about 4% by weight; (b) drying said particulate admixture in a gas stream in said dielectrically heated drying zone to form said stable, solid, substantially anhydrous product; (c) discharging said stable, solid, substantially anhydrous product from the drying zone and dividing it into a first portion and a second portion; (d) recycling said first portion to the co-mingling zone; and (e) recovering said second portion.

Claim 15

The process of claim 11 in which the carbohydrate is fructose.

Claim 16

The process of any one of claims 1, 3 or 11 in which the stable, solid, substantially anhydrous particulate product is free-flowing.