Device for producing spray-dried agglomerates

Patent metadata

Field	Value
Publication number	US-11235259-B2
Application number	US-201615164294-A
Country	US
Kind code	B2
Filing date	May 25, 2016
Priority date	May 29, 2015
Publication date	Feb 1, 2022
Grant date	Feb 1, 2022

Abstract

The invention is in the field of devices for producing particles, in particular large agglomerate particles.

First claim

The invention claimed is:

1. A device for the spray-drying agglomeration of particles, comprising
(1) a chamber containing
(i) in an upper region of the chamber a spray drying segment (A) in which a feed liquid atomizer (Z 1 ) is placed and an inlet at the top of the spray drying segment (A) for spraying a slurry; and
(ii) in a lower region of the chamber an integrated fluidized bed (B), said integrated fluidized bed (B) containing
(a) a nozzle or atomizer construction (Z 2 ) for spraying a binder liquid,
(b) an outlet port (H) located at the bottom of a side wall of the integrated fluidized bed (B) and
(c) a dam construction (G) located between the outlet port (H) and a zigzag classifier (P) for regulating the product amount,

(2) the zigzag classifier (P) connected to the dam construction (G) and located outside of the lower region of the chamber, and
(3) an external pathway connecting the zigzag classifier (P) and the inlet at the top of the spray drying segment (A) for returning fine dust.

2. The device of claim 1 , wherein the nozzle or atomizer construction (Z 2 ) in the internal fluidized bed (B) consists of a ring line, the nozzles or atomizers being evenly spaced along the ring line.

3. The device of claim 1 , wherein the nozzle or atomizer construction (Z 2 ) comprises at least 3 nozzles or atomizers.

4. The device of claim 3 , wherein the nozzle or atomizer construction (Z 2 ) comprises at least 4 nozzles or atomizers.

5. The device of claim 1 , wherein the binder liquid from the nozzle or atomizer construction (Z 2 ) in the internal fluidized bed is sprayed from the bottom to the top.

6. The device of claim 1 , wherein the nozzles or atomizers in the nozzle or atomizer construction (Z 2 ) are pressure-spray nozzles.

7. The device of claim 1 , wherein the nozzles or atomizers in the nozzle or atomizer construction (Z 2 ) are a twin-fluid spray nozzle.

8. The device of claim 1 , wherein the input temperature at the feed atomizer is between 100° C. to 220° C. and the output temperature at the zigzag classifier (P) is from 20° C. to 100° C., with the slurry throughput being within the range of 300 to 1200 kg/hour, and being atomized at 30 to 200 bar.

9. The device of claim 1 , wherein the temperature in the fluidized bed during agglomeration is between 5-90° C.

10. The device of claim 1 wherein the obtained spray-drying agglomeration of particles have a dust value of under 2.

11. The device of claim 1 wherein the obtained spray-drying agglomeration of particles have a particle size of larger than 600 μm.

12. The device of claim 1 wherein the fine dust is returned to the headspace of the spray drying segment (A).

Assignees

• Symrise Ag

Inventors

• Balde Alexander
• Diring Alexander
• Gruber Eric
• Hoffmann Marc
• Silbernagel Alexander
• Vorrat Viktor
• Weiβbrodt Jenny

Classifications

• B01D1/18 Primary

  to obtain dry solids (B01D1/24 takes precedence) · CPC title

• A23V2002/00

  Food compositions, function of food ingredients or processes for food or foodstuffs · CPC title

• B01D1/20

  Sprayers (in general B05B) · CPC title

• A23P10/22

  Agglomeration or granulation with pulverisation of solid particles, e.g. in a free-falling curtain · CPC title

• A23P10/40

  free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added (A23P10/20, A23P10/30 take precedence) · CPC title