Process for fluidized bed granulation of amino acid-containing fermentation broths

Patent metadata

Field	Value
Publication number	US-9649609-B2
Application number	US-201514678408-A
Country	US
Kind code	B2
Filing date	Apr 3, 2015
Priority date	Apr 7, 2014
Publication date	May 16, 2017
Grant date	May 16, 2017

Abstract

Process for fluidized bed granulation of amino acid-containing fermentation broths comprising the steps
Introduction of a drying gas with a temperature of 100° C.-450° C. into the fluidized bed granulation chamber Spraying of the amino acid-containing fermentation broth into the fluidized bed granulation chamber Discharge of the granules granulated in the fluidized bed granulation chamber with the drying gas stream, and drying of the discharged granules in a fluidized bed drying step,

wherein the discharged granulated granules are a granule mixture with various particle sizes and contains an oversize fraction, wherein the oversize comprises the particle sizes which lie above a desired particle size, an wherein the oversize fraction is removed from the discharged granule mixture and then comminuted and the comminuted oversize and the granule mixture from which the oversize was separated are fed into the fluidized bed drying step.

First claim

The invention claimed is:

1. Process for fluidized bed granulation of amino acid-containing fermentation broths comprising the steps
Introduction of a drying gas with a temperature of 100° C.-450° C. into the fluidized bed granulation chamber
Spraying of the amino acid-containing fermentation broth into the fluidized bed granulation chamber
Discharge of the granules granulated in the fluidized bed granulation chamber with the drying gas stream, and
drying of the discharged granules in a fluidized bed drying step,
wherein the discharged granulated granules are a granule mixture with various particle sizes and contains an oversize fraction and wherein the oversize comprises the particle sizes which lie above a desired particle size, wherein the oversize fraction is removed from the discharged granule mixture and then comminuted and wherein the comminuted oversize and the granule mixture from which the oversize was separated, are fed into the fluidized bed drying step.

2. Process according to claim 1 , wherein the fluidized bed drying has at least one drying zone and at least one cooling zone and wherein the drying gas stream in the drying zone has a temperature of 80 to 350° C. and the cooling gas stream in the cooling zone has a temperature of 35 to 0° C.

3. Process according to claim 1 , wherein the amino acid-containing fermentation broths contain >0% to 100% of the biomass formed during the fermentation and that the amino acid is selected from the group consisting of L-lysine, L-valine, L-methionine, L-tryptophan and L-threonine.

4. Process according to claim 1 , wherein the separation of the oversize is effected by sieving.

5. Process according to claim 1 , wherein the oversize comprises particle sizes>900 μm.

6. Process according to claim 1 , wherein the oversize comprises particle sizes>1800 μm.

7. Process according to claim 1 , wherein the comminution of the oversize is effected with a roller mill.

8. Process according to claim 1 , wherein at least 20 wt. % of the comminuted oversize has a particle size>100 μm.

9. Process according to claim 1 , wherein the content of the granule mixture with a particle size<100 μm is discharged from the fluidized bed drying with the fluidized bed gas.

10. Process according to claim 1 , wherein the content of the granule mixture with a particle size<100 μm is recycled into the fluidized bed granulation.

Assignees

• Evonik Industries Ag
• Evonik Degussa Gmbh

Inventors

• Alt Hans Christian
• Oelmann Ansgar
• Höfler Andreas
• Becker Franz Ulrich
• Blümke Wilfried

Classifications

• B01J2/16 Primary

  by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain · CPC title

• A23K20/142

  Amino acids; Derivatives thereof · CPC title

• A23K10/12

  by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass · CPC title

• A23K40/10

  by agglomeration; by granulation, e.g. making powders · CPC title