Powders and granules and process for making such powders and granules

Patent metadata

Field	Value
Publication number	US-11028350-B2
Application number	US-201716309339-A
Country	US
Kind code	B2
Filing date	Jun 1, 2017
Priority date	Jun 20, 2016
Publication date	Jun 8, 2021
Grant date	Jun 8, 2021

Abstract

Process for making a powder or granule containing at least one chelating agent selected from alkali metal salts of methyl glycine diacetic acid (MGDA) and glutamic acid diacetate (GLDA) and iminodisuccinic acid (IDS), said process comprising the steps of (a) introducing an aqueous solution or aqueous slurry of the respective chelating agent (A) into a spray-dryer or spray-granulator, and removing most of said water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250° C., (b) withdrawingpowder or granules, respectively, from the spray-dryer or spray-granulator, respectively, (c) separating off fines from said powder or granules, wherein said fines have a maximum particle diameter of 350 μm, (d) separating off lumps from said powder or granules, wherein said lumps have a particle diameter of 1,500 μm or more, (e) milling said lumps to a maximum particle diameter of 500 μm, (f) re-introducing said fines from step (c) and milled lumps from step (e) into the spray-dryer or spray-granulator, wherein the share of fines is in the range of from 0.5 to 20% by weight of the total chelating agent (A) withdrawn in step (b) and the share of milled lumps is in the range of from 5 to 60% by weight of the total chelating agent (A) withdrawn in step (b).

First claim

The invention claimed is:

1. A process for making a powder or granule comprising at least one chelating agent selected from the group consisting of an alkali metal salt of methyl glycine diacetic acid (MGDA), an alkali metal salt of glutamic acid diacetate (GLDA), and an alkali metal salt of iminodisuccinic acid (IDS), wherein the alkali metal salt has a formula selected from the group consisting of formula (I a), (I b) and (I c):
[CH 3 —CH(COO)—N(CH 2 —COO) 2 ]M 3-x H x   (I a)

wherein in formula (I a), M is, independently at each occurrence, an alkali metal cation, and x is from zero to 1.0,
[OOC—CH 2 CH 2 C—CH(COO)—N(CH 2 —COO) 2 ]M 4-x H x   (I b)

wherein in formula (I b), M is, independently at each occurrence, an alkali metal cation, and x is from zero to 2.0,
[H—N—(CH(COO)—CH 2 COO) 2 ]M 4-x H x   (I c)

wherein in formula (I c), M is, independently at each occurrence, an alkali metal cation, and x is from zero to 2.0,
the process comprising:
(a) introducing an aqueous solution or aqueous slurry of the chelating agent into a spray-dryer or spray-granulator, and removing most of the water by spray-drying or spray granulation using a gas with an inlet temperature of 125 to 250° C.,
(b) withdrawing powder or granules, from the spray-dryer or spray-granulator,
(c) separating off fines from the powder or granules, wherein the fines have a maximum particle diameter of 30 μm in the case of powders and a maximum particle diameter of 350 μm in the case of granules,
(d) separating off lumps from the powder or granules, wherein the lumps have a particle diameter of 250 μm in the case of powders and 1,000 μm or more in the case of granules, respectively,
(e) milling the lumps to a maximum particle diameter of 500 μm in the case of granules or to 40 μm in the case of powders, and
(f) re-introducing the fines from (c) and milled lumps from (e) into the spray-dryer or spray-granulator,

wherein the amount of fines is in a range of from 4 to 18% by total weight of the chelating agent withdrawn in (b), and the amount of milled lumps from (e) is in a range of from 20 to 40% by total weight of the chelating agent withdrawn in (b).

2. The process according to claim 1 , wherein in (c) a range of from 80 to 99% by weight of the fines is separated off.

3. The process according to claim 1 , wherein the aqueous solution or slurry in (a) comprises at least one (co)polymer (B) selected from the group consisting of homo- and copolymers of (meth)acrylic acid and polyalkylenimines that may be polyalkoyxylated or substituted with carboxymethyl groups.

4. The process according to claim 3 , wherein the powder or granule comprises in a range of from 80 to 99.9% by weight of the chelating agent and 0.1 to 20% by weight of the (co)polymer (B), wherein percentages refer to a solids content of the powder or granule.

5. The process according to claim 1 , wherein the chelating agent is at least one selected from the group consisting of the trisodium salt of MGDA and the tetrasodium salt of GLDA.

6. The process according to claim 3 , wherein the (co)polymer (B) is a per-sodium salt of polyacrylic acid.

7. The process according to claim 3 , wherein the (co)polymer (B) is a polyethylenimine that may be polyethoxylated.

8. The process according to claim 3 , wherein the (co)polymer (B) has an average molecular weight M w in a range of from 1,200 to 30,000 g/mol, determined by gel permeation chromatography and referring to the respective free acid.

Assignees

• Basf Se

Inventors

• Mueller Michael Klemens
• Stamm Armin
• Jaekel Frank
• Sueling Carsten

Classifications

• C11D11/0082 Primary

  one or more of the detergent ingredients being in a liquefied state, e.g. slurry, paste or melt, and the process resulting in solid detergent particles such as granules, powders or beads · CPC title

• C07C229/16

  to carbon atoms of hydrocarbon radicals substituted by amino or carboxyl groups, e.g. ethylenediamine-tetra-acetic acid, iminodiacetic acids · CPC title

• C07C227/00

  Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton · CPC title

• C11D11/00

  Special methods for preparing compositions containing mixtures of detergents · CPC title

• C11D11/02

  Preparation in the form of powder by spray drying · CPC title