WO2018011027A1 - Process for manufacturing of mgda and glda containing granules, the granules and their use - Google Patents

Process for manufacturing of mgda and glda containing granules, the granules and their use Download PDF

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Publication number
WO2018011027A1
WO2018011027A1 PCT/EP2017/066705 EP2017066705W WO2018011027A1 WO 2018011027 A1 WO2018011027 A1 WO 2018011027A1 EP 2017066705 W EP2017066705 W EP 2017066705W WO 2018011027 A1 WO2018011027 A1 WO 2018011027A1
Authority
WO
WIPO (PCT)
Prior art keywords
range
alkali metal
acid
granule
glda
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/EP2017/066705
Other languages
English (en)
French (fr)
Inventor
Marta Reinoso Garcia
Michael Klemens Mueller
Carsten Sueling
Verena MORMUL
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Priority to CN201780042857.1A priority Critical patent/CN109415663A/zh
Priority to BR112018077082-5A priority patent/BR112018077082B1/pt
Priority to RU2019104062A priority patent/RU2744632C2/ru
Priority to MX2019000662A priority patent/MX2019000662A/es
Priority to EP17735138.4A priority patent/EP3484988B1/en
Priority to JP2019501998A priority patent/JP6878564B2/ja
Priority to US16/316,266 priority patent/US10865362B2/en
Publication of WO2018011027A1 publication Critical patent/WO2018011027A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/0047—Detergents in the form of bars or tablets
    • C11D17/0065—Solid detergents containing builders
    • C11D17/0073—Tablets
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/36—Racemisation of optical isomers
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00—Special methods for preparing compositions containing mixtures of detergents
    • C11D11/02—Preparation in the form of powder by spray drying
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00—Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/06—Powder; Flakes; Free-flowing mixtures; Sheets
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16—Organic compounds
    • C11D3/26—Organic compounds containing nitrogen
    • C11D3/33—Amino carboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/22—Organic compounds
    • C11D7/32—Organic compounds containing nitrogen
    • C11D7/3245—Aminoacids

Definitions

  • Step (a2.1 ) can be started by adding the solution resulting from step (a.1 ) to an aqueous solution of alkali metal hydroxide or adding an aqueous solution of alkali metal hydroxide to a solution resulting from step (a.1 ).
  • the solution resulting from step (a.1 ) and an aqueous solution of alkali metal hydroxide are added simultaneously to a vessel.
  • step (a2.2) is carried out with an excess of base of 1 .01 to 1.2 moles of hydroxide per mole of nitrile group.
  • the second spray dryer is charged with a fluidized bed with solid from the first spray dryer, and aqueous solution obtained according to step (a) is sprayed onto or into the fluidized bed, together with a hot gas inlet stream.
  • the hot gas inlet stream may have a temperature in the range of from 125 to 350°C, preferably 160 to 220°C.
  • step (b) examples of additional optional steps during step (b) are removal of fines, removal of particles that are too big, so called “overs”, recycling of fines, and milling down and recycling of such milled down overs.
  • fines may be defined as particles with a maximum diameter of 150 ⁇ or less and generated during step (b), for example 1 to 150 ⁇ .
  • overs or lumps may have a minimum diameter of 1 mm or more, for example 1 mm up to 5 mm.
  • Such lumps may be removed from the spray granulator and milled down to a maximum particle diameter of 500 ⁇ , preferably to a maximum particle diameter of 400 ⁇ .
  • the milling may be performed in any type of mills.
  • alkoxylated alcohols are, for example, compounds of the general formula (IV) in which the variables are defined as follows: is identical or different and selected from hydrogen and linear Ci-Co-alkyl, preferably iden tical in each case and ethyl and particularly preferably hydrogen or methyl,
  • EO is ethylene oxide, CH 2 CH 2 -0,
  • Suitable hydrophobic monomers are, for example, isobutene, diisobutene, butene, pentene, hexene and styrene, olefins with 10 or more carbon atoms or mixtures thereof, such as, for example, 1-decene, 1-dodecene, 1 -tetradecene, 1 -hexadecene, 1 -octadecene, 1-eicosene, 1 - docosene, 1 -tetracosene and 1 -hexacosene, C22-a-olefin, a mixture of C2o-C24-a-olefins and polyisobutene having on average 12 to 100 carbon atoms per molecule.
  • poly(propylene oxide-co-ethylene oxide) (meth)acrylate and ethoxypoly(propylene oxide-co-ethylene oxide) (meth)acrylate.
  • Polyalkylene glycols here may comprise 3 to 50, in particular 5 to 40 and especially 10 to 30 alkylene oxide units per molecule.
  • Particularly preferred sulfonic-acid-group-containing monomers here are 1-acrylamido-
  • inventive solid detergent compositions for hard surface cleaning and inventive solid laundry detergent compositions are free from heavy metals apart from zinc compounds.
  • this may be understood as meaning that detergent compositions for cleaners and laundry detergent compositions according to the invention are free from those heavy metal compounds which do not act as bleach catalysts, in particular of compounds of iron and of bismuth.
  • "free from” in connection with heavy metal compounds is to be understood as meaning that the content of heavy metal compounds which do not act as bleach catalysts is in sum in the range from 0 to 100 ppm, determined by the leach method and based on the solids content.
  • formulation according to the invention has, apart from zinc, a heavy metal content below 0.05 ppm, based on the solids content of the formulation in question. The fraction of zinc is thus not included.
  • the hygroscopicity was determined by storing at 25°C and 50% relative humidity over a period of 24 hours. In the alternative, so-called tropic conditions are storing at 35°C and 70 to 90% relative humidity over a period of 24 hours. Grade: from zero (free flowing granule/powder) to 4 (granule/powder has dissolved)
  • the hot saponification was performed at 180 °C and 24 bar in a tubular plug flow reactor at 30 min retention time.
  • the solution obtained under steady state conditions was treated in a stirred reactor at 970 mbar at 97 °C. Then it is stripped in a wiped film evaporator at 1 10 °C and 900 mbar to further evaporate ammonia. Then, the concentration of total complexing agent (A.1 ) was adjusted to approximately 40 wt% (based on iron binding capacity).
  • Tablets were formed from inventive granule with a tablet press, make: Korsch XP1. The following conditions were applied:

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Detergent Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
PCT/EP2017/066705 2016-07-15 2017-07-05 Process for manufacturing of mgda and glda containing granules, the granules and their use Ceased WO2018011027A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
CN201780042857.1A CN109415663A (zh) 2016-07-15 2017-07-05 制备含有mgda和glda的颗粒的方法、颗粒及其用途
BR112018077082-5A BR112018077082B1 (pt) 2016-07-15 2017-07-05 Processo para fabricação de grânulos de sais, grânulo, uso de um grânulo
RU2019104062A RU2744632C2 (ru) 2016-07-15 2017-07-05 Способ получения гранул, содержащих mgda и glda, гранулы и их применение
MX2019000662A MX2019000662A (es) 2016-07-15 2017-07-05 Proceso para la fabricacion de granulos que contienen mgda y glda, los granulos y su uso.
EP17735138.4A EP3484988B1 (en) 2016-07-15 2017-07-05 Process for manufacturing of mgda and glda containing granules, the granules and their use
JP2019501998A JP6878564B2 (ja) 2016-07-15 2017-07-05 顆粒の製造方法、及び顆粒とその使用方法
US16/316,266 US10865362B2 (en) 2016-07-15 2017-07-05 Process for manufacturing MGDA/GLDA granules, granules, and their use

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP16179707 2016-07-15
EP16179707.1 2016-07-15

Publications (1)

Publication Number Publication Date
WO2018011027A1 true WO2018011027A1 (en) 2018-01-18

Family

ID=56511340

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP2017/066705 Ceased WO2018011027A1 (en) 2016-07-15 2017-07-05 Process for manufacturing of mgda and glda containing granules, the granules and their use

Country Status (8)

Country Link
US (1) US10865362B2 (https=)
EP (1) EP3484988B1 (https=)
JP (1) JP6878564B2 (https=)
CN (1) CN109415663A (https=)
BR (1) BR112018077082B1 (https=)
MX (1) MX2019000662A (https=)
RU (1) RU2744632C2 (https=)
WO (1) WO2018011027A1 (https=)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019162130A1 (en) * 2018-02-23 2019-08-29 Unilever N.V. Shaped detergent product comprising aminopolycarboxylate
WO2020094480A1 (en) 2018-11-07 2020-05-14 Basf Se Process for manufacturing granules, and granules and their use
EP3822335A1 (en) * 2019-11-15 2021-05-19 Basf Se Cleaning compositions and their use
US20210317392A1 (en) * 2018-09-27 2021-10-14 Basf Se Process for making a granule or powder
US20220073842A1 (en) * 2018-12-21 2022-03-10 Nouryon Chemicals International B.V. Crumbly phase composition of methylglycine n,n diacetic acid
WO2022184551A1 (en) * 2021-03-04 2022-09-09 Basf Se Process for making a particulate coated organic salt, and particulate coated salt
US11932723B2 (en) 2018-12-28 2024-03-19 Daicel Corporation High-purity 3,4-epoxycyclohexylmethyl methacrylate

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA3069043A1 (en) * 2017-07-07 2019-01-10 Nouryon Chemicals International B.V. Sodium methyl glycine-n,n-diacetic acid compound, process to prepare it and use thereof
EP4073217B1 (en) 2019-12-11 2024-07-24 Basf Se Granules of mgda and (meth)acrylic acid homo- or co-polymer; process for making the same
WO2021170637A1 (en) * 2020-02-28 2021-09-02 Basf Se Automatic dishwashing composition comprising at least one imidazole-based compound
CN115916742B (zh) * 2020-06-19 2024-08-30 诺力昂化学品国际有限公司 使用甲基甘氨酸n,n二乙酸盐的易碎相组合物制备甲基甘氨酸n,n二乙酸盐共生颗粒的方法
CN112010769B (zh) * 2020-09-01 2023-01-31 河南清水源科技股份有限公司 一种绿色螯合剂甲基甘氨酸二乙酸钠盐的制备方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0851023A2 (en) 1996-12-23 1998-07-01 Unilever N.V. Machine dishwashing tablets containing a peracid
DE19819187A1 (de) 1998-04-30 1999-11-11 Henkel Kgaa Festes maschinelles Geschirrspülmittel mit Phosphat und kristallinen schichtförmigen Silikaten
WO2009103822A1 (en) 2008-04-01 2009-08-27 Unilever Nv Preparation of free flowing granules of methyglycine diacetic acid
WO2012168739A1 (en) 2011-06-09 2012-12-13 Pq Silicas Bv Builder granules and process for their preparation
WO2015036324A1 (en) 2013-09-13 2015-03-19 Basf Se Mixtures of enantiomers, and process for making such mixtures
WO2015121170A1 (en) * 2014-02-13 2015-08-20 Basf Se Powder and granule, process for making such powder and granule, and use thereof

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5200236A (en) * 1989-11-15 1993-04-06 Lever Brothers Company, Division Of Conopco, Inc. Method for wax encapsulating particles
EP2438042A1 (en) * 2009-06-05 2012-04-11 Akzo Nobel Chemicals International B.V. Process to prepare a chelating agent or precursor thereof using a cyanide salt
US8802894B2 (en) * 2011-04-04 2014-08-12 Basf Se Process for the preparation of aqueous solutions of methylglycine-N,N-diacetic acid trialkali metal salts
US8813268B1 (en) * 2011-09-05 2014-08-26 Outdoor Cap Company, Inc. Lighted headwear with recessed light source and lens
US20130284210A1 (en) * 2012-04-25 2013-10-31 Basf Se Solid formulations, their preparation and use
EP3194553A1 (en) * 2014-09-19 2017-07-26 Basf Se Detergent composition
EP3026100B1 (en) * 2014-11-26 2018-07-25 The Procter and Gamble Company Cleaning pouch
EP3224338B1 (en) * 2014-11-26 2019-04-17 Basf Se Aqueous solution containing combination of complexing agents

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0851023A2 (en) 1996-12-23 1998-07-01 Unilever N.V. Machine dishwashing tablets containing a peracid
DE19819187A1 (de) 1998-04-30 1999-11-11 Henkel Kgaa Festes maschinelles Geschirrspülmittel mit Phosphat und kristallinen schichtförmigen Silikaten
WO2009103822A1 (en) 2008-04-01 2009-08-27 Unilever Nv Preparation of free flowing granules of methyglycine diacetic acid
WO2012168739A1 (en) 2011-06-09 2012-12-13 Pq Silicas Bv Builder granules and process for their preparation
WO2015036324A1 (en) 2013-09-13 2015-03-19 Basf Se Mixtures of enantiomers, and process for making such mixtures
WO2015121170A1 (en) * 2014-02-13 2015-08-20 Basf Se Powder and granule, process for making such powder and granule, and use thereof

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019162130A1 (en) * 2018-02-23 2019-08-29 Unilever N.V. Shaped detergent product comprising aminopolycarboxylate
WO2019162133A1 (en) * 2018-02-23 2019-08-29 Unilever N.V. Shaped detergent product composition comprising aminopolycarboxylate
CN111788293A (zh) * 2018-02-23 2020-10-16 荷兰联合利华有限公司 包含氨基多羧酸盐和有机酸的洗涤剂固体组合物
US12134749B2 (en) 2018-02-23 2024-11-05 Conopco Inc. Shaped detergent product composition comprising aminopolycarboxylate
AU2019225946B2 (en) * 2018-02-23 2021-07-01 Unilever Global Ip Limited Shaped detergent product comprising aminopolycarboxylate
AU2019223671B2 (en) * 2018-02-23 2021-07-15 Unilever Global Ip Limited Detergent solid composition comprising aminopolycarboxylate and inorganic acid
US20210317392A1 (en) * 2018-09-27 2021-10-14 Basf Se Process for making a granule or powder
US12006487B2 (en) * 2018-09-27 2024-06-11 Basf Se Process for making a granule or powder
WO2020094480A1 (en) 2018-11-07 2020-05-14 Basf Se Process for manufacturing granules, and granules and their use
US12258541B2 (en) * 2018-12-21 2025-03-25 Nouryon Chemicals International B.V. Crumbly phase composition of methylglycine N,N diacetic acid
US20220073842A1 (en) * 2018-12-21 2022-03-10 Nouryon Chemicals International B.V. Crumbly phase composition of methylglycine n,n diacetic acid
US11932723B2 (en) 2018-12-28 2024-03-19 Daicel Corporation High-purity 3,4-epoxycyclohexylmethyl methacrylate
US20220403295A1 (en) * 2019-11-15 2022-12-22 Basf Se Cleaning compositions and their use
WO2021094182A1 (en) * 2019-11-15 2021-05-20 Basf Se Cleaning compositions and their use
EP3822335A1 (en) * 2019-11-15 2021-05-19 Basf Se Cleaning compositions and their use
WO2022184551A1 (en) * 2021-03-04 2022-09-09 Basf Se Process for making a particulate coated organic salt, and particulate coated salt

Also Published As

Publication number Publication date
JP2019525984A (ja) 2019-09-12
MX2019000662A (es) 2019-05-20
RU2019104062A (ru) 2020-08-17
BR112018077082A2 (pt) 2019-04-30
US20200181537A1 (en) 2020-06-11
RU2019104062A3 (https=) 2020-09-23
US10865362B2 (en) 2020-12-15
EP3484988B1 (en) 2020-09-09
BR112018077082B1 (pt) 2023-03-28
EP3484988A1 (en) 2019-05-22
RU2744632C2 (ru) 2021-03-12
JP6878564B2 (ja) 2021-05-26
CN109415663A (zh) 2019-03-01

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