YU48473B - Silicates based softener of alkali metals for detergent, production procedures for cogranulates and cogranulat produced by such procedure - Google Patents

Silicates based softener of alkali metals for detergent, production procedures for cogranulates and cogranulat produced by such procedure

Info

Publication number
YU48473B
YU48473B YU35092A YU35092A YU48473B YU 48473 B YU48473 B YU 48473B YU 35092 A YU35092 A YU 35092A YU 35092 A YU35092 A YU 35092A YU 48473 B YU48473 B YU 48473B
Authority
YU
Yugoslavia
Prior art keywords
alkali metal
silicate
weight
carbonate
content
Prior art date
Application number
YU35092A
Other languages
Serbo-Croatian (sh)
Other versions
YU35092A (en
Inventor
Patrick Boittiaux
Daniel Joubert
Jean-Claude Kiefer
Jerome La Roux
Original Assignee
Rhone-Poulenc Chimie
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 Rhone-Poulenc Chimie filed Critical Rhone-Poulenc Chimie
Publication of YU35092A publication Critical patent/YU35092A/en
Publication of YU48473B publication Critical patent/YU48473B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/04Water-soluble compounds
    • C11D3/08Silicates
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/10Salts
    • C11D7/14Silicates

Abstract

Omekšivač na bazi silikata alkalnih metala za deterdžent, koji je sastojak deterdženta, naznačen time, što se sastoji od silikata alkalnog metala molarnog odnosa SiO2/M2O između 1.6 i 3.5, poželjno između 1.8 i 2.6 i to natrijuma ili kalijuma, sa najmanje 30% atoma silicijuma u obliku Q2 i Q3, što predstavlja stepen združivanja atoma silicijuma među sobom, tako što Q2 znači da svaki atom silicijuma učestvuje u dve veze -Si-O-Si-, dok su druge dve veze završetak -Si-O-X, gde je X alkalni metal ili vodonik, a Q3 znači da svaki atom silicijuma učestvuje u tri veze -Si-O-Si-, dok je preostala veza završetak -Si-O-X, gde je X alkalni metal ili vodonik. Omekšivač na bazi silikata alkalnih metala za deterdžent, koji je sastojak deterdženta, prema zahtevu 1, naznačen time, što se sastoji od silikata alkalnog metala, i to natrijuma ili kalijuma, sa najmanje 50% atoma silicijuma u obliku Q2 i obliku Q3. Postupak dobijanja okruglog kogranulatna hidratisanih silakata alkalnih metala, naznačen time, što se vrši rasprašivanje vodenog rastvora na bazi silikata alkalnih metala ili smeše silikata i karbonata alkalnih metala po kotrljajućem sloju čestica na bazi karbonata alkalnih metala, a količina rastvora silikata ili smeše silikata i karbonata, koja se raspršuje, kao i količine čestica na bazi karbonata, odgovaraju odnosu protoka tečnosti i protoka čestica, koji iznosi između 0.2 i 0.8 lit/kg, pa se tako dobijeni kogranulati zgušnjavaju na temperaturi na kojoj se vrši i kotrljanje kogranulata i tako zgušnjeni kogranulati suše se fluidizacijom do sadržaja vezane vode u silikatu, koji odgovara masenom odnosu silikata izraženog kao suva materija prema vezanoj vodi u silikatu reda 100/120 do 100/40, a tako osušeni kogranulat ima sadržaj karbonata između 47% i 87% mase, bolje između 64% i 69% mase, ima sadržaj silikata između 8% i 38% mase, bolje između 24% i 31% mase i ima sadržaj vode između 5% i 25% mase, bolje između 12% i 20% mase. Kogranulat dobijen postupkom prema zahtevu 8 i 9, na značen time, što čestice koje čine kotrljajući sloj sadrže manje od 10% masenih čestica kogranulata strukture različite od karbonata alkalnog metala, a imaju prečnik i gustinu odgovarajuću česticama karbonata alkalnog metala. Okrugli kogranulat na bazi silikata alkalnih metala, naz načen time, što je i na bazi karbonata alkalnih metala i što je sadržaj silikata, molarnog odnosa SiO2/MO2 između 1.6 i 3.5, između 8% i 38% masenih, sadržaj karbonata između 47% i 87% maAn alkali metal silicate softener for detergent, which is a detergent ingredient, comprising an alkali metal silicate of a SiO2 / M2O molar ratio of 1.6 to 3.5, preferably between 1.8 and 2.6, of sodium or potassium, with at least 30% atoms of silicon in the form of Q2 and Q3, which represents the degree of association of the silicon atoms with each other, such that Q2 means that each silicon atom participates in two -Si-O-Si- bonds, while the other two bonds are terminated -Si-OX, where X is an alkali metal or hydrogen, and Q3 means that each silicon atom participates in three -Si-O-Si- bonds, while the remaining bond is the termination -Si-OX, where X is an alkali metal or hydrogen. An alkali metal silicate softener for detergent, which is a detergent ingredient according to claim 1, consisting of an alkali metal silicate, sodium or potassium, with at least 50% of silicon atoms in the form of Q2 and in the form of Q3. A process for producing a round cogranulate hydrated alkali metal silicate, by atomising an aqueous solution based on alkali metal silicates or a mixture of alkali metal silicates and carbonates by a rolling layer of alkali metal carbonate particles, and the amount of silicate or carbonate solution silicate, carbonate which is dispersed, as well as the amounts of carbonate-based particles, correspond to a ratio of fluid flow to particle flow, which is between 0.2 and 0.8 lit / kg, so that the co-granulates thus obtained thicken at the temperature at which both the co-granulates are rolled and the co-granulates thus dried by fluidizing to a content of bound water in silicate, corresponding to a weight ratio of silicate expressed as dry matter to bound water in silicate of the order 100/120 to 100/40, and thus the dried cogranulate has a carbonate content of between 47% and 87% by weight, preferably between 64 % to 69% by weight, has a silicate content of between 8% and 38% by weight, preferably between 24% and 31% by weight and has a water content of between 5% and 25% by weight, preferably between 12% and 20% by weight. The cogranulate obtained by the method of claims 8 and 9, characterized in that the particles constituting the rolling layer comprise less than 10% by weight of the co-granulate particles of structure other than alkali metal carbonate and have a diameter and density corresponding to the alkali metal carbonate particles. A round cogranulate based on alkali metal silicates, which is also based on alkali metal carbonates and having a silicate content, a SiO2 / MO2 molar ratio of between 1.6 and 3.5, between 8% and 38% by weight, a carbonate content of between 47% and 87% ma

YU35092A 1991-06-24 1992-04-03 Silicates based softener of alkali metals for detergent, production procedures for cogranulates and cogranulat produced by such procedure YU48473B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9107710A FR2677994B1 (en) 1991-06-24 1991-06-24 BUILDER AGENT BASED ON ALKALINE METAL SILICATES FOR DETERGENT COMPOSITIONS.

Publications (2)

Publication Number Publication Date
YU35092A YU35092A (en) 1996-01-09
YU48473B true YU48473B (en) 1998-08-14

Family

ID=9414180

Family Applications (1)

Application Number Title Priority Date Filing Date
YU35092A YU48473B (en) 1991-06-24 1992-04-03 Silicates based softener of alkali metals for detergent, production procedures for cogranulates and cogranulat produced by such procedure

Country Status (11)

Country Link
BG (1) BG61772B1 (en)
BR (1) BR9202228A (en)
CZ (1) CZ191992A3 (en)
FR (1) FR2677994B1 (en)
HU (1) HU213171B (en)
IE (1) IE69867B1 (en)
PL (3) PL170381B1 (en)
RO (1) RO110009B1 (en)
RU (1) RU2097411C1 (en)
SK (1) SK191992A3 (en)
YU (1) YU48473B (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2909490A (en) * 1954-07-28 1959-10-20 Olin Mathieson Manufacture of duplex composition of sodium tripolyphosphate and sodium silicate solution
GB1029263A (en) * 1963-05-17 1966-05-11 Procter & Gamble Ltd Manufacture of detergent briquettes
DE2707280A1 (en) * 1976-02-26 1977-09-01 Colgate Palmolive Co PROCESS FOR THE PRODUCTION OF FREE-FLOWING SPRAY-DRIED PARTICLES FROM BUILDER SALT
DE2903058A1 (en) * 1978-02-01 1979-08-09 Unilever Nv METHOD FOR PRODUCING DETERGENT POWDER
US4169806A (en) * 1978-08-09 1979-10-02 The Procter & Gamble Company Agglomeration process for making granular detergents
US4761248A (en) * 1986-11-06 1988-08-02 Kerr-Mcgee Chemical Corporation Process for preparing particulate detergent products

Also Published As

Publication number Publication date
FR2677994A1 (en) 1992-12-24
PL170367B1 (en) 1996-12-31
PL294977A1 (en) 1993-06-28
HU9202083D0 (en) 1992-09-28
IE920823A1 (en) 1992-12-30
PL170411B1 (en) 1996-12-31
IE69867B1 (en) 1996-10-16
RO110009B1 (en) 1995-08-30
PL170381B1 (en) 1996-12-31
FR2677994B1 (en) 1995-01-20
HU213171B (en) 1997-03-28
BG96516A (en) 1994-03-24
CZ191992A3 (en) 1993-01-13
YU35092A (en) 1996-01-09
BR9202228A (en) 1993-02-02
BG61772B1 (en) 1998-05-29
SK191992A3 (en) 1995-01-05
HUT62028A (en) 1993-03-29
RU2097411C1 (en) 1997-11-27

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