EP0082823B1 - Verfahren zum Bleichen von Fasermaterialien unter Verwendung von Oligomeren von Phosphonsäureestern als Stabilisatoren in alkalischen, peroxydhaltigen Bleichflotten - Google Patents

Verfahren zum Bleichen von Fasermaterialien unter Verwendung von Oligomeren von Phosphonsäureestern als Stabilisatoren in alkalischen, peroxydhaltigen Bleichflotten Download PDF

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Publication number
EP0082823B1
EP0082823B1 EP82810551A EP82810551A EP0082823B1 EP 0082823 B1 EP0082823 B1 EP 0082823B1 EP 82810551 A EP82810551 A EP 82810551A EP 82810551 A EP82810551 A EP 82810551A EP 0082823 B1 EP0082823 B1 EP 0082823B1
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EP
European Patent Office
Prior art keywords
component
weight
bis
bleaching
bleaching liquor
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.)
Expired
Application number
EP82810551A
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German (de)
English (en)
French (fr)
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EP0082823A1 (de
Inventor
Paul Dr. Schäfer
Hans-Ulrich Berendt
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 Schweiz AG
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Ciba Geigy AG
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Publication date
Application filed by Ciba Geigy AG filed Critical Ciba Geigy AG
Publication of EP0082823A1 publication Critical patent/EP0082823A1/de
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Publication of EP0082823B1 publication Critical patent/EP0082823B1/de
Expired legal-status Critical Current

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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
    • C11D3/39Organic or inorganic per-compounds
    • C11D3/3902Organic or inorganic per-compounds combined with specific additives
    • C11D3/3937Stabilising agents
    • C11D3/394Organic compounds
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L4/00Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
    • D06L4/10Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which develop oxygen
    • D06L4/12Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which develop oxygen combined with specific additives

Definitions

  • the present invention relates to a process for bleaching cellulose-containing fiber materials, in which an oligomeric phosphonic acid ester with at least four phosphorus atoms is used as a stabilizer in the aqueous, alkaline, peroxide-containing bleaching liquor.
  • DE-B-1 082 235 discloses monomeric or dimeric phosphonic esters with one or two phosphorus atoms, which act as complexing agents for metal ions such as e.g. Magnesium, calcium, zinc, copper and iron ions are used, the complex formation of e.g. Copper ions and others the decomposition of per compounds is avoided.
  • metal ions such as e.g. Magnesium, calcium, zinc, copper and iron ions are used, the complex formation of e.g. Copper ions and others the decomposition of per compounds is avoided.
  • metal ions such as e.g. Magnesium, calcium, zinc, copper and iron ions are used, the complex formation of e.g. Copper ions and others the decomposition of per compounds is avoided.
  • metal ions such as e.g. Magnesium, calcium, zinc, copper and iron ions are used, the complex formation of e.g. Copper ions and others the decomposition of per compounds is avoided.
  • US-A-3 621 081 discloses the oligomeric phosphonic acid esters used according to the invention. According to US Pat. No. 3,621,081, these oligomeric phosphonic acid esters are used thanks to their sequestering properties, above all for calcium ions, as softening agents in water treatment and as builders in detergents.
  • the present invention thus relates to a process for bleaching cellulose-containing fiber materials with aqueous, peroxide-containing, alkaline liquors, characterized in that liquors are applied to the fiber materials by adding water-soluble oligomers of the formula or their alkali metal salts are stabilized, in which Y is hydrogen or -CO-T1, R 1 , Q, and T, are each alkyl having 1 to 4 carbon atoms, and n 1 is 1 to 16, and then the fiber materials are stored in a moist state .
  • oligomers according to formula (1) as stabilizers in aqueous, peroxide-containing, alkaline liquors for bleaching cellulose-containing fiber materials and the bleaching liquor for carrying out the bleaching process, which contains oligomers according to formula (1) as stabilizers, are further objects of the present invention Invention.
  • the water-soluble compounds of the formula (1) are preferably present as alkali metal salts, especially as sodium and in particular as potassium salts. All or only some of the hydrogen atoms of the -P (O) (OH) - or> P (O) (OH) groups can be substituted by alkali metal atoms.
  • Suitable alkyl radicals for R 1 , Q 1 and T are isobutyl, preferably isopropyl, especially n-butyl and n-propyl and in particular ethyl and methyl, methyl being particularly preferred.
  • Y 1 is -CO-T 1
  • T and R preferably have the same meanings. Hydrogen as the meaning of Y, however, is of primary interest.
  • the limit values for n are 1 and 16. Preferred values are 1 to 12, the main constituent of the mixture being oligomers with average values for n of about 5 to 9, preferably about 5 or 6. Oligomers with n - 1 and oligomers with n - 12 to 16, especially 12, are always present in smaller amounts in the mixture.
  • Oligomers of the formula are preferred or their sodium or potassium salts, in which Y 2 is hydrogen or -CO-R 1 , n 2 1 to 14 and R 1 has the meaning given, and in particular the formula or their potassium salts, wherein R 2 is methyl or ethyl and n 3 is 1 to 12.
  • the oligomers according to formula (1) per se, their preparation and their use as emulsion breakers, decalcifying agents and as paper auxiliaries are e.g. in US-A-3 621 081, US-A-4 254 063 and EP-A-0 029 076.
  • the oligomers are obtained in the form of their free phosphonic acids.
  • an alkali metal hydroxide e.g. Sodium or especially potassium hydroxide
  • the acidic solutions of the oligomers e.g. with sodium and in particular potassium hydroxide, preferably in the form of their aqueous solutions, so added that the pH of the solutions rises to 3 to 7, preferably 3.5 to 4.
  • the potassium salts of the oligomers are preferred over the sodium salts because of their higher solubility.
  • the oligomers according to formula (1) can also be used in combination with other stabilizers such as e.g. Aminoalkanediphosphonic acids according to DE-A-2 625 767 or DE-A-2 115 737 are used in the bleaching liquors according to the invention.
  • other stabilizers such as e.g. Aminoalkanediphosphonic acids according to DE-A-2 625 767 or DE-A-2 115 737 are used in the bleaching liquors according to the invention.
  • the process according to the invention for bleaching cellulose-containing fiber materials using the oligomers of the formula (1) for stabilizing the aqueous, peroxide-containing alkaline liquors is carried out in such a way that the bleaching liquors are first applied to the fiber material, as a rule, e.g. by immersion and preferably by padding in e.g. 10 to 60 ° C, but preferably at room temperature (15 to 25 ° C), the liquor absorption after squeezing is about 50 to 120, preferably 90 to 110 percent by weight.
  • the fiber material After impregnation, the fiber material is usually subjected to a so-called wet storage or wet storage process without drying in the wet state or after squeezing in the padding process while still wet, in which the material is rolled up in an airtight manner, if necessary in a plastic film and optionally under pressure at a maximum of 150 ° C for about 10 minutes, but preferably under normal pressure at 80 to 98 ° C for about 1 to 5 hours or in particular at room temperature (15 to 25 ° C) for about 10 to 30 hours .
  • the treatment of the fiber materials can also be carried out in so-called long liquors (exhaust processes) with a liquor ratio of e.g. 1: 3 to 1: 100, preferably 1: 8 to 1:25 at 20 to 100, preferably 80 to 98 ° C.
  • the pull-out can also be carried out up to 150 ° C under pressure in so-called high-temperature equipment (HT equipment). If the bleaching takes place in the exhaust process, the fiber material is at the specified temperatures and during the specified times in the apparatus used for the extraction, e.g. in a reel skid.
  • Continuous processes are particularly important in industrial operation, in which similar residence times for the fiber material in the bleaching liquor are required at the temperatures indicated. Treatment temperatures of 98 ° C are advantageously not exceeded in order to prevent any fiber damage. With special HT equipment, however, the fiber materials can also be used in industrial continuous processes under pressure up to e.g. 2.5 bar at higher temperatures, e.g. up to 150 ° C, if the treatment time is kept so short that fiber damage is excluded.
  • the fiber materials are then generally rinsed thoroughly with hot water at around 90 to 98 ° C and then with cold water, if necessary with e.g. Neutralized acetic acid and then dried preferably at elevated temperatures (e.g. up to 150 ° C).
  • Component (a) can also be a solid, e.g.
  • Preferred optional components (d) are alkali metal peroxydisulfates and in particular sodium peroxydisulfate (Na 2 S 2 0 8 ), which is preferably used as a solid.
  • Suitable surfactants for the optional component (s) are both anionic and nonionic surfactants, but especially their mixtures.
  • Preferred anionic surfactants are e.g. Alkylarylsulfonates, fatty acid condensation products, protein cleavage products or their salts and especially alkylsulfate salts and alkylbenzenesulfonic acids with 12 to 22 carbon atoms in the alkyl radical.
  • Preferred nonionic surfactants are e.g. Adducts of alkylene oxides, especially propylene and especially ethylene oxide and alkylphenols with e.g.
  • the preferred optional component (f) are higher alcohols, e.g. Isooctyl alcohol, but especially silicone-based defoaming and / or deaerating agents, in particular silicone oil emulsions.
  • Components (e) and (f) are preferably combined with commercially available aqueous, about 10 to 60, preferably 30 to 40 percent by weight formulations of non-foaming surfactant mixtures.
  • the preferred optional component (g) is e.g. water-soluble alkali metal silicates, in particular soda-water glass with a content of 24 to 28% SiO, especially as aqueous, about 30 to 40 weight percent solutions.
  • optical brighteners used as optional component (h) generally belong to the styryl and stilbene series, e.g. Distyrylarylenes, diaminostilbenes, ditriazolylstilbenes, phenylbenzoxazolylstilbenes, stilbene naphthotriazoles and dibenzoxazolylstilbenes.
  • Optical brighteners of the distyrylbiphenyl or bistriazinylaminostilbene type which contain sulfonic acid groups, e.g.
  • Sulfonated distyrylbiphenyl and bistriazinyl derivatives in particular the bis (phenylamino-dialkylamino-triazinyl) -stilbene-disulfonic acids and bis (phenylamino-morpholino-striazinyl) -stilbene disulfonic acids present as alkali metal salts, especially as potassium or preferably as sodium salts. These are preferably used as commercially available aqueous, about 20 to 30 percent by weight liquid formulations.
  • bleaching liquors are used in the continuous process, it may be necessary to have reinforced, approximately 3 to 5 times stronger bleaching liquors (bleaching liquors with 3 to 5 times the concentration) as so-called make-up or storage baths in order to reduce the concentration of the bleaching bath after bleaching a certain amount of material.
  • the cellulose-containing material which is bleached according to the invention is in a wide variety of processing stages, e.g. as loose material, yarn, woven or knitted fabric. As a rule, these are always textile fiber materials which are produced from pure textile cellulose fibers or from mixtures of textile cellulose fibers with textile synthetic fibers.
  • cellulosic fibers come e.g. those made from regenerated cellulose, e.g. Cellulose and viscose, those made from native cellulose, e.g. Hemp, linen and jute and especially cotton and, as synthetic fibers, those made of polyacrylonitrile and especially polyester and polyamide.
  • regenerated cellulose e.g. Cellulose and viscose
  • native cellulose e.g. Hemp, linen and jute and especially cotton
  • synthetic fibers those made of polyacrylonitrile and especially polyester and polyamide.
  • Fabrics made of cotton or regenerated cellulose or blended fabrics made of cotton and polyester and made of cotton and polyamide are particularly well suited to be bleached according to the invention, cotton fabrics and knitted fabrics being of primary interest. With e.g. Prewashed materials are also suitable. It is also possible to bleach sized cotton fibers, bleaching after or before desizing.
  • the fiber materials bleached according to the invention are notable for their shell freedom, their good rewettability, their low ash content and, above all, their high degree of whiteness.
  • the presence of the mixtures of the formula (1) as a stabilizer means that silicates (water glass) are not required or only in small amounts in the bleaching liquors, so that little or no incrustation of the bleaching apparatus and incrustations occur on the bleached fiber material.
  • the stabilizing action of the compounds of formula (1) used according to the invention is clearly superior to the action of known stabilizers previously used in bleaching liquors.
  • the reaction mixture is then in the form of a completely homogeneous, clear melt.
  • This melt is then cooled to 80 ° C. and kept under reduced pressure (-25 to -15 bar) for 1 hour, about 10 parts of by-products being removed from the reaction mixture.
  • the melt at 20 ° C with 275 parts of a 20% aqueous potassium hydroxide solution to a pH of 3.5 and then diluted with water so that 420 parts of an aqueous, clear, colorless solution is obtained 35% of the oligomers according to the formula contains as a partial potassium salt.
  • aqueous surfactant solution contains and brought to a fleet absorption of 100% by squeezing.
  • 25% aqueous surfactant solution 5 g of a 48% aqueous solution of pentadecane-1-sulfonic acid (sodium salt) and the addition product of 4 mol ethylene oxide with 1 mol of a primary (C 9 -C 11 ) Alcohol in a weight ratio of 3: 1 can be used.
  • the impregnated fabric is rolled up and stored in the wet state for 24 hours at room temperature (15 - 25 ° C). The fabric is then rinsed thoroughly with hot water (90 - 98 ° C) and then with cold water (5 - 25 ° C) and then dried.
  • the increase in the degree of whiteness of the bleached fabric obtained in comparison with the raw fabric before bleaching is assessed according to the CIBA-GEIGY white scale (cf. R. Griesser, "Tenside Detergents", 12 [2], 93-100 (1975)).
  • the DP degree (average degree of polymerization of cellulose) of the bleached and unbleached fabric is 2,400 in accordance with SNV 195 598.
  • the ash content (ashing at 800 ° C for 2 hours) of the bleached fabric is only 0.30%.
  • the bleached fabric is shell-free and has excellent rewettability.
  • a 5-fold strengthened bleaching liquor used as a make-up bath or storage bath has an active oxygen content (measured by reacting the active oxygen with an excess of arsenite solution and then iodometrically determining the unreacted excess arsenite) after 97 hours after 24 hours , 91.4% after 48 hours, 90.7% after 72 hours and 89.0% after 96 hours of storage.
  • the 5-fold strengthened bleaching liquors are colorless and remain at; 5%, which is 5%, water id by quenching solution (sodium salt) of storage completely clear. There are no deposits or crusts on the equipment.
  • 5-fold strengthened bleaching liquors of an analogous composition which contain water glass instead of the oligomers according to formula (1)
  • turbidity and precipitations form after 24 hours of storage.
  • these unstabilized, 5-fold bleaching liquors have an active oxygen content of only 50.8% after 24 hours, 43.7% after 48 hours, 42.3% after 72 hours and 41.3% after 36 hours of storage .
  • Example 1 contains, and brought to a fleet absorption of 100% by squeezing. Instead of the 25% aqueous surfactant solution, 4 g of the further surfactant solution according to Example 1 can also be used.
  • the impregnated fabric is rolled up and stored in a moist state at 90 ° C. for 75 minutes. The fabric is then rinsed and dried as described in Example 1.
  • the whiteness of the bleached fabric is 57 (raw fabric -62).
  • the bleached fabric is shell-free and has excellent rewettability and a low ash content.
  • the impregnated fabric is rolled up, packed airtight with a film and stored in a moist and airtight state for 24 hours at room temperature (15 - 25 ° C). The fabric is then rinsed thoroughly as described in Example 1 and dried. The whiteness of the bleached fabric is 194 (before bleaching -36). The bleached fabric is shell-free, has excellent rewettability and a low ash content.
  • Example 1 contains, and brought to a fleet absorption of 100% by squeezing.
  • 5 g of the further surfactant solution according to Example 1 can also be used.
  • the impregnated fabric is rolled up and stored in a moist state for 24 hours at room temperature (15-25 ° C).
  • the fabric is then rinsed and dried as described in Example 1.
  • the whiteness of the bleached fabric is 57 (raw fabric -62).
  • the bleached fabric is shell-free, has excellent rewettability and a low ash content.
  • Example 1 contains, and brought to a fleet absorption of 100% by squeezing.
  • 5 g of the further surfactant solution according to Example 1 can also be used.
  • the impregnated fabric is rolled up and stored in a moist state for 24 hours at room temperature (15 - 25 ° C).
  • the fabric is then rinsed and dried as described in Example 1.
  • the whiteness of the bleached fabric is 70 (raw fabric -62).
  • the bleached fabric is shell-free, has excellent rewettability and a low ash content.
  • the mixed fabric is treated according to example 1.
  • the whiteness of the bleached blended fabric is 46 (raw fabric 0).
  • the tissue contains, and brought to a fleet absorption of 100% by squeezing.
  • the tissue is rolled up and stored in a moist state at 20 to 25 ° C. for 24 hours.
  • the fabric is then rinsed and dried according to Example 1.
  • the whiteness of the bleached fabric is 24 (raw fabric -63).

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Textile Engineering (AREA)
  • Detergent Compositions (AREA)
EP82810551A 1981-12-23 1982-12-17 Verfahren zum Bleichen von Fasermaterialien unter Verwendung von Oligomeren von Phosphonsäureestern als Stabilisatoren in alkalischen, peroxydhaltigen Bleichflotten Expired EP0082823B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH829981 1981-12-23
CH8299/81 1981-12-23

Publications (2)

Publication Number Publication Date
EP0082823A1 EP0082823A1 (de) 1983-06-29
EP0082823B1 true EP0082823B1 (de) 1986-09-03

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EP82810551A Expired EP0082823B1 (de) 1981-12-23 1982-12-17 Verfahren zum Bleichen von Fasermaterialien unter Verwendung von Oligomeren von Phosphonsäureestern als Stabilisatoren in alkalischen, peroxydhaltigen Bleichflotten

Country Status (6)

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US (1) US4496472A (enrdf_load_stackoverflow)
EP (1) EP0082823B1 (enrdf_load_stackoverflow)
JP (1) JPS58126364A (enrdf_load_stackoverflow)
CA (1) CA1216706A (enrdf_load_stackoverflow)
DE (1) DE3273072D1 (enrdf_load_stackoverflow)
ZA (1) ZA829421B (enrdf_load_stackoverflow)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4515596A (en) * 1982-07-27 1985-05-07 Ciba-Geigy Corporation Process for aftertreating dyed fibrous material made of or containing cellulose
US4515597A (en) * 1982-12-10 1985-05-07 Ciba Geigy Corporation Magnesium complexes of oligomeric phosphonic acid esters, a process for their preparation and their use as stabilizers in alkaline, peroxide-containing bleach liquors
JPS61231262A (ja) * 1985-04-02 1986-10-15 日本化学工業株式会社 繊維類の漂白浴
US4725281A (en) * 1985-07-19 1988-02-16 Ciba-Geigy Corporation Aqueous alkaline, silicate-containing composition and the use thereof for bleaching cellulosic fiber materials in the presence of per compounds
US4751023A (en) * 1985-07-19 1988-06-14 Ciba-Geigy Corporation Aqueous alkaline, silicate-containing composition for bleaching cellulosic fibre materials in the presence of per compounds
DE3720277A1 (de) * 1987-06-19 1988-12-29 Degussa Verfahren zur verminderung der neigung zum zusammenbacken von teilchenfoermigen aktivsauerstoffverbindungen
US4970019A (en) * 1988-10-27 1990-11-13 Fmc Corporation Particulate composition containing bleach and optical brightener and process for its manufacture
US5482516A (en) * 1993-05-24 1996-01-09 Surry Chemicals, Inc. Process for bleaching textiles
US5527361A (en) * 1993-05-24 1996-06-18 Surry Chemicals, Inc. Low temperature process for bleaching textiles
US5616280A (en) * 1993-08-25 1997-04-01 Burlington Chemical Co., Inc. Bleaching composition
US5464563A (en) * 1993-08-25 1995-11-07 Burlington Chemical Co., Inc. Bleaching composition
US20030126689A1 (en) * 2001-12-07 2003-07-10 The Procter & Gamble Company Process for providing improved whiteness to fabric and for removing formaldehyde and formaldehyde conjugates from treated fabric
DE102006060049B4 (de) * 2006-06-27 2010-06-10 Lg Display Co., Ltd. Flüssigkristallanzeige und Ansteuerungsverfahren

Family Cites Families (11)

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NL242785A (enrdf_load_stackoverflow) * 1958-09-06 1900-01-01
NL252116A (enrdf_load_stackoverflow) * 1959-06-03
DE1264687B (de) * 1965-11-24 1968-03-28 Therachemie Chem Therapeut Mittel zur Verminderung der Schaedigung von Haaren beim Bleichen und Faerben
US3562169A (en) * 1968-12-23 1971-02-09 Procter & Gamble Detergent compositions containing oligomeric ester chain condensates of ethane-1-hydroxy-1,1-diphosphonic acid as builders
US3621081A (en) * 1968-12-23 1971-11-16 Procter & Gamble Oligomeric ester chain condensates of ethane-1-hydroxy-1,1-diphosphonic acid
US3766078A (en) * 1971-06-03 1973-10-16 Monsanto Co Processes for stabilizing peroxy solutions
DE2602030C2 (de) * 1976-01-21 1983-12-01 Henkel KGaA, 4000 Düsseldorf Diphosphonoalkancarbonsäuren und Verfahren zu deren Herstellung
US4190615A (en) * 1978-09-11 1980-02-26 Betz Laboratories, Inc. Oligomeric ester chain condensates of substituted 1-hydroxy-1,1-diphosphonic acid
US4263160A (en) * 1979-04-30 1981-04-21 Olin Corporation Process for the preparation of stable dispersions of alkyl phosphate esters
US4254063A (en) * 1979-05-07 1981-03-03 Betz Laboratories, Inc. Method for preparing oligomeric ester chain condensates of substituted 1-hydroxy-1,1-diphosphonic acid
US4323465A (en) * 1981-04-23 1982-04-06 Fmc Corporation Stabilized sodium sulfate-hydrogen peroxide-sodium chloride adduct and alkaline bleach composition containing same

Also Published As

Publication number Publication date
JPH0335428B2 (enrdf_load_stackoverflow) 1991-05-28
JPS58126364A (ja) 1983-07-27
ZA829421B (en) 1983-09-28
DE3273072D1 (en) 1986-10-09
CA1216706A (en) 1987-01-20
US4496472A (en) 1985-01-29
EP0082823A1 (de) 1983-06-29

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