US3056652A - Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing - Google Patents

Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing Download PDF

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Publication number
US3056652A
US3056652A US698911A US69891157A US3056652A US 3056652 A US3056652 A US 3056652A US 698911 A US698911 A US 698911A US 69891157 A US69891157 A US 69891157A US 3056652 A US3056652 A US 3056652A
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United States
Prior art keywords
anhydrous sodium
sodium tripolyphosphate
hydrating
temperature
tripolyphosphate
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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 - Lifetime
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US698911A
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English (en)
Inventor
Frederick V Ryer
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Lever Brothers Co
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Lever Brothers Co
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Filing date
Publication date
Priority to NL233632D priority Critical patent/NL233632A/xx
Application filed by Lever Brothers Co filed Critical Lever Brothers Co
Priority to US698911A priority patent/US3056652A/en
Priority to FR1208869D priority patent/FR1208869A/fr
Application granted granted Critical
Publication of US3056652A publication Critical patent/US3056652A/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • C11D3/02Inorganic compounds ; Elemental compounds
    • C11D3/04Water-soluble compounds
    • C11D3/06Phosphates, including polyphosphates
    • C11D3/062Special methods concerning phosphates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/26Phosphates
    • C01B25/38Condensed phosphates
    • C01B25/40Polyphosphates
    • C01B25/41Polyphosphates of alkali metals
    • C01B25/418After-treatment

Definitions

  • the present invention relates to the treatment of Form II anhydrous sodium tripolyphosphate, and more particularly to a process for converting fast hydrating Form II anhydrous sodium tripolyphosphate into slow hydrating Form 11 anhydrous sodium tripolyphosphate.
  • Sodium tripolyphosphate also called sodium triphosphate
  • the anhydrous crystalline form may be either Form I or Form H, the anhydrous tripolyphosphate produced in the high temperature regions being known as Form I, While the an hydrous tripolyphosphate produced in the low temperature regions is known as Form II.
  • the Form I variety hydrates quite rapidly, while the Form II variety hydrates at a much slower rate than the Form I variety. This property of rapid hydration causes lumping in aqueous slurries and accordingly the soap and detergent industry has preferred to employ the Form II variety to avoid hydration as much as possible.
  • Detergent compositions containing tripolyphosphates have advantages over detergent compositions containing other phosphates, such as pyrophosphates or orthophosphates. Repeat washing tests in hard water indicate that clothes washed with detergent compositions containing tripolyphosphates have a lower ash content than clothes washed with detergent compositions containing a pyrophosphate. A given weight of a tripolyphosphate s questers more calcium from the Wash Water than does a pyrophosphate, and hence clearer solutions are obtainable in hard waters with detergent compositions containing tripolyphosphates than with detergent compositions containing pyrophosphates.
  • This tripolyphosphate may be graded into fast hydrating and slow hydrating types by the following test procedure. Preheat under running hot tap water a Wide mouthed Dewar flask of approximately one pint capacity, a four-bladed glass stirrer and a thermometer, and then quickly assemble the apparatus so that the stirrer just clears the bottom of the flask and the thermometer bulb just clears the stirrer blades. Add 25 grams of anhydrous sodium sulfate and 100 cc. of boiling water to the flask and start the stirrer motor. When the sodium sulfate solution has cooled to 170 F., add grams of the Form II anhydrous sodium tripolyphosphate to the flask and start a stopwatch.
  • a fast hydrating Form II anhydrous sodium tripolyphosphate may be converted into a slow hydrating Form II anhydrous sodium tripolyphosphate by heating the fast hydrating Form II anhydrous sodium tripolyphosphate.
  • the temperature of heating may be from about C. to about 380 C., the time of heating, of course, being less at the higher temperature.
  • conversion is obtained by heating the fast hydrating Form II anhydrous sodium tripolyphosphate for about six hours or more at a temperature of about 100 C. or for about one hour or more at a temperature of about 380 C.
  • Form II anhydrous sodium tripolyphosphate The fundamental difierence between the fast and slow hydrating varieties of Form II anhydrous sodium tripolyphosphate cannot be readily established by wet chemical analyses, X-ray diffractograms, Form I content, or particle size determinations. While it will be appreciated that the invention is not to be limited by any theory expressed herein, it is believed that Form II anhydrous sodium tripolyphosphate exists in both a fast hydrating and a slow hydrating variety because of small variations in adsorbed Water on the tripolyphosphate.
  • the fast hydrating Form II anhydrous sodium tripolyphosphate contains more adsorbed water than the slow hydrating Form II anhydrous sodium tripolyphosphate which adsorbed water catalyzes the rate of hydration and the fast hydrating variety is therefore converted into a slow hydrating variety by heating the fast hydrating variety to thereby remove the adsorbed water.
  • the process of the present invention makes possible the avoidance of troublesome increases in viscosity in a spray mix of a tripolyphosphate detergent composition both in the crutcher and during the time between the completion or" the mixing operation and the arrival of the mix at a spray nozzle.
  • Example 1 A lot of Form II anhydrous sodium tripolyphosphate as received from the supplier was divided into two portions. 75 grams of one portion was added to 100 cc. of water containing 25 grams of anhydrous sodium sulfate and having a temperature of 170 F. in accordance with the above test procedure. During the next 15 minutes the slurry thickened and the temperature thereof rose as shown below, thereby indicating that the tripolyphosphate was a fast hydrating variety.
  • Example 2 A lot of Form 11 anhydrous sodium tripolyphosphate as received from the supplier was divided into four portions. 75 grams of one portion was added to 100 cc. of
  • Example 3 Two samples of an aqueous slurry of the following typical detergent composition (calculated on a powder basis) having an overall water content of 40% were agitated in a crutcher for 45 minutes at a temperature 75 of 160 F.
  • the spray-dried product of Formula A was also undesirable in that an aqueous solution thereof contained a large amount of silica floc and hence was quite turbid as contrasted with an aqueous solution of the spray-dried product of Formula B which had only a slight amount of silica floc and hence would not be unsightly to the consumer.
  • the spray-dried product of Formula A contained a large amount of decomposition products (pyroand orthophosphates) of the tripolyphosphate
  • the spray-dried product of Formula B employing the slow hydrating variety of Form II anhydrous sodium tripolyphosphate produced in accordance with the process of the invention contained only a slight amount of decomposition products.
  • the process of converting fast hydrating Form II anhydrous sodium tripolyphosphate into slow hydrating Form II anhydrous sodium tripolyphosphate comprising heating the solid fast hydrating Form II anhydrous sodium tripolyphosphate alone at a temperature of from about 100 C. to about 380 C. for a time of from at least about 6 hours to at least about 1 hour respectively to remove the adsorbed water; said fast hydrating Form II anhydrous sodium tripolyphosphate being characterized by the fact that a stirred aqueous slurry thereof consisting of 100 parts of water, 25 parts of anhydrous sodium sulfate, and parts of said fast hydrating phosphate at an initial temperature of 170 F.
  • said slow hydrating Form II anhydrous sodium tripolyphosphate being characterized by the fact that a stirred aqueous slurry thereof consisting of parts water, 25 parts of anhydrous sodium sulfate, and 75 parts of said slow hydrating phosphate at an initial temperature of F. will remain thin and the temperature will fall during standing for 15 minutes.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic 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)
US698911A 1957-11-26 1957-11-26 Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing Expired - Lifetime US3056652A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
NL233632D NL233632A (enrdf_load_stackoverflow) 1957-11-26
US698911A US3056652A (en) 1957-11-26 1957-11-26 Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing
FR1208869D FR1208869A (fr) 1957-11-26 1958-11-25 Perfectionnements relatifs aux polyphosphates

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US698911A US3056652A (en) 1957-11-26 1957-11-26 Modification of the hydration characteristics of form ii sodium tripolyphosphate prior to detegent processing

Publications (1)

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US3056652A true US3056652A (en) 1962-10-02

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FR (1) FR1208869A (enrdf_load_stackoverflow)
NL (1) NL233632A (enrdf_load_stackoverflow)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3272752A (en) * 1961-03-07 1966-09-13 Knapsack Ag Method of producing detergents
US3852212A (en) * 1972-11-29 1974-12-03 Fmc Corp Method of producing hydrated sodium tripolyphosphate composition
US4255274A (en) * 1979-01-02 1981-03-10 Fmc Corporation Preparation of granular sodium tripolyphosphate products
US4283299A (en) * 1978-10-03 1981-08-11 Lever Brothers Company Production of detergent compositions
US10343212B2 (en) 2016-01-19 2019-07-09 Wenhui Jiang Hardfacing containing tungsten carbide particles with barrier coating and methods of making the same
US11466364B2 (en) 2019-09-06 2022-10-11 Applied Materials, Inc. Methods for forming protective coatings containing crystallized aluminum oxide

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB680346A (en) * 1948-10-21 1952-10-01 Procter & Gamble Detergent composition
US2622068A (en) * 1948-06-04 1952-12-16 Procter & Gamble Process of making heat dried detergent compositions containing form ii sodium triphosphate
US2920939A (en) * 1957-02-14 1960-01-12 Monsanto Chemicals Method of producing phosphates

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2622068A (en) * 1948-06-04 1952-12-16 Procter & Gamble Process of making heat dried detergent compositions containing form ii sodium triphosphate
GB680346A (en) * 1948-10-21 1952-10-01 Procter & Gamble Detergent composition
US2920939A (en) * 1957-02-14 1960-01-12 Monsanto Chemicals Method of producing phosphates

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3272752A (en) * 1961-03-07 1966-09-13 Knapsack Ag Method of producing detergents
US3852212A (en) * 1972-11-29 1974-12-03 Fmc Corp Method of producing hydrated sodium tripolyphosphate composition
US4283299A (en) * 1978-10-03 1981-08-11 Lever Brothers Company Production of detergent compositions
US4255274A (en) * 1979-01-02 1981-03-10 Fmc Corporation Preparation of granular sodium tripolyphosphate products
US10343212B2 (en) 2016-01-19 2019-07-09 Wenhui Jiang Hardfacing containing tungsten carbide particles with barrier coating and methods of making the same
US11466364B2 (en) 2019-09-06 2022-10-11 Applied Materials, Inc. Methods for forming protective coatings containing crystallized aluminum oxide

Also Published As

Publication number Publication date
FR1208869A (fr) 1960-02-26
NL233632A (enrdf_load_stackoverflow)

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