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US2430674A - Method of bleaching - Google Patents

Method of bleaching Download PDF

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Publication number
US2430674A
US2430674A US472052A US47205243A US2430674A US 2430674 A US2430674 A US 2430674A US 472052 A US472052 A US 472052A US 47205243 A US47205243 A US 47205243A US 2430674 A US2430674 A US 2430674A
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Prior art keywords
solution
bleaching
chlorite
aldehyde
bleached
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US472052A
Inventor
Clifford A Hampel
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Mathieson Alkali Works Inc
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Mathieson Alkali Works Inc
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Priority to BE465974D priority Critical patent/BE465974A/xx
Application filed by Mathieson Alkali Works Inc filed Critical Mathieson Alkali Works Inc
Priority to US472052A priority patent/US2430674A/en
Priority to US472053A priority patent/US2433661A/en
Priority to GB1796/44A priority patent/GB576909A/en
Priority to GB1872/44A priority patent/GB576910A/en
Priority to FR928932D priority patent/FR928932A/en
Application granted granted Critical
Publication of US2430674A publication Critical patent/US2430674A/en
Priority to DES19567A priority patent/DE833943C/en
Priority to DES19908A priority patent/DE943105C/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B35/00Extraction of sucrose from molasses
    • C13B35/02Extraction of sucrose from molasses by chemical means
    • C13B35/04Extraction of sucrose from molasses by chemical means by precipitation as alkaline earth metal saccharates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09FNATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
    • C09F1/00Obtaining purification, or chemical modification of natural resins, e.g. oleo-resins
    • C09F1/04Chemical modification, e.g. esterification
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20Organic compounds not containing metal atoms
    • C10G29/22Organic compounds not containing metal atoms containing oxygen as the only hetero atom
    • C10G29/24Aldehydes or ketones
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G73/00Recovery or refining of mineral waxes, e.g. montan wax
    • C10G73/42Refining of petroleum waxes
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B11/00Recovery or refining of other fatty substances, e.g. lanolin or waxes
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B11/00Recovery or refining of other fatty substances, e.g. lanolin or waxes
    • C11B11/005Lanolin; Woolfat
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/02Refining fats or fatty oils by chemical reaction
    • C11B3/08Refining fats or fatty oils by chemical reaction with oxidising agents
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C1/00Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
    • C11C1/08Refining
    • 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
    • C11D13/00Making of soap or soap solutions in general; Apparatus therefor
    • C11D13/02Boiling soap; Refining
    • C11D13/06Bleaching of soap or soap solutions
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B20/00Purification of sugar juices
    • C13B20/08Purification of sugar juices by oxidation or reduction
    • 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
    • D06L4/13Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which develop oxygen using inorganic agents
    • 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
    • D06L4/20Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen
    • D06L4/21Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen combined with specific additives
    • 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
    • D06L4/20Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen
    • D06L4/22Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents
    • D06L4/24Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents using chlorites or chlorine dioxide
    • 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
    • D06L4/20Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen
    • D06L4/22Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents
    • D06L4/24Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents using chlorites or chlorine dioxide
    • D06L4/26Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents using chlorites or chlorine dioxide combined with specific additives
    • 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
    • D06L4/70Multi-step processes

Definitions

  • This invention relates to an improved process for effecting color improvement or bleaching of non-cellulosic organic materials.
  • the invention is applicable to the treatment of a wide variety of such materials including the following: Carbohydrates such as sugar and starch; synthetics such as acetate rayon and nylon; sponges; walnut shells; resins such as shellac; oils, fats, waxes, soaps-and the like and fatty acids, such as oleic acid or red oil.
  • the material to be bleached is subjected hyde in the presence of water.
  • the material being treated is admixed with the chlorite and aldehyde in aqueous solution, the pH of the solution during the bleaching operation generally being maintained at not less than aboutfl.
  • the function of the aldehyde in my improved bleaching process appears to be that of activating the chlorite rather than a direct action upon the organic material itself.
  • the chlorites, or reaction products thereof are enabled to efiect the bleaching of the organic mato simultaneous action of a chlorite and an aldeterial either in an alkaline or substantially neutral environment.
  • Chlorites useful in my process are those sufficiently soluble in water to provide an adequate concentration to efl'ect the desired bleaching. When the bleaching requirement is relatively low, less soluble chlorites may be used. However, for most purposes, I prefer the chlorites of the alkali and alkaline earth metals, such as sodium chlorite, NaClOz, and calcium chlorite, Ca(C1O2)2.
  • aldehydes may be used, including the aliphatic aldehydes, aromatic aldehydes, other carbocyclic aldehydes and heterocyclic aldehydes.
  • formaldehyde, acetaldehyde, paraformaldehyde, furfural, benzaldehyde, and 5 and 6 carbon atom aldose sugars and inverted sugars are particularly useful. All of these compounds are characterized by the CH0 group. In addition to those highly soluble in water, the relatively insoluble aldehydes have been found to function satisfactorily in most instances.
  • Temperatures and concentrations are not usually critical and may be varied over a wide range. Increasing the temperature has generally been found to increase the rate of bleaching. Also, the ratio of chlorite to aldehyde may be widely varied. However, a molar ratio of chlorite to aldehyde of about 1:1 has been found generally useful.
  • the temperature best suited for a particular operation will, to a considerable extent, depend upon the nature of the material being treated. Ordinary room temperature may frequently be employed with advantage but higher temperatures are usually desirable when treating a material normally solid where it is desired to effect the melting or solution thereof. Temperatures at which the material being treated becomes unstable or at which the material is deleteriously affected are to be avoided.
  • Alkali metal phosphates such as the monosodium and disodium orthophosphates have been found to be particularly advantageous buffers for the purpose of the present invention, though other builers may be used with advantage. I have found that in the presence of such phosphates the consumption of chlorite in the bleaching operation is materially reduced, In some instances a saving of 50% of chlorite has been effected by the use of these phosphates, in conjunction with the other constituents of my bleaching solution previously noted.
  • my invention is particularly useful in the treatment of either natural or synthetic materials of this type, including unsaponifiable petroleum waxes and saponiilable oils and waxes such as beeswax, carnauba wax, candelilla wax, corn oil and soya bean oil. It is especially applicable to the bleaching of soaps and similar alkaline reacting materials.
  • such sponges may be bleached to an exceptionally high degree with no substantial tendering or weakening of their fiber structure so that their normal resistance to tearing apart in use is not substantially impaired.
  • the bleaching of starch in accordance with my present invention, is with advantage enacted by subjecting the starch to the action of the chlorite and the aldehyde while in aqueous suspension.
  • the bleaching of sugar, oils, fats, waxes, soaps, shellac, fatty acid and the like is with advantage effected by treating the material while in a liquid condition, 1. e., either molten or in aqueous solution, depending upon the characteristics of the particular material being treated.
  • such materials either molten or in aqueous solution, may be admixed with a chlorite in the presence of water and the aidehyde thereafter added or the material to be treated may be admixed with the aldehyde in the presence of water and the chlorite added to this mixture.
  • the resultant mixture is maintained at a temperature usually ranging from room temperature to about C., for a period of time sumcient to effect the desired bleaching and is thereafter cooled and separated.
  • the soap may be melted by heating in water, the soap solution admixed with an aqueous chlorite solution and the desired amount of aldehyde thereafter added gradually or as a series of small proportions during agitation.
  • the material In the treatment of wax or the like, which is solid at normal temperatures, the material is with advantage melted and an aqueous solution of the chlorite and the aldehyde admixed therewith or the chlorite and aldehyde may be separately added.
  • Example I An aqueous solution was prepared by admixing 50 c. c. of pH 7 sodium phosphate buffer solution, 50 c. c. of an aqueous sodium chlorite solution containing 10 grams of available chlorine and 100 c. c. of a dilute aqueous formalin solution containing 2.2 grams of HCHO. 100 grams of soy-bean oil was then admixed with the resultant solution and allowed to stand for 2 hours, at the end of which time much of the original yellow color of the oil had been removed and, upon separation from the solution, a superior product was obtained. During the admixing of the oil with the solution and during the following 2 hour period a pH of about 7 and a temperature of about 25 C. were maintained.
  • Example [I Beeswax was not only bleached but the texture thereof was made smoother by the following treatment: To 50 grams of beeswax melted in a water bath there was added 50 c. c. of an aqueous pH 7 sodium phosphate buffer solution, 100 c. c. of an aqueous sodium chlorite solution-containing 5 grams of available chlorine as chlorite and 1.9 c. c. of furfural. After admixing the solution and the melted beeswax, the admixture was permitted to stand for 1 hour at a temperature of 60 C. Thereafter, the wax was separated and allowed to solidify. The resultant product was found to have a much lighter 0010 than the original wax.
  • Example III Cocoabutter was saponified by treatment with caustic soda and 200 grams of the resulting soap was melted with 200 grams of water. 1 gram of sodium chlorite dissolved in an equal weight of water was then added and admixed with the soap solution. This was followed by the addition of c. c. of aqueous formaldehyde solution prepared by dissolving 0.53 gram of 36% formalin in 100 c. c. of water. The addition of 10 ct, c. of
  • this aqueous formaldehyde solution was repeated at 10 minute intervals until a total of 100 c. c. of the solution had been added. During this, period, the pH of the solution was approximately 9.3, no buffer being used, and the mixture was kept hot (about 100 C.) by the passage of steam therethrough. Thereafter, the bleached soap was cooled and separated. Its color was very white.
  • Example IV A still further batch of cocoabutter soap was bleached, as described in Example III, except that the 10 c. 0. portions of the formaldehyde solutions were added at minute intervals. Re-
  • Example VI 200 grams of yellow laundry soap was melted with an equal weight of water containing 0.48 gram of 36% formalin. At 15 minute intervals, 10 c. c. portions of an aqueous solution 'of commercial sodiiun chlorite, each containing 0.1 gram of chlorite, were added until a total of 100 c. c. of the chlorite'solution had been added. During this period, the pH of the solution was about 9.3, no buffer being used. A temperature of about 100 C. was maintained during this period, and thereafter until all of the available chlorite had disappeared, by the passage of steam through the,solution. Thereafter the soap was salted out and was found to be of a very good white color.
  • Example VII For the purpose of illustrating the advantages derived from the use of the aldehyde in my and a still further bleaching of the soap obtained, During these tests, the pH of the soap solution was about 9.3. no buil'er being used.
  • Example VIII A 25 gram piece of acetate rayon fabric was immersed in an aqueous .solution prepared by process, results of'the following experiments are presented To 500 grams of the yellow laundry soap of used in this operation.
  • Example IX To 50 parts of crude brown sugar dissolved in 100 parts of water there was added 20 parts of a solution of sodium chlorite containing 1 part of available chlorine and 0.78 part of a formaldehyde solution containing 0.22 part of CHzO. The mixture was buffered at pH '7 by the presence of a phosphate bufier and was held at 40 0., for 1 hour. At the end of this period the solution was.
  • Example X 118 parts of dark, reddish-brown shellac was dissolved in 11.8 parts of soda ash and 1000 part of water. To 100 parts of this solution there was added 1 part of available chlorine as sodium chlorite in 20 parts of aqueous solution and 0.78 part of a formaldehyde solution containing 0.22 part of 'CHzO. The solution was maintained at a temperature of 40 C. for one hour. No buffer was used and the pH of the solution was between '7 and 8.2. By the end of this period of treatment, the original dark purple colored solution had been bleached to-a light tan.
  • Example XI A small reddish-brown sponge was immersed for 1 hour in 200 parts of an aqueous solution containing 1 part of available chlorine as sodium chlorite and 0.22 part of CHzO. During this period the solution was held at a temperature of 50 0., and at a pH of 6.6 by the use of a buffer. Thereafter the sponge was removed from the bleaching solution, washed and dried and was found to be of a light bufi' color.
  • Example XII To 25 parts of crude corn starch of a greenish tint suspended inwater, there was added 1 part of available chlorine a sodium chlorite dissolved in 20 parts of aqueous solution and 0.22 part of CHzO in 20 parts of aqueous solution, the entire aqueous mixture amounting to 200 parts by weight. This suspension was held at a temperature of 50 C., for 1 hour. At the beginning of this period the pH of the solution was 7 and at the eiid thereof the pH had dropped to about 6.5. The starch was then filtered, washed and dried and was found to be of a pure white color free from any objectionable tints.
  • Example XIII T0 50'- parts of red oil (oleic acid), heated in aboiling water bathto a temperature of about 100 and agitated by the passage of steam therethrough, there was added 0.5 part of available chlorine as sodium chlorite dissolved in parts of water. A solution of 0.25 part of 36% formalin in 10 parts of water was prepared and 1 part of this solution was added at 5 minute intervals until the total had been added. A few minutes after the final addition, all available chlorine had reacted. The fatty acid was then separated and was found to be a well bleached prodnot.
  • the improvement which comprises subjecting the material to be bleached to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of an aldehyde.
  • the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
  • the improvement which comprises admixing the material to be bleached with a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of water and an aldehyde at a pH not less than about '7.
  • the improvement which comprises admixing the material to be bleached with a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of water and an aldehyde and maintaining the hydrogen. ion concentration of the mixture at a pH not less than about '7 by the presence of an alkali metal phosphate buffer,
  • the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than 8 about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
  • the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than about 7 and containing a chlorite of a metal 01' the group consisting of the alkali and alkaline earth metals and an aldehyde.
  • the improvement which comprises subjecting the starch to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
  • the improvement which comprises subjecting the sugar to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
  • the improvement which comprises subjecting the sugar to the action of an aqueous solution having a pH of about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde at a temperature of about 40 C. for a period of about 1 hour.

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  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Textile Engineering (AREA)
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Description

Patented Nov. 11, 1947 2,430,674 7 METHOD or BLEACHING Clifford A. Hampel, Painesville, Ohio, assignor to The Mathieson Alkali Works, Inc., New York, N. Y., a corporation of Virginia No Drawing. Application January 11, 1943, Serial No. 472,052
10 Claims. 1
This invention relates to an improved process for effecting color improvement or bleaching of non-cellulosic organic materials. The invention is applicable to the treatment of a wide variety of such materials including the following: Carbohydrates such as sugar and starch; synthetics such as acetate rayon and nylon; sponges; walnut shells; resins such as shellac; oils, fats, waxes, soaps-and the like and fatty acids, such as oleic acid or red oil.
The application of my present process to the bleaching of cellulosic materials is described and claimed in my copending application Serial No. 414,139, filed October 8, 1941, granted January 23, 1945, as Patent No. 2,367,771, of which my present application is in part a continuation.
In accordance with the process of my present invention, the material to be bleached is subjected hyde in the presence of water. Advantageously, the material being treated is admixed with the chlorite and aldehyde in aqueous solution, the pH of the solution during the bleaching operation generally being maintained at not less than aboutfl.
Various methods have heretofore been proposed for the bleaching of organic materials. Many of such methods have involved the use of acids and other strong chemicals which have a tendency to injure the material being bleached or require very careful, critical control to avoid such injury.
Many of these previously proposed bleaching methods, especially those involving the use of acid solutions, tend to char or cause an undesirable reaction between the organic material and the acid constituent of the solution and are not applicable to the treatment of many materials of this type, particularly soaps or other alkaline reacting materials.
I have discdvered that a wide variety of organic materials, including organic substances such as previously mentioned, can economically be bleached to an exceptionally high degree without substantial degradation or danger of deleteriously affecting their desirable characteristics by subjecting them to the action of a chlorite in an alkaline or substantially neutral aqueous solution in the presence of an aldehyde, as hereinafter more fully described.
The function of the aldehyde in my improved bleaching process appears to be that of activating the chlorite rather than a direct action upon the organic material itself. Thus activated, the chlorites, or reaction products thereof, are enabled to efiect the bleaching of the organic mato simultaneous action of a chlorite and an aldeterial either in an alkaline or substantially neutral environment.
Chlorites useful in my process are those sufficiently soluble in water to provide an adequate concentration to efl'ect the desired bleaching. When the bleaching requirement is relatively low, less soluble chlorites may be used. However, for most purposes, I prefer the chlorites of the alkali and alkaline earth metals, such as sodium chlorite, NaClOz, and calcium chlorite, Ca(C1O2)2.
Various aldehydes may be used, including the aliphatic aldehydes, aromatic aldehydes, other carbocyclic aldehydes and heterocyclic aldehydes. For example, I have found formaldehyde, acetaldehyde, paraformaldehyde, furfural, benzaldehyde, and 5 and 6 carbon atom aldose sugars and inverted sugars to be particularly useful. All of these compounds are characterized by the CH0 group. In addition to those highly soluble in water, the relatively insoluble aldehydes have been found to function satisfactorily in most instances.
Temperatures and concentrations are not usually critical and may be varied over a wide range. Increasing the temperature has generally been found to increase the rate of bleaching. Also, the ratio of chlorite to aldehyde may be widely varied. However, a molar ratio of chlorite to aldehyde of about 1:1 has been found generally useful. I
The optimum operating conditions, with respect. to temperature, concentration and ratio of chlorite to aldehyde, are to a considerable extent interdependent and will vary with the particular material being bleached, the degree of bleaching required, the length of the period of treatment and, to some extent, with the particular chlorite and aldehyde employed.
The temperature best suited for a particular operation will, to a considerable extent, depend upon the nature of the material being treated. Ordinary room temperature may frequently be employed with advantage but higher temperatures are usually desirable when treating a material normally solid where it is desired to effect the melting or solution thereof. Temperatures at which the material being treated becomes unstable or at which the material is deleteriously affected are to be avoided.
Though the hydrogen ion concentration of my improved bleaching solution may be varied over a considerable range, a decided acid condition of the solution is generally to be avoided, as previously noted. Where the material being treated has an acid reaction, I have found it usually desirable to employ a bufferto maintain the solution substantially neutral or on the alkaline side. The use of a buffer having the characteristics and in sufficient quantity to maintain the solution at a pH of about 7 is generally desirable in the treatment of material such as oils and waxes. In the bleaching of soap a higher pH is usually desirable and no bufler need be employed.
Generally satisfactory results have been obtained where the pH is maintained at about '7 or higher, for instance within the range of about '7 to about 11. While solutions having a pH slightly lower than 7 may be used in the treatment of acid materials such as fatty acids and of various other materials with good results, a pH substantially on the acid side should generally be avoided.
Alkali metal phosphates such as the monosodium and disodium orthophosphates have been found to be particularly advantageous buffers for the purpose of the present invention, though other builers may be used with advantage. I have found that in the presence of such phosphates the consumption of chlorite in the bleaching operation is materially reduced, In some instances a saving of 50% of chlorite has been effected by the use of these phosphates, in conjunction with the other constituents of my bleaching solution previously noted.
As applied to the bleaching of oils, fats, waxes, soaps and the like, my invention is particularly useful in the treatment of either natural or synthetic materials of this type, including unsaponifiable petroleum waxes and saponiilable oils and waxes such as beeswax, carnauba wax, candelilla wax, corn oil and soya bean oil. It is especially applicable to the bleaching of soaps and similar alkaline reacting materials.
The consumer market of sugar requires a highly bleached product. Also, in numerous commercial uses of starch, current trade requirements necessitate bleaching and the attainment of a high degree of white while at the same time precluding any substantial chemical reaction with the starch. By my improved process, sugars and starches may be bleached without deleteriously affecting the product or imparting thereto objectionable tastes or odors.
It will be recognized that in a strictly scientific sense there is a great variety of so-called sponges. Some of these are composed of hard. calcareous or siliceous substances. However, the familiar bath sponges which are the remains of marine animals belonging to species of the genera Euspongia and Hippspongia are made up of horny fibers closely resembling silk in composition. It is to the bleaching of the familiar bath sponges which the present invention relates.
In their natural stage these sponges are of a dark color and unattractive appearance. The desirability of bleaching sponges to improve their appearanceand salability has heretofore been recognized. Though sponges have been bleached to a greater or less degree, such color improvement has generally been accomplished at the expense of durability of the sponge if excessive bleaching is effected.
By my improved bleaching method, such sponges may be bleached to an exceptionally high degree with no substantial tendering or weakening of their fiber structure so that their normal resistance to tearing apart in use is not substantially impaired.
The bleaching of starch, in accordance with my present invention, is with advantage enacted by subjecting the starch to the action of the chlorite and the aldehyde while in aqueous suspension. The bleaching of sugar, oils, fats, waxes, soaps, shellac, fatty acid and the like is with advantage effected by treating the material while in a liquid condition, 1. e., either molten or in aqueous solution, depending upon the characteristics of the particular material being treated.
For example, such materials, either molten or in aqueous solution, may be admixed with a chlorite in the presence of water and the aidehyde thereafter added or the material to be treated may be admixed with the aldehyde in the presence of water and the chlorite added to this mixture. The resultant mixture is maintained at a temperature usually ranging from room temperature to about C., for a period of time sumcient to effect the desired bleaching and is thereafter cooled and separated.
In the bleaching of soap, for instance, the soap may be melted by heating in water, the soap solution admixed with an aqueous chlorite solution and the desired amount of aldehyde thereafter added gradually or as a series of small proportions during agitation.
In the treatment of wax or the like, which is solid at normal temperatures, the material is with advantage melted and an aqueous solution of the chlorite and the aldehyde admixed therewith or the chlorite and aldehyde may be separately added.
My invention and its application to the bleaching of various types of non-cellulosic organic materials thereby contemplated will be further illustrated by the following specific examples:
Example I An aqueous solution was prepared by admixing 50 c. c. of pH 7 sodium phosphate buffer solution, 50 c. c. of an aqueous sodium chlorite solution containing 10 grams of available chlorine and 100 c. c. of a dilute aqueous formalin solution containing 2.2 grams of HCHO. 100 grams of soy-bean oil was then admixed with the resultant solution and allowed to stand for 2 hours, at the end of which time much of the original yellow color of the oil had been removed and, upon separation from the solution, a superior product was obtained. During the admixing of the oil with the solution and during the following 2 hour period a pH of about 7 and a temperature of about 25 C. were maintained.
Example [I Beeswax was not only bleached but the texture thereof was made smoother by the following treatment: To 50 grams of beeswax melted in a water bath there was added 50 c. c. of an aqueous pH 7 sodium phosphate buffer solution, 100 c. c. of an aqueous sodium chlorite solution-containing 5 grams of available chlorine as chlorite and 1.9 c. c. of furfural. After admixing the solution and the melted beeswax, the admixture was permitted to stand for 1 hour at a temperature of 60 C. Thereafter, the wax was separated and allowed to solidify. The resultant product was found to have a much lighter 0010 than the original wax.
Example III Cocoabutter was saponified by treatment with caustic soda and 200 grams of the resulting soap was melted with 200 grams of water. 1 gram of sodium chlorite dissolved in an equal weight of water was then added and admixed with the soap solution. This was followed by the addition of c. c. of aqueous formaldehyde solution prepared by dissolving 0.53 gram of 36% formalin in 100 c. c. of water. The addition of 10 ct, c. of
this aqueous formaldehyde solution was repeated at 10 minute intervals until a total of 100 c. c. of the solution had been added. During this, period, the pH of the solution was approximately 9.3, no buffer being used, and the mixture was kept hot (about 100 C.) by the passage of steam therethrough. Thereafter, the bleached soap was cooled and separated. Its color was very white.
Example IV Example V A still further batch of cocoabutter soap was bleached, as described in Example III, except that the 10 c. 0. portions of the formaldehyde solutions were added at minute intervals. Re-
suits comparable with those of Example III were obtained, indicating that the time factor is not critical.
Example VI 200 grams of yellow laundry soap was melted with an equal weight of water containing 0.48 gram of 36% formalin. At 15 minute intervals, 10 c. c. portions of an aqueous solution 'of commercial sodiiun chlorite, each containing 0.1 gram of chlorite, were added until a total of 100 c. c. of the chlorite'solution had been added. During this period, the pH of the solution was about 9.3, no buffer being used. A temperature of about 100 C. was maintained during this period, and thereafter until all of the available chlorite had disappeared, by the passage of steam through the,solution. Thereafter the soap was salted out and was found to be of a very good white color.
Example VII For the purpose of illustrating the advantages derived from the use of the aldehyde in my and a still further bleaching of the soap obtained, During these tests, the pH of the soap solution was about 9.3. no buil'er being used.
Example VIII A 25 gram piece of acetate rayon fabric was immersed in an aqueous .solution prepared by process, results of'the following experiments are presented To 500 grams of the yellow laundry soap of used in this operation.
To 500 grams of the same soap, maintained at its melting point, there was added 2.5 grams of sodium chlorite and 0.932 gram of 36.6% formalin solution. After stirring the mixture for '20 minutes, all available chlorine had disappeared and the soap was well bleached. After removing a 100 gram sample of the soap, an additional 1.25 grams of sodium chlorite and 0.466 gram of formalin was added. After 15 minutes of stirring, the available chlorine had disappeared admixing 250 c. c. of pH '7 phosphate buffer solution, c. c. of aqueous sodium chlorite solution containing 5 grams of available chlorine and c. c. of diluted formalin containing 2.2 grams of CHaO. After an hour's treatment at 60 C., the fabric was removed, rinsed and dried. The color of the fabric was found to-be considerably improved and the original line texture the eof was completely unaffected.
Example IX To 50 parts of crude brown sugar dissolved in 100 parts of water there was added 20 parts of a solution of sodium chlorite containing 1 part of available chlorine and 0.78 part of a formaldehyde solution containing 0.22 part of CHzO. The mixture was buffered at pH '7 by the presence of a phosphate bufier and was held at 40 0., for 1 hour. At the end of this period the solution was.
found to be bleached to a substantially waterwhite color. A check test, under the identical conditions and using the ame quantities of the same reagents except that the formaldehyde was omitted, gave no bleaching whatever. In fact the solution appeared to be slightly darker after the treatment than before.
Example X 118 parts of dark, reddish-brown shellac was dissolved in 11.8 parts of soda ash and 1000 part of water. To 100 parts of this solution there was added 1 part of available chlorine as sodium chlorite in 20 parts of aqueous solution and 0.78 part of a formaldehyde solution containing 0.22 part of 'CHzO. The solution was maintained at a temperature of 40 C. for one hour. No buffer was used and the pH of the solution was between '7 and 8.2. By the end of this period of treatment, the original dark purple colored solution had been bleached to-a light tan.
Example XI A small reddish-brown sponge was immersed for 1 hour in 200 parts of an aqueous solution containing 1 part of available chlorine as sodium chlorite and 0.22 part of CHzO. During this period the solution was held at a temperature of 50 0., and at a pH of 6.6 by the use of a buffer. Thereafter the sponge was removed from the bleaching solution, washed and dried and was found to be of a light bufi' color.
Example XII To 25 parts of crude corn starch of a greenish tint suspended inwater, there was added 1 part of available chlorine a sodium chlorite dissolved in 20 parts of aqueous solution and 0.22 part of CHzO in 20 parts of aqueous solution, the entire aqueous mixture amounting to 200 parts by weight. This suspension was held at a temperature of 50 C., for 1 hour. At the beginning of this period the pH of the solution was 7 and at the eiid thereof the pH had dropped to about 6.5. The starch was then filtered, washed and dried and was found to be of a pure white color free from any objectionable tints.
Example XIII T0 50'- parts of red oil (oleic acid), heated in aboiling water bathto a temperature of about 100 and agitated by the passage of steam therethrough, there was added 0.5 part of available chlorine as sodium chlorite dissolved in parts of water. A solution of 0.25 part of 36% formalin in 10 parts of water was prepared and 1 part of this solution was added at 5 minute intervals until the total had been added. A few minutes after the final addition, all available chlorine had reacted. The fatty acid was then separated and was found to be a well bleached prodnot.
By my improved process, a high degree of bleaching may thus be accomplished with economy in time and chemicals while avoiding deleteriously aifecting the material being treated and the necessity of critical control of time, temperature and concentration heretofore required to avoid injuring the material.
I claim:
1. In the bleaching of non-cellulosic organic materials, the improvement which comprises subjecting the material to be bleached to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of an aldehyde.
2. In the bleaching of non-cellulosic organic materials, the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
3. In the bleaching of non-cellulosic organic materials, the improvement which comprises admixing the material to be bleached with a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of water and an aldehyde at a pH not less than about '7.
4. In the bleaching of non-cellulosicorganic materials, the improvement which comprises admixing the material to be bleached with a chlorite of a metal of the group consisting of the alkali and alkaline earth metals in the presence of water and an aldehyde and maintaining the hydrogen. ion concentration of the mixture at a pH not less than about '7 by the presence of an alkali metal phosphate buffer,
5. In the bleaching of non-cellulosic carbohydrates, the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than 8 about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
6. In the bleaching of sponge, the improvement which comprises subjecting the material to be bleached to the action of an aqueous solution having a pH not less than about 7 and containing a chlorite of a metal 01' the group consisting of the alkali and alkaline earth metals and an aldehyde.
7. In the bleaching of starch, the improvement which comprises subjecting the starch to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
8. In the bleaching of starch, the process which comprises subjecting the starch to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde at a temperature of about 50 C. for a period of about one hour.
9. In the bleaching of sugar, the improvement which comprises subjecting the sugar to the action of a substantially non-acidic aqueous solution of a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde.
10. In the bleaching of sugar, the improvement which comprises subjecting the sugar to the action of an aqueous solution having a pH of about 7 and containing a chlorite of a metal of the group consisting of the alkali and alkaline earth metals and an aldehyde at a temperature of about 40 C. for a period of about 1 hour.
CLIFFORD A. HAMPEL.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS OTHER REFERENCES White et al., Industrial and Engr. Chem., pages 782-792, July 1942.
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GB1796/44A GB576909A (en) 1943-01-11 1944-01-31 Improvements in the bleaching of organic materials
GB1872/44A GB576910A (en) 1943-01-11 1944-02-01 Improvements in the bleaching of organic materials
FR928932D FR928932A (en) 1943-01-11 1946-06-11 Bleaching process
DES19567A DE833943C (en) 1943-01-11 1950-09-26 Process for bleaching organic compounds
DES19908A DE943105C (en) 1943-01-11 1950-09-30 Process for bleaching organic materials other than cellulose

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US2684360A (en) * 1950-08-03 1954-07-20 Courtaulds Ltd Process for the simultaneous stabilization and bleaching of cellulose acetate by the use of sodium chlorite
US2694059A (en) * 1951-05-17 1954-11-09 Hercules Powder Co Ltd Corrosion inhibition in chlorite bleaching of cellulose derivatives
US2694060A (en) * 1951-05-17 1954-11-09 Hercules Powder Co Ltd Process of bleaching cellulose esters with chlorites
US2766121A (en) * 1951-11-14 1956-10-09 Olin Mathieson Process for bleaching and deodorizing meat
US3036936A (en) * 1960-01-14 1962-05-29 Nat Ind Products Company Starch product
US3050359A (en) * 1959-01-17 1962-08-21 Degussa Hexamethylene tetramine activated chlorite bleach
US3063782A (en) * 1960-02-29 1962-11-13 Olin Mathieson Bleaching cellulosic materials
US3257324A (en) * 1955-04-20 1966-06-21 Colgate Palmolive Co Solid bleach composition and method of making and using same
JPS5167472A (en) * 1974-12-06 1976-06-11 Santo Tekkosho Kk Senihinno hyohakuhoho
US4141685A (en) * 1976-07-26 1979-02-27 Manufacture De Produits Chimiques Protex Societe Anonyme Method of bleaching textile fibers and activated bath for the cold bleaching of such fibers
US4157300A (en) * 1976-12-17 1979-06-05 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for the purification of phenol and phenol formaldehyde containing waste water
US4241093A (en) * 1978-05-11 1980-12-23 U and I, Incorporated Food supplement from vegetable pulp and method of preparing same
US4992288A (en) * 1987-06-04 1991-02-12 American Crystal Sugar Company Method of removing sulfite from sugarbeets
US5112638A (en) * 1989-09-11 1992-05-12 American Crystal Sugar Company Process for the improvement of edible fiber and product
US5137744A (en) * 1989-09-11 1992-08-11 American Crystal Sugar Company Process and system for the improvement of edible fiber and product
US5599571A (en) * 1989-12-06 1997-02-04 Estrada; Joe J. Process for preserving leafy produce
US20090226583A1 (en) * 2008-03-05 2009-09-10 Joe Jess Estrada Compositions and methods for reducing spoilage of leafy produce

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FR955483A (en) * 1946-12-21 1950-01-14
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DE4329959A1 (en) * 1993-09-04 1995-03-16 Hoechst Ag Alkaline chlorite bleach

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FR584738A (en) * 1924-11-18 1925-02-12 Preparation of fatty acids and their alkaline combinations
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US1435332A (en) * 1921-07-18 1922-11-14 Kohnstamm & Co Inc H Laundering method and material
US1880046A (en) * 1930-09-06 1932-09-27 Brown Co Processing of cellulose fiber
US2022262A (en) * 1932-02-19 1935-11-26 Mathieson Alkali Works Inc Stain removal
US2220426A (en) * 1937-08-28 1940-11-05 Aldox Corp Method of treating cellulose fibers
US2343048A (en) * 1940-08-03 1944-02-29 Anheuser Busch Process of bleaching starch

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2684360A (en) * 1950-08-03 1954-07-20 Courtaulds Ltd Process for the simultaneous stabilization and bleaching of cellulose acetate by the use of sodium chlorite
US2694059A (en) * 1951-05-17 1954-11-09 Hercules Powder Co Ltd Corrosion inhibition in chlorite bleaching of cellulose derivatives
US2694060A (en) * 1951-05-17 1954-11-09 Hercules Powder Co Ltd Process of bleaching cellulose esters with chlorites
US2766121A (en) * 1951-11-14 1956-10-09 Olin Mathieson Process for bleaching and deodorizing meat
US3257324A (en) * 1955-04-20 1966-06-21 Colgate Palmolive Co Solid bleach composition and method of making and using same
US3050359A (en) * 1959-01-17 1962-08-21 Degussa Hexamethylene tetramine activated chlorite bleach
US3036936A (en) * 1960-01-14 1962-05-29 Nat Ind Products Company Starch product
US3063783A (en) * 1960-02-29 1962-11-13 Olin Mathieson Bleaching cellulosic materials
US3063782A (en) * 1960-02-29 1962-11-13 Olin Mathieson Bleaching cellulosic materials
JPS5167472A (en) * 1974-12-06 1976-06-11 Santo Tekkosho Kk Senihinno hyohakuhoho
JPS538827B2 (en) * 1974-12-06 1978-04-01
US4141685A (en) * 1976-07-26 1979-02-27 Manufacture De Produits Chimiques Protex Societe Anonyme Method of bleaching textile fibers and activated bath for the cold bleaching of such fibers
US4157300A (en) * 1976-12-17 1979-06-05 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for the purification of phenol and phenol formaldehyde containing waste water
US4241093A (en) * 1978-05-11 1980-12-23 U and I, Incorporated Food supplement from vegetable pulp and method of preparing same
US4992288A (en) * 1987-06-04 1991-02-12 American Crystal Sugar Company Method of removing sulfite from sugarbeets
US5112638A (en) * 1989-09-11 1992-05-12 American Crystal Sugar Company Process for the improvement of edible fiber and product
US5137744A (en) * 1989-09-11 1992-08-11 American Crystal Sugar Company Process and system for the improvement of edible fiber and product
US5599571A (en) * 1989-12-06 1997-02-04 Estrada; Joe J. Process for preserving leafy produce
US20090226583A1 (en) * 2008-03-05 2009-09-10 Joe Jess Estrada Compositions and methods for reducing spoilage of leafy produce

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