US3489586A - Clay treatment - Google Patents

Clay treatment Download PDF

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Publication number
US3489586A
US3489586A US620229A US3489586DA US3489586A US 3489586 A US3489586 A US 3489586A US 620229 A US620229 A US 620229A US 3489586D A US3489586D A US 3489586DA US 3489586 A US3489586 A US 3489586A
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United States
Prior art keywords
kaolin
clay
brightness
bleaching
oxidizing agent
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Expired - Lifetime
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US620229A
Inventor
John H Chapman
Padraic Partridge
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Georgia Kaolin Co
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Georgia Kaolin Co
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Publication date
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Publication of US3489586A publication Critical patent/US3489586A/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/10Eliminating iron or lime
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/04Clay; Kaolin
    • C04B33/06Rendering lime harmless
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/30Drying methods

Definitions

  • This invention relates to clay treatment and particularly to a method of reclaiming those kaolins which have heretofore been considered of such poor color that no treatment would render them fit for use in those industrial applications requiring a reasonable degree of whiteness, e.g., paper coating and filling, paint and rubber fillers and ceramics.
  • this large group of kaolins has an original color (unbleached) of such poor quality that not enough increase can be obtained by any bleaching step heretofore practiced in the kaolin field to warrant its being mined, or more important, to meet any customer specifications.
  • any bleaching step heretofore practiced in the kaolin field to warrant its being mined, or more important, to meet any customer specifications.
  • the original color (unbleached) is good but the kaolin fails to respond to any of the conventional bleaching steps, normally used to bring a normal kaolin up to standard specifications.
  • Our process consists in the addition of an oxidizing agent, such as a per compound or a chlorate or hypochlorite, to a clay to be treated. Holding the clay until oxidation reactions have effectively ceased and then bleaching by any of the standard kaolin bleaching techniques e.g.,
  • any of the per compounds such as peroxides, perborates, perchlorates, the chlorates and the hypochlorites are very effective in our process.
  • EXAMPLE I A kaolin fraction of less than 2 microns E.S.D. with an unbleached brightness of 74.2 and a bleached brightness, by conventional reducing bleaching techniques, of 74.2 was slurried and treated as in Example I to produce an unbleached brightness following oxidation pretreatment of 86.0 and after final bleach with Na S O a final brightness of 86.6.
  • EXAMPLE III A kaolin fraction of 80% less than 2 microns BSD. and an unbleached brightness of 81.5 was bleached in the conventional manner with Na S O to produce a final brightness of 83.0. Another slurry of the same clay was pretreated according to our process with sodium hypochlorite to produce an unbleached brightness of 83.0. The pretreated clay was then bleached with Na S O to produce a final brightness of 85.5.
  • EXAMPLE IV The same clay from Example III was treated with sodium chlorate to produce an unbleached brightness of 82.5 and thereafter bleached with Na S O to a final brightness of 85.0.
  • EXAMPLE V A clay of 80% less than 2 microns with an unbleached brightness of 82.6 and a bleached brightness (using Na S- O in conventional manner) of 85.4 (normally acceptable in the trade), was treated by our process using hydrogen peroxide to an unbleached brightness of 85.5 and thereafter bleached with conventional practices using Na S O to a final brightness of 88.6.
  • the method of treating white and discolored white kaolin to improve its brightness and color comprising the steps of forming a slurry of a fraction of said kaolin having 80% below 2 microns E.S.D., adding to said clay an 3 oxidizing agent, permitting said oxidizing agent to react with said clay and thereafter bleaching said kaolin with a reducing bleaching agent.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Detergent Compositions (AREA)

Description

United States Patent US. Cl. 106-288 6 Claims ABSTRACT OF THE DISCLOSURE A clay treatment method for improving whiteness by adding an oxidizing agent to a slurry of the clay and thereafter bleaching with a reducing bleaching agent.
This invention relates to clay treatment and particularly to a method of reclaiming those kaolins which have heretofore been considered of such poor color that no treatment would render them fit for use in those industrial applications requiring a reasonable degree of whiteness, e.g., paper coating and filling, paint and rubber fillers and ceramics.
It is well known in the kaolin industry that there are numerous large deposits of kaolin that have heretofore gone unclaimed due to their poor response to normal bleaching techniques for kaolin. The normal reducing type bleaching agents used in the kaolin industry have very little if any effect on the pigment whiteness or brightness of these clays.
In general, this large group of kaolins has an original color (unbleached) of such poor quality that not enough increase can be obtained by any bleaching step heretofore practiced in the kaolin field to warrant its being mined, or more important, to meet any customer specifications. There are also a few instances where the original color (unbleached) is good but the kaolin fails to respond to any of the conventional bleaching steps, normally used to bring a normal kaolin up to standard specifications.
We have discovered a process which makes it possible to bring these poorly colored clays up to the specifications for color which are generally used in the kaolin trade. We have found that, if these clays are given a unique pretreatment prior to the normal bleaching step, a quality clay capable of meeting customer specifications for color can be had. We discovered, surprisingly, that by treatment of these clays with an oxidizing agent we are able to so alter the clay that the subsequent addition of the normal reducing bleaching agents will be effective to produce a clay whose whiteness meets normal customer specifications in the trade.
We have also found that working the clay prior to pre treatment and bleaching would effectively raise the whiteness and brightness upon bleaching.
Our process consists in the addition of an oxidizing agent, such as a per compound or a chlorate or hypochlorite, to a clay to be treated. Holding the clay until oxidation reactions have effectively ceased and then bleaching by any of the standard kaolin bleaching techniques e.g.,
Na S2O4, ZHS2O4, etc.
We have found that any of the per compounds such as peroxides, perborates, perchlorates, the chlorates and the hypochlorites are very effective in our process. For example, we have used hydrogen peroxide, sodium peroxide, sodium perborate, sodium perchlorate, sodium chlorate, sodium hypochlorite and other members of this group with unique success. We have discovered that the precise amount of oxidizing agent, the pH, the time and temperature will vary from clay to clay and should be determined on a small fraction of a given clay prior to beice ginning an extended mill run. However, we have found no case where the technique here described was not effective to improve the whiteness and brightness of the kaolin treated. We have worked in both acid and alkaline slurries of kaolin with equal success and at temperatures up to 100 C. and at times from 30 minutes to 72 hours and have obtained improvement in every case. However, the maximum improvement will be obtained if a check is first made to determine the optimum condition as outlined above.
This invention can perhaps best be illustrated by referring to the following examples.
EXAMPLE I EXAMPLE II A kaolin fraction of less than 2 microns E.S.D. with an unbleached brightness of 74.2 and a bleached brightness, by conventional reducing bleaching techniques, of 74.2 was slurried and treated as in Example I to produce an unbleached brightness following oxidation pretreatment of 86.0 and after final bleach with Na S O a final brightness of 86.6.
EXAMPLE III A kaolin fraction of 80% less than 2 microns BSD. and an unbleached brightness of 81.5 was bleached in the conventional manner with Na S O to produce a final brightness of 83.0. Another slurry of the same clay was pretreated according to our process with sodium hypochlorite to produce an unbleached brightness of 83.0. The pretreated clay was then bleached with Na S O to produce a final brightness of 85.5.
EXAMPLE IV The same clay from Example III was treated with sodium chlorate to produce an unbleached brightness of 82.5 and thereafter bleached with Na S O to a final brightness of 85.0.
The effectiveness of our method in improving a normally acceptable kaolin is illustrated in the following example.
EXAMPLE V A clay of 80% less than 2 microns with an unbleached brightness of 82.6 and a bleached brightness (using Na S- O in conventional manner) of 85.4 (normally acceptable in the trade), was treated by our process using hydrogen peroxide to an unbleached brightness of 85.5 and thereafter bleached with conventional practices using Na S O to a final brightness of 88.6.
We have, in the foregoing specification, given certain preferred practices and techniques of our invention; however, it will be understood that this invention may be otherwise embodied within the scope of the following claims.
We claim:
1. The method of treating white and discolored white kaolin to improve its brightness and color comprising the steps of forming a slurry of a fraction of said kaolin having 80% below 2 microns E.S.D., adding to said clay an 3 oxidizing agent, permitting said oxidizing agent to react with said clay and thereafter bleaching said kaolin with a reducing bleaching agent.
2. The method of treating kaolin as claimed in claim 1 wherein the oxidizing agent is selected from the group consisting of per compounds, chlorates and hypochlorites.
3. The method of treating kaolin as claimed in claim 1 wherein the oxidizing agent is hydrogen peroxide.
4. The method of treating kaolin as claimed in claim 1 wherein the oxidizing agent is sodium hypochlorite.
5. The method of treating kaolin as claimed in claim 1 wherein the oxidizing agent is sodium chlorate.
References Cited UNITED STATES PATENTS 11/1967 Duke 106-72 1/1967 Mercade 10672 JAMES E. POER, Primary Examiner U.S. Cl. X.R.
US620229A 1967-03-03 1967-03-03 Clay treatment Expired - Lifetime US3489586A (en)

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US62022967A 1967-03-03 1967-03-03

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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3861934A (en) * 1972-06-13 1975-01-21 Engelhard Min & Chem Method for improving the brightness of kaolin clay
US4190632A (en) * 1976-03-10 1980-02-26 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for treating air-borne (metallic) dusts containing silicon dioxide to form precipitated silicic acids and silicates
US4226837A (en) * 1976-11-11 1980-10-07 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for converting silicon dioxide containing waste flue dust to crystalline zeolitic molecular sieves of type Y with a Faujasite structure
US4310496A (en) * 1976-11-11 1982-01-12 Degussa Process for converting silicon dioxide containing waste flue dust to crystalline zeolitic molecular sieves of type A
US4618374A (en) * 1985-03-29 1986-10-21 Georgia Kaolin Company, Inc. High solids processing of kaolinitic clays with post-leaching oxidation
US4935391A (en) * 1989-03-31 1990-06-19 Fmc Corporation Process for preparing a purified mineral coating
US5342443A (en) * 1993-04-06 1994-08-30 Engelhard Corporation Method for bleaching kaolin clay
CN110436473A (en) * 2019-08-27 2019-11-12 陕西国防工业职业技术学院 A kind of coal slime activation method for capableing of iron-removal and whitening

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3301695A (en) * 1965-05-19 1967-01-31 Minerals & Chem Philipp Corp Mineral bleaching process
US3353668A (en) * 1963-12-16 1967-11-21 Mineral & Chemicals Philipp Co Method for improving the brightness of clay

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3353668A (en) * 1963-12-16 1967-11-21 Mineral & Chemicals Philipp Co Method for improving the brightness of clay
US3301695A (en) * 1965-05-19 1967-01-31 Minerals & Chem Philipp Corp Mineral bleaching process

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3861934A (en) * 1972-06-13 1975-01-21 Engelhard Min & Chem Method for improving the brightness of kaolin clay
US4190632A (en) * 1976-03-10 1980-02-26 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for treating air-borne (metallic) dusts containing silicon dioxide to form precipitated silicic acids and silicates
US4226837A (en) * 1976-11-11 1980-10-07 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for converting silicon dioxide containing waste flue dust to crystalline zeolitic molecular sieves of type Y with a Faujasite structure
US4310496A (en) * 1976-11-11 1982-01-12 Degussa Process for converting silicon dioxide containing waste flue dust to crystalline zeolitic molecular sieves of type A
US4618374A (en) * 1985-03-29 1986-10-21 Georgia Kaolin Company, Inc. High solids processing of kaolinitic clays with post-leaching oxidation
US4935391A (en) * 1989-03-31 1990-06-19 Fmc Corporation Process for preparing a purified mineral coating
US5342443A (en) * 1993-04-06 1994-08-30 Engelhard Corporation Method for bleaching kaolin clay
CN110436473A (en) * 2019-08-27 2019-11-12 陕西国防工业职业技术学院 A kind of coal slime activation method for capableing of iron-removal and whitening

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