Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
  • D21H13/36—Inorganic fibres or flakes
  • D21H13/38—Inorganic fibres or flakes siliceous
  • D21H13/42—Asbestos
• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
  • C04B20/02—Treatment
  • C04B20/08—Defibrillating asbestos
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H5/00—Special paper or cardboard not otherwise provided for
  • D21H5/12—Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials
  • D21H5/18—Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials of inorganic fibres with or without cellulose fibres
  • D21H5/183—Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials of inorganic fibres with or without cellulose fibres of asbestos fibres

Definitions

• United States Patent a The invention relates to the processing of asbestos. It aims to provide a simple, inexpensive yet completely novel method for: (1')" opening up aggregates of fibers of ord nar'y asbestos, releasing a large proportion ofthe constituent long fibrils of very small diameter (of the order of several hundred angstroms), and making possible a more homogeneous and highly dispersed slurry of asbestos fibrils and fibril aggregates whereby the use of asbestos may be "facilitated and enhanced, particularl in the formation of papers'of high purity, uniform texture, and 1ncreased absorbency properties, and (2) to reduce substantially the energy requirements for the conversion of asbestos, chemically pretreated by the method disclosed in my co-pending U.S. application Ser. No. 436,304, into stablecolloidalgels and dispersions containing a significant proportion of particles less than one micron in maximum dimensions.
• asbestos is recovered from veins of rock such as deposits of serpentine by mechanical crushing and screen classification procedures.
• the resulting commercial fibrous asbestos consists largely of bundles of fibers, including tightly bound clusters of fibers called pencils because of their rigidity; these are the components in ordinary asbestos which give it a coarse hand.
• the "fibers in turn consist of fibrils having diameters of the order of 200-300 A, thousands going into each fiber. It is possible to break up pencils into fibers by further severe mechanical action approaching that of carding textile yarns, but only a very small percentage, if any, of the thousands of fibrils that make up a single asbestos fiber can be freed in this manner.
• DMSO dimethylsulfoxide
• dispersion of the slurry with the attendant release of individual fibrils or fibril fragrnents, respectively, may be aided by treatment of the DMSO slurry in a Simple pulping device such as a beater or a Bauer refiner to provide the appropriate mild mechanical action desired.
• a Simple pulping device such as a beater or a Bauer refiner to provide the appropriate mild mechanical action desired.
• the exces DMSO is separated from the opened-up asbestos as by centrifuge, filter, or squeeze rolls, and asbestos Washed free of DMSO, dried, and packaged ready for use.
• the preferred treatment for soaking or slurrying is to use the DMSO undiluted, dilution with water or any miscible solvent is operable.
• the DMSO, either undiluted or diluted may be also reused for the steeping and/or slurrying treatments' inasmuch as there is no evidence that it is' significantly changed chemically during the soaking or slurry steps.
• the rate. of dispersing the fibrils may be enhanced, although operating temperatures of the order of' degrees 'centigrade or less are preferred. Soak or slurry times of only 15 minutes are usually adequate, although much longer times may be de: sirable in some instances depending on the natural compactness of the fibril aggregations. Inasmuch as time and temperature are not critical, they can be varied to suit the convenience of the operator.
• DMSO has beenfound also to be uniquely effective in the chemical pretreatment and modification of asbestos to produce microcrystalline asbestos, as disclosed in my copending application Ser. No. 436,304, wherein asbestos is treated with dilute acid to affect the appropriate chemical modification which makesthe asbestos receptive to an identical manner with 0.4 M HCl alone.
• the raw material may be commercial asbestos as normally received, or it may be highly opened asbestos that has been further treated to loosen the pencils and fiber bundles by mechanical means such as by a hammer mill or the like.
• a raw material comprising ordinary mechanically open asbestos
• it may be added to a beater or other vessel equipped with appropriate stirring facilities and possessing a heating jacket to control temperature; preferably the vessel may be an autoclave or a digester, closed at the top to prevent contamination.
• the slurry may be passed through a disintegrator such as Bauer refiner or treated in a Cowles'dissolver to affect a still further dispersion of the fibers into individual fibrils.
• the bulk of the DMSO is then separated mechanically from the opened-up asbestos, and recovered forte-use.
• the DMSO remaining on theasbestos is washed from it with water (other solvents for DMSO may be used), and the DMSO recovered from the wash liquors, by steam distillation or other means. Removal of impurities from the raw asbestos after the DMSO soak and/or slurry to produce a final product of outstanding purity may be done by flotation, or by electromagnetic separation, or sedimentation using an appropriately diluted slurry prior to final filtration, drying and packaging.
• Products produced in the foregoing manner are espe cially advantageous for the manufacture of asbestos papers, and self-supporting asbestos films having remarkable softness and fiexilibity because of the high proportion of fibrils in the paper web, yet the dimensional stability of the inherent asbestos composition is maintained.
• the absorbency of such papers for impregnation with plastic prepolymers for the manufacture of decorative laminates or laminated plastic structures is improved.
• Asbestos highly opened in this manner also is particularly useful as a viscosity builder for polar liquids such as glycerine, ethylene glycol, etc.
• the DMSO treatment makes possible the formation of smooth, stable colloidal dispersions and gels, free of any ropiness due to the presence of the long fibrils because the combination of chemical pretreatment and mechanical disintegration produces much shorter fibril fragments, a large percentage of them being under one micron in maximum dimension by contrast the fibrils freed using ordinary, untreated as- Chrysotile asbestos, recovered by the mechanical disintegration of serpentine rock, and further opened by mechanical crushing and sieving techniques such as to have a surface area of about 30 square meters per gram was slurried in a pulp beater as follows: 180 pounds was added to 820 pounds of dimethylsulfoxide in the beating vessel, and agitated at 100 r.p.m., for minutes at room temperture degrees centigrate).
• the resulting slurry was centrifuged, and the effluent diverted to the DMSO recovery unit along with the water used to wash the product free of DMSO.
• the asbestos cake recovered from the centrifuge contained a large proportion of free asbestos fibrils having diameters in the 200-300 angstrom range, and lengths averaging several millimeters in length.
• the cake was then redispersed at low consistencyonly 0.2%with water in a paper beater, and paper made from this product on a conventional Fourdrinier machine,
• the resulting paper possessed an unusual soft texture, smooth surface, and absorbed a solution of melamine formaldehyde prepolymer rapidly.
• the excess DMSO-water was squeezed out to produce a paste of 30% solids, and this paste was passed through a Bauer refiner at /2 mm. clearance.
• the attrited paste was slurried in water, filtered, and the wash water was retained to permit DMSO recovery.
• the filtered product was oven dried and packaged as a low-density flour, or powder.
• the chemical modification useful to produce microcrystalline material involves an increase in the silica to magnesia ratio so that the ratio is between about 1.05:1 and 1.30:1 by weight.
• This range of ratio is obtained by proper selection of acid concentration and time.
• the necessary acid concentration varies with the concentration of asbestos in the slurry increasing slightly as the concentration is increased. This is due to the fact that the asbestos has some material alkalinity which absorbs a portion of the acid before it can work chemically on the fiber itself.
• Example 3 Treatment of low grade asbestos fines
• Thirty-five pounds of Coalinga chrysotile asbestos were charged with 65 pounds of DMSO into a soaking kettle, and held 60 minutes at 80 degrees centigrade, with mild agitation.
• the mass was centrifuged, put through a Bauer refiner at /2 mil clearance, Washed free of DMSO, spray dried and packaged.
• the product was completely open, and contained a large proportion of the constituent platelet having a diameter of about 200-400 angstrom units. This ultra-fine form of asbestos was effective as a fiocullant for sewage densification.
• Example 4 Microcrystalline asbestos A long fiber premium grade chrysotile was pretreated with 0.4 M hydrochloric acid at 10% solids for 25 minutes at degrees centigrade, and the product was washed and dried. The dried product was fed through a hammer mill to open it up mechanically, then added to a soaking kettle where water and DMSO were added to form a 10% paste of the asbestos in 50:50 water-DMSO. The material was agitated at 100 rpm. for 60 minutes at room temperature after which the excess DMSO was squeezed out, washed free of DMSO in a washing tank and fed at 30% solids through a Rietz extractor during which intense mechanical working of the asbestos occurred as evidenced by the asbestos becoming very hot.
• the attrited paste was reduced to a 2% slurry in a mixing tank and put through an electromagnetic separator to remove the iron oxide and dried in a drum drier.
• the product contained at least 15 percent of particles under one micron in size, and made excellent thixotropic dispersions in water and organic phosphates, silicone oils, esters and alcohols.
• Example 5 Commercial chrysotile asbestos of intermediate fiber length was fed into a soaking kettle with water and DMSO to produce a paste in a 75% DMSO-% water mixture. The mixture was agitated at 200 r.p.m. for 120 minutes at room temperature, filtered, washed free of DMSO in a washing tank and purified in a flotation tank after which it was made up into a 2% slurry in a beater. When made into paper, the product was exceptionally white, and performed most effectively as base paper of high dimensional stability and ideal absorbency for water color paintings.
• Example 6 A- low grade highly mechanically opened commercial ohrysotile was fed into a soaking kettle along with DMSO, water and hydrochloric acid to produce a 10% paste in a 25% DMSO-75% water mixture containing sufficient acid to produce a 0.4 molar solution. It should be noted that there is sufiicient alkalinity in the asbestos to neutralize a portion of this hydrochloric acid so that the effective amount of acid is lowered to produce about the same activity as 0.2 molar acid on a 5% basis. The mixture was agitated at 100 r.p.m. for 50 minutes at 100 degrees centigrade after which it was centrifuged, washed free of DMSO in a slurry washing tank and oven dried.
• the product contained substantial percentages of microcrystalline asbestos under one micron in particle size.
• the mechanical action in the centrifuge and in the slurrying tank in the presence of DMSO was sufficient to break up the product sufficiently so that a sufiicient amount of sub-micron particles was formed to produce a stable colloidal dispersion in water.
• Example 7 --Microcrystalline asbestos A long fiber ohrysotile was dry fluffed in a large Waring Blendor and was soaked in DMSO, water and hydrochloric acid to product a 10% paste in a DMSO- 70% water mixture containing sufiicient acid to yield a 0.4 M solution. It was heated at 100 degrees centigrade at 150 rpm. for 30 minutes after which the product was filtered, washed free 'of water and dried in a drum dryer.
• This product like the product of the last example and the other acid treated products of Examples 2 and 4 were obtained in yields of about 85-90% based on the original asbestos and contained a ratio of Si0 to MgO higher than that in original asbestos.
• Example 8 Commercial ohrysotile of an intermediate grade was dry fiuffed in a Reitz distintegrator and soaked at 12% concentration with an DMSO-20% water mixture. Agitation was at 150 rpm. and continued for minutes at 50 degrees centigrade. The material was put into squeeze rollers, washed with DMSO, put into a tank and spray dried. The resultant product contained a large proportion of fibrils in the A. diameter range.
• the method of opening up asbestos which comprises submitting it to mechanical action in a slurry with dimethylsulfoxide for a time sufficient to allow the dimethylsulfoxide to penetrate through the asbestos mass and for the mechanical action to largely separate the asbestos into fibrils with a diameter of the order of a few hundred angstrom units, and thereafter washing the asbestos free of dimethylsulfoxide.
• the method of producing microcrystalline asbestos having a large proportion of particles under one micron in largest dimension which comprises treating asbestos with dilute acid to increase the ratio of silica to magnesia to between about 1.05:1 and 1.30:1 by weight, and submitting it to mechanical action in a slurry with dimethylsulfoxide for a time sufficient to allow the dimethylsulfoxide to penetrate through the asbestos whereby the product is opened up and largely converted to a material of submicron particle size, and thereafter washing the asbestos free of dimethylsulfoxide.
• the method of opening up asbestos which comprises submitting said asbestos soaked in dimethylsulfoxide in an amount suflicient to aid in the opening of said asbestos to mechanical action, continuing the mechanical action to obtain asbestos particles and fibrils: ranging from less than a micron to a few hundred angstrom units in their largest dimension, and then washing the asbestos free of dimethylsulfoxide.

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• Chemical & Material Sciences (AREA)
• Inorganic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Ceramic Engineering (AREA)
• Materials Engineering (AREA)
• Structural Engineering (AREA)
• Organic Chemistry (AREA)
• Paper (AREA)
• Processing Of Solid Wastes (AREA)

Priority Applications (6)

Applications Claiming Priority (1)

Publications (1)

Family

ID=23904742

Family Applications (1)

Country Status (6)

Cited By (2)

Citations (3)

• 1965
  • 1965-08-13 US US479620A patent/US3410751A/en not_active Expired - Lifetime
• 1966
  • 1966-05-25 GB GB23324/66A patent/GB1156221A/en not_active Expired
  • 1966-07-29 FR FR71521A patent/FR1529562A/fr not_active Expired
  • 1966-08-03 DE DE19661571480 patent/DE1571480A1/de active Pending
  • 1966-08-10 BE BE685327D patent/BE685327A/xx unknown
  • 1966-08-12 NL NL6611412A patent/NL6611412A/xx unknown

Patent Citations (3)

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