US1978022A - Rubber asphalt dispersion - Google Patents

Rubber asphalt dispersion Download PDF

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Publication number
US1978022A
US1978022A US496041A US49604130A US1978022A US 1978022 A US1978022 A US 1978022A US 496041 A US496041 A US 496041A US 49604130 A US49604130 A US 49604130A US 1978022 A US1978022 A US 1978022A
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Prior art keywords
dispersion
rubber
bitumen
asphalt
fibrous
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US496041A
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Kirschbraun Lester
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Patent and Licensing Corp
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Patent and Licensing Corp
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L7/00Compositions of natural rubber
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch
    • C08L95/005Aqueous compositions, e.g. emulsions

Definitions

  • This invention is concerned with the art of manufacturing waterproof fibrous products, and is directed particularly to improvements inthe art of producing stocks, composed of fibrous pulp 5 and waterproofing materials in admixture therewith, in condition rendering the same readily susceptible to felting on standard-types of paper making machinery.
  • any suitable or desired grade of rubber may-be employed, 'such for example as paleor brown crepe, smoked sheet, or the like and in order to efiect dispersions thereof in teeter, the rubber is first subjected to a preliminary plasticization which may be accomplished conveniently by subjecting a mass of the rubber to the action of a rubber roll mill of the standard and well known types. This action of the rubber may be continued until the desired degree of plasticity is imparted to the rubber, the time required for this purpose varying from twenty to eighty or more minutes depending upon the toughness and other characteristics of the particular rubber employed.
  • the skilled op--- erator will be able to recognize when this condition of the rubber is attained by its compara tive softness, and. its ability to retain to a degree the form to which it is stretched, compressedor otherwise manipulated by the fingers.
  • the rubber may then be transferred to a kneading or masticating machine containing a relatively thick aqueous paste of colloidal material such for example as may be prepared by hydrating a colloidal clay such as bentonite with five to ten times its weight of water.
  • the kneading or masticating machine is preferably ofthe two-blade type, with the blades'rotating at different speeds, and preferably also is provided with'jackets for circulation of steam or other temperature regulatingmedium.
  • This machine may consist of the well-known Wemer-Pfieiderer 1o. mixer.
  • the prepla'sticized rubber may conveniently be dispersed in the aqueous paste with the vresult that a rather viscous or pasty dispersion containing three to ten parts by weight of rubber for each part of bentonite, and from 40 to 60% by weight of water is produced. It is to be understood, however, that any other suitable method of dispersing-the rubber in water. may be employed.
  • the aqueous dispersion of rubber in its thick' pasty condition as it comes from the kneading or masticating machine is then employed as a media. for effecting dispersion of the bitumen therein.
  • the bitumen may comprise asphalt of 100 to 200 F. melting point, or any equivalent heat liquefiable bituminous substance that may be desired.
  • the rubber dispersion is placed in a suitable emulsifier or retained in the same apparatus and if necessary or desired may be adjusted to the desirable hydrogen ion concentration for the particular bitumen to be dispersed whereupon the bitumen in molten and fluid condition is fed gradually into the emulsifier as rapidly as it can be assimilated by the rubber dispersion in the emulsifier under the attenuating action of the agitating blades.
  • additional quantities of water may be fed to the emulsifier to maintain the mass therein at the proper viscosity for promotion of the interfacial trituration necessary to bring about the attenuation and subdivision of the bitumen into finely divided parti cles.
  • the dispersion system'thus produced may contain 20 to 30% rubber, 20 to 30% bitumen and 40 to water. I believe, though I do not wish this belief to be taken as confining the scope of the invention, that in the final dispersion system as thus produced. there are two separate internal phases, one of rubber and the other of bitumen, the clay colloid being adsorbed main- ,ly on the surfaces of the rubber particles, and
  • the hereinabove described method of securing rubber and bitumen in aqueous dispersion involves substantially the same plant equipment and labor-which would be required to make separately a dispersion of rubber and a dispersion of the bitumen, and possesses the distinct advantage of avoiding the labor and trouble normally incurred in mixing the separately prepared dispersions of rubberand of bitumen to, produce'the combined system.
  • the rubber-bitumen dispersion system produced as described is capable of ready admixture with fibrous stock'for the formation of waterproof sheets or boards on well known types of paper making machines.
  • the dispersion system may be incorporated with any desired fibrous pulp, either inthe beaters or in the stuff chest and with slight agitation the whole mass may be made uniform as to distribution .of the dispersed material in the aqueous pulp.
  • the relative quantities of dispersion and fibrous material will manifestly vary within wide limits depending upon the characteristics desired in the final product. In general, however, the quantity of dispersion employed for admixture with the fibrous stock will be such that the combined dry weight of rubber and of bitumen will range upwardly to' 60% of the dry weight of thefinished product.
  • a suitable precipitant such as lime
  • alum or sodium silicate and alum may be added to the mixture to cause the dispersed particles to then be converted into the desired articles by.
  • the prdess which comprises effecting Elispersion of rubber in an aqueous paste of 'a colloidal clay, and subsequently effecting dispersion of a normally non-fluid bitumen in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for philic colloid, and subsequently efiecting dispersion of asphalt in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for the asphalt.

Description

Patented Oct. 23, 1934* UNITED. STATES PATENT oFFicE mesne assignments, to
The Patent and Licensing Corporation, New York, N. Y., a corporation of Massachusetts No Drawing. Application November 15, 1930, Serial No. 496,041
This invention is concerned with the art of manufacturing waterproof fibrous products, and is directed particularly to improvements inthe art of producing stocks, composed of fibrous pulp 5 and waterproofing materials in admixture therewith, in condition rendering the same readily susceptible to felting on standard-types of paper making machinery.
in prior patents Ihave disclosed methods of incorporating normally non-fluid, heat-liquefiable bitumens such as asphaltwith fibrous stock, by first effecting a dispersion of the bitumen in water and mixing the dispersion with the fibrous pulp in the heaters or the stuff chests of the paper making machines to produce a stock which is capable of being felted into paper formation, dried,- and calendered, all without incurring gumming or sticking of the bitumen to the paper making instrumentalities. Various adaptions of this general process are disclosed in my previous Patents Nos. 1,536,399, 1,725,645, 1,725,647, 1,722,434. These processes have gone into extensive use for the manufacture of water-resistant sheets, boards and other articles.
For certain articles, however, it is desirable to produce a sheet having homogeneously incorporated therein, substantial quantities of rubber in addition to substantial quantities of bitumen.
To this end, it has been proposed to combine dispersions of asphalt, such as' might be made by processes described in earlier patents of mine, with rubber latex, or with an artificially prepared dispersion of rubber, and then to mix the combined dispersions with fibrous pulp and felt the mixture on a paper making machine. It has been observed, however, that when an attempt is made to combine a dispersionof bitumen such as asphalt, with a dispersion of rubber, there is a marked tendency in many instances for the asphalt dispersion to cause breaking, or at least an excessive premature flocculation of the rubber dispersion, particularly so when rubber latex is employed, and it is necessary therefore to resort to special precautions in order to bring about 'a satisfactory combination of the rubber dispersion with the bituminous dispersion.
It is one of the objects of my present invention to provide a process of procuring a combination of rubber and a bituminous substance in the form of a dispersion which can readily be mixed with fibrous pulp of any desired character, for fabrication on standard types of paper making machines, into homogeneous sheets or boards having the bitumen and the rubber uniformly disseminated therethrough in the form of continuous films coating and surrounding the fibers.
Without intending to restrict the invention, be.- yond what may be required by the prior art my present invention briefly stated, consists in first 8 making an artificial dispersion of rubber, then em'-. ploying this primary dispersion as a medium for dispersing thebitumerl thereby to form a dispersion system having what may be termed. a double internal phase, and then combining this 85 system with fibrous pulp and running the mixture off on a paper machine.
In the practical embodiment of the invention any suitable or desired grade of rubber may-be employed, 'such for example as paleor brown crepe, smoked sheet, or the like and in order to efiect dispersions thereof in teeter, the rubber is first subjected to a preliminary plasticization which may be accomplished conveniently by subjecting a mass of the rubber to the action of a rubber roll mill of the standard and well known types. This action of the rubber may be continued until the desired degree of plasticity is imparted to the rubber, the time required for this purpose varying from twenty to eighty or more minutes depending upon the toughness and other characteristics of the particular rubber employed. Generally, however, the skilled op-- erator will be able to recognize when this condition of the rubber is attained by its compara tive softness, and. its ability to retain to a degree the form to which it is stretched, compressedor otherwise manipulated by the fingers. In this condition, the rubber may then be transferred to a kneading or masticating machine containing a relatively thick aqueous paste of colloidal material such for example as may be prepared by hydrating a colloidal clay such as bentonite with five to ten times its weight of water. The kneading or masticating machine is preferably ofthe two-blade type, with the blades'rotating at different speeds, and preferably also is provided with'jackets for circulation of steam or other temperature regulatingmedium. This machine may consist of the well-known Wemer-Pfieiderer 1o. mixer. By the use of a kneading o'r masticating machine of this type, the prepla'sticized rubber may conveniently be dispersed in the aqueous paste with the vresult that a rather viscous or pasty dispersion containing three to ten parts by weight of rubber for each part of bentonite, and from 40 to 60% by weight of water is produced. It is to be understood, however, that any other suitable method of dispersing-the rubber in water. may be employed.
In accordance with the invention the aqueous dispersion of rubber in its thick' pasty condition as it comes from the kneading or masticating machine is then employed as a media. for effecting dispersion of the bitumen therein. The bitumen may comprise asphalt of 100 to 200 F. melting point, or any equivalent heat liquefiable bituminous substance that may be desired. The rubber dispersion is placed in a suitable emulsifier or retained in the same apparatus and if necessary or desired may be adjusted to the desirable hydrogen ion concentration for the particular bitumen to be dispersed whereupon the bitumen in molten and fluid condition is fed gradually into the emulsifier as rapidly as it can be assimilated by the rubber dispersion in the emulsifier under the attenuating action of the agitating blades. During the attenuation and subdivision of the bitumen, additional quantities of water may be fed to the emulsifier to maintain the mass therein at the proper viscosity for promotion of the interfacial trituration necessary to bring about the attenuation and subdivision of the bitumen into finely divided parti cles. The dispersion system'thus produced may contain 20 to 30% rubber, 20 to 30% bitumen and 40 to water. I believe, though I do not wish this belief to be taken as confining the scope of the invention, that in the final dispersion system as thus produced. there are two separate internal phases, one of rubber and the other of bitumen, the clay colloid being adsorbed main- ,ly on the surfaces of the rubber particles, and
the bitumen particles being surrounded and precluded from coalescing one with another by the rubber particles which themselves carry adsorbed films of clay aswell as by the clay itself. As the water is removed from this system by evaporation or otherwise the clay walls surrounding the rubber are permeated by the bitumen thus bringing about fluxing and coalescence of the rubbet and the bitumen. The hereinabove described method of securing rubber and bitumen in aqueous dispersion involves substantially the same plant equipment and labor-which would be required to make separately a dispersion of rubber and a dispersion of the bitumen, and possesses the distinct advantage of avoiding the labor and trouble normally incurred in mixing the separately prepared dispersions of rubberand of bitumen to, produce'the combined system. i
The rubber-bitumen dispersion system produced as described is capable of ready admixture with fibrous stock'for the formation of waterproof sheets or boards on well known types of paper making machines. For this purpose the dispersion system may be incorporated with any desired fibrous pulp, either inthe beaters or in the stuff chest and with slight agitation the whole mass may be made uniform as to distribution .of the dispersed material in the aqueous pulp. The relative quantities of dispersion and fibrous material will manifestly vary within wide limits depending upon the characteristics desired in the final product. In general, however, the quantity of dispersion employed for admixture with the fibrous stock will be such that the combined dry weight of rubber and of bitumen will range upwardly to' 60% of the dry weight of thefinished product. After the desired quantities .of the dispersion have been uniformly distributed through the aqueous pulp, a suitable precipitant such as lime,
alum or sodium silicate and alum may be added to the mixture to cause the dispersed particles to then be converted into the desired articles by.
cutting, stamping, embossing or other operations as required.
While I have herein referred to the use of colloidal clay in the production of the initial dispersion of rubber, it is tobe understood that any paste forming hydrophilic colloid which will give a dispersion inert to electrolyte may serve as well in lieu of bentonite. It is further to be understood that while I have referred specifically to the use of asphalt, the process is not by any means limited thereto, and that any normally non-fluid but heat-liquefiable bitumen such as certain pitches, resins, and waxes may be employed in lieu of the asphalt, depending upon the charactertistics desired in the finai product.
I claim as my invention: I
1. The process which comprises effecting dispersion of rubber in an aqueous paste of a hydrophilic colloid, and subsequently effecting dispersion of a normally non-fluid bitumen in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for the bitumen. I
2. The prdess which comprises effecting Elispersion of rubber in an aqueous paste of 'a colloidal clay, and subsequently effecting dispersion of a normally non-fluid bitumen in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for philic colloid, and subsequently efiecting dispersion of asphalt in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for the asphalt.
5. The process which comprises effecting dispersion of rubber in an aqueous paste of a hydrophilic colloid, subsequently effecting dispersion of a normally non-fluid bitumen in the rubber dispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for the bitumen, mixing the resultant dispersion with fibrous stock and running off the mixture on a paper making machine.
6. The process which comprises effecting dispersion'of rubber in an aqueous paste of'a hydrophilic colloid, subsequently effecting dispersion of asphalt in the rubberdispersion by employing said rubber dispersion in thick pasty condition as the dispersing media for the asphalt, mixing the resultant dispersion with fibrous stock and running off the mixture on a paper making machine.
LESTER KIRSCHBRA'Ub T.
US496041A 1930-11-15 1930-11-15 Rubber asphalt dispersion Expired - Lifetime US1978022A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2639989A (en) * 1946-04-25 1953-05-26 United States Gypsum Co Treatment of cellulosic pulps
AU582825B2 (en) * 1985-02-21 1989-04-13 Canadian Liquid Air Ltd. Carbon dioxide gas shroud

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2639989A (en) * 1946-04-25 1953-05-26 United States Gypsum Co Treatment of cellulosic pulps
AU582825B2 (en) * 1985-02-21 1989-04-13 Canadian Liquid Air Ltd. Carbon dioxide gas shroud

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