US1774609A - Method of pleparing dispersions - Google Patents

Method of pleparing dispersions Download PDF

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US1774609A
US1774609A US304336A US30433628A US1774609A US 1774609 A US1774609 A US 1774609A US 304336 A US304336 A US 304336A US 30433628 A US30433628 A US 30433628A US 1774609 A US1774609 A US 1774609A
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materials
sulphite
particles
product
action
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US304336A
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Elman B Myers
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HOWARD W DIX
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HOWARD W DIX
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/0004Preparation of sols
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S516/00Colloid systems and wetting agents; subcombinations thereof; processes of
    • Y10S516/01Wetting, emulsifying, dispersing, or stabilizing agents
    • Y10S516/02Organic and inorganic agents containing, except water

Definitions

  • colloidizing it is generally understood articles, when dealing with solid. materials, is a controlling factor, and inability to attain a desired range of particle size has militated against the effectiveness of purely mechanical preparations. To overcome this difficulty it has been proposed to subject solidarticles, however prepared, to the action 0 various organic substances known as stabilizers or peptizing agents.
  • the preferred stabilizers cover a rather wide range of organic materials, usually of starchy or feculous nature, used alone, or in conjunction with gums, resins, and like materials.
  • a common characteristic of colloidizing agents, so called, is the necessity of having. them substantially alkaline, in order to exert a desired protective or colloidizing action.
  • the best known of the agents to be used has-been'ammonium tannate, which is a reaction product of tannic acid and ammonia set forth in various disclosures.
  • Yet another object of this invention is the provision of the use of an improved colloidizing agent of a chemical nature used with any suitable mechanical means.
  • Yet another object of this invention is the combination of the improved colloidizing e, 1e2s. Serial No. 304,336.
  • a suitable material to be colloidized is ground or triturated in a suitable vehicle, such as varmospirits or .cellosolve.
  • a suitable vehicle such as varmospirits or .cellosolve.
  • a very high degree of mechanical disintegration such as may be obtained by the types of disintegrators generally known as mills, sometimes referred to as colloid mil-ls, it is possible to secure a relatively stable suspension of particles of the pigment in the vehicle.
  • the particle size ordinarily obtainable by mechanical means ranges, generally, from .5 to 2.0 micra. To secure a suspension of substantially permanent stabillty, it is necessary to attain a particle size of about .5 micra or less. As will be.
  • waste material available for many uses, its main use, heretofore, being restricted to its application as. a substitute for pitch, or the like as a cementing or binding agent for artificial fuels, roadways, etc.
  • This sulphite material is further treated by desiccation and the powdered-product used for the purposes above enumerated.
  • compositions under test contained neither glue, gelatine, tannic acid, dextrine, or feculous material of the types normally considered necessary for stability.
  • any suitable quantity of sulphite liquor may be used for the purposes described, various materials requiring different amounts to impart the necessary stabilizing property'of the product. Generally from 4 to 10 per cent of the adjuvant will be sufficient for light weight materials and liquids, while as much as. 20 to 40 per. cent may be required for heavy materials. The specific amounts required will depend entirely upon the particular material being-treated and will have to be determined by th-euser in a preliminary test or series of tests.
  • This uniform occurrence and distribution of particle size in the materials prepared according to the process of the present invention markedly increases the reactive capacity of such materials and involves, as a consequence, a distinct increase in economy of preparation of any desired product, it being well known that the reaction rate is a direct function of the surfaces of the reacting materials exposed to one another.
  • the desideratum in the preparation of emulsions is the dispersion ofabodyof liquid disintegrated into fine particles or globules, as a disperse lis a in a continuous phase of the carrying m I mulsions hitherto have been stabilized by the addition of glues, gelatine, soaps, starches, and other stabilizing materials which have materially afiected the quality of the emulsion and the cost of manufacture.
  • the combinationof means set forth in the present invention. enables the preparation of stable emulsions, generally, due to the 'fact that the globules or particles of liquid to be dispersed are literally torn apart after being greatly attenuated, and the protective action of the sulphite, or other adjuvant materials is instantly rendered available, there! Joy preventing coalescence of the dispersed particles and the consequent formation of globules.
  • the methodof preparing colloidal suspensions comprising subjecting the material to be dispersed to the conjoint action of sulphite waste liquor and a grinding surface which is flexibly supported.

Description

Patented Sept. 2, 1930 UNITED STATES PATENT OFFICE ELMAN B. MYERS, OF
METHGD OF PREPARING DISPERSIONS No Drawing. Application filed September Hitherto it has been proposed to colloidize substances, generally, by a variety of methods, the more permanent results of which involve, in the case of solid materials, trituration in the presence of neutral solvent, or formation of the desired product by chemical precipitation.
These methods have not met with any material success for reasons which are not as yet clearly known.
In colloidizing it is generally understood articles, when dealing with solid. materials, is a controlling factor, and inability to attain a desired range of particle size has militated against the effectiveness of purely mechanical preparations. To overcome this difficulty it has been proposed to subject solidarticles, however prepared, to the action 0 various organic substances known as stabilizers or peptizing agents. The preferred stabilizers cover a rather wide range of organic materials, usually of starchy or feculous nature, used alone, or in conjunction with gums, resins, and like materials. A common characteristic of colloidizing agents, so called, is the necessity of having. them substantially alkaline, in order to exert a desired protective or colloidizing action. The best known of the agents to be used has-been'ammonium tannate, which is a reaction product of tannic acid and ammonia set forth in various disclosures.
It is an object of the present invention to provide an improved method of preparing stable colloidal suspensions and emulsions.
It is a furtherobject of this invention to provide a novel method which is adapted to improve the colloidizing of materials generally, including mineral and vegetable oils and the like.
Yet another object of this invention is the provision of the use of an improved colloidizing agent of a chemical nature used with any suitable mechanical means.
Yet another object of this invention is the combination of the improved colloidizing e, 1e2s. Serial No. 304,336.
agent with improved mechanical means.
These-and other desirable objects and ad-- vantages of the present invention will be described 1n the following specification, preferred embodiments beinggiven by way of,
illustration only, for, since the underlying principles may be incorporated in other specific methods and devices, it is not intended to be limited to the "ones herein disclosed, except as such limitations are clearly imposed by the appended claims.
In the practice of the present invention a suitable material to be colloidized, as for example, a pigment, is ground or triturated in a suitable vehicle, such as varmospirits or .cellosolve. a very high degree of mechanical disintegration, such as may be obtained by the types of disintegrators generally known as mills, sometimes referred to as colloid mil-ls, it is possible to secure a relatively stable suspension of particles of the pigment in the vehicle. The particle size ordinarily obtainable by mechanical means ranges, generally, from .5 to 2.0 micra. To secure a suspension of substantially permanent stabillty, it is necessary to attain a particle size of about .5 micra or less. As will be. readily appreciated the mechanical difliculties involved in the preparation of particles of this size is very great, due to the fact that in the region between the microscopic and ultramicroscopic, the particles have atendency to flow in the direction of the rotating element of the disintegrator, thereby preventing any reaction upon themselves by the opposed grinding or crushing surfaces. Such a condition is remedied, to a considerable extent, by the use of a mill of the type described in my co-pending application, Number 301,804, in which the attrition or disintegration of the particles 'is. effected by forcing them under positive pressure be-, tween two flexibly supported counter-revolving opposed discs. In such a type of instrument there are set up opposed forces, which, acting at high speed, exert a positive disrup tive effect upon any particles positioned between the counter-revolving discs.
NORRISTOWN, PENNSYLVANIA, ASSIGNOR OE TEN PER CENT 'IO HOWARD W. DIX, OF NEW YORK, N.
By subjecting such material to I Such a device gives an improved result, and with this type of machine the particles retain what may be defined as a relatively permanent stability of solution.
While starchy materials and the like have been proposed as adjuvants in the practice of such processes, their use involves considerable trouble, both in time and labor involved in preparation, as well as the inability to secure compositions of known physical and mechanical characteristics whereby uniform results could be obtained at will. A further marked disadvantage of the stabilizers noted, is the high cost on the market. Tannic acid, the
been found that excellent results can be secured by the use of organic wood derivatives, or the like, the preferred composition being that known in the art as sulphite Waste liquor. This liquor is, as its name implies, a waste product fromthe process of making paper pulp. The tonnage of this product is enormous and pulp mills generally, are now after many years of experimenting, endeavoring to find a method of disposing of this material and look to fin ding a substantial market or it.
Various methods have been adopted to make this so-called waste material available for many uses, its main use, heretofore, being restricted to its application as. a substitute for pitch, or the like as a cementing or binding agent for artificial fuels, roadways, etc. This sulphite material is further treated by desiccation and the powdered-product used for the purposes above enumerated.
In the practice of the present invention the inclusion of a moderate, amount of sulphite liquor in the aqueous vehicle above considered, when subjected to the action of the improved mill heretofore referred to, pro- .duces a remarkable increase in efficiency of the colloidizing process, and in fact, gives a result that materially surpasses any result heretofore obtained by any agent used alone.
One great advantage of the agent under discussion is its conjoined action with the mill referred to, besides the fact that it is neutral, as for example,.inks prepared from pigments in asuitable mill, of the type described, in the presence of sulphite liquor showed no deposition of particles over a considerable period of time,and it is further to be noted that the compositions under test contained neither glue, gelatine, tannic acid, dextrine, or feculous material of the types normally considered necessary for stability.
7 Any suitable quantity of sulphite liquor may be used for the purposes described, various materials requiring different amounts to impart the necessary stabilizing property'of the product. Generally from 4 to 10 per cent of the adjuvant will be sufficient for light weight materials and liquids, while as much as. 20 to 40 per. cent may be required for heavy materials. The specific amounts required will depend entirely upon the particular material being-treated and will have to be determined by th-euser in a preliminary test or series of tests.
While the sulphite liquor, or its equivalent in the desiccated condition, gives improved results in the ordinary methods of preparation, such as hand-grinding in a mortar, or grinding in a ball-mill or colloid mills of the fixed and rotating or nested cone types, the combination with a device of the counterrevolving opposed disc type noted above,
sulphite solution, is not known, but the fact of the improved results obtained by the use of such a combination of means, is herewith set forth for the purpose of fully illustrating the present invention, and for definitely stating theremarkable results.
Material prepared in the above manner, examined under the ultra-microscope, shows a particle size substantially below .5 micra in diameter, and is further characterized by the fact that the particle size is substantially uniform throughout the Whole mass, there being no aggregates or clumps of material such as is commonly found in the materials prepared by the ordinary colloidizing processes, where there is a distinct gradation in particle size. This uniform occurrence and distribution of particle size in the materials prepared according to the process of the present invention, markedly increases the reactive capacity of such materials and involves, as a consequence, a distinct increase in economy of preparation of any desired product, it being well known that the reaction rate is a direct function of the surfaces of the reacting materials exposed to one another.
Another feature of considerable scientific and commercial importance, is that the use of the relatively cheap sulphite liquor does away with high-priced alkaline reagents such-as ammonia, and the like, the neutral sulphite liquor requiring no care or calibration in its use. The neutrality of the material used is a highly desirabl condition to he obtained,
as it is well known t I at the maximum results,
. my said application preparation of susj ity of the average relative to stability of suspensions, emulsions, etc., are obtained at or near the neutral point, i. e., in a solution having a-p of about 7.0 or slightly above,
he rapidity of action of the improved stabilizer of the present invention permits of great economies in point of'time, the reacting materials merely requiring a single treatment in an approved grinding and disintegrating apparatus to assure complete reaction.
In the preparation of-paints,.inks, and other like pigment base material, it is pos sible to produce tons of a finished product in the time formerly required for as many ounces In addition, the'fineness of theresulting particles and their intimate association or' dispersion in the carrying medium insures homogeneity of product, which fea-'v ture makes for a marked economy, both in sale :as well as in use.
lVhile the sulphite liquor has been discussed with relation .to the preparation of colloidal materials of the suspensoid type, it is e ually efiicient when used in conjunction with the mills of the type disclosed in pensions of liquid in liquid, of the mutually insoluble or immiscible types, .which products are commonly known .as emulsions. The desideratum in the preparation of emulsions is the dispersion ofabodyof liquid disintegrated into fine particles or globules, as a disperse lis a in a continuous phase of the carrying m I mulsions hitherto have been stabilized by the addition of glues, gelatine, soaps, starches, and other stabilizing materials which have materially afiected the quality of the emulsion and the cost of manufacture.
While not markedly deleterious in their ef-- feet the ordinary stabilizing agents have not I been particularly eliicient, which fact may be attested by housewives, to whom the instabilrepared emulsion of ed1- ble oil in acidulateg water, commonly known as mayonnaise, iswell known. This trouble is due to the tendency of the dispersed oil particles to coalesce into large globules, until they finally attain a suflicient size to separate out from the body of the emulsion. This separating out is a progressive action which is stimulated by the presence of any large globules, and is gfnerally the outstanding difiiculty met wit in' industries where one or more liquids are dispersed into a liquid vehicle. The ramifications of the problems involved in preparing suitable emulsions extend into the paint and'varnish industry as well as foods and pharmaceuticals.
The combinationof means set forth in the present invention. enables the preparation of stable emulsions, generally, due to the 'fact that the globules or particles of liquid to be dispersed are literally torn apart after being greatly attenuated, and the protective action of the sulphite, or other adjuvant materials is instantly rendered available, there! Joy preventing coalescence of the dispersed particles and the consequent formation of globules.
It will now, be seen that there has been provided an improved process for colloidizing solid and liquid materials, generally, which process permits the use of a relatively cheap waste product to secure highly efficient and economical results, as well as permitting the preparation of :new combinations of materials which have hitherto not been available.
The simplicity of'operation and freedom from involved processing steps is in. marked contrast to the hitherto obtaining methods and permits increased efiiciency in m-anufac- 1 ture distribution and sale of the resulting products.
What is claimed is:
1. The methodof preparing colloidal suspensions comprising subjecting the material to be dispersed to the conjoint action of sulphite waste liquor and a grinding surface which is flexibly supported.
2. The method of preparing colloidal suspensions comprising subjecting the material to be dispersed to the conjoint action of sulphite waste liquor and counter-mtolving flexibly supported opposed disintegrating surfaces. a
3. The method of preparing colloidal suspensions comprising subjecting the material to be dispersed to a preliminary grinding in the presence of sulphite waste liquor, and
subsequently subjecting the resulting. product to the action of a plurality of flexibly supported counter-revolving opposed disintegrating surfaces.
4. The method of reparing materials from relatively immiscible fluids-comprising subjecting the material to be dispersed to a preliminary grinding in the presence of sulphite waste liquor, and subsequently subjectmgthe resulting product'to the action of a plurality of flexibly supported counterrevolving opposed disintegrating surfaces.
5. The product of the conjoint action of sulphite liquor and flexibly su ported grinding surfaces characterized by a particle diameter of substantially less than .5 micra.
- ELMAN B. MYERS.
US304336A 1928-09-06 1928-09-06 Method of pleparing dispersions Expired - Lifetime US1774609A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433877A (en) * 1941-10-09 1948-01-06 Int Cigar Mach Co Tobacco sheets and filaments and methods of making them
US2565052A (en) * 1942-08-13 1951-08-21 American Mach & Foundry Smoking article
US2658016A (en) * 1948-08-31 1953-11-03 Brown Laurie Oakley Production of fine aqueous dispersion of sulfur
US3252809A (en) * 1963-01-23 1966-05-24 Gen Motors Corp Dry grinding of ceramics

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433877A (en) * 1941-10-09 1948-01-06 Int Cigar Mach Co Tobacco sheets and filaments and methods of making them
US2565052A (en) * 1942-08-13 1951-08-21 American Mach & Foundry Smoking article
US2658016A (en) * 1948-08-31 1953-11-03 Brown Laurie Oakley Production of fine aqueous dispersion of sulfur
US3252809A (en) * 1963-01-23 1966-05-24 Gen Motors Corp Dry grinding of ceramics

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