US2646361A - Dust-laying emulsion - Google Patents

Dust-laying emulsion Download PDF

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US2646361A
US2646361A US170487A US17048750A US2646361A US 2646361 A US2646361 A US 2646361A US 170487 A US170487 A US 170487A US 17048750 A US17048750 A US 17048750A US 2646361 A US2646361 A US 2646361A
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emulsion
water
petroleum
resinous
dust
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Fritz S Rostler
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Golden Bear Oil Co
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/22Materials not provided for elsewhere for dust-laying or dust-absorbing

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  • This invention relates to agglomerant and adhesive materials, particularly useful in binding together and agglomerating dry, solid particles such as dusts and fines present in aggregates and minerals, and also useful in the treatment of soils, roads, and other paved and unpaved earth and other similarly loose materials which are easily disturbed by wind and/or trafiic. It is particularly related to and designed for use inconsolidating and stabilizing earth and soils and fines, and has particular utility as a dustlaying agent for roads, playgrounds, unpaved earth surfaces, and similar terrestrial areas.
  • this type of material It is characteristic of ,this type of material that it is brittle at relatively low temperatures, such as wintry weather, due to a high content of asphaltic components, and it becomes brittle in time, even in milder weather, due to oxidation and to the evaporation of low boiling components. The result is that earth if originally consolidated may soon be broken up.
  • the asphalts and-oils of the 'prior art contain saturated hydrocarbon components, which have little or no bonding power to consolidate, agglomerate, and bond dust, soil, earth, or aggregate particles to each other.
  • the saturated hydrocarbons fill the voids between the solid particles and act to lubricate and separate the particles from each other.
  • the saturated hydrocarbon content should form but a minor fraction of the petroleum fraction employed forthe purposes of tain a better bond between solid particles by em' ploying such a material than by employing a larger amount of a petroleum fraction having a higher content of saturated components, even though eventually the same ratio of unsaturated components to the earth particles are employed in both procedures.
  • the resinous component is substantially free of black, asphaltic materials. Because of the high bonding power of the resinous component, a materially lesser amount of the component is necessary as compared to the requirements when usingthe petroleum fractions employed by the prior art. Thus, although the resinous components are colored, substantially no discoloration of the earth results when it is used as a dust-laying agent, earth or soil stabilizer, or in other such and similar uses.
  • the above components of petroleum oil which I have found particularly useful in the compacw tion and stabilization of earth and in the laying of dust, are those fractions which are undesirable in petroleum lubricating oils and which are usually removed in refining procedures, such as clay treatment, solvent extraction, acid treatment, and other refining procedures.
  • refining procedures such as clay treatment, solvent extraction, acid treatment, and other refining procedures.
  • These materials have, in addition to the physica1 and chemical characteristics which I. have found to be desirable for my purposes, the advantage of being waste materials at the presenttime, or byproducts from petroleum refining, and are, consequently, available at low cost.
  • I may isolate these resinous components, having properties such as described herein, by solvent refining of waxy, naphthenic or mixed base oil fractions, either residual or distillates, and by de-waxing procedures, if necessary I may also obtain those desirable resinous materials by removing them from clays which have been employed in the 'clay treatment of residual or distilled oil fractions, and which clays carry the resins which they have adsorbed from oils which have beenrefined by such clays. Such methods for recovery of the adsorbed fractions from clays are well known in the prior art.
  • the components of l the petroleum oil suited for my invention are the unsaturated, resinous components of the selective solvent extract fraction, preferably of a distillate produced from a naphthenic base crude, naturally substantially free of solid wax fractions.
  • Many different selective solvents for extraction of such oil have been suggested for the manufacture of lubricating oils, as is evidenced by the art of selective solvent extraction of petroleum oils.
  • Current commercial practice in the lubricating oil industry generally is to use sulfur may be a substantial quantity of the saturated hydrocarbon fractions dissolved in the extract. This may be minimized, as is well known in the art, by several expedients, such as temperature control, solvent to oil ratio, and rejection pro- V cedures such as supplementary solvent washes (as with light hydrocarbons), the addition of water, etc.
  • resins having the unique properties and giving the unique results described are found in those solvent extracts (most usefully produced from distillate fractions) which are substantially free of asphaltic materials and wax which are reddish in color in bulk and transparent in thin layers, and which contain a preponderant proportion of unsaturated components and but a minor proportion of saturated components and usefully less than 25% saturated components, preferably less'than 15% of saturated components, and, in fact, the lower the per- 7 centage of saturated components the better.
  • extracts having, in addition to the desirable concentration of unsaturated components, the following characteristics are desirable PHYSICAL CHARACTERISTICS Example 1
  • Example 2 Example 3
  • Example 4 Example 5 Initial boiling point C. at 10 C. at 10 Above 200 C. at Above 220 C. at 180 C. at 10 mm. H mm. Hg. 10 mm. Hg 10 mm. Hg. mm. Hg. I Flash point Above 250 0. Above 250 0. Above 250 0"... Above 250 C Above 250 0, Mixed aniline point 33.5 C 324 C 0 C 40 C. Viscosity at 25 C. (cos.) 12,000 800 40,000, Viscosity at 90 C. (cps.) 30 l0 40 Specific gr 1.02 1.01 1,01,
  • CHEMICAL COMPOSITION 6 Bear Oil Co. as Golden Bear sulfonates, and constituting the water soluble sodium salts of the sulfonic acids extracted by alcohol in the refining of white oil with sulfuric acid; and bentonite.
  • the mixed aniline point shall be determined on the fraction diluted with equal parts of normal heptane by A. S. T. M. Method D611-47T; the viscosity and the specific gravity shall be determined by conventional procedure, as will be understood by those skilled in the art.
  • the solvent extract is emulsified with water.
  • I avoid the diinculties inherent in stickiness and high viscosity of the product which make the handling of the product difi'icult.
  • I am able to retain the advantages and utilize the adhesive properties, high viscosity, and inherent high boiling point of the effective resinous components by employing the product as an emulsion in water. Diluting the extract with a hydrocarbon or other volatile organic solvent would reduce viscosity but would, at the same time, reduce the adhesive strength and create a fire hazard, besides being more expensive than water.
  • the emulsion should preferably have the following characteirstics. It should be light yellow in color and be free-flowing, containing dispersed semi-liquid, resinous petroleum bodies, preferably within the range of 5'7 to 63 parts by weight and water as the continuous phase not less than about parts by weight and preferably in the range of 3'7 to 43 parts by weight, and also an emulsifier.
  • the resinous petroleum bodies should have a sufficiently high initial boiling point to give a flash point in excess of 400 F. and have a specific gravity of from 1 to 1.04 when measured at F. as compared to water at 60 F. (60/60).
  • the emulsion is stable in the sense that it will not break when stored for long periods in clean, closed containers at ordinary atmospheric temperature above freezing.
  • emulsifiers may be used for such resins to produce such emulsions.
  • I may use: cetyl pyridinium chloride, fatty alcohol sulfates, water soluble petroleum sulfonates, such as those sold by Oronite Chemical Co. as Oronite Wetting Agent, andsodium petroleum sulfonates, for instance, as sold by Golden This list is not intended to be'exhaustive, and is but suggestive of the emulsifying agents which may be employed.
  • Many agents useful for emulsifying petroleum oils are effective in various concentrations. Those listed. above will be found to be useful in concentrations of 5% or less. based on the resin phase.
  • stabilizers may be used to stabilize the emulsion against electrolytes which may be present in the Water used for making or diluting the emulsion.
  • the use of hard water or water treated with chlorine will require the addition of such stabilizers to the emulsion.
  • Stabilizers will also guard against premature breaking of the emulsion by the soil before it has reached the interstices thereof.
  • Such stabilizers include casein, glue, and various gums and synthetic protective colloids'and thickeners. Again, it is desirable to use highly active ingredients so that the amount employed may, for practical reasons, be kept to a minimum.
  • These synthetic, highly active stabilizers include, for example, hydroxy-ethylcellulose, sold by Carbide & Carbon Chemicals Corp.
  • Such emulsions containa dispersed resin phase of small particle size of a gravity close to thatof The emulsion has sufiiciently high viscosity to prevent coalescence or stratification on standing.
  • Emulsions of concentrations in excess of about 75 parts by weight of resin phase and less than 25 parts by weight of water are frequently too thick and become pasty, while concentrations muchbelow 50 parts by weight of resin phase and above about 50 parts by weight of water tend to stratify into a water layer and a concentrated emulsion layer which, however, is stable and may be readily remixed with the water layer.
  • Ihe dilute emulsions are also bulky and contain unnecessary water, which adds to storage and shipping costs. Therefore, while of course any dilution which gives a suitably stable emulsion may be employed, as indicated below, I prefer to make this initial emulsion concentrate of the order of 50-70 parts of dispersed resin phase, and 30 to 50 parts by weight of water continuous phase.
  • the emulsions may be made more resistant to coagulation by electrolytes by adding stabilizer, as disclosed above.
  • Phase 1 Parts by weight Phase 1:
  • Phase 2 containing 8% saturated hydrocarbons 60 50% solution of Golden Bear sulfonates dissolved in a light extract (specific gravity 0.98) 1.80 Phase 2:
  • I may similarly emulsify the above resinous components using an equal weight of water and as emulsifier 1% of cetylpyridiniumchloride or of Duponol WA Paste or 5% of bentonite. I may also emulsify the resin in the ratio of 60 parts of resin to 40 parts of water, using of sodium oleate.
  • the emulsion Due to the content of surface active agents as emulsifier, the emulsion has great wetting power for soil, and will ordinarily penetrate, when used in proper concentrations, as fast and as deep as water. It is sometimes desirable that the ground be preparedso that it is open and porous near the surface in order for the emulsion to penetrate afsufiicient distance within a reasonable period of time.
  • the successful application of the emulsion depends primarily upon two factors: good penetration and saturation ofthe soil to the depth to which it will be disturbed by traffic. Disking, or other methods of roughening the surface to be treated, is, therefore, desirable where the surface consists of solidly compacted fine particles.
  • the type of soil influences both the amount of fluid required to saturate it and the time required (i. e., number of applications) to reach the depth of penetration desired.
  • a lesser volume of emulsion is required to saturate and penetrate into sand than for. loam, and less is required for loam than for clay. Since the rate of penetration is rapid with sand, moderately fast with loam, and slow with clay, it appears that while with sandy soil one application, consisting of the total amount to be applied, will be satisfactory, with soils containing high amounts of clay, it is advisable to apply thetotal amount required in several applications.
  • the emulsion may be diluted, preferably near the point of use, with any convenient amount of water prior to application. If only one or two applications are to be made on soil containing high amounts of clay, wetting can best be accomplished by disking and/ or mixing with a blade while applying the emulsion.
  • the new surface thus produced is, however, substantially free of dust, and the bond between the earth and dust particles, which is formed by the resinous bonding material of my invention, remains in place. It is sometimes desirable, since some mechanical disintegration and grinding action occurs during the above procedure, and since dust is ordinarily brought in from other places by wind action and is sometimes stirred up from lower layers of earth which have become exposed by the movement over the area of heavy vehicles or the hoofs of animals, to repair such areas by a supplementary application of the emulsion.
  • the bonding material is non-volatile, plastic, and not brittle, and remains so even when the surface is exposed r for prolonged periods to air and sun, under'which' *conditions asphaltic materials oxidize and become brittle. .
  • This phenomenon is a property-of the resinous, unsaturated components which produce a stable and flexible bond between the particles,whereas the asphaltenes (the eifective components of .asphalts) form a brittle bond which becomes more brittle on exposure and which finally, on. prolonged exposure, have no morebinding power for the particles.
  • Such a surface consisting of rigid and brittle lumps of earth particles bonded by asphaltenes, when broken up by trafiic, especially by heavy machinery, cannot be re-worked to a smooth surface by blading and compaction as can a surface treated with the emulsion according to this invention. It is necessary to remove the disintegrated asphaltic layer and to replace it with a new surface.
  • Emulsions formulated according to my invention have uses in addition to the treatment of terrestrial areas and are also suitable for eliminating or consolidating the fines and dusts present in aggregates, minerals, ores, etc., such as in gravel, coal, and in friable manufactured products such as coke. This is accomplished by spraying these materials with an emulsion of suitable resin concentration.
  • nitrophenols such as dinitrocresol and the polychlorophenols, such as pentachlorophenol, are well known herbicides which are fortifying agents for general contact weed killers, and may also be employed.
  • the inorganic salts mentioned above are most preferably added in dry form to the stabilized emulsion under slight agitation. I have found that if the salt is added to the emulsion as a water solution, the emulsion is broken even in the presence of the stabilizer.
  • Example 7 Istabilize the emulsion formulated as given in Examplefi by adding to each gallon of the emulsion (which contains 60 parts of petroleum resins) of a gallon of a 5% aqueous solution of Methocel (15 cps); I then dilutehthis s0- stabilized emulsion by adding 4 parts of water to 1 part of the emulsion. I then add, under slight agitation, 0.1t0'0.2 pound of'sodium chlorate (the amount required to sterilize one square yard of soil'for several years) to each gallon of fluid. This material is then spread on the area to be treated at the rate of 1 gallon per square yard.
  • the so-treated area is thus freed of weeds, is free of dust, will not support vegetation for several. years, and has the advantage, when used on shoulders or dividing strips of roads, due to it light color, of adding to the safety of traffic in that motorists will not. mistake the dividing strips or shoulders for the road.
  • the polynitrophenols or polychlorophenols or other organic phytocidal chemicals such as 2,-dichlorophenoxyacetic acid and its derivatives (the so-called 2,4-D preparations) or trichloroacetic acid derivatives
  • I find that since they are readily soluble in the resin phase I may first incorporate these ingredients into the petroleum resins before forming the emulsion.
  • herbicidal ingredients which are soluble in the resin phase may beused and are classed along with the above ingredients as herbicidal additives for the purposes of this invention.
  • concentration of such herbicides may "be varied up to the solubility limit of the herbicide in the oil phase at ordinary temperatures.
  • Example 8 The resinous phase is prepared by dissolving in parts by' weight solvent extract (specific gravity of about 1.04)';'6 parts by weight commercial pentachlorophenol; and 1 part by weight sodium petroleum sulfonates.
  • the water phase is prepared by dissolving in 67 parts by weight water; 4 parts by weight sodium petroleum sulfonates; and 0.5 part by weight Vinsol NVX.
  • the two phases are then mixed and homogenized in a high-speed homogenizing machine.
  • composition of a commercial weed killer is as follows:
  • Example 9 The emulsion is prepared by dissolving onehalf of the sodium petroleum sulfonates and the pentachlorophenol in the resin phase and the other one-half of the sodium petroleum sulfonates and all of the Vinsol NVX in the water.
  • Both phases are then heated to 70-80 C. before emulsification.
  • the pentachlorophenol content of the above emulsion may be reduced to about 0.5 to 1% of the total weight of the emulsion.
  • cencentrated weed-killer emulsions are, for practical applications; usually diluted with Water to give /2% pentochlorophenol in the final spray.
  • the emulsions are characterized by being stable for practically an unlimited period of time if kept in clean, closed containers and if not exposed to extreme temperatures, that is, above freezing or below boiling.v
  • a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding .of earths and solid particles comprising water as the continuous phase and adispersed phase comprising a resinous petroleum fraction substantially free of asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction.
  • composition of matter a water emulsion of an agglomerant and adhesive material about of the said resinous petroleum fraction.
  • a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising water as the continuous phase and a dispersed phase comprising a thermoplastic resinous petroleum fraction having a viscosity at C. in excess of about 750 centipoises and a specific gravity not less than one (measured at 60 F.) substantially free'of asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction.
  • a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths sion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising Water as the continuous phase an amount at least equal to about 25 parts by weight and a dispersed phase comprising a thermoplastic resinous petroleum frac- 60 F.) of not less than one and not inpe'xcess of 1.05, substantially free of.
  • asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction said resinous fraction'comprising an amount not in excess of '75 parts by Weight and said emulsion also containing an emulsifier in addition to said parts by Weight of Water and petroleum fraction.
  • composition of matter a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising Water as the conin addition to said parts by Weight of water and petroleum fraction.
  • composition of matter an emulsion comprising as the continuous phase Water inamount ranging from 37 to 43 parts by weight and a thermoplastic resinous petroleum fraction having a viscosity in excess of about 750 centipoises and a specific gravity not less than one, and not materially in excess of 1.05, substantially free of asphaltenes and containing saturated components in amount not substantially greater than 25%, said resinous fraction being in amount ranging from 5'7 to 63 parts by weight and said emulsion also containing an emulsifier in addition to said parts by Weight of water and petroleum fraction.
  • composition of matter an emulsion comprising as the continuous phase Water in amount ranging from 3'7 to 43 parts by Weight and a thermoplastic resinous petroleum fraction having a viscosity in excess of about 750 centipoises and a specific gravity not less than one. and not materiallyin excess of 1.05, substantially free of asphaltenes and containing sat- FRITZ S. ROSTLER.
  • thermoplastic resinous petroleum fraction UNITED STATES PATENTS having a viscosity at 25 C. in excess of about 750 centipoises and a specific gravity not less g gg g g Apr 23 than one (measured at 60 F.) free of asphaltenes 2:377:639 Miner Julie 1945 and containing saturated components in amount not substantially greater than about 15% of the FOREIGN PATENTS said resinous petroleum fraction.
  • Number Country 7 Date 5 As a composition of matter, a water emul- 515,000 Great Britain Nov. 23, 1939

Description

Patented July 21, 1953 UNITE:
2,646,361" DUST-LAYING EMULSION No Drawing. Application June 26, 1950,
Serial No. 170,487
This invention relates to agglomerant and adhesive materials, particularly useful in binding together and agglomerating dry, solid particles such as dusts and fines present in aggregates and minerals, and also useful in the treatment of soils, roads, and other paved and unpaved earth and other similarly loose materials which are easily disturbed by wind and/or trafiic. It is particularly related to and designed for use inconsolidating and stabilizing earth and soils and fines, and has particular utility as a dustlaying agent for roads, playgrounds, unpaved earth surfaces, and similar terrestrial areas.
The art of earth stabilization, road-making, anddust palliation by meansof petroleum fractions has hada longhistory, and the prior art discloses the use of petroleum oil fractions, usually of residual and asphaltic character, either as such or in the form of emulsions.
A number of difficulties has detracted from the utility of the prior art practice employing these oil fractions. One important factor is the necessity for a low-cost product, since large quantities are required to treat an extended area effectively. The residual oil fractions have all been black because of their high content of asphaltic components and free carbon. The use of materials of this type, for example, as dust-laying agents, causes the earth to become blackened, and, particularly when used in driveways, parking places, and playgrounds, this material causes a soiling of clothes and body of the person coming in contact therewith.
It is characteristic of ,this type of material that it is brittle at relatively low temperatures, such as wintry weather, due to a high content of asphaltic components, and it becomes brittle in time, even in milder weather, due to oxidation and to the evaporation of low boiling components. The result is that earth if originally consolidated may soon be broken up.
Another considerable difficulty encountered in treating areas with asphaltic materials is the sensitivity of suchmaterials to alkali.
For some applications, such as on school grounds where dark-colored oils are undesirable, the more expensive neutral oils (distillate fractions of petroleum) have been used. The use of light, neutral oils in quantities sufficient to lay the dust actually creates oily surfaces since the oil only fills thevoids between the dust particles (in the same way that water is held by a sponge) until it evaporates if sufficiently volatile, or, if the sand layer is deep enough, until it percolates downward away from the surface, thus restoring the original dusty condition. The neutral oil thus acts similarly to water to wet the 8 Claims. (01. 106.-238) there is actually no bond between neutral oil and the dust particles; Such a dust palliative is then useful but for ashort period of time, and repeated treatment of the area is necessary, Al-' though less 'obviousto the eye, the light colored neutral ,oils also provide a surface whichwill soil or stain clothing with oil spots.
An extensive investigation into the interactionsions thereof arise from the-nature of the-oils and asphalts employed.
I have-discovered that the asphalts and-oils of the 'prior art contain saturated hydrocarbon components, which have little or no bonding power to consolidate, agglomerate, and bond dust, soil, earth, or aggregate particles to each other. In fact, the saturated hydrocarbons fill the voids between the solid particles and act to lubricate and separate the particles from each other.
As a result of extensive investigation, I have foundthat it is the asphaltenes or the unsaturated components of the oil which impart the adhesive and bonding power to the oil. Thus, while an increase .in the amount of oil used in treating a soil will increase the ratio of bondparticles. It can be shown by experiment that imparting unsaturated components to the earth such oil employed in a given volume of earth treated. In fact, by increasing the amount of oil sufiiciently the initial bonding obtained may be decreased. While I do not wish to be bound by any theory of this action, I believe that the saturated components, as stated above, are substantially unadsorbed by the earth particles and are contained in the interstices of the particles and act to lubricate and separate them, and by diluting the unsaturates, reduce their adhesive and bonding power. 7
I have found that I may avoid the above deficiencies of the priorart type of petroleum oil fractions and solve the difficulties inherent in the prior art procedures employing such oils, by removing from such oils the asphaltic components and the saturated hydrocarbon components, and isolating from these petroleum fractions a highly unsaturated resinous component, understanding these components in terms of the test methods referred to below.
I have found that the saturated hydrocarbon content should form but a minor fraction of the petroleum fraction employed forthe purposes of tain a better bond between solid particles by em' ploying such a material than by employing a larger amount of a petroleum fraction having a higher content of saturated components, even though eventually the same ratio of unsaturated components to the earth particles are employed in both procedures. The resinous component is substantially free of black, asphaltic materials. Because of the high bonding power of the resinous component, a materially lesser amount of the component is necessary as compared to the requirements when usingthe petroleum fractions employed by the prior art. Thus, although the resinous components are colored, substantially no discoloration of the earth results when it is used as a dust-laying agent, earth or soil stabilizer, or in other such and similar uses.
I have found that there is present in crude oils of the naphthenic, substantially wax-free type a component or fraction of such viscosity characteristics as to be properly termed resinous. These components of such crude oils are the unsaturated components thereof which have such a large temperature coefficient of viscosity as to be highly viscous or semi-solid at ordinary temperatures, being thermoplastic solids of resinous or resinophoric character and thereby liquid at elevated temperatures. The resinous fraction which I have found'particularly desirable is a material of honey-like to solid consistency at ordinary atmospheric temperature, and liquid at elevated temperature having the properties of thermoplastic resins, being substantially nonvolatile and substantially stableunder atmospheric conditions in that it will not change to a hard, brittle product on prolonged exposure to air and sunlight. Unlike the saturated oils, these petroleum resins form a strong adhesive bond with the solid particles.
The above components of petroleum oil, which I have found particularly useful in the compacw tion and stabilization of earth and in the laying of dust, are those fractions which are undesirable in petroleum lubricating oils and which are usually removed in refining procedures, such as clay treatment, solvent extraction, acid treatment, and other refining procedures. These materials have, in addition to the physica1 and chemical characteristics which I. have found to be desirable for my purposes, the advantage of being waste materials at the presenttime, or byproducts from petroleum refining, and are, consequently, available at low cost.
Thus, for example, I may isolate these resinous components, having properties such as described herein, by solvent refining of waxy, naphthenic or mixed base oil fractions, either residual or distillates, and by de-waxing procedures, if necessary I may also obtain those desirable resinous materials by removing them from clays which have been employed in the 'clay treatment of residual or distilled oil fractions, and which clays carry the resins which they have adsorbed from oils which have beenrefined by such clays. Such methods for recovery of the adsorbed fractions from clays are well known in the prior art.
Thus, I have found that the components of l the petroleum oil suited for my invention are the unsaturated, resinous components of the selective solvent extract fraction, preferably of a distillate produced from a naphthenic base crude, naturally substantially free of solid wax fractions. Many different selective solvents for extraction of such oil have been suggested for the manufacture of lubricating oils, as is evidenced by the art of selective solvent extraction of petroleum oils. Current commercial practice in the lubricating oil industry generally is to use sulfur may be a substantial quantity of the saturated hydrocarbon fractions dissolved in the extract. This may be minimized, as is well known in the art, by several expedients, such as temperature control, solvent to oil ratio, and rejection pro- V cedures such as supplementary solvent washes (as with light hydrocarbons), the addition of water, etc.
The preferred type of resins having the unique properties and giving the unique results described are found in those solvent extracts (most usefully produced from distillate fractions) which are substantially free of asphaltic materials and wax which are reddish in color in bulk and transparent in thin layers, and which contain a preponderant proportion of unsaturated components and but a minor proportion of saturated components and usefully less than 25% saturated components, preferably less'than 15% of saturated components, and, in fact, the lower the per- 7 centage of saturated components the better.
As an example, and not as a limitation of my invention, extracts having, in addition to the desirable concentration of unsaturated components, the following characteristics are desirable PHYSICAL CHARACTERISTICS Example 1 Example 2 Example 3 Example 4 Example 5 Initial boiling point C. at 10 C. at 10 Above 200 C. at Above 220 C. at 180 C. at 10 mm. H mm. Hg. 10 mm. Hg 10 mm. Hg. mm. Hg. I Flash point Above 250 0. Above 250 0. Above 250 0"... Above 250 C Above 250 0, Mixed aniline point 33.5 C 324 C 0 C 40 C. Viscosity at 25 C. (cos.) 12,000 800 40,000, Viscosity at 90 C. (cps.) 30 l0 40 Specific gr 1.02 1.01 1,01,
e V The color of Examples 1, 2, 3, and JP-reddish brown in bulk, and transparent in thin layers. The color of Example 5-light yellow in bulk and transparent inthin layers.
CHEMICAL COMPOSITION 6. Bear Oil Co. as Golden Bear sulfonates, and constituting the water soluble sodium salts of the sulfonic acids extracted by alcohol in the refining of white oil with sulfuric acid; and bentonite.
.berg, published in Industrial & Engineering Chemistry, vol. 41, pp. 598-609, March 1949.
The mixed aniline point shall be determined on the fraction diluted with equal parts of normal heptane by A. S. T. M. Method D611-47T; the viscosity and the specific gravity shall be determined by conventional procedure, as will be understood by those skilled in the art.
The direct application of these products to earth is not practical due to their high viscosity. In employing these fractions according to my invention, the solvent extract is emulsified with water. In this form I avoid the diinculties inherent in stickiness and high viscosity of the product which make the handling of the product difi'icult. However, I am able to retain the advantages and utilize the adhesive properties, high viscosity, and inherent high boiling point of the effective resinous components by employing the product as an emulsion in water. Diluting the extract with a hydrocarbon or other volatile organic solvent would reduce viscosity but would, at the same time, reduce the adhesive strength and create a fire hazard, besides being more expensive than water.
I have found that for the purposes of my invention the emulsion should preferably have the following characteirstics. It should be light yellow in color and be free-flowing, containing dispersed semi-liquid, resinous petroleum bodies, preferably within the range of 5'7 to 63 parts by weight and water as the continuous phase not less than about parts by weight and preferably in the range of 3'7 to 43 parts by weight, and also an emulsifier. The resinous petroleum bodies should have a sufficiently high initial boiling point to give a flash point in excess of 400 F. and have a specific gravity of from 1 to 1.04 when measured at F. as compared to water at 60 F. (60/60). The emulsion is stable in the sense that it will not break when stored for long periods in clean, closed containers at ordinary atmospheric temperature above freezing.
Many different emulsifiers may be used for such resins to produce such emulsions. For example, I may use: cetyl pyridinium chloride, fatty alcohol sulfates, water soluble petroleum sulfonates, such as those sold by Oronite Chemical Co. as Oronite Wetting Agent, andsodium petroleum sulfonates, for instance, as sold by Golden This list is not intended to be'exhaustive, and is but suggestive of the emulsifying agents which may be employed. Many agents useful for emulsifying petroleum oils are effective in various concentrations. Those listed. above will be found to be useful in concentrations of 5% or less. based on the resin phase.
In addition to the emulsifying agent, stabilizers may be used to stabilize the emulsion against electrolytes which may be present in the Water used for making or diluting the emulsion. The use of hard water or water treated with chlorine will require the addition of such stabilizers to the emulsion. Stabilizers will also guard against premature breaking of the emulsion by the soil before it has reached the interstices thereof. Such stabilizers include casein, glue, and various gums and synthetic protective colloids'and thickeners. Again, it is desirable to use highly active ingredients so that the amount employed may, for practical reasons, be kept to a minimum. These synthetic, highly active stabilizers include, for example, hydroxy-ethylcellulose, sold by Carbide & Carbon Chemicals Corp. as Cellosize, and methylcellulose, sold by Dow Chemical Co., as Methocel, the grade preferred for my use being 25 centipoises, or one of lower viscosity; sodium oarboxy-methylcellulose, sold by Drilling Specialties Co. as Driscose, or as sold by Hercules Powder Co., as Hercules CMC, the sodium salt of Vinsol Resin, as sold by Hercules Powder Co. as Vinsol NVX, Vinsol Resin, a darkcolored resin having a specific gravity of about 1.218, a melting point of 234-239 largely insoluble in petroleum solvents, and derived'from pine wood and containing phenol, aldehyde, and ether groups.
The following is an example of a formulation for dust-laying emulsions having the above preof any one of the resins of Examples 1 to 5, in-
- water.
elusive, containing about 0.9 part of Golden Bear sulfonates, as listed in the above table, is mixed, by strong mechanical agitation, with water containing 0.9 part of such sulfonates and 0.12 part of Vinsol NVX using sufficient water to make up about parts. The mixture is agitated to produce astable emulsion.
Such emulsions containa dispersed resin phase of small particle size of a gravity close to thatof The emulsion has sufiiciently high viscosity to prevent coalescence or stratification on standing.
Emulsions of concentrations in excess of about 75 parts by weight of resin phase and less than 25 parts by weight of water are frequently too thick and become pasty, while concentrations muchbelow 50 parts by weight of resin phase and above about 50 parts by weight of water tend to stratify into a water layer and a concentrated emulsion layer which, however, is stable and may be readily remixed with the water layer. Ihe dilute emulsions are also bulky and contain unnecessary water, which adds to storage and shipping costs. Therefore, while of course any dilution which gives a suitably stable emulsion may be employed, as indicated below, I prefer to make this initial emulsion concentrate of the order of 50-70 parts of dispersed resin phase, and 30 to 50 parts by weight of water continuous phase. The emulsions may be made more resistant to coagulation by electrolytes by adding stabilizer, as disclosed above.
I thus find it desirable to limit the composition to the preferred range of '7 to 63 parts by weight of resin and 37 to 43 parts by weight of water and use an emulsifier and'stabilizer to give a stable emulsion. I have been able to formulate these emulsions in the manner described and illustrated above so that they are so stable that they will remain unbroken for three months or longer when stored in clean, closed containers at temperatures above freezing and below boiling.
, In formulating these emulsions I find it desirable, where the emulsifier, or combination of emulsifiers, is suitably soluble to distribute the emulsifier between the resin and the water and mix the resultant solutions to produce the emulsion. For example, I have found the following to be a practical formulation for the emulsion of this invention:
Parts by weight Phase 1:
Solvent extract (specific gravity 1.02),
containing 8% saturated hydrocarbons 60 50% solution of Golden Bear sulfonates dissolved in a light extract (specific gravity 0.98) 1.80 Phase 2:
Water 37.00 50% solution of Golden Bear sulfonates in water 1.80 Vinsol NVX 0.12
These phases are mixed under strong mechanical agitation.
These emulsions, formulated as described above, have been found to be highlyeffective in the stabilization and consolidation of earth, and parti-cularly in the laying of dust, by spraying or otherwise incorporating the emulsions into the earth layer, or when employed for the laying of dust, a simple spraying operation over the road, playground, yard, or other area is suitable if necessary precautions in the use thereof are observed, as described below.
I may similarly emulsify the above resinous components using an equal weight of water and as emulsifier 1% of cetylpyridiniumchloride or of Duponol WA Paste or 5% of bentonite. I may also emulsify the resin in the ratio of 60 parts of resin to 40 parts of water, using of sodium oleate.
The above examples are merely illustrative and those skilled in the art will be able from the above teachings to adjust the formulations to produce the stable emulsions.
Due to the content of surface active agents as emulsifier, the emulsion has great wetting power for soil, and will ordinarily penetrate, when used in proper concentrations, as fast and as deep as water. It is sometimes desirable that the ground be preparedso that it is open and porous near the surface in order for the emulsion to penetrate afsufiicient distance within a reasonable period of time. The successful application of the emulsion depends primarily upon two factors: good penetration and saturation ofthe soil to the depth to which it will be disturbed by traffic. Disking, or other methods of roughening the surface to be treated, is, therefore, desirable where the surface consists of solidly compacted fine particles.
tive in the soil and the resinous material applied 7 on the ground is not lost as long as it penetrates, Insufficient amounts, however, will not bind together all the fines, and the application should, therefore, be repeated until satisfactory saturation, or a satisfactory ground condition, has been attained.
The type of soil influences both the amount of fluid required to saturate it and the time required (i. e., number of applications) to reach the depth of penetration desired. Thus, a lesser volume of emulsion is required to saturate and penetrate into sand than for. loam, and less is required for loam than for clay. Since the rate of penetration is rapid with sand, moderately fast with loam, and slow with clay, it appears that while with sandy soil one application, consisting of the total amount to be applied, will be satisfactory, with soils containing high amounts of clay, it is advisable to apply thetotal amount required in several applications. In order to increase the rate of penetration and generally the ease of application, the emulsion may be diluted, preferably near the point of use, with any convenient amount of water prior to application. If only one or two applications are to be made on soil containing high amounts of clay, wetting can best be accomplished by disking and/ or mixing with a blade while applying the emulsion.
There is little change in the original color of a' surface treated with the emulsion. The surface has the appearance of a freshly watered area, being slightly darker in shade than is the surrounding area. A surface properly treated with the emulsion is substantially free of dust. Heavy traffic such as trucks and tractors stir up no perceptible dust under conditions where, prior to treatment, heavy dust clouds were created by such traffic.
It is also notable that surfaces which have become rutted and heavily disturbed by traffic may be smoothed and compacted by ordinary procedures usually employed for this purpose.
The new surface thus produced is, however, substantially free of dust, and the bond between the earth and dust particles, which is formed by the resinous bonding material of my invention, remains in place. It is sometimes desirable, since some mechanical disintegration and grinding action occurs during the above procedure, and since dust is ordinarily brought in from other places by wind action and is sometimes stirred up from lower layers of earth which have become exposed by the movement over the area of heavy vehicles or the hoofs of animals, to repair such areas by a supplementary application of the emulsion.
These results are possible because the bonding material is non-volatile, plastic, and not brittle, and remains so even when the surface is exposed r for prolonged periods to air and sun, under'which' *conditions asphaltic materials oxidize and become brittle. .This phenomenon is a property-of the resinous, unsaturated components which produce a stable and flexible bond between the particles,whereas the asphaltenes (the eifective components of .asphalts) form a brittle bond which becomes more brittle on exposure and which finally, on. prolonged exposure, have no morebinding power for the particles. Such a surface, consisting of rigid and brittle lumps of earth particles bonded by asphaltenes, when broken up by trafiic, especially by heavy machinery, cannot be re-worked to a smooth surface by blading and compaction as can a surface treated with the emulsion according to this invention. It is necessary to remove the disintegrated asphaltic layer and to replace it with a new surface.
Emulsions formulated according to my invention .have uses in addition to the treatment of terrestrial areas and are also suitable for eliminating or consolidating the fines and dusts present in aggregates, minerals, ores, etc., such as in gravel, coal, and in friable manufactured products such as coke. This is accomplished by spraying these materials with an emulsion of suitable resin concentration.
Tests have shown that the resin phase of the emulsions of my invention, while to a certain degree phytocidal to growing plants, has nosoil sterilization effect, and the emulsions may be used to prevent loss of top soil by preventing generation or loss of fines. The soil may thus be treated with the emulsion, avoiding the spraying of growing valuable vegetation, in the man ner described. above, without impairing the agronomic value of the soil thus treated; that is, soils may be treated with the emulsion with.- out impairment of their vegetation bearingproperties, and ma thus be seeded ata later date nitrophenols, such as dinitrocresol and the polychlorophenols, such as pentachlorophenol, are well known herbicides which are fortifying agents for general contact weed killers, and may also be employed.
I have found that I can incorporate these ingredients into the emulsion, thus making preparations useful for binding dust and simultaneously killing weeds and/or sterilizing the soil. It is advantageous to add a stabilizer to the emulsion before incorporating the phytocidal or soil-sterilizing ingredient. The inorganic salts mentioned above are most preferably added in dry form to the stabilized emulsion under slight agitation. I have found that if the salt is added to the emulsion as a water solution, the emulsion is broken even in the presence of the stabilizer. The following is an example of an emulsion suitable for soil sterilization and dust laying, and is given for purposes of illustration, and not as a limitation of my invention.
10 Example 7 Istabilize the emulsion formulated as given in Examplefi by adding to each gallon of the emulsion (which contains 60 parts of petroleum resins) of a gallon of a 5% aqueous solution of Methocel (15 cps); I then dilutehthis s0- stabilized emulsion by adding 4 parts of water to 1 part of the emulsion. I then add, under slight agitation, 0.1t0'0.2 pound of'sodium chlorate (the amount required to sterilize one square yard of soil'for several years) to each gallon of fluid. This material is then spread on the area to be treated at the rate of 1 gallon per square yard. The so-treated area is thus freed of weeds, is free of dust, will not support vegetation for several. years, and has the advantage, when used on shoulders or dividing strips of roads, due to it light color, of adding to the safety of traffic in that motorists will not. mistake the dividing strips or shoulders for the road. In usingthe polynitrophenols or polychlorophenols or other organic phytocidal chemicals, such as 2,-dichlorophenoxyacetic acid and its derivatives (the so-called 2,4-D preparations) or trichloroacetic acid derivatives, I find that since they are readily soluble in the resin phase I may first incorporate these ingredients into the petroleum resins before forming the emulsion. Other herbicidal ingredients which are soluble in the resin phase may beused and are classed along with the above ingredients as herbicidal additives for the purposes of this invention. The concentration of such herbicides may "be varied up to the solubility limit of the herbicide in the oil phase at ordinary temperatures.
The higher the concentration of herbicide in the oil the moreeifectiveis the composition and the greater the permissible dilution with water. Thus, I desire to use from a smallam'ount, i. e.,
less than .1%' of the oil phase up to saturation percentages of the herbicide in the oil phase.
Thus, I prepare a 0.5 to 12.0% solution of the polynitrophenols or polychlorophenols, and form the emulsion in the manner described above, but use somewhat more emulsifying agent than for the dustrlaying emulsion.
An example of an emulsion containing pentachlorophenol as the fortifying agent of the emulsion to be used as a general contact weed killer visthe following preparation:
Example 8 The resinous phase is prepared by dissolving in parts by' weight solvent extract (specific gravity of about 1.04)';'6 parts by weight commercial pentachlorophenol; and 1 part by weight sodium petroleum sulfonates.
The water phase is prepared by dissolving in 67 parts by weight water; 4 parts by weight sodium petroleum sulfonates; and 0.5 part by weight Vinsol NVX.
.The two phases are then mixed and homogenized in a high-speed homogenizing machine.
Another example of a composition of a commercial weed killer is as follows:
Example 9 The emulsion is prepared by dissolving onehalf of the sodium petroleum sulfonates and the pentachlorophenol in the resin phase and the other one-half of the sodium petroleum sulfonates and all of the Vinsol NVX in the water.
Both phases are then heated to 70-80 C. before emulsification.
The pentachlorophenol content of the above emulsion may be reduced to about 0.5 to 1% of the total weight of the emulsion.
These cencentrated weed-killer emulsions are, for practical applications; usually diluted with Water to give /2% pentochlorophenol in the final spray.
The emulsions are characterized by being stable for practically an unlimited period of time if kept in clean, closed containers and if not exposed to extreme temperatures, that is, above freezing or below boiling.v
While I have described a particular embodiment of my' invention for the purpose of illustration, it should be understood that various modifications and adaptations thereof may be made within the spirit of the invention as set forth in the appended claims. The present application is a continuation in part of my copending application Serial No. 168,864 for a Petroleum Herbicide Emulsion filed June 17, 1950.
I claim:
1. As a composition of matter, a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding .of earths and solid particles comprising water as the continuous phase and adispersed phase comprising a resinous petroleum fraction substantially free of asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction. 7
2. As a composition of matter, a water emulsion of an agglomerant and adhesive material about of the said resinous petroleum fraction.
3. As a composition of matter, a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising water as the continuous phase and a dispersed phase comprising a thermoplastic resinous petroleum fraction having a viscosity at C. in excess of about 750 centipoises and a specific gravity not less than one (measured at 60 F.) substantially free'of asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction.
4. As a composition of matter, a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths sion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising Water as the continuous phase an amount at least equal to about 25 parts by weight and a dispersed phase comprising a thermoplastic resinous petroleum frac- 60 F.) of not less than one and not inpe'xcess of 1.05, substantially free of. asphaltenes and containing saturated components in amount not substantially greater than about 25% of the said resinous petroleum fraction, said resinous fraction'comprising an amount not in excess of '75 parts by Weight and said emulsion also containing an emulsifier in addition to said parts by Weight of Water and petroleum fraction.
6. As a composition of matter, a water emulsion of an agglomerant and adhesive material suitable for agglomeration and binding of earths and solid particles comprising Water as the conin addition to said parts by Weight of water and petroleum fraction.
7. As a composition of matter an emulsion comprising as the continuous phase Water inamount ranging from 37 to 43 parts by weight and a thermoplastic resinous petroleum fraction having a viscosity in excess of about 750 centipoises and a specific gravity not less than one, and not materially in excess of 1.05, substantially free of asphaltenes and containing saturated components in amount not substantially greater than 25%, said resinous fraction being in amount ranging from 5'7 to 63 parts by weight and said emulsion also containing an emulsifier in addition to said parts by Weight of water and petroleum fraction.
8. As a composition of matter an emulsion comprising as the continuous phase Water in amount ranging from 3'7 to 43 parts by Weight and a thermoplastic resinous petroleum fraction having a viscosity in excess of about 750 centipoises and a specific gravity not less than one. and not materiallyin excess of 1.05, substantially free of asphaltenes and containing sat- FRITZ S. ROSTLER.
and solid particles comprising Water as the con- 65 tinuous phase and a dispersed phase compris- References Cited in the file Of this P nt ing a thermoplastic resinous petroleum fraction UNITED STATES PATENTS having a viscosity at 25 C. in excess of about 750 centipoises and a specific gravity not less g gg g g Apr 23 than one (measured at 60 F.) free of asphaltenes 2:377:639 Miner Julie 1945 and containing saturated components in amount not substantially greater than about 15% of the FOREIGN PATENTS said resinous petroleum fraction. Number Country 7 Date 5. As a composition of matter, a water emul- 515,000 Great Britain Nov. 23, 1939

Claims (1)

1. AS A COMPOSITION OF MATTER, A WATER EMULSION OF AN AGGLOMERANT AND ADHESIVE MATERIAL SUITABLE FOR AGGLOMERATION AND BINDING OF EARTHS AND SOLID PARTICLES COMPRISING WATER AS THE CONTINUOUS PHASE AND A DISPERSED PHASE COMPRISING A RESINOUS PETROLEUM FRACTION SUBSTANTIALLY FREE OF ASPHALTENES AND CONTAINING SATURATED COMPONENTS IN AMOUNT NOT SUBSTANTIALLY GREATER THAN ABOUT 25% OF THE SAID RESINOUS PETROLEUM FRACTION.
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2704967A (en) * 1951-03-28 1955-03-29 Golden Bear Oil Co Method of constructing roads
US3432321A (en) * 1963-04-19 1969-03-11 Witco Chemical Corp Methods for improvement of asphalts and oil emulsions useful therein
US4067818A (en) * 1976-01-22 1978-01-10 Exxon Research And Engineering Company Dust laying
US4561905A (en) * 1984-07-20 1985-12-31 Paul A. Kittle Method for suppressing coal dust
US4780233A (en) * 1987-09-04 1988-10-25 Betz Laboratories, Inc. Dust suppression methods and compositions
US4780143A (en) * 1987-04-24 1988-10-25 Betz Laboratories, Inc. Methods for suppressing cement clinker dust emissions
US4897218A (en) * 1987-04-24 1990-01-30 Betz Laboratories, Inc. Methods for suppressing cement clinker dust emissions
US4960532A (en) * 1987-08-24 1990-10-02 Carbochem Inc. Dust suppressant forming a resilient layer
US5296264A (en) * 1991-09-30 1994-03-22 Blacklidge Emulsions, Inc. Method for sealing and priming prepared substrates for roadways
US5503871A (en) * 1991-09-30 1996-04-02 Blacklidge Emulsions, Inc. Method for sealing and priming prepared substrates for roadways and substrate thereof
US7503724B2 (en) 2005-11-18 2009-03-17 Blacklidge Emulsions, Inc. Method for bonding prepared substrates for roadways using a low-tracking asphalt emulsion coating
US10273637B2 (en) 2010-02-24 2019-04-30 Blacklidge Emulsions, Inc. Hot applied tack coat

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB515000A (en) * 1938-05-16 1939-11-23 Albert Frederick Suter Improvements relating to the treatment of lac or shellac
US2346930A (en) * 1944-04-18 Road construction
US2377639A (en) * 1942-08-10 1945-06-05 Hercules Powder Co Ltd Soil stabilization

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2346930A (en) * 1944-04-18 Road construction
GB515000A (en) * 1938-05-16 1939-11-23 Albert Frederick Suter Improvements relating to the treatment of lac or shellac
US2377639A (en) * 1942-08-10 1945-06-05 Hercules Powder Co Ltd Soil stabilization

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2704967A (en) * 1951-03-28 1955-03-29 Golden Bear Oil Co Method of constructing roads
US3432321A (en) * 1963-04-19 1969-03-11 Witco Chemical Corp Methods for improvement of asphalts and oil emulsions useful therein
US4067818A (en) * 1976-01-22 1978-01-10 Exxon Research And Engineering Company Dust laying
US4561905A (en) * 1984-07-20 1985-12-31 Paul A. Kittle Method for suppressing coal dust
US4897218A (en) * 1987-04-24 1990-01-30 Betz Laboratories, Inc. Methods for suppressing cement clinker dust emissions
US4780143A (en) * 1987-04-24 1988-10-25 Betz Laboratories, Inc. Methods for suppressing cement clinker dust emissions
US4960532A (en) * 1987-08-24 1990-10-02 Carbochem Inc. Dust suppressant forming a resilient layer
US4780233A (en) * 1987-09-04 1988-10-25 Betz Laboratories, Inc. Dust suppression methods and compositions
US5296264A (en) * 1991-09-30 1994-03-22 Blacklidge Emulsions, Inc. Method for sealing and priming prepared substrates for roadways
US5503871A (en) * 1991-09-30 1996-04-02 Blacklidge Emulsions, Inc. Method for sealing and priming prepared substrates for roadways and substrate thereof
US7503724B2 (en) 2005-11-18 2009-03-17 Blacklidge Emulsions, Inc. Method for bonding prepared substrates for roadways using a low-tracking asphalt emulsion coating
US20090169901A1 (en) * 2005-11-18 2009-07-02 Blacklidge Emulsions, Inc. Method For Bonding Prepared Substrates For Roadways Using A Low-Tracking Asphalt Emulsion Coating
US7918624B2 (en) 2005-11-18 2011-04-05 Blacklidge Emulsions, Inc. Method for bonding prepared substrates for roadways using a low-tracking asphalt emulsion coating
US10273637B2 (en) 2010-02-24 2019-04-30 Blacklidge Emulsions, Inc. Hot applied tack coat

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