CN101287801A - Asphalt paving composition and asphalt paving method - Google Patents

Abstract

The present invention provides an asphalt composition, a method of preparing an asphalt paving composition, and an asphalt paving method that retains the sufficient performance characteristics of conventional hot-mix paving but has lower mixing, paving, and compaction temperatures than conventional hot-mix paving. The paving method of the invention comprises the following steps: injecting a foamable solution containing a lubricating substance into a hot asphalt binder to provide a hot foam mixture; adding the hot, foamed mixture to a suitable hot aggregate; further mixing the hot, foamed mixture with hot aggregate to coat the hot aggregate with a hot foamed asphalt binder to form a hot paving material; supplying a hot paving material to a paving machine; applying a hot paving material to a road surface to be paved by a paving machine; and compacting the applied paving material to form a paved surface.

Description

Asphalt paving composition and asphalt paving method

technical field

The field of the invention relates generally to an asphalt paving composition and an asphalt paving method, and more particularly to an asphalt paving composition comprising a combination of a foam lubricating substance, an asphalt binder, and an aggregate.

Background technique

The use of asphalt aggregate mixes for paving roads, driveways, parking lots and the like is well known. Typically, a suitable aggregate mixture comprising crushed stone, gravel, sand, etc. is heated at an elevated temperature of about 270°F to 370°F and combined with an equally hot asphalt-based binder such as Bituminous binder (asphalt plus polymer) is mixed until the aggregate particles are coated with the binder. Paving mixes prepared in this temperature range are often referred to as hot mixes. Mixing is usually done off-site, and the mix is then transported to the paving site and fed to the paver. The mixture of asphalt and aggregate applied to the road surface by pavers is then compacted by rollers, usually still at elevated temperatures, with other equipment. The compacted aggregate and bituminous material is finally hardened by cooling. Due to the large amount of material used to pave roads or commercial parking lots, the cost of obtaining the heat necessary for mixing and paving needs to be considered. For commonly used binders, the thermal viscosity characteristics of the binder will affect the temperature required to provide adequate coating of the aggregate, as well as considerations of environmental conditions suitable for paving. As a result, many methods have been devised to optimize aggregate wrapping and pavement binding while minimizing material and/or process costs.

An alternative to the hot mix method is the cold mix method, in which cold and moist aggregate is mixed with a hot or cold binder, which may be obtained by dispersing bitumen in water with a suitable surfactant The emulsion is either a mixture of bitumen (often called light bitumen) and a suitable hydrocarbon solvent (called some such as naphtha, #1 oil, or #2 oil). The emulsified bitumen particles coat and bind the aggregate and remain after the water has evaporated. When light bitumen is used, the hydrocarbon solvent evaporates at different rates, depending on the volatility of the solvent. Irrespective of the volatility of the solvent, the subsequent residue will act as a paving material in which the asphalt component gradually hardens or thickens with the time the solvent is removed. The binder can be alternately foamed and mixed with the aggregate to increase coating effectiveness. Although cold mixes are less expensive than hot mixes, cold mixes are usually of lower quality than hot mixes and may also have poorer wrapping properties of the binder, resulting in poorer cohesive compaction) and durability. In addition, lightweight asphalt mixes have a greater impact on the environment due to the use of volatile hydrocarbon solvents. Some emulsions also utilize hydrocarbon solvents other than water to produce materials tailored to specific applications.

Recently, in an attempt to combine the advantages of hot mix and cold mix, a warm mix method has been reported. In one example of the warm mix method, the "soft" component of the asphalt binder (the component with a lower viscosity at a given temperature than the "hard" component) and the "hard" component ( components that have a higher viscosity than the "soft" components at a given temperature). The soft component is melted and mixed with the aggregate at about 110°F to 265°F, depending on the particular soft component. The hot hard component is then mixed with warm water to create a foam which is mixed with the hot soft component/aggregate mixture to give the final coated paving material. Although warm-mix paving materials can be paved at lower temperatures than hot-mix materials, the production of warm-mix mixtures requires a more extensive and complex approach than the production of hot-mix mixtures.

Although the aggregate is covered, if there is insufficient bonding between the binder and the aggregate, the binder can detach, or "peel," from the aggregate, causing the material to not maintain adequate compaction and thereby reducing the overall strength of the pavement . To aid in the bonding of binder to aggregate, the aggregate, or more generally asphalt binder, may be treated with an anti-stripping compound or material (such as a surfactant) so that it acts as aggregate particles with the asphalt binder The adhesive between them can substantially reduce the detachment of the bond.

Regardless of the aggregate/binder mixing method used, the cladding paving material must not harden together, or lack the ability to be compacted to a suitable density, during transport or while in a paver. Insufficiently coated aggregate material, while easy to mix and handle, can result in a pavement that does not maintain compaction, does not properly support vehicular traffic, or does not resist abrasion and weathering well.

Contents of the invention

The present invention provides a method of asphalt paving suitable for initial construction with significantly lower mixing, paving, and compaction temperatures (30°F to 80°F lower than conventional hot mix paving methods) F), while maintaining adequate hardening, density, and durability properties of conventional hot mix paving. Generally, the method of the present invention involves injecting a foamable lubricating solution into a hot asphalt binder to form a foam-containing asphalt-based mixture; adding the mixture to the hot aggregate; and further mixing the foam-containing asphalt binder using, for example, a static mixer mixing aggregate and aggregate so that the aggregate is coated to form a paving material; applying the paving material to the surface to be paved; and then compacting the applied paving material to form the paved surface.

The present invention also provides an asphalt paving composition, comprising about 0.01wt.%-3wt.% of lubricating substances relative to the weight of the asphalt binder; about 3wt.%-9wt.% of the asphalt binder; and about 91wt.%-97wt.% aggregate. Typically the lubricious substance is about 5 wt.% to 10 wt.% cationic, anionic or nonionic surfactant, such as soap solids, and about 90 wt.% to 95 wt.% water. The optional lubricating substances may contain soap solids as low as 1 wt.%, and usually practice an upper limit of 30 wt.%-40 wt.% to ensure the pumpability of the soap solution.

The composition may further contain an anti-stripping material, such as primary amine, secondary amine, tertiary amine, iminoamine, imidazoline, or phosphate ester, wherein the number of carbon atoms in the anti-stripping material ranges from about 7 to about 20. Alternatively, other anti-stripping materials known in the art are also suitable. When used in the composition, the anti-stripping material is present in an amount ranging from about 0.1 wt.% to about 10 wt.%, based on the weight of the lubricious material.

Detailed ways

In one embodiment, the method of the present invention comprises injecting a foamable solution containing a lubricating substance into hot asphalt binder to form a hot, foaming mixture; The mixture is added to a suitable aggregate heated to a temperature higher than that of the hot, foaming mixture; the two are further mixed to coat the hot aggregate with the hot, foaming mixture to form a hot paving material; The hot paving material is transferred to a paver; the hot paving material is applied to the surface to be paved using the paver at paving temperature; and the applied paving material is then compacted to form a paved surface.

A feature of using a foamable lubricity solution (such as a water-based foam) is that it imparts lubricity so that the temperature of the paving material during paving is significantly lower than that required to soften the binder (e.g., about 30°F- 80°F) to provide similar buildability. Another feature is that water-based foams containing lubricating substances or lubricating materials require less water than conventional emulsions or aqueous solutions to likewise disperse the lubricating material. Therefore, small amounts of water have to be released, treated, and eventually evaporated from the paving mix. A suitable lubricious material is soap. Non-limiting examples of suitable soaps include sodium fatty acid soaps, sodium sulfonate soaps, ethoxylated non-phenols, quaternary ammonium chlorides, and tall oil and refined sodium tall oil soaps or potassium soap. Other cationic, anionic or nonionic surfactants may also be used as suitable lubricious materials.

The significantly lower paving temperatures provided by the present invention can: (1) reduce the cost of thermal energy used without adversely affecting the paving process or the resulting pavement; (2) reduce emissions of volatile components, thereby reducing Air pollution; or (2) Allowing the use of "stickier" grades of asphalt in paving materials. For example, at the same warm mix process temperature, a more accelerated PG 64-22 binder mixed with a lubricating foam can be used in place of the less viscous PG 58-28 binder, resulting in a bond that utilizes PG 58-28 The hot mix pavement produced by the material has the same performance as the pavement.

Asphalt-based binders include petroleum-based binders. For example, an asphalt binder may include additives, such as polymeric materials. Suitable asphalt-based or asphalt binders include those conforming to ASTM D-6373, D-3387, or D-946. However, some asphalt binders that essentially but not fully comply with ASTM D-6373, D-3387, or D-946 may also be used. The aggregate may comprise recycled asphalt pavement (RAP).

In one embodiment of the method of the invention, the foamable solution is an aqueous solution containing a lubricious substance made of soap. The paving material contains about 91 wt.% to 97 wt.% aggregate and about 3 wt.% to 9 wt.% asphalt-based binder. The amount of soap solids used in a given amount of aggregate is from about 0.01 wt.% to about 3 wt.%, relative to the weight of asphalt-based binder used.

The hot, foamed asphalt binder mixture is heated to a temperature lower than that used to form a conventional hot mix. A suitable temperature range is approximately 180°F to 340°F, depending on the particular asphalt binder used. Similarly, a suitable aggregate is heated to a temperature in the range of about 180°F to 300°F and the hot paving material is heated and mixed at a temperature in the range of about 180°F to 300°F. The paving material is spread at a temperature in the range of about 170°F to 290°F and compacted at a temperature in the range of about 150°F to 270°F. The foamable soap solution can be at any temperature that does not cause the liquid to freeze, boil, or adversely affect the lather, but preferably has a temperature in the range of about 80°F to 150°F.

This embodiment can be implemented by injecting a foamable solution into a hot asphalt binder; adding the hot, foamable mix to a suitable aggregate and mixing it in situ at or near the job site to form a hot paving material . An advantage of the present invention is that the volume of liquid used to mix the asphalt binder and aggregate is significantly reduced, which facilitates on-site construction and reduces the need to transport large quantities of water.

In another embodiment of the method of the present invention, the aqueous solution comprises about 30 wt.% soap solids and about 70 wt.% water; the asphalt binder comprises PG58-28 asphalt; and the paving material comprises about 94.5 wt.% aggregate and about 5.5 wt.% of PG58-28 asphalt binder; and the amount of soap solids used is less than about 1 wt.% relative to the amount of asphalt binder used. For this particular binder, the hot, foamed asphalt binder mix is heated to a temperature of about 240°F-340°F; the suitable aggregate is heated to a temperature in the range of about 180°F-300°F °F; and heating the hot paving material and mixing at a temperature in the range of about 180°F-300°F. The paving material is paved at a temperature ranging from about 170°F to 290°F and compacted at a temperature ranging from about 150°F to 270°F.

In another embodiment, the aqueous solution contains about 30 wt.% soap solids and about 70 wt.% water; the asphalt binder contains PG 64-22 bitumen; the paving material contains about 94.5 wt.% aggregate and about 5.5 wt. wt.% of PG 64-22 asphalt binder; and the amount of soap solids used is less than about 1 wt.% relative to the amount of asphalt binder used. For this particular asphalt binder, the hot, foamed asphalt binder mixture is heated to a temperature of approximately 240°F-340°F; the suitable aggregate is heated to a range of approximately 180°F-300°F and heating the hot paving material and mixing at a temperature ranging from about 180°F to 300°F. The paving material is paved at a temperature ranging from about 170°F to 290°F and compacted at a temperature ranging from about 150°F to 270°F. Those of ordinary skill in the art will appreciate that hot, foamed asphalt binder mixes and suitable aggregates can be heated and mixed at higher temperatures and paving materials can also be laid at higher temperatures and compaction without negatively affecting the performance of the paving material, but doing so will be higher in terms of thermal energy expenditure.

Typically, the asphalt temperature needs to be higher than the aggregate temperature. Depending on the bitumen grade, the bitumen should be 325°F or higher to allow it to be pumped and foamed. Since the aggregate constitutes about 90% by weight of the mix, the temperature of the aggregate essentially controls the temperature of the mix. Aggregate temperature needs to be controlled within the warm mix temperature range of approximately 180°F - 300°F. When mixing aggregates with viscous binders or binders containing polymers, the temperature of conventional aggregates and mixes can be as high as 350°F, which is hot mix, but with the present invention, in the same aggregate and binder In cases where aggregate and mix temperatures can be reduced to 300°F without negatively affecting the resulting pavement performance, this is considered warm mix.

In another embodiment of the method of the present invention, the foamable solution further contains an anti-stripping material. Non-limiting examples of suitable anti-stripping materials are primary amines, secondary amines, tertiary amines, iminoamines, imidazolines, or phosphate esters, where the number of carbon atoms in these materials ranges from about 7 to about 20.

In another embodiment of the method of the present invention, the aqueous solution further comprises an anti-stripping material such that the foamable solution contains about 30 wt.% soap solids, about 5 wt.% anti-stripping material, and about 65 wt.% water.

Example

The following examples provide methods and test data for some asphalt binders and aggregates, with and without lubricating substances or lubricants, carried out under conventional hot mix conditions as well as under conditions employing the method of the present invention.

In these examples, the E-1 compound is a specific compound type that meets the Wisconsin Department of Transportation's ("WIDOT") design life in excess of 20 years for a design load of 1 million equivalent single axle loads (ESAL) road surface requirements. The same applies to E-10, except that it has an ESAL of 10 million. The term ESAL is well known to those working in the asphalt paving industry.

In general, tall oil soaps and tall oil soaps can be made by reacting tall or refined tall oil with sodium or potassium hydroxide by any of the well-known methods for making soaps. Tall oil and refined tall oil were supplied by Arizona Chemical, Jacksonville, FL; Georgia Pacific, Atlanta, GA; and MeadWestvaco, Stamford, CT. Molex anti-stripping material is a polycycloamine blend supplied by Air Products, Allentown, PA. Alpha-olefin sulfonates were supplied by Stepan Chemical, Winder, GA. The choice of bitumen grade depends on location-specific variables such as a particular geographic location, local climate, traffic load, etc.

A test of the performance of paved pavement materials is to simulate vehicle traffic pressure by measuring the number of times a roller (roller, roller) carrying a specific weight load repeatedly rolls the pavement to cause ruts of a specific depth on the material. Testing of the compacted material produced by the method of the present invention was accomplished by using what is known as the Hamburg Wheel Tracking ("HWT"), also known as the PMW Wheel Tracker tester, which is manufactured by Precision Machine and Welding, Salina , provided by KS. The number of Hamburg passes required to achieve a rut depth of 10 mm was used as a comparative evaluation when testing compacted material in dry conditions. The test condition is 1581b. wheel load, using hot air at the test temperature to roll 52 times per minute to reach the sample test temperature. In general, all other variables being substantially equal, the greater the number of passes, the better the desired properties of the paving mix. Based on the results presented when samples are subjected to these test conditions, one of ordinary skill in the art, as well as those familiar with HWT, will identify suitable paving materials for a particular application.

In Table 1, for the particular binder processed and tested, examples with a mixing temperature ranging from 270°F to 280°F and a compaction temperature of about 275°F or higher are considered conventional hot mix ; Examples having a mixing temperature in the range of 230°F to 235°F and a compaction temperature in the range of 215°F to 220°F are considered warm mix. Thus, Examples 1, 4, 6, 7, and 10 were hot mix, while the other examples were warm mix for the binder.

Table 1:

Example number and mixing formula asphalt binder Aggregate mixing temperature and conditions Surfactant solution blends and/or anti-stripping materials Wt% of surfactant, soap solids, or anti-stripping material relative to the weight of the binder Compaction temperature Rolling times when the rut depth is 10mm under dry conditions #1: E-1 Control Mix at 280°F, Lab Mix PG58-28 280°F, 2 hours aging at 275°F none none 275°F Rolled 2.361 times at 50°C #2: E-1, same as #1 blend, laboratory mixed PG58-28 230°F, Aging 30 minutes at 230°F Tall oil soap + Molex anti-flaking material 1% 215°F-220°F Rolled 1,031 times at 50°C #3: E-1, same as #1 blend PG58-28 230°F, Aging 30 minutes at 230°F tall oil soap 1% 215°F-220°F Rolled 791 times at 50°C #4: E-10 Mix PG58-28 280°F, 2 hours aging at 275°F  Add anti-stripping material to the binder and mix at normal temperature none 275°F Rolled 1,975 times at 58.3°C #5: E-10 compound, same as #4 PG58-28 230°F, Aging 30 minutes at 230°F Refined tall oil soap + anti-flaking material added to soap 1% 215°F-220°F Rolled 1,625 times at 57.8°C #6: E-1 Compound, Control Test PG58-28 280°F lab mix, 275°F aged for 2 hours not added none 275°F Rolled 3,351 times at 58.5°C #7: E-1 compound, same as #6 PG58-28 Mix at 280°F, mature at 275°F for 4 hours not added none 275°F Rolled 5,376 times at 58.4°C

Continued Table 1

Example number and mixing formula asphalt binder Aggregate mixing temperature and conditions Surfactant solution blends and/or anti-stripping materials Relative to the weight of the binder, the wt% of surfactant, soap solids, or anti-stripping agent Compaction temperature Rolling times at a rut depth of 10 mm, dry conditions #8: E-1 mix, same as #6 warm test mix PG58-28 PG58-28 + 230°F mixed soap, aged 30 minutes at 230°F Refined tall oil soap 1% 215°F-220°F Rolled 981 times at 58°C #9: E-1 mix, same as #6 warm test mix PG64-22 PG64-22 + 230°F mixed soap, aged 30 minutes at 230°F Refined tall oil soap 1% 215°F-220°F Rolled 1,875 times at 58.3°C #10: E-1 compound, same as #6 PG58-28 Mix at 280°F, mature at 275°F for 2 hours none none 275°F Rolled 1,601 times at 58.6°C #11: E-1 mix, same as #6 warm test mix PG64-22 PG 64-22+surfactant+anti-flaking, 230°F lab mix, 230°F cure for 30 minutes Alpha olefin sulfonate + phosphate ester anti-stripping material 1% Surfactant Solids 215°F-220°F Rolled 1,226 times at 58.3°C #12: E-1 mix, same as #6 warm test mix PG64-22 PG 64-22+soap+anti-flaking, 230°F lab mix, 230°F for 30 minutes Tall oil soap + amine anti-stripping material 1% soap solids 215°F-220°F 3,351 crushes at 58.4°F #13: Field Mix Test, E-1 Mix PG64-22 PG64-22AC+soap, factory mixed at 230°F-235°F Refined tall oil soap solution at ~50°F during production 0.9%-1% soap solids 210°F-220°F On-site mixing and compaction in the laboratory, 1,626 times of rolling at 58.3°C

Continued Table 1

Example number and mixing formula asphalt binder Aggregate mixing temperature and conditions Surfactant solution blends and/or anti-stripping materials Relative to the weight of the binder, the wt% of surfactant, soap solids, or anti-stripping agent Compaction temperature Rolling times at a rut depth of 10 mm, dry conditions #14: E-10 Blend + 15% RAP + Soap PG64-22 E-10 mix + 15% RAP + soap, 230°F laboratory mix, 230°F aging for 30 minutes Refined tall oil soap 0.046% soap solids 215°F-220°F Rolled 6,601 times at 58.5°C #15: E-10 Blend + 15% RAP + Soap PG64-22 E-10 mix + 15% RAP + soap, 230°F laboratory mix, 230°F aging for 30 minutes Refined tall oil soap 0.069% soap solids 215°F-220°F Rolled 5,101 times at 58.5°C #16: E-1 Mix + Soap PG64-22 E-1 mix + soap, 230°F lab mix, 230°F for 30 minutes Refined tall oil soap 0.75% soap solids 215°F-220°F Rolled 1,451 times at 58.2°C #17: E-1 Mix + Soap PG64-22 E-1 mix + soap, 230°F lab mix, 230°F for 30 minutes Refined tall oil soap 0.075% soap solids 215°F-220°F Rolled 2,225 times at 58.2°C #18: E-1 Mix + Soap PG64-22 E-1 mix + soap, 230°F lab mix, 230°F for 30 minutes Refined tall oil soap 0.15% soap solids 215°F-220°F Rolled 1,826 times at 58.0°C #19: Field mix test, E-1 mix with 10% RAP, PG64-22+ soap PG64-22 E-1 Mix with 10% RAP, PG 64-22AC+Soap, Mill Mixed at 230°F-240°F Refined tall oil soap, on-site soap solution temperature ~35°F 0.97% soap solids Spread and compact at 210°F-225°F Rolled 1,976 times at 58.3°C

As the data show, generally, using the same binder for warm mix as hot mix does not yield the same results, but does provide an acceptable paving material. Warm mix has a lower number of hamburger rolls. The reason for the low number of times may be due to the fact that in the warm mixing process, due to the lower mixing temperature and shorter curing time, the aging and curing of the binder is not so sufficient, as shown in comparative examples 1, 2, and 3 as shown. Examples 1, 6, and 7 illustrate that aging improves hot mix performance to a large extent, while Examples 16, 17, and 18 also illustrate that aging can promote improved performance even with reduced soap levels. Examples 1 and 4 show that only adding anti-stripping agent in hot mixing can not improve the road surface. Example 4 was tested at a slightly higher temperature and shows that the anti-stripping material improves performance. All other conditions being the same, by increasing the test temperature by 8°C, the number of rolling times to roll out a 10mm rut depth can be reduced by as much as 50%. Examples 8 and 9 illustrate that the use of the present invention using a binder containing PG 64-22 which is thicker than PG 58-28 can result in improved performance. Examples 14 and 15 illustrate that the present invention achieves the best pavement performance using PG 64-22, 15% RAP, and 30 minutes of curing. The data show that warm mixes can be produced using binders of higher initial consistency to produce approximately equal properties to those of less viscous binders used to produce hot mixes. The PG 58-28 binder was less viscous than the PG 64-24 binder, but as the data show, using the PG 64-22 binder in warm mix produced a Hamburg result that was approximately the same as the hot mix. Results of PG 58-28 in the mix. Thus, using the present invention, it is possible to replace PG 58-28 with PG 64-22, resulting in a suitable road surface.

Claims (19)

1. A preparation method for asphalt paving composition, comprising the following steps: (a) injecting a foamable solution containing a lubricating substance into hot asphalt binder to provide a hot, foaming mixture; (b) adding said hot, foaming mixture to a suitable hot aggregate; and (c) further mixing the hot, foamed mixture with hot aggregate to coat the hot aggregate with hot, foamed asphalt binder to form a hot paving composition. 2. The method according to claim 1, wherein said foamable solution is an aqueous solution; said lubricious substance is soap; said paving material contains about 91wt.%-97wt.% aggregate and about 3wt. % to 9 wt.% of asphalt binder; and the amount of soap used is about 0.01 wt.% to 3 wt.% for a given amount of aggregate relative to the weight of asphalt binder used. 3. The method of claim 1, wherein the aqueous solution comprises about 5 wt.% to 10 wt.% soap solids and about 90 wt.% to 95 wt.% water. 4. The method of claim 1, wherein the foamable solution is an aqueous solution; the lubricious substance is a cationic, anionic, or nonionic surfactant; and the paving material comprises about 91 wt.%- 97wt.% aggregate and about 3wt.%-9wt.% asphalt binder; and relative to the weight of the used asphalt binder, the amount of surfactant is about 0.01wt.%-3wt.%. 5. The method of claim 1, wherein the temperature of the hot asphalt binder is 30°F to 80°F lower than conventional hot mix temperatures. 6. The method of claim 1, further comprising the step of adding an anti-stripping material to the hot paving composition. 7. A method for paving asphalt, comprising the steps of: (a) Injecting a foamable solution containing a lubricating substance into an asphalt binder to provide a hot, foamed mixture, wherein the asphalt binder is heated to a higher temperature than conventional hot mix used for the asphalt binder Mix at temperatures 30°F-80°F lower; (b) adding said hot, foaming mixture to a suitable aggregate; (c) further mixing said hot, foamed mixture with hot aggregate such that said hot, foamed asphalt binder coats said hot aggregate to form a hot paving material; (d) supplying said hot paving material to a paver; (e) applying said paving material to the road surface to be paved by said paver; and (f) compacting said applied paving material to form a paving surface. 8. The method of claim 7, wherein the temperature of the hot asphalt binder is about 180°F to 340°F. 9. The method of claim 7, wherein the hot bitumen temperature is less than about 230°F. 10. The method of claim 7, wherein the foamable solution further comprises an anti-stripping material. 11. The method of claim 7, wherein the suitable aggregate comprises recycled asphalt pavement material. 12. An asphalt paving composition comprising, relative to the weight of the asphalt binder, about 0.01 wt.% to 3 wt.% of a lubricating substance; about 3 wt.% to 9 wt.% of the asphalt binder; and about 91 wt.% - 97 wt.% of aggregates. 13. The composition of claim 12, wherein the lubricious substance is about 5 wt.% to 10 wt.% soap solids and about 90 wt.% to 95 wt.% water. 14. The composition according to claim 13, wherein the soap solid is fatty acid sodium soap, sodium sulfonate soap, ethoxylated nonylphenol, quaternary ammonium chloride, or tall oil and refined tall oil Sodium or potassium soap. 15. The composition of claim 12, wherein the lubricious substance is about 5wt.%-10wt.% of a cationic, anionic, or nonionic surfactant and about 90wt.%-95wt.% of water . 16. The composition of claim 12, further comprising an anti-stripping material. 17. compositions according to claim 16, wherein, described anti-stripping material is primary amine, secondary amine, tertiary amine, iminoamine, imidazoline or phosphoric acid ester, wherein the number of carbon atoms in the anti-stripping material The range is about 7 to 20. 18. The method of claim 17, wherein the anti-stripping material is used in an amount ranging from about 0.1 wt.% to 10 wt.% of the lubricious substance. 19. The composition of claim 12, wherein the lubricious substance comprises about 30 wt.% soap solids, about 5 wt.% anti-stripping material, and about 65 wt.% water.