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Publication numberUS3245930 A
Publication typeGrant
Publication dateApr 12, 1966
Filing dateMay 21, 1963
Priority dateMay 21, 1963
Publication numberUS 3245930 A, US 3245930A, US-A-3245930, US3245930 A, US3245930A
InventorsDonald E Mcdowell, George A Weisgerber
Original AssigneeExxon Research Engineering Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Compositions containing paraffin wax, semi-microcrystalline wax, ethylenevinyl acetate copolymer and polyethylene
US 3245930 A
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Description  (OCR text may contain errors)

REFRACTIVE INDEX AT 2|2F. (ASTM Dl747-6OT) April 12, 1966 .M DOWELL ETAL COMPOSITIONS CONTAINING PARAFFIN WAX, SEMI-MICROCRYSTALLINE- WAX, ETHYLENE-VINYL ACETATE COPOLYMER AND POLYETHYLENE Filed May 21, 1963 Microcrystalline Waxes (Viscosity lOcs r Higher) Semi-Microcrystalline Waxes (Viscosity Less Than lOcs) George A. We/sgerber v W m gb'r W I A Pure Normal Hydrocarbon Line O Wax A Wax B A Wax C A Wax D I I I I I I I CONGEALING POINT, "F. (ASTM D938) Dona/a E McDowell [NVENTORS PATENT ATTORNEY United States Patent C COMPOSHTIONS CONTAINING PARAFFHN WAX, SEMLMTRRYSTALLINE WAX, ETHYLENE VINYL ACETATE COPOLYMER AND PGLY- ETHYLENE Donald E. McDowell, Linden, and George A. Weisgerher,

Cranford, N.J., assignors to Essa Research and Engineering Company, a corporation of Delaware Filed May 21, 1963, fier. No. 282,038 6 Claims. (Cl. 26028.5)

The present invention is concerned with an improved wax-plastic composition which is particularly adapted for the coating of fibrous substances such as paper and the like. In accordance with the present invention, an unexpectedly improved wax-plastic composition is secured by the blending of a specific paraffin wax, a semimicrocrystalline and/ or a micro wax and a copolymer of ethylene and vinyl acetate having certain critical physical properties. Particularly desirable wax compositions comprise the use of polyethylene in conjunction with the above formulations. The resulting compositions yield coatings which exhibit superior quality in a number of respects, e.g., moisture barrier, oil resistance, scuff resistance, gloss and sealing strength. These are the performance qualities widely sought for package coatings for a number of end uses.

In the refining of hydrocarbon oils such as petroleum oils, it is known to segregate parafiin waxes from socalled paraflin distillates, waxy lubes and the like. The segregation of these waxes is secured by a number of processes. For example, it is known to chill the selected wax-containing fraction in order to secure crystallization of the wax and to remove the wax crystals from the oil by filtering, centrifuging and the like. It is also known to use various dewaxing solvents such as liquid normally gaseous hydrocarbons, such as propane, as well as other solvents, such as methylethyl ketone and the like. It is also known to utilize in dewaxing operations solvent mixtures wherein one solvent comprises a wax precipitating solvent while the other comprises a solvent having a high solubility for oil. A solvent mixture of this character, for example, comprises 60% by volume of toluene and 40% volume of methylethyl ketone. In utilizing a mixture of this character, it has been the practice to add the mixture in toto or incrementally to the waxy distillate as it is being chilled. In dewaxing operations, it is also known to use various filter aids and other agents in order to render the dewaxing and filtering operations more eflicient.

The wax segregated from the hydrocarbon oil, termed slack wax, usually contains from about 10% to 40% of oil. The slack wax is refined either by conventional sweating or by solvent crystallization to produce crude scale wax in a manner to reduce the oil content to less than about by weight. The slack wax may be distilled to obtain the desired boiling range prior to sweating, if desired. This crude scale wax generally has an oil content of about 1% to 3% by weight. In order to remove this oil from the scale wax to produce a refined wax having an oil content below about 0.5%, usually below about 0.3%, various procedures have been proposed and employed.

It is also known in the art to separate a petroleum wax which may be identified as a semi-microcrystalline wax from distillate lubricating oil fractions. The process for this preparation differs from the process for paraffin wax manufacture in the conditions of crystallization. Paraffins are prepared under conditions of relatively higher temperatures in a solvent crystallization process to yield a greater amount of straight chain hydrocarbon fractions. Semi-microcrystalline waxes are prepared at relatively lower temperatures, which cause crystallization of more of the so-called non-normal hydrocarbons, which include the iso-parafiinic and cyclic hydrocarbon structures.

It is also known in the art to segregate microcrystalline waxes from residual oils. These microcrystalline waxes are of a relatively high melting point and of different crystalline structure than the paraflin waxes described in the foregoing paragraphs. The microcrystalline wax is obtained from a so-called petrolatum which may be prepared from any of the parafiinic or mixed base crude oils. The undistilled residue may be treated with sulfuric acid and neutralized to remove the tarry matter and unsaturated hydrocarbons. The undistilled residue also may be deasphalted. The treated stock, containing a fairly high percentage of wax, as evidenced by a very high pour point, may be dewaxed by blending with a dewaxing solvent, such as propane, methylethyl ketonc-benzol, or petroleum naphtha, chilling, and filtering or centrifuging to separate the petrolatum stream from the oil solution.

This deoiling operation produces the so-called petrolatum, which contains microcrystalline wax together with about 10 to 30% oil. The wax may be again put in solution with more solvent or naphtha and chilled, and filtered or recentrifuged to further reduce the oil content. The wax which separates in these operations is referred to .as crude microcrystalline wax. This wax, separated in the second deoiling process, after stripping to remove solvent is fairly dry and of a low oil content. This wax should not be confused with petroleum jellies which contain large amounts of oil. The crude microcrystalline wax may be again treated to remove color and odor constituents. In one method of treatment, the crude wax is again put into solution with naphtha and filtered through clay or an equivalent material in order to improve its color. The clay filtered solution is distilled to remove the naphtha, the residue being a refined microcrystalline wax having a melting point within the range of about 122 F. to F. Additionally, color may be improved by hydrofining the microwax. The source of the crude oil, the conditions of crystallization and the oil content of the refined microcrystalline product will affect the melting point of the final wax product. The refined microcrystalline wax, sometimes called amorphous wax, is of very small crystal structure.

For purposes of this invention a system for classifying waxes based upon certain physical constants of the waxes is used. By this system, its congealing point in F., is measured by ASTM D938, its refractive index at 212 F., is measured by ASTM D1747-60T, and its viscosity at 210 F., in centistokes, is measured by ASTM D445. The data on congealing point and refractive index are then plotted and compared with the standard reference plot of pure normal hydrocarbons which is reproduced in the drawing, which is the only figure in this case. In this plot, the position of the normal hydrocarbons line is expressed by the equation:

n =.00025l4 t+1.3861 where t=congealing point in F. and n =refractive index at 212 F. The solid line, which separates commercial paraffin waxes from semimicrocrystalline and microcrystalline waxes, is expressed by the equation:

n =.0001943 t+'1.3994 where t=congealing point in F. and n =refractive index at 212 F. For purposes of this invention, waxes which have a congealing point and refractive index such that their coordinates fall in the area between the two lines, are identi fied as parafiin waxes. Waxes having coordinates which fall on or above the parafiin wax line are identified as either semi-microcrystalline or microcrystalline, depending upon their viscosity. A wax with coordinates above the solid line and having a viscosity of less than 10 cs. is identified as a semi-microcrystalline wax, while a wax with coordinates above the solid line and having a viscosity of 10 cs. or greater is identified herein as a microcrystalline wax.

For the purposes of the present invention the following precise definitions are used:

Paraffin wax.A petroleum wax consisting principally of normal alkanes, having an observed refractive index at 212 F. lower than that given by the expression n =0.0001943 t+1.3994 but higher than that given by the expression n =0.0002514 t+1.3861, where t is the observed congealing point, F.

Semi-micrcrystalline wax.-A petroleum wax containing substantial proportions of hydrocarbons other than normal alkanes, having an observed refractive index at212 F. equal to or higher than that given by the expression n =0.0001943 t+1.3994, where t is the observed congealing point, F. and having a viscosity at 210 F. below centistokes.

Microcrystalline wax.A petroleum Wax containing substantial proportions of hydrocarbons other than normal alkanes, having an observed refractive index at 212 F. equal to or higher than that given by the expression n =0.O00l943 t+1.3994 where t is the observed congr formance. For instance, U.S. 2,756,217 teaches the addition of butadiene-styrene copolymer to wax coating compositions. Also US. 2,877,196 discloses a wax coating composition containing a copolymer of ethylene-vinyl acetate in conjunction with either a paraffin or microcrystalline wax.

It has now been found that wax compositions containing an unusually high melting parafiin Wax of 150 F. (Wax A), a semi-microcrystalline Wax melting at 155 F. (Wax B), polyethylene and an ethylene-vinyl acetate copolymer having certain critical physical properties will have unexpectedly superior flexibility characteristics while maintaining the excellent hardness properties expected of a brittle, high melting paraflin wax blend. This makes our composition of broader value in a wide variety of end use applications than previously obtainable. In particular, it has been discovered that adding a copolymer of ethylene-vinyl acetate having the following characteristics:

Ethylene-vinyl acetate copolymer X (l) Inherent viscosity at 30 C. (0.25% by wt. in toluene) (2) Comonomer ratio, wt. percent ethylene/ vinyl acetate 72/28 (3) Melt index (ASTM D 1238-57T) 15 (4) Tensile strength, p.s.i 2000 (5) Elongation at break, percent 750 (6) Density, g./cc. at 30 C. 0.95 (7) Refractive index, 11 1.482 (8) Softening point, ring and ball, F. 276

to a wax composition containing a wax such as Wax A will yield a coating which will have unexpectedly superior flexibility properties when compared to coatings containing lower melting and more flexible parafiin waxes combined with the same ethylene-vinyl acetate copolymer. Furthermore, thisenhancement of the coatings flexibility properties does not arise when a very similar but lower molecular weight ethylene-vinyl acetate copolymer is used in conjunction with Wax A discussed above. The properties of the waxes described in this paper are summarized in Table I.

Table 1 Composition, Wt. Percent Wax A Wax B Wax C Wax D Wax F 140 F. Paraffin Wax 150 F. Paraflin Wax"-.. 155 F. Semi-Micro Wax 175 F. Micro Wax Kinematic Viscosity at 210 F.,

5. 6 7. 04 4. 3 1. 4282 1. 4309 -1. 425 Congealmg Point, F- 151 15 -142 Characterization Paraffin Semi- Paraflin Micro ASTM Melting Point, F 150 140 Pctrolatum Melting Point, F- 155 Tensile Strength, p.s.i.:

At 73 F 262 At F 383 Elongation,

At 73 F 25 21 At 0 F 23 20 Plastic At 3 9 9 At 40 F 7 6 Scuff, Inga/100 in. Coating on Sulfite Paper 30.0 22.8 35.0 23. 4

11 As described by the chart in Figure 1. b 2,000 gram load, smooth side of abrasive paper.

A preferred composition range for the present invention is -95% of Wax A and 540% of copolymer X in the two component embodiment. When Wax B and polyethylene are also added the preferred composition range is 42-65% of Wax A, 28-37% of Wax B, 65-25%- of copolymer X and 1.55% of polyethylene. Specific desirable compositions are described in the examples given later, in this paper.

Table II compares the coating properties of Wax C with that of Wax A when blended with a constant amount above paraffin waxes with Wax D and a low molecular weight polyethylene M.W. approx. 1,500). These additives, as is known in the art, produce coating compositions having enhanced physical properties. However, the singular feature of Wax A yielding blends superior in both hardness and flexibility properties compared to that of the Wax C remains unaltered. Unexpectedly it hasadditionally been found that Wax B can be successfully used in the above blends without the loss of any desirable properties, while enhancing certain critical properties of the coating. Furthermore, the addition of polyethylene in minor amounts to these coating compositions will also increase the values of the desirable physical properties of the blend. A preferred polyethylene form is one that would have a molecular weight in the range of 1,000 to 20,000, preferably 1,500. Use of such low molecular weight polyethylene yields the desired coating properties without increasing the viscosity of the blend, which tends to be high due to the presence of the ethylene-vinyl acetate copolymer.

Each of the physical properties of the coating compositions given in Table II is important in one or more of the end-use applications. The methods by which these properties are determined are give-n below:

(a) Scufi.-The method used to determine the scuffing tendency of the various wax-copolymer blends uses a modification of the Marathonscuif tester, using 3-M Tri- M-ite abrasive-polishing paper as the scufiing agent. By this method, sulphite paper coated with common parafiin waxes gives a scuff tendency of about 30-40 mgs. of coating scuffed off per 100 in. of surface When loaded with a 2000 gram weight using the polishing side of the paper as the scuff medium. The scuffing tendency of wax coated paper is an important property for some end-use applications where a hard, difiicult-to-scratch surface is desired (such as for milk cartons, frozen food cartons, etc.).

(b) Tensile strength.-'Ihis property is determined by stretching a durnb bell mold of wax (at 40 F.) until it fails on an Instron Tensile Tester. When tested, the mold is placed in the jaws of the Tensile Tester so that the initial jaw separation is 0.8" and the cross section of the neck of the mold is 0.5" x 0.5" in size. Due to the rather high viscosity encountered with blends having relatively large concentration of the eythlene-vinyl acetate copolymer, it is necessary, in order to get reproducible results, to preheat the molds to the temperature of the molten wax (220-250 F.). If this is not done, the test wax will shrink appreciably during the cooling and will give erroneous results on the Instron Tensile Tester. The tensile strength is a measure of the maximum force perunit area that the wax can withstand before f-ailure. An average value for ordinary paraffin waxes is 300 psi.

(0) Elongation and plastic-flow.These properties are also determined by subjecting a Wax mold of the desired blend to stretching in an Instron Tensile Tester until the wax fails. The sample mold is dumb-bell shaped and has the dimensions described in the tensile strength test. The properties of elongation and plastic flow are a measuse of the toughness and the flexibility of the wax. This is important for such applications as milk carton coatings, frozen food coatings, bread wraps, etc., Where the wax coating must withstand bending or dropping without breaking or cracking at temperatures near or below the freezing point of water. Elongation is the total stretch in inches of the sample from the initial stress point to the breaking point. Plastic flow is the inelastic distortion and is measured from the point of inelastic .of the particular ethylene-vinyl acetate copolymer.

5 stretching to the breaking point. Average values for normal parafiin waxes based on molds having a.0.8" effective test length are: elongation=30 10 in. which is equivalent to about 4% longitudinal elongation and plastic flow=5 10- in. which is equivalent to about 1% of longitudinal elongation.

Table II COATING PROPERTIES [E'tl1y1enevinyl acetate copolymer X:25%

Scuff, mgs./100 in. (2,000 g. load):

Wax C=10.0 75 Wax A=314 65% Wax C+10% Wax 13:40 65% Wax A+-10% Wax D=2.6 Tensile strength, p.s.i. (Instron 40 F.):

75 Wax 0:672 75 Wax A=7 1-1 65% Wax C+10% Wax D=732 65% Wax A+ 10% Wax D=753 Elongation, -in. 10- (Instron 40 F.):

75 Wax C=66 75 Wax A=97 65% Wax-6+10% Wax D=86- 65% Wax A+'l0% Wax D=l 2l 60% Wax C+l0% Wax D+5% lmw. polyethylene=107 60% Wax A+ 10% Wax D+5% lmw. 1 polyethylene=121 Plastic flow, in. 10- (Instron 40 F.):

75 Wax C=32 75 Wax A=63 65% Wax C+10% Wax D=53 65% Wax A+l0% Wax D=92 60% Wax C+l0% Wax D+5% lmw. 1 polyethylene=78 60% Wax A+10% Wax D+5% lmw. 1 polyethylene=89 1 Low molecular weight.

Table III illustrates the critical nature of the choice It compares wax blends derived from the ethylene-vinyl acetate copolymer X whose composition has'been previously described in thispaper with those derived' from an ethylene-vinyl acetate copolymer Y having the same chemical properties but differentphysical properties. The latter copolymer has the following characteristics:

Ethylene-vinyl acetate copolymer Y (1) Inherent viscosity at 30 C. (0.25% by Wt.

in toluene) 0.78 (2) Cornonomer ratio, wt. percent ethylene/vinyl acetate 72/28 (3) Melt index (ASTM D l23857T) 25 (4) Tensile strength, p.s.i 1000 (5) Elongation at break, percent 700 (6) Density, g./cc. at 30 C 0.95 (7) Refractive index, n;;. 1.482 '(8) Softening point, ring and ball, F. 255

The copolymers X and Y are each blended with Wax E which is a mixture of Wax B and C, and Wax F, a mixture of Wax A and B (as shown in Table I'). The results show quite clearly that unexpected higher flexibility values for the blends containing, Wax A compared with similar blends containing Wax C occur when Wax A is combined with copolymer X but not when the same waxes are combined with copolymer Y. Also, the table shows that the addition of Wax B improves the properties of both Wax A and Wax C in the cases where copolymer X is used. This improvement is not found when Wax B is added to Wax A and Wax C in conjunction with copolymer Y.

Table III COATING PROPERTIES Ethylene-Vinyl Acetate Copolymer X Ethylene-Vinyl Acetate Copolymer Y Wax F Exhibits Superior Properties Wax F Shows Little or No Improvement Scuff mgs./100 in. (2,000 g. load) 75% Wax C+25% Copolymer X 10.0 75% Wax A+25% Copolymer X 3. 4 75% Wax A+25% Copolymer Y- 4. 6 75% Wax E+25% Copolyrner X 3. 3 75% Wax E+25% Copolymcr Y-" 5. O 75% Wax E+25% Copolymer X 1. 6 75% Wax E+25% Copolymer Y 37 3 Tensile Strength, p.s.i. (Instron at 40 F.)

75% Wax (E+25% Copolyiner X 672 75% Wax A+25% Copolymer X 711 75% Wax A+25% Copolymer Y 711 75% Wax E+25% Copolymer X 779 75% Wax E+25% Copolymer Y..- 676 75% Wax E+25% Copolymer X 816 75% Wax E+25% Copolymer Y 673 Elongation, in. X (Instron at 40 F.)

75% Wax (E+% Copolymer X 66 75% Wax A+25% Copolymer X 97 75% Wax A+25% Oopolymer Y 82 75% Wax E+25% Copolymer X 84 75% Wax E+25% Copolymer Y 86 75% Wax E+25% Copolyrner X 108 75% Wax E+25% Copolymer Y 86 Plastic Flow, in. X 10' (Instron at 40 F.)

75% Wax (E+25% Copolymer X 32 75% Wax A+25% Copolymer X 63 75% Wax E+25% Oopolymer X 54 75% Wax E+25% Oopolymer Y 54 75% Wax E+25% Copolymer X.. 77 75% Wax E+25% Copolymer Y 56 Table IV discloses that the enhancing efiect of copolymer X on the flexibility characteristics of Wax blends containing Wax A are in evidence over a rather wide range of copolymer X concentrations. Further, Wax A maintains its superior hardness properties as shown by its consistently lower scufi values.

resin, e.g. M.W.=1,500, to 250 F. with good agitation (at Lightnin mixer or similar equipment should be employed). Copolymer X (ethylene-vinyl acetate copolymers having the requisite physical properties defined for copolymer X are commercially available) is then added with continuous stirring until a total of about 6.5 parts Table IV INSTRON FLEXIBILITY AT F.

Tensile Elongation, Sealing Strength, South Strength, in. 10 gmsJin. Inga/100 p.s.i. in.

Typical Paraifin Wax 252 17 35.0 With 5% Copolymer X:

Wax C 592 30 28. 9 ax A 568 30 24. 8 With 15% Copolymer X:

Wax O 687 14. 2 Wax A 668 66 5. 9-8. 4 With 25% Co Wax C 072 66 10.0 Wax A- 711 97 3. 4 Wax A+ 753 121 400 Paper Tear 2. 6 Wax A+28% Wax B 816 108 do 1. 6 With 40% Copolymer X Wax 860 184 500 Paper Tear. 1 Wax A- 773 550 do 1 1 Using 2,000 gm. load and Tri-M-ite polishing paper.

paper substrate tears apart, rather than the wax seal.

4 Also containing 5% low molecular weight polyethylene.

Compositions containing blends of Wax A and copolymer X are especially suitable for use as coatings on milk cartons, frozen food and other cold storage containers, nested containers, and flexible packages, and as hot melt adhesives. Further possible uses include direct coatings for food such as meats and cheeses, coatings for metallic surfaces as in cans, binders or nonskid backings for rugs and fabrics, coatings for corrugated cartons and other laminated structures, low cost dielectric coatings, and molding compounds.

Example I An excellent coating composition is prepared by heating about parts of Wax A, about 37 parts of Wax B, and

of the copolymer resin has been introduced. The copolymer should be added slowly so as to insure uniform dispersion. The stirring is then continued until no resin particles remain (3060 minutes). The finished blend can be pumped directly to coating equipment or can be cast into slabs for subsequent remelting prior to use.

Example II The method of Example I is used to prepare a blend containing the following proportion of materials:

Parts Wax A 53 Wax B 35 Copolymer X 10 about 1.5 parts of a low molecular weight polyethylene Polyethylene (low m.w. 1500) 2 Example III The method of Example I is used to prepare a blend containing the following proportion of materials:

Parts Wax A 46 Wax B 30 Copolymer X 20 Polyethylene (low m.w. 1500) 4 Example IV The method of Example I is used to prepare a blend containing the following proportion of materials:

Parts Wax A 42 Wax B 28 Polyethylene (low m.w. 1500) Copolymer X 25 The excellent properties of the wax-copolymer blends given in the above examples are summarized in Table V. Each of these compositions will be especially desirable for particular end uses, which uses will be obvious to one skilled in the art.

l Brookfield viscosity in cps. using Model LVF, #2 Spindle at 60 rpm. 2 3-M Tri-M-ite polishing paper with a 2,000 gm. load.

It is understood that this invention is not limited to the specific examples, which examples have been offered merely for the purpose of illustration, and that modifications may be made thereof without departing from the spirit of the invention.

What is claimed is:

1. An improved wax composition consisting essentially of about 42-55% of a paraflin wax having a congealing point of about 151 F., a refractive index of about 1.4282

at 212 F. and a kinematic viscosity at 210 F. of about 5.6 cs., about 28-37% of a semi-microcrystalline wax having a congealing point of about 154 R, a refractive index of about 1.4309 at 212 F. and a kinematic viscosity at 210 F. of about 7 cs., about 65-25% of an ethylene-vinyl acetate copolymer, said copolymer having a cornonomer ratio of ethylene to vinyl acetate of about 72 to 28, an ASTM melt index of about 15 and a ring and ball softening point of about 276 F., and about 1.5-5% polyethylene having a molecular weight in the range of 1,000 to 20,000.

2. The composition of claim 1 consisting essentially of about of said paraflin wax, about 37% of said semimicrocrystalline wax, about 6.5% of said ethylene-vinyl acetate copolymer and about 1.5% polyethylene of about 1,500 molecular weight.

3. The composition of claim 1 consisting essentially of about 53% of said paraffin wax, about 35% of said semimicrocrystalline wax, about 10% of said ethylene-vinyl acetate copolymer and about 2% polyethylene having a molecular weight of about 1,500.

4. The composition of claim 1 consisting essentially of about 46% of said paraflin Wax, about 30% of said semimicrocrystalline wax, about 20% of said ethylene-vinyl acetate copolymer and about 4% polyethylene having a molecular weight of about 1,5 00.

5. The composition of claim 1 consisting essentially of about 42% of said parafiin wax, about 28% of said semimicrocrystalline wax, about 25% of said ethylene-vinyl acetate copolymer, and about 5% polyethylene having a molecular weigh-t of about 1,500.

6. An article of manufacture comprising a surface coated with the composition described in claim 1.

References Cited by the Examiner UNITED STATES PATENTS 2,728,735 12/1955 Anderson 260-28.5 2,877,196 3/1959 Reding 260-28.5 2,999,765 9/1961 Boenau 260-285 3,048,553 8/1962 Moss 260-28.5 3,117,101 1/1964 Moyer 260-28.5 3,146,214 8/1964 Jakaitis et a1. 260-28.5

MORRIS LIEBMAN, Primary Examiner.

ALEXANDER H. BRODMERKEL, Examiner.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3322709 *Jul 28, 1964May 30, 1967Mobil Oil CorpCoating compositions
US3388085 *Aug 10, 1965Jun 11, 1968Witco Chemical CorpFood coating compositions comprising ethylene-vinyl acetate copolymer and acetylated monoglyceride
US3394096 *Mar 11, 1965Jul 23, 1968Sun Oil CoWax compositions for impregnating paperboard
US3407162 *Mar 30, 1966Oct 22, 1968Chevron ResHot tack high gloss wax compositions
US3496062 *Aug 10, 1967Feb 17, 1970Exxon Research Engineering CoWax composition for sealing paper to polyethylene film
US3515691 *May 29, 1967Jun 2, 1970Shell Oil CoWax polymer coating compositions
US3684012 *Jun 12, 1970Aug 15, 1972John W ScheffelMethod and composition for treating high-temperature subterranean formations
US3888811 *Sep 26, 1973Jun 10, 1975Nat Starch Chem CorpWater-moistenable hot-melt applicable adhesive composition
US4234655 *Aug 1, 1979Nov 18, 1980Chisso CorporationCrystalline polypropylene, ethylene-vinyl acetate copolymer optionally saponified
US4323626 *Sep 18, 1980Apr 6, 1982Chisso CorporationCrystalline polypropylene, ethylene-vinyl acetate-vinyl alcohol te
US4619848 *Apr 9, 1984Oct 28, 1986W. R. Grace & Co.Compositions and methods for sealing containers
US8502012Jun 16, 2009Aug 6, 2013The Procter & Gamble CompanyAbsorbent structures including coated absorbent material
US20090318884 *Jun 4, 2009Dec 24, 2009Axel MeyerAbsorbent structures with immobilized absorbent material
Classifications
U.S. Classification524/480, 524/585, 525/222
International ClassificationC09D191/08
Cooperative ClassificationC09D191/08
European ClassificationC09D191/08