SLIP RESISTANT SHOE COVER
20210337930 · 2021-11-04
Assignee
Inventors
- Thomas M. McKnatt (Surathani, TH)
- Buncha Tomogol (Bangkok, TH)
- Noppadol Polbundit (Bangkok, TH)
- Dave Narasimhan (Flemington, NJ)
- Sudarshan Narasimhan (Flemington, NJ, US)
Cpc classification
C08J5/02
CHEMISTRY; METALLURGY
B29D35/0054
PERFORMING OPERATIONS; TRANSPORTING
B29K2105/0064
PERFORMING OPERATIONS; TRANSPORTING
A43B13/226
HUMAN NECESSITIES
B29C41/003
PERFORMING OPERATIONS; TRANSPORTING
B32B2250/248
PERFORMING OPERATIONS; TRANSPORTING
C08J3/244
CHEMISTRY; METALLURGY
B32B25/042
PERFORMING OPERATIONS; TRANSPORTING
C08L2201/52
CHEMISTRY; METALLURGY
B29L2031/50
PERFORMING OPERATIONS; TRANSPORTING
B32B3/30
PERFORMING OPERATIONS; TRANSPORTING
B29C41/34
PERFORMING OPERATIONS; TRANSPORTING
B29C41/22
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29C41/00
PERFORMING OPERATIONS; TRANSPORTING
B29C41/22
PERFORMING OPERATIONS; TRANSPORTING
B29C41/34
PERFORMING OPERATIONS; TRANSPORTING
B32B25/04
PERFORMING OPERATIONS; TRANSPORTING
B32B3/30
PERFORMING OPERATIONS; TRANSPORTING
C08J3/24
CHEMISTRY; METALLURGY
Abstract
A shoe cover is a natural latex article with reduced amount of sulfur cross linking agent and accelerators including zinc dithiocarbamate that break catalytically soluble sulfur S.sub.8 sulfur rings forming sulfur linear chains. Surfactants present in the pre-vulcanization composition wets natural polyisoprene particles and permeates small sized sulfur into the interior of these particles thereby pre-vulcanizing the particles. The latex emulsion also has post-vulcanization composition with accelerators that crosslink between particles during the post vulcanization cure cycle. The dipped natural polyisoprene article is substantially uniformly cured both in the inter-particle and intra-particle regions and reliably exhibits high cross link density, uniform distribution of double bonds and zinc segregation at the boundaries or original particles. The natural rubber films exhibit high tensile strength, tensile modulus, tear strength, elongation with low modulus of the shoe cover. The bottom surface of the shoe cover is etched to produce a slip resistant surface.
Claims
1. A natural polyisoprene latex shoe cover article comprising: a. natural polyisoprene particles that are pre-vulcanized by the addition of soluble sulfur catalytically broken to chains of sulfur and incorporated into natural latex particles by use of one or more surfactants; b. said natural polyisoprene forming a latex bath applied to a coagulant coated shoe cover former thereby forming a first natural latex layer; c. the first latex layer coated former is dipped in a thicker higher viscosity natural latex to form a thicker second latex layer only on the bottom ground contacting portion of the shoe cover; d. the second latex layer is etched in a slow moving parallel flowing laminar flow of nonpolar solvent and polar solvents which form discrete parallel streams and polar solvents dissolve natural latex coating forming parallel grooves and non polar solvent does not attack natural latex coating forming ridges surrounding the grooves; e. the first latex layer coated former with etched second natural latex layer over first latex natural layer is dipped in a polymer solution and passed through three ovens set at 110° C., 120° C. and 130° C. curing the latex layers and the polymeric wear resistant coating; whereby said natural polyisoprene latex shoe cover article with etched grooves bound by ridges in the bottom of the shoe cover directs any oil or water to the rear of the shoe cover providing enhanced friction preventing the slip of the shoe cover held essentially by the elastic stretch of the shoe cover over the shoe worn by the user.
2. The natural polyisoprene latex article of claim 1, wherein said first natural latex layer is 200 to 350 microns thick.
3. The natural polyisoprene latex article of claim 1, wherein said second natural latex layer is 800 to 1200 microns thick.
4. The natural polyisoprene latex article of claim 1, wherein said nonpolar solvent is toluene.
5. The natural polyisoprene latex article of claim 1, wherein said nonpolar solvent is benzene.
6. The natural polyisoprene latex article of claim 1, wherein said polar solvent is ethyl alcohol.
7. The natural polyisoprene latex article of claim 1, wherein said polar solvent is acetic acid which serves to coagulate the thick latex layer applied.
8. A method for producing natural polyisoprene latex shoe cover article comprising: a. pre-vulcanizing natural polyisoprene particles by the addition of soluble sulfur catalytically broken to chains of sulfur and incorporated into natural latex particles by use of one or more surfactants; b. applying a coagulant coated shoe cover former in natural polyisoprene latex bath applied thereby forming a first natural latex layer; c. dipping the first latex layer coated former in a thicker higher viscosity natural latex forming a thicker second latex layer; d. etching the second latex layer in a slow moving parallel flowing laminar flow of nonpolar solvent and polar solvents which form discrete parallel streams and polar solvents dissolve natural latex coating forming parallel grooves and non polar solvent does not attack natural latex coating forming ridges surrounding the grooves; e. dipping the former with etched second natural latex layer over first latex natural layer in a polymer solution; f. passing the polymer solution coated former with first and second natural latex coatings through three ovens set at 110° C., 120° C. and 130° C. curing the latex layers and the polymeric wear resistant coating; whereby said natural polyisoprene latex shoe cover article with etched grooves bound by ridges in the bottom of the shoe cover directs any oil or water to the rear of the shoe cover providing enhanced friction preventing the slip of the shoe cover held essentially by the elastic stretch of the shoe cover over the shoe worn by the user.
9. A method for manufacturing natural polyisoprene article according to claim 8 wherein said soluble sulfur comprises high level of S.sub.8 sulfur rings.
10. A method for manufacturing natural polyisoprene article according to claim 8 wherein said pre-vulcanization composition accelerators selected from the group consisting of zinc diethyldithiocarbamate (ZDEC) or zinc dibutyldithiocabamate (ZDBC) and combinations thereof.
11. A method for manufacturing natural polyisoprene article according to claim 8 wherein said surfactant comprises potassium caprylate, polyoxyethylene cetyl/stearyl ether, alkyl aryl sulphonate, alkyl sulphonate, olefin sulphonate, an alcohol sulphate or and combinations thereof.
12. A method for manufacturing natural polyisoprene article according to claim 8 wherein said alkyl aryl sulphonate is sodium dodecylbenzenesulphonate (SDBS).
13. A method for manufacturing natural polyisoprene article according to claim 8 wherein said alkyl sulphonate is olefin sulphonate.
14. A method for manufacturing natural polyisoprene article according to claim 8 wherein said alcohol sulphate is sodium lauryl sulphate.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0023]
[0024]
[0025]
[0026]
[0027]
DETAILED DESCRIPTION OF THE INVENTION
[0028] The present invention is predicated on the discovery of soluble sulfur such as S.sub.8 rings of sulfur is catalyzed by a zinc complex of dithiocarbamate in combination with potassium caprylate and sodium dodecyl benzene sulphonate (SDBS) surfactant creating pre-vulcanized, natural polyisoprene particles in a latex composition. This latex composition enables the production of latex film articles by dipping coagulant coated or coagulant free formers into the composition. The surfactant package inhibits natural polyisoprene particle agglomeration and flocculation. The latex dipped film has natural polyisoprene particles that become crosslinked and regions between the particles are crosslinked during the vulcanization cure forming both intra-crosslinked and inter-crosslinked bonds. The articles that result comprise a high quality and uniform latex film.
[0029] The latex-stabilizing composition is one that keeps the particles of natural polyisoprene separated from each other in the aqueous medium. Since the polyisoprene particles do not touch each other, they are unable to agglomerate and flock. This is important because, once the particles begin to agglomerate, the particles may never be separated due to van der Waals forces. Preferably, the latex-stabilizing composition comprises a surfactant package containing at least one surfactant. An anionic surfactant is preferred, especially one that can be stably maintained for a period of well over one month and up to two months or more. An example of such a surfactant is sodium dodecyl benzene sulphonate (SDBS). Other examples include, but are not limited to, other alkyl aryl sulphonates, alkyl sulphonates (e.g., C14 olefin sulphonate, which is sold under the trade name Calsoft AOS-40 (Pilot Chem. Co., Red Bank, N.J.)), olefin sulphonates, and alcohol sulphates (e.g., sodium lauryl sulphate). SDBS or another alkyl aryl sulphonate is preferably present in an amount of about 0.1-0.35 wt %, based on the dry weight of the polyisoprene. SDBS or another alkyl aryl sulphonate can be combined with one or more other surfactants, such as potassium caprylate, polyoxyethylene cetyl/stearyl ether, and the like. For example, SDBS or another alkyl aryl sulphonate can be combined with potassium caprylate, alone or in further combination with polyoxyethylene cetyl/stearyl ether. When SDBS or another alkyl aryl sulphonate is used in combination with one or more other surfactants, preferably each surfactant is present in an amount of about 0.05-1.2 wt %, based on the dry weight of the polyisoprene, and the total amount of the surfactant package is about 0.4-1.2 wt %, based on the dry weight of the polyisoprene. When SDBS or another alkyl aryl sulphonate is used in combination with potassium caprylate and polyoxyethylene cetyl-stearyl ether, preferably the polyoxyethylene cetyl-stearyl ether is present in an amount of about 0.1-0.5 wt %, based on the dry weight of the polyisoprene.
[0030] In view of the above, the present invention provides a surfactant-stabilized, pre-vulcanized, natural polyisoprene latex composition having a chloroform index rating of 3.0. The chloroform index test measures the extent of pre-vulcanization of natural latex particles in an aqueous latex emulsion by combining equal volumes of latex and chloroform at room temperature and allowing the mixture to stand for 3 min. Chloroform coagulates the latex, and the resulting consistency is numerically rated. The consistency of the coagulum indicates the degree of pre-vulcanization of the latex. As the latex becomes more pre-vulcanized, the coagulum loses more of its tackiness and becomes more crumbly. A rating of 2.5 indicates that small lumps form, whereas a rating of 3.0 indicates that the lumps are non-tacky, a rating of 3.5 indicates that, not only are the lumps non-tacky, the lumps disintegrate easily, and a rating of 4.0 indicates that dry crumbs form, evidencing a high degree of pre-vulcanization of the natural latex particles. The pre-vulcanization is monitored to assure that the natural latex emulsion is ready for dipping.
[0031] The pre-vulcanization composition includes potassium caprylate and SDBS or another alkyl aryl sulphonate surfactants with zinc dithiocarbamate and soluble sulfur. The latex emulsion with surfactants wets the natural polyisoprene particles, catalytic action of zinc dithiocarbamate breaks the ring of soluble S.sub.8 molecule forming linear chain of soluble sulfur pre-vulcanizing particles of synthetic polyisoprene. The post-vulcanization composition has sulfur and other accelerators that cause inter-particle cross-linking during vulcanization cure. Such cross-linking results in a more homogeneous latex film having greater strength and elongation properties and crosslink density.
[0032] Sulfur is preferably present in the natural polyisoprene latex emulsion in an amount of about 0.8-1.8 wt %, based on the dry weight of polyisoprene. If zinc oxide is used, preferably it is present in an amount of about 0-0.5 wt %, based on the dry weight of polyisoprene, whereas, zinc diethyldithiocarbamate or zinc dibutyldithiocarbamate is used it is preferably present in an amount of about 0.3-1.0 wt % or more preferably about 0.3-0.45 wt %, based on the dry weight of polyisoprene.
[0033] Examples of suitable wetting agents include, but are not limited to, salts (e.g., sodium salt or potassium salt) of fatty acids, which are anionic, e.g., sodium stearate, sodium oleate, and potassium caprylate. Potassium caprylate is advantageously used with a salt of a short-chain fatty acid, SDBS and polyoxyethylene cetyl/stearyl ether. Potassium caprylate is used in an amount of 0.1-0.5 wt %, based on the dry weight of polyisoprene.
[0034] The penetration of the components of the pre-vulcanizing composition into the polyisoprene particles is a strong function of the polyisoprene particle size and size distribution. Typically, smaller particles have a larger surface area, and the components of the pre-vulcanizing composition penetrate these small particles more rapidly. However, these larger surface areas result in more intra particle regions as those smaller particles tend to pre-vulcanize faster than larger particles. The larger particles may be aggregates of smaller particles and are difficult to pre-vulcanize. Larger particles have a smaller surface area, and the components of the pre-vulcanizing composition penetrate these large particles more slowly. The smaller surface areas result in less intra particle regions. Therefore, there is a delicate balance in selecting the size and size range distribution of the natural polyisoprene particles to produce optimal strength properties that balance pre-vulcanization intra-particle cross-linking with post-vulcanization inter-particle cross-linking. As indicated above, particles in the range of about 0.2-2 micrometers provide optimal results. The penetration of the components of the pre-vulcanizing composition into the natural polyisoprene particles is also a function of the diffusion process itself, which is a linear function of time and an exponential function of temperature, reflecting a thermally activated process. Therefore, increasing the temperature by a few degrees during the pre-vulcanization step increases significantly the pre-vulcanization rate. For example, pre-vulcanization at room temperature requires from about 3-5 days to as much as about 9 days, while pre-vulcanization at an elevated temperature, e.g., about 50-70° C., requires only about 3-7 hours. However faster pre-curing is typically avoided so as to prevent pre-vulcanization taking place only on periphery of large aggregates as that would result in poor ultimate strength properties of the film: this is the case hardening reaction and the use of potassium caprylate has demonstrated that it would facilitate transporting curative agents in to the particles thus accelerating the rate of pre-vulcanization.
[0035] Preferably, the post-vulcanization composition comprises sodium dibutyl dithiocarbamate (SDBC), sulfur, a thiuram compound, and/or a xanthogen compound, alone or in further combination with a surfactant. Examples of suitable xanthogens include, but are not limited to, diisopropyl xanthogen polysulphide (DXP), diisopropyl xanthogen, tetraethylthiuram disulfide, and xanthogen sulfide. DXP is a preferred xanthogen. When present, the xanthogen is present in an amount of about 0.05 to 0.5 wt %, based on the dry weight of polyisoprene. An example of a thiuram compound is tetrabenzyl thiuram disulfide. When present, tetrabenzyl thiuram disulfide is present in an amount up to about 0.1 to 0.75 wt %, based on the dry weight of polyisoprene. The post-vulcanization composition is one that causes inter-particle cross-linking upon activation at the elevated temperature (e.g., 110-130° C.). In addition, this post-vulcanization cure also crosslinks the natural polyisoprene particles with permeated sulfur. Such crosslinking results in a more homogeneous latex film having greater strength and elongation properties.
[0036] The method comprises adding a latex-stabilizing composition, such as one comprising a surfactant package comprising at least one surfactant, such as at least one surfactant selected from the group consisting of an alkyl aryl sulphonate (e.g., SDBS), an alkyl sulphonate (e.g., olefin sulphonate) and an alcohol sulphate (e.g., sodium lauryl sulphate). If SDBS is present, preferably it is present in an amount of about 0.1-0.35 wt %, based on the dry weight of the polyisoprene. SDBS can be combined with potassium caprylate, alone or with polyoxyethylene cetyl/stearyl ether. A preferred surfactant package comprises SDBS, potassium caprylate, and polyoxyethylene cetyl/stearyl ether. If polyoxyethylene cetyl/stearyl ether is present, preferably it is present in an amount of about 0.1-0.5 wt %, based on the dry weight of the polyisoprene. Upon addition of the latex-stabilizing composition, the emulsion is stirred, e.g., for about 1 day, to keep the polyisoprene particles from touching each other.
[0037] Then, the method comprises the steps of adding a pre-vulcanization composition to formulate a natural polyisoprene latex emulsion (a) a zinc dithiocarbamate selected from zinc diethyldithiocarbamate and zinc dibutyldithiocarbamate and combinations thereof; (b) sulfur, preferably with high S.sub.8 content and (c) a wetting agent. The wetting agent is preferably a salt of a fatty acid, such as sodium stearate, sodium oleate, or potassium caprylate. The aqueous latex emulsion is stirred for about 3-4 days at about 20-25° C. or about 3-7 hours at about 50-70° C. and periodically examined for permeation of pre-vulcanization agents into the synthetic polyisoprene particles by using the isopropanol index test. The reason why this sequence is adopted is because the polyisoprene latex has an inherent tendency to flock and ‘case harden’ due to peripheral reaction with sulfur catalyzed by ZDBC or ZDEC. This has to be prevented so that tightly bonded particles do not result. The presence of surfactants and creation of opened out S.sub.8 chains of sulfur enables the diffusion of sulfur into the particles.
[0038] The method further comprises the steps of adding post-vulcanization composition to the natural polyisoprene latex emulsion with accelerators selected from the group consisting of SDBC, reactive zinc oxide, sodium diethyldithiocarbamate, sodium dibutyldithiocarbamate, thiuram such as tetrabenzyl thiuram disulfide and xanthogen. If reactive zinc oxide is present, preferably it is present in an amount of about 0 to 0.5 wt %, based on the dry weight of polyisoprene. The thiuram can be tetraethylthiuram disulfide, tetrabenzyl thiuram disulfide, which, if present, is preferably present in an amount up to about 0.75 wt %, based on the dry weight of polyisoprene. The xanthogen can be DXP, diisopropyl xanthogen, or xanthogen sulfide. If a xanthogen is present, preferably it is present in an amount of about 0.2 to 0.8 wt %, based on the dry weight of polyisoprene. The composition thus produced is stable for up to about 60 days at 25° C. and can be used in a production line.
[0039] Table 1 below shows an example of a composition that exhibits pre-vulcanization behavior.
TABLE-US-00001 TABLE 1 Quantity per hundred dry Formulation rubber (phr) Natural Latex 100 SDBS 0.1-0.3 potassium caprylate 0.1-0.46 polyoxyethylene cetyl/stearyl ether 0.1-0.5 sulfur 0.8-1.8 reactive zinc oxide 0.05-0.5 ZDEC 0.4-1.0 SDBC 0.05-0.5 DXP 0.2-0.6 Wingstay L antioxidant 0.5-1.0
[0040] Thus, the present invention further provides a method of forming a natural polyisoprene latex article. The former can be any suitable former as is known in the art. The present inventive composition is particularly useful for layering onto formers for shoe covers. The method comprises dipping a coagulant coated former in the above-described pre-vulcanized natural polyisoprene aqueous latex emulsion composition with a solid content of 50 to 55% with a viscosity of 18 to 22 second using ford cup #4 to form a thin layer of latex film with a thickness of 200 to 350 microns with individual particles of pre-vulcanized natural polyisoprene touching each other on the surface of the former.
[0041] After the first layer of latex film is not runny with a typical thickness of 200 to 350 microns, the bottom portion of the shoe cover is dipped in a denser natural polyisoprene emulsion with a solid content of 50 to 55% and having viscosity of 25 to 30 seconds with ford cup #6 to form a thicker latex layer of about 800 to 1200 microns at the bottom portion of the shoe cover. This enhanced thickness of the latex layer at the bottom prevents tearing as the shoe cover is donned. The method further comprises etching the thicker layer of natural latex with an etching solution of toluene, ethyl alcohol an acetic acid which forms three separate streams due to the immiscibility of toluene with ethyl alcohol and acetic acid. Following this there is an immersion of the entire shoe cover into a polymer solution. The natural rubber film is post-vulcanized by heating the film, e.g., to about 110 to 130° C. for about 8 to 15 min. During this period, the inter-particle regions are cross-linked. The intra-particle regions also undergoes further crosslinking, producing a more homogeneous latex product. Then, the method comprises stripping the latex film from the former.
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[0043]
[0044]
[0045]
[0046]
[0047] All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
[0048] The use of the terms “a,” “an,” “the,” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to illuminate better the invention and does not pose a limitation on the scope of the invention, unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.