US1945173A - Artificial leather manufacture - Google Patents
Artificial leather manufacture Download PDFInfo
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- US1945173A US1945173A US625032A US62503232A US1945173A US 1945173 A US1945173 A US 1945173A US 625032 A US625032 A US 625032A US 62503232 A US62503232 A US 62503232A US 1945173 A US1945173 A US 1945173A
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- Prior art keywords
- latex
- web
- rubber
- sheet
- plies
- Prior art date
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- Expired - Lifetime
Links
- 238000004519 manufacturing process Methods 0.000 title description 12
- 239000002649 leather substitute Substances 0.000 title description 8
- 229920000126 latex Polymers 0.000 description 54
- 239000004816 latex Substances 0.000 description 46
- 229920001971 elastomer Polymers 0.000 description 30
- 239000000835 fiber Substances 0.000 description 29
- 239000010985 leather Substances 0.000 description 23
- 239000000701 coagulant Substances 0.000 description 21
- 239000000243 solution Substances 0.000 description 16
- 238000005507 spraying Methods 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- 239000007921 spray Substances 0.000 description 11
- 238000001035 drying Methods 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229940037003 alum Drugs 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 238000004073 vulcanization Methods 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 3
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000009950 felting Methods 0.000 description 3
- 229920000742 Cotton Polymers 0.000 description 2
- NQRYJNQNLNOLGT-UHFFFAOYSA-N Piperidine Chemical compound C1CCNCC1 NQRYJNQNLNOLGT-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000007900 aqueous suspension Substances 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 238000009960 carding Methods 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000975 dye Substances 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 230000000750 progressive effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- 239000001263 FEMA 3042 Substances 0.000 description 1
- 241001076195 Lampsilis ovata Species 0.000 description 1
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 239000004902 Softening Agent Substances 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 239000003026 cod liver oil Substances 0.000 description 1
- 235000012716 cod liver oil Nutrition 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 1
- 229940033123 tannic acid Drugs 0.000 description 1
- 235000015523 tannic acid Nutrition 0.000 description 1
- 229920002258 tannic acid Polymers 0.000 description 1
- 210000003371 toe Anatomy 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/28—Organic non-cellulose fibres from natural polymers
- D21H13/34—Protein fibres
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
- D06N3/04—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D06N3/10—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof with macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds with styrene-butadiene copolymerisation products or other synthetic rubbers or elastomers except polyurethanes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/35—Polyalkenes, e.g. polystyrene
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H5/00—Special paper or cardboard not otherwise provided for
- D21H5/12—Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials
- D21H5/1209—Special paper or cardboard not otherwise provided for characterised by the use of special fibrous materials of protein fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
Definitions
- This invention relates to the manufacture of formed into the web, I prefer to add a solution artificial leather ,throughthe use of suitable of the coagulant, as by spraying, to the wet, fibrous material and aqueous rubber dispersions freshly-formed web immediately before it reof the nature of latex as raw materials. ceives the latex and is then plied.
- waste leather stock e. g., waste leather of use as the fibrous material promoting felting chrome or other tannage
- waste natural silk such as is available at a cost leather stock can be beaten in water to form a not exceeding that of rag stock, wood pulp, or pulp, but the pulp thus produced is of such a similar cellulosic fiber.
- coagulant solution may,
- I 45 stock is generally formed into a multi-ply sheet for instance, be one of alum of about 10% from a single web built up on a so-called makestrength.
- the latex can be sprayed onto the web up roll or from a number of webs plied on a mulat various solids contents, but, considering the ti-cylinder machine. It isthus seen that my inparticular results which I am seeking, it is prefvention fits nicely into the picture when leather erable to work with latex of a solids content,
- the latex may, for example, be properly the web while it is pursuing its course as usual compounded with sulphur, zinc oxide, an accelthrough the machine. erator of vulcanization, and suitable pigments While the rubber coagulant may be incorporator dyes, all colloidally suspended in the latex, so
- the compounded latex may be prepared by adding to latex of about 30% solids content about 3% to 8% sulphur, about 5% to 7% zinc oxide, about 4% piperidine or other accelerator of vulcanization, and'a suitable dye or pigment, e. g., analine black, yellow, or green. These proportions of compounding agents are all based on the weight of the solids content of the latex.
- the compounded latex may be passed through a homogenizer or colloid mill, to ensure a condition therein compatible with its being properly ,sprayed.
- the latex so treated may be diluted,
- Figure 1 illustrates diagrammatically and conventionally a cylinder machine equipped for the practice of the. present invention.
- Figure 2 is a similar illustration of a multicylinder machine equipped for the same purpose.
- a cylinder mould 10 rotates partially submerged in a pulp suspension kept in the cylinder vat 11.
- the .pulp may be of the character hereinbefore described or any other kind lending itself to deposition from water as a coherent, felted web.
- the web of pulp progressively deposited on the periphery of the mould is carried out of the vat and is then picked up by the usual transfer felt 12 making constant contact with the unsubmerged portion of the mould under the action of the roll 13.
- the felt conveys the wetweb to a make-up roll 14 shown. stationed above a roll 15 constituting the terminal roll for the felt.
- each ply or convolution receives first a spray of alum solution from a nozzle 16, then a spray of properly compounded latex from a nozzle 17, and finally aspray of alum solution from a nozzle 18.
- Each spray should be delivered over the full width of the web and is preferably kept within a chamber defined by the roll 14 and a box 19 whose inner edges clear the roll sufficiently to permit the web to be built up to the desired thickness.
- the latex is completely coagulated on each of the plies, there is no tendency to squeeze latex from the web in the nip of the rolls 14 and 15 so as to gum the felt. Aside from the fact that the fibers of each of the plies are treated with rubber, the freshly coagulated rubber film developed between the plies ensures tenacious ply adhesion.
- the sheet is cut axially of the roll and removed in fiat condition from the roll as ordinarily. The fiat sheet is then dried at elevated temperature for the purpose of causing vulcanization of the rubber binder therein.
- a multi-cylinder machine such as depicted in Figure 2 is employed in making the plied one cylinder mould .and then acquires anotherfrom the next cylinder mould directly on the web previously picked up.
- Each ply receives the suecessive sprays of alum solution, latex, and alum solution while carried by the felt, before the next ply is deposited thereon.
- the multi-ply sheet may be taken from the terminal roll 25 for the felt 20 and delivered over a bank of heated drier drums 26, which conduce to vulcanization of the rubber in the sheet, as well as drying of the sheet.
- An important feature of the process of my invention is that a comparatively small amount of rubber need be used in producing a finished article of extraordinary toughness andstrength. In-.
- aqueous rubber dispersions of the nature of latex rather than natural latex, as the coagulable binding agent.
- latex is used in the specification and claims in its comprehensive sense to mean not only natural latex, but also synthetic or artificial latices partaking of the qualities of natural latex. So, too, various wellknown acid solutions or acid salt solutions may be used in lieu of the alum solution as the coagulant for the latex.
- the strength of coagulant solution may be varied, but in any event, it is desirable to use a solution of such strength as will cause quick and complete coagulation of the latex spray as it strikes the freshly-formed web wet of tanning agent serves as raw'material, this insufficiency may be made up by adding more chromium tanning agent, tannic acid, or the like.
- fat liquors containing sulphonated castor oil, cod liver oil, or other softening agents for the leather fibers may be added to the furnish for the purpose of lending pliancy and mellowness to the finished articles.
- the principles of the present invention extend to the manufacture of a plied sheet from webs of cotton and/or wool or the like formed in a dry way as on carding machines.
- a web or felt produced in this way may be treated with coagulant solution and latex as it is being wound on a mandrel or take-off roll to the desired thickness.
- the felt plied sheet removed from the mandrel may be dried and its rubber content vulcanized, if desired.
- Such an adaptation of my method may be of value especially in those instances when a thick artificial leather, say one whose thickness is A to is desired for such uses as shoe outer soles.
- the artificial leather fabricated in accordance with my invention is characterized by having its rubber content distributed therethrough in such a way that, not only does each ofthe plies contain. rubber latex coagulated on its fibers and penetrating thereinto, but the latex coagulated as a film between the plies serves to integrate them most effectively, especially since this film is substantially continuous with the latex coagulated in the plies themselves.
- a multi-ply the latex coagulated in said film being substanwaterlaid sheet of leather fibers and a smaller proportion of natural silk fibers containing rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film being substantially continuous with the latex coagulated in the plies.
- a process which comprises treating a web of fibers containing a rubber coagulant with latex, plying the resulting web containing freshly coagulated rubber into a sheet of the desired thickness, and drying the plied sheet.
- a process which comprises treating a web of waterlaid fibers containing a rubber coagulant with latex, plying the resulting web containing freshly coagulated rubber into a sheet of the desired thickness, and drying the plied sheet at elevated temperature to cause vulcanization of the rubber therein.
- a process which comprises spraying an aqueous solution of a rubber coagulant onto a wet, freshly-formed web of waterlaid fibers, spraying latex onto the web, plying the resulting web containing freshly coagulated rubber with similarly treated web into a sheet of the desired thickness, and drying the plied sheet.
- a process which comprises the following progressive steps, viz., depositing fibers from aqueous suspension into a web, spraying an aqueous solution of rubber coagulant onto the wet, freshly-formed web, spraying latex onto the web, again spraying an aqueous solution'of rubber coagulant onto the web, and plying the resulting web containing, freshly coagulated rubher with similarly treated web into a sheet 'of the desired thickness.
- a process which comprises the following progressive steps, viz., depositing fibers from aqueous suspension into a web, spraying an aqueous solution of rubber coagulant onto the wet, freshly-formed web, spraying latex onto the web, again spraying an aqueous solution of rubber coagulant onto the web, plying the resulting web containing freshly coagulated rubber with similarly treated web into-a sheet of the desired 20 thickness, and treating the plied sheet at elevated temperature to cause vulcanization of the rubber therein 12.
- a process which comprises beating stock consisting essentially of waste leather in the 5 presence of water until it has been reduced to a pulp, forming the pulp into a web, spraying latex onto the wet, freshly-formed web, plying the resulting web containing freshly'coagulated rubber with similarly treated, web into a sheet of the 13 desired thickness, and drying the plied sheet.
- a process which comprises beating stock consisting essentially of chrome-tanned leather waste while it is still wet with tanning liquor in the presence of water until it has been reduced 5 to a pulp, forming the pulp into a web, spraying the web in wet, freshly-formed condition with latex and coagulant solution, plying the resulting web containing freshly coagulated rubber with similarly treated web into a sheet of the 140 desired thickness, and drying the plied sheet.
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- Molecular Biology (AREA)
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Description
Jan. 30, 1934. O, WQODRUFF 1,945,173
ARTIFICIAL LEATHER MANUFACTURE Filed July 27, 1932 pasted Jan. 30,1934 1,945,l73
UNITED STATES PATENT OFFICE i 1,945,173 ARTIFICIAL LEATHER MANUFACTURE Frank 0. Woodrufi, Newton, Mass., assignor, by
mesne assignments, to Beckwith Manufacturing Company, Boston, Mass, a corporation of Massachusetts Application July 27, 1932. Serial No. 625,032 13 Claims. (01. 92-41) This invention relates to the manufacture of formed into the web, I prefer to add a solution artificial leather ,throughthe use of suitable of the coagulant, as by spraying, to the wet, fibrous material and aqueous rubber dispersions freshly-formed web immediately before it reof the nature of latex as raw materials. ceives the latex and is then plied. Indeed, even In making artificial leather from latex and a when a coagulant is added to the stock, I prefer 60 web of fibers, such as formed on a papermaking to spray coagulant solution onto the web, then or carding machine, it is difiicult to accomplish to apply the latex, and finally again to spray a satisfactory distribution of rubber as-a binder coagulant solution on the latex, as this ensures throughout the web, especially when the web is a complet gulation of the latex, attendedy built up to a considerable thickness. In the case the o ing of the fib r wi h r b r n the d 65 of multi-ply webs such as made on cylinder pavelopment of a bonding fiber of rubber between permaking machines, there is the additional probplies. This sort of practice further means that lem of securing adequate ply adhesion so that when subsequent plying of the web is done under therejwill be little tendency for the rubber-imp s u th r is no t nd y r u a d pregnated product to split on the planes of bondlatex B t e edges of the Sheet and 110 70 ing between plies. gum the felts or other instrumentalities of the In accordance with the present invention, I machine. prepare a plied sheet which is properly impreg- Assuming that chrome-tanned leather waste is nated with rubber and whose plies are so tenaused as a raw material, I prefer to procure such ciously bonded together that there are no defiwaste while it is still wet with the chrome tan- :5 nite planes of cleavage therein. In the case of ning liquor. In this condition, the leather waste waterlaid webs made on papermaking machines, may be put into a heater engine and readily disthese results are had by incorporating a rubber integrated in the presence of water into a pulp coagulant in the wet, freshly-formed web and'apamenable to web formation. Along with the plying latex to the web, as by spraying, before leather water, I prefer to use a relatively small so it is built up into a multi-ply structure as on a proportion, say 10%, o ot fiber, so as to ma-ke-up roll and is then dried, or before it is prove the felting action of the leather fiber united with other webs being similarly treated on the papermaking machine. Cellulose fiber, on a multi-cylinder machine. I e. g., cotton rag fiber, promotes good felting ac- While the process of the present invention is tion, but I have found that natural silk fiber s5 applicable when'cellulosic and/or other kinds of does the same and additionally enhances the fiber are being formed into a web on papermakstrength, pliancy, and smoothness of surface ing or other machinery, it is especially useful in the ultimate product. Accordingly, I prefer to when waste leather stock, e. g., waste leather of use as the fibrous material promoting felting chrome or other tannage, is to serve as raw maaction of the beaten leather stock a low grade terial for making'a leather substitute. Such waste natural silk such as is available at a cost leather stock can be beaten in water to form a not exceeding that of rag stock, wood pulp, or pulp, but the pulp thus produced is of such a similar cellulosic fiber.
slow or slimy'nature that the desired dewater- The wet, freshly-formed web of pulp receives,
40 ing on the papermaking machine, coupled with a' in accordance with my preferred procedure, first running of the machine at an acceptable rate of a spray of coagulant solution, "then a spray of speed, can be had only with a comparatively thin latex, and finally another spray of coagulant web. Consequently, in order to re lize a web solution, before'it is plied into a sheet of the of the desired thickness, such bea en leather desired thickness. The coagulant solution may,
I 45 stock is generally formed into a multi-ply sheet for instance, be one of alum of about 10% from a single web built up on a so-called makestrength. The latex can be sprayed onto the web up roll or from a number of webs plied on a mulat various solids contents, but, considering the ti-cylinder machine. It isthus seen that my inparticular results which I am seeking, it is prefvention fits nicely into the picture when leather erable to work with latex of a solids content,
50 stock is being formed as .ordinarily into a plied including compounding agents, of about 15% to sheet, as I can add the coagulant and latex to 30%. p The latex may, for example, be properly the web while it is pursuing its course as usual compounded with sulphur, zinc oxide, an accelthrough the machine. erator of vulcanization, and suitable pigments While the rubber coagulant may be incorporator dyes, all colloidally suspended in the latex, so
5 ed into the beaten leather stock before it is that there will be no trouble in the spraying operation. The compounded latex may be prepared by adding to latex of about 30% solids content about 3% to 8% sulphur, about 5% to 7% zinc oxide, about 4% piperidine or other accelerator of vulcanization, and'a suitable dye or pigment, e. g., analine black, yellow, or green. These proportions of compounding agents are all based on the weight of the solids content of the latex. The compounded latex may be passed through a homogenizer or colloid mill, to ensure a condition therein compatible with its being properly ,sprayed. The latex so treated may be diluted,
if desired, with water, to a solids content of about 15% for the spraying operation. By the use of such compounded latex, it is possible to realize a smooth, flexible, vulcanized sheet of the desired color and simulating in its strength, tear resistance, toughness, feel, and other qualities a natural leather. The sheet thus produced may be embossed and subjected to other customary leather-finishing operations. The finished sheet can, like natural leather, go into furniture upholstering, automobile tops, book covers, pocketbooks shoe inner and outer soles, counters and box toes for shoes, and other uses.
On the accompanying drawing,
Figure 1 illustrates diagrammatically and conventionally a cylinder machine equipped for the practice of the. present invention.
Figure 2 is a similar illustration of a multicylinder machine equipped for the same purpose.
As shown in Figure 1, a cylinder mould 10 rotates partially submerged in a pulp suspension kept in the cylinder vat 11. The .pulp may be of the character hereinbefore described or any other kind lending itself to deposition from water as a coherent, felted web. The web of pulp progressively deposited on the periphery of the mould is carried out of the vat and is then picked up by the usual transfer felt 12 making constant contact with the unsubmerged portion of the mould under the action of the roll 13. The felt conveys the wetweb to a make-up roll 14 shown. stationed above a roll 15 constituting the terminal roll for the felt. As the web is being convoluted on the roll 14 to the desired thickness, each ply or convolution receives first a spray of alum solution from a nozzle 16, then a spray of properly compounded latex from a nozzle 17, and finally aspray of alum solution from a nozzle 18. Each spray should be delivered over the full width of the web and is preferably kept within a chamber defined by the roll 14 and a box 19 whose inner edges clear the roll sufficiently to permit the web to be built up to the desired thickness.
Inasmuch as the latex is completely coagulated on each of the plies, there is no tendency to squeeze latex from the web in the nip of the rolls 14 and 15 so as to gum the felt. Aside from the fact that the fibers of each of the plies are treated with rubber, the freshly coagulated rubber film developed between the plies ensures tenacious ply adhesion. After the desired sheet thickness has been reached on the make-up roll, the sheet is cut axially of the roll and removed in fiat condition from the roll as ordinarily. The fiat sheet is then dried at elevated temperature for the purpose of causing vulcanization of the rubber binder therein.
When a multi-cylinder machine such as depicted in Figure 2 is employed in making the plied one cylinder mould .and then acquires anotherfrom the next cylinder mould directly on the web previously picked up. Each ply receives the suecessive sprays of alum solution, latex, and alum solution while carried by the felt, before the next ply is deposited thereon. For this purpose, I have shown a series of three sprays 24 located under the felt 20 and inback of each cylinder mould, so that each ply becomes properly treated with rubber before the next ply is superposed thereon. The multi-ply sheet may be taken from the terminal roll 25 for the felt 20 and delivered over a bank of heated drier drums 26, which conduce to vulcanization of the rubber in the sheet, as well as drying of the sheet. a
An important feature of the process of my invention is that a comparatively small amount of rubber need be used in producing a finished article of extraordinary toughness andstrength. In-.
deed, I have found that the incorporation, through my process, of only about 15% to 50% of latex solids into a sheet composed essentially of chrome-tanned leather fibers and built up of plies to a thickness of 70/1000 of an inch makes for a product of such strength and toughness that its tearing cannot be initiated with ones hands.
It is, of course, possible to use artificial aqueous rubber dispersions of the nature of latex, rather than natural latex, as the coagulable binding agent. If desired, a prevulcanized latex such as is sold on the market as Vultex, may be used, in=which case mere drying of the latex even under room temperature conditions yields a vulcanized rubber. Accordingly, the term latex is used in the specification and claims in its comprehensive sense to mean not only natural latex, but also synthetic or artificial latices partaking of the qualities of natural latex. So, too, various wellknown acid solutions or acid salt solutions may be used in lieu of the alum solution as the coagulant for the latex. The strength of coagulant solution may be varied, but in any event, it is desirable to use a solution of such strength as will cause quick and complete coagulation of the latex spray as it strikes the freshly-formed web wet of tanning agent serves as raw'material, this insufficiency may be made up by adding more chromium tanning agent, tannic acid, or the like.
So, too, one may use along with the leather stock 3 various proportions of cellulosic, silk, or other fibers to improve the texture of the web formed on the paper-making machine, as well as to lend 1 other desirable characteristics to the ultimate article. By controlling the beater furnish through the use of the appropriate fibers or mixtures of fibers, as well as tanning or other modifying agents, I can realize in my finished article the qualities of flexibility, softness, or stiffness, as
desired. For instance, so-called fat liquors containing sulphonated castor oil, cod liver oil, or other softening agents for the leather fibers may be added to the furnish for the purpose of lending pliancy and mellowness to the finished articles.
The principles of the present invention extend to the manufacture of a plied sheet from webs of cotton and/or wool or the like formed in a dry way as on carding machines. A web or felt produced in this way may be treated with coagulant solution and latex as it is being wound on a mandrel or take-off roll to the desired thickness. The felt plied sheet removed from the mandrel may be dried and its rubber content vulcanized, if desired. Such an adaptation of my method may be of value especially in those instances when a thick artificial leather, say one whose thickness is A to is desired for such uses as shoe outer soles.
The artificial leather fabricated in accordance with my invention is characterized by having its rubber content distributed therethrough in such a way that, not only does each ofthe plies contain. rubber latex coagulated on its fibers and penetrating thereinto, but the latex coagulated as a film between the plies serves to integrate them most effectively, especially since this film is substantially continuous with the latex coagulated in the plies themselves.
What I claim is: 4
1. As an article of manufacture, a multi-ply sheet of fibers containing rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film being substantially continuous with the latex coagulated in the plies.
2. As an article of manufacture, a multi-ply waterlaid sheet of essentially leather fibers con-' taining rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film bein substantially continuous with the latex coagulated in the plies.
3. As an article of manufacture, a multi-ply waterlaid sheet of essentially chrome-tanned leather fibers containing rubber latex in coagulated and vulcanized condition not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film being substantially continuous with the latex coagulated in the plies.
4. As an article of manufacture, a multi-ply waterlaid sheet of leather fibers and a. smaller proportion of other fibers containing rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, tially continuous with the plies.
5. As an article of manufacture, a multi-ply waterlaid sheet of leather fibers and a smaller proportion of cellulosic fibers containing rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film being substantially continuous with the latex coagulated in the plies.
6. As an article of manufacture, a multi-ply the latex coagulated in said film being substanwaterlaid sheet of leather fibers and a smaller proportion of natural silk fibers containing rubber latex coagulated not only in its plies but also in between its individual plies as a film serving to integrate the plies, said film being substantially continuous with the latex coagulated in the plies.
'7. A process which comprises treating a web of fibers containing a rubber coagulant with latex, plying the resulting web containing freshly coagulated rubber into a sheet of the desired thickness, and drying the plied sheet.
3. A process which comprises treating a web of waterlaid fibers containing a rubber coagulant with latex, plying the resulting web containing freshly coagulated rubber into a sheet of the desired thickness, and drying the plied sheet at elevated temperature to cause vulcanization of the rubber therein.
9. A process which comprises spraying an aqueous solution of a rubber coagulant onto a wet, freshly-formed web of waterlaid fibers, spraying latex onto the web, plying the resulting web containing freshly coagulated rubber with similarly treated web into a sheet of the desired thickness, and drying the plied sheet.
10. A process which comprises the following progressive steps, viz., depositing fibers from aqueous suspension into a web, spraying an aqueous solution of rubber coagulant onto the wet, freshly-formed web, spraying latex onto the web, again spraying an aqueous solution'of rubber coagulant onto the web, and plying the resulting web containing, freshly coagulated rubher with similarly treated web into a sheet 'of the desired thickness.
ll. A process which comprises the following progressive steps, viz., depositing fibers from aqueous suspension into a web, spraying an aqueous solution of rubber coagulant onto the wet, freshly-formed web, spraying latex onto the web, again spraying an aqueous solution of rubber coagulant onto the web, plying the resulting web containing freshly coagulated rubber with similarly treated web into-a sheet of the desired 20 thickness, and treating the plied sheet at elevated temperature to cause vulcanization of the rubber therein 12. A process which comprises beating stock consisting essentially of waste leather in the 5 presence of water until it has been reduced to a pulp, forming the pulp into a web, spraying latex onto the wet, freshly-formed web, plying the resulting web containing freshly'coagulated rubber with similarly treated, web into a sheet of the 13 desired thickness, and drying the plied sheet.
13. A process which comprises beating stock consisting essentially of chrome-tanned leather waste while it is still wet with tanning liquor in the presence of water until it has been reduced 5 to a pulp, forming the pulp into a web, spraying the web in wet, freshly-formed condition with latex and coagulant solution, plying the resulting web containing freshly coagulated rubber with similarly treated web into a sheet of the 140 desired thickness, and drying the plied sheet.
FRANK O. WOODRUFF.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US625032A US1945173A (en) | 1932-07-27 | 1932-07-27 | Artificial leather manufacture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US625032A US1945173A (en) | 1932-07-27 | 1932-07-27 | Artificial leather manufacture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1945173A true US1945173A (en) | 1934-01-30 |
Family
ID=24504299
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US625032A Expired - Lifetime US1945173A (en) | 1932-07-27 | 1932-07-27 | Artificial leather manufacture |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1945173A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2418282A (en) * | 1942-10-07 | 1947-04-01 | Carborundum Co | Abrasive manufacture |
| US2653870A (en) * | 1949-10-22 | 1953-09-29 | Richard P Kast | High-strength paper and method of making |
| US2778284A (en) * | 1954-05-14 | 1957-01-22 | Patent & Licensing Corp | Method of and apparatus for applying aqueous dispersions in manufacture of paperboard and the like |
| US2870689A (en) * | 1952-12-04 | 1959-01-27 | Helen E Brennan | Method of producing strip material |
| US3051612A (en) * | 1962-08-28 | Substitute leathers and the manufacture thereof | ||
| US3102837A (en) * | 1961-03-13 | 1963-09-03 | United Shoe Machinery Corp | Stiffener material for shoes |
| US20220282343A1 (en) * | 2021-03-04 | 2022-09-08 | Omnia Advanced Materials LLC | Process for manufacturing reconstituted leather product |
-
1932
- 1932-07-27 US US625032A patent/US1945173A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3051612A (en) * | 1962-08-28 | Substitute leathers and the manufacture thereof | ||
| US2418282A (en) * | 1942-10-07 | 1947-04-01 | Carborundum Co | Abrasive manufacture |
| US2653870A (en) * | 1949-10-22 | 1953-09-29 | Richard P Kast | High-strength paper and method of making |
| US2870689A (en) * | 1952-12-04 | 1959-01-27 | Helen E Brennan | Method of producing strip material |
| US2778284A (en) * | 1954-05-14 | 1957-01-22 | Patent & Licensing Corp | Method of and apparatus for applying aqueous dispersions in manufacture of paperboard and the like |
| US3102837A (en) * | 1961-03-13 | 1963-09-03 | United Shoe Machinery Corp | Stiffener material for shoes |
| US20220282343A1 (en) * | 2021-03-04 | 2022-09-08 | Omnia Advanced Materials LLC | Process for manufacturing reconstituted leather product |
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