US2971879A - Water-laid fibrous sheets - Google Patents
Water-laid fibrous sheets Download PDFInfo
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- US2971879A US2971879A US695520A US69552057A US2971879A US 2971879 A US2971879 A US 2971879A US 695520 A US695520 A US 695520A US 69552057 A US69552057 A US 69552057A US 2971879 A US2971879 A US 2971879A
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- United States
- Prior art keywords
- slurry
- fibers
- zinc oxide
- rubber
- added
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims description 66
- 239000011787 zinc oxide Substances 0.000 claims description 33
- 239000002002 slurry Substances 0.000 claims description 31
- 239000000835 fiber Substances 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 16
- 229920003051 synthetic elastomer Polymers 0.000 claims description 13
- 239000005061 synthetic rubber Substances 0.000 claims description 13
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 9
- 239000000908 ammonium hydroxide Substances 0.000 claims description 9
- 229920006174 synthetic rubber latex Polymers 0.000 claims description 8
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052725 zinc Inorganic materials 0.000 claims description 7
- 239000011701 zinc Substances 0.000 claims description 7
- 239000004816 latex Substances 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- 239000000243 solution Substances 0.000 claims description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052749 magnesium Inorganic materials 0.000 claims description 3
- 239000011777 magnesium Substances 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 239000000725 suspension Substances 0.000 claims description 2
- 229960001296 zinc oxide Drugs 0.000 description 32
- 229920001971 elastomer Polymers 0.000 description 18
- 239000005060 rubber Substances 0.000 description 18
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 14
- 229920000126 latex Polymers 0.000 description 10
- 235000012434 pretzels Nutrition 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 238000013019 agitation Methods 0.000 description 6
- 229920001577 copolymer Polymers 0.000 description 6
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 229920001084 poly(chloroprene) Polymers 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 239000002655 kraft paper Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 2
- 229940037003 alum Drugs 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 239000007799 cork Substances 0.000 description 2
- BUACSMWVFUNQET-UHFFFAOYSA-H dialuminum;trisulfate;hydrate Chemical compound O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O BUACSMWVFUNQET-UHFFFAOYSA-H 0.000 description 2
- 229920001821 foam rubber Polymers 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- 241000088885 Chlorops Species 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 241001237728 Precis Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000005083 Zinc sulfide Substances 0.000 description 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 1
- 235000011128 aluminium sulphate Nutrition 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- NTXGQCSETZTARF-UHFFFAOYSA-N buta-1,3-diene;prop-2-enenitrile Chemical compound C=CC=C.C=CC#N NTXGQCSETZTARF-UHFFFAOYSA-N 0.000 description 1
- IRLQAJPIHBZROB-UHFFFAOYSA-N buta-2,3-dienenitrile Chemical compound C=C=CC#N IRLQAJPIHBZROB-UHFFFAOYSA-N 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- -1 diphenyl amines Chemical class 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 235000011147 magnesium chloride Nutrition 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
- IPCXNCATNBAPKW-UHFFFAOYSA-N zinc;hydrate Chemical compound O.[Zn] IPCXNCATNBAPKW-UHFFFAOYSA-N 0.000 description 1
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 description 1
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
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
- D21H17/675—Oxides, hydroxides or carbonates
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/76—Processes or apparatus for adding material to the pulp or to the paper characterised by choice of auxiliary compounds which are added separately from at least one other compound, e.g. to improve the incorporation of the latter or to obtain an enhanced combined effect
- D21H23/765—Addition of all compounds to the pulp
Definitions
- the process contemplates pretreating the fibers with a watersoluble'salt of aluminum, magnesium, or zinc, followed by the addition of ammonium hydroxide to form the insoluble metallic hydroxide.
- a synthetic rubber latex brings about the smooth and even deposition of the rubber particles on the individual fibers in the slurry.
- the rubber coated :furnish fiber; stock is then fed to a paper-forming machine such as a Fourdrin ier, cylinder machine, or the like. This process allows 2,971,879 Patented F eb, 14, 1961 excellent control of the deposition of rubber on fibers in a papermaking slurry.
- the invention contemplates the addition of finely divided zinc oxide subsequent to the step of adding the ammonium hydroxide to form the metal hydroxide in the Pretzel process and prior to the step of adding the'synthetic rubber latex.
- the result of the addition of zinc oxide at this point in the Pretzel process is that the stock possesses a higher Canadian freeness, presents a more clumpy appearance to the eye, and enables the formation of a thicker sheet.
- the fibers contemplated for treatment by the present invention are cellulosic fibers such as kraft, rags, soda. pulp, wood pulp, cotton linters, and the like.
- the fibers may be present in the slurry along with additional, sheetforming materials such as finely divided cork or finely divided scrap foam rubber; use of finely divided cork with fibers is fully described in US. Patent 2,613,190Feigley.
- the fibers and additional material, if any, aretaken up in water in the usual manner to form a slurry which will generally be in the consistency range of about 0.5-5%.
- This slurry may then be subjected to mechanical refining in the usual refiners such as Jordan engines, beaters, disc refiners, and the like.
- the consistency- may be adjusted to that desired for further treatment. Generally this consistency will be in the range of about l3%.
- a water-soluble salt of a suitable electrolyte such as papermakers alum, aluminum chloride, aluminum sulphate, magnesium chloride, magnesium sulphate, zinc chloride, and the like.
- a suitable electrolyte such as papermakers alum, aluminum chloride, aluminum sulphate, magnesium chloride, magnesium sulphate, zinc chloride, and the like.
- the salt may be added in the form of its water solution.
- the amount of the electrolyte to be added will generally be in the range of about 25-75% I by weight based on the amount of rubber to be deposited on the fibers subsequently. 1
- reaction proceeds rapidly, and gentle agitation for-' a few minutes is all that is needed.
- the presentinvention calls for the addition of zinc water; the slurry is simply poured into the papermaking slurry with gentle agitation.
- the zinc oxide is added as finely divided zinc oxide commonly known as pigment grade or filler grade zinc oxide; these are readily available incommerce.
- the amount of zinc oxide to be added 1 of aluminum hydroxide which has been formed in the papermaking slurry. Since will be controlled by the amount the amount of aluminum hydroxide is controlled to some oxide at this point.
- the zinc oxide is preferably added in the form of a slurryin- :acrnere r extent by the amount of rubber to be "deposited on "ihe fibers, it can be seen that the amount of rubber ultimately controls the amount of zinc oxide to be added. Generally speaking, the zinc oxide will be added in an amount of about 3-50% j by" weight based on the total weight of rubber to be deposited on the fibers.
- Typical of these synthetic rubbers arethe products *known as; GR+S, which is a copolymer of butadiene and-styrene containing about 50% to about 70% butadiene.
- GR+S which is a copolymer of butadiene and-styrene containing about 50% to about 70% butadiene.
- GR+S which is a copolymer of butadiene and-styrene containing about 50% to about 70% butadiene.
- as l lycars which are copolymers of'butadiene-and acrylonitrile containing about 50% to about 80% butadiene.
- the polychloroprenes may also be'used.
- Example 1 mm 3,750 parts of water there was asse-1" kraft fiber, and 20 parts "Of finelydi'vide'd foam rubber scrap. There was then added 10 -parts papermakers are polymers'of-Z-chlordbutadiene-1,3. If desired homop'olyin'erso'f 'butadiene may begemployed as well as homopolymers and/or copolymers of butadiene homologues snchasisoprene. T hese materials can be vgenerally designated as "synthetic rubbers and more specifically designated asrubberlike polymers of butadiene, isoprene,
- the latices are added in an amount suflicie'nt 'to introduce the required amount of r'ubberto be deposited on the fib ers. Normally this will bein'the range; of about 10-1 00% iby weight rubber based on the dry Weight of'the fiber s. v V U V I
- Theselected latex is simplypoured into the zinc oxide treated slurry withgentle agitation. Therubber content or the latex coagulats and evenly deposits upon the fibers. Since'zinc oxide is subst'antiallyiinsoluble in water under the beater saturation conditions of the Pretzel process, the rubber particles carry with-them all the zinc-oxide which is suspended in the whitewater.
- the resulting coatedfibers carrfyaninner coating of Zinc oxide and an outer'coating'of a synthetic rubber binder, which binder distributed throughout additional particles of zinc 0x1 e.
- a butadiene-styrene latex containing styrene, 40% by weight solids (FRS-ZOOO was added to the resulting slurry in anamount of 45 parts.
- Antioxidantstofstabilize the rubber against oxidation were "also added, ifria 1.34 partsof a 45% dispersion ofainixtureoff I and 'di-heptyl'diphenyl amines, and 0,75 part .poly merized l,2-dihydro'-2,2,4-trimethyl quinolijne. 'rreeipi: tation of the rubber was 'complete'in 5 minutes,
- Sheets were prepared fromboth stocks in a 12" x 12" laboratory mold and werefsubse'cfintly dried in an aircirculating oven maintained at "195 F.
- the zinc oxide treated stock drained faster and allowed the production of a thicker sheet than did the stock not treated with zinc oxide.
- Example Two slurries were prepared having'the ingredients listed below. The various ingredients were added in the order given.
- Canadian Freeness 530 760 clear containing jno suspended particles either o rubber or zinc oxide;
- the Canadian freeness .of the zinc oxide treated slurry will .be higher than an identical slurry not treated with 'zinc'oxide.
- the completed slurryi's next form ed into a sh eet 'on the usual papermaking machine such as -a Fourdrinier wire, cylinder machine, or the like.
- the resulting sheet on the wire especially in heavier gauges, will befaster (65% dispersion in water.)
- the slurry prepared in -run 1 was smooth while the slurry prepared in run 2 was very-clumpy. 60
- I claim: 7 1. -In the process or producing" by suspending fibers ma-salaries containing thedis solveiif salt of the metal of the group consisting of aluminum, magnesium, and zinc, mixing with said solution and the fibers suspended therein an aqueous solution of am monium hydroxide to a substantially neutral pH, and thereafter mixing with the thus treated fibers in suspension a latex of a synthetic rubber to form a papermaking slurry of rubber-coated fibers, the step of improving the drainage rate of said slurry by adding finely divided zinc oxide thereto subsequent to the addition of said ammonium hydroxide and prior to the addition of said synthetic rubber latex.
- a water-laid fibrous sheet comprising cellulosic fibers having an inner coating of zinc oxide and an outer coating of a synthetic rubber containing zinc oxide dispersed therethrough.
- a sheet according to claim 4 containing zinc oxide in an amount of about 3-50% by weight based on the dry weight of said rubber.
- a sheet according to claim 4 wherein said synthetic rubber comprises a butadiene-styrene copolymer.
- a sheet according to claim 4 wherein said synthetic rubber comprises a butadiene-acrylonitrile copolymer.
- a sheet according to claim 4 wherein said synthetic rubber comprises a polychloroprene.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
Description
WATER-LAID FIBROUS SHEETS Jay -L. Piersol, East Hempfield Township, Lancaster County,1 Pa., assignor to Armstrong Cork Company, Lancaster, Pa., a corporation ofPennsylvania No Drawing. Filed Nov. 12, 1957, Ser. No. 695,520 9 Claims. Cl. 162-169) i Add paper I maker's alum Add ammonium hydroxide Add finely divided zinc oxide I Add ,i synthetic rubber latex Form sheet I l f I In US. Patent 2,375,245--Pretzel, issued May 8, 1945, there is described a' process of controlling the deposition of a synthetic rubber binder onto cellulosic fibers. The process contemplates pretreating the fibers with a watersoluble'salt of aluminum, magnesium, or zinc, followed by the addition of ammonium hydroxide to form the insoluble metallic hydroxide. The subsequent addition of a synthetic rubber latex brings about the smooth and even deposition of the rubber particles on the individual fibers in the slurry. The rubber coated :furnish fiber; stock is then fed to a paper-forming machine such as a Fourdrin ier, cylinder machine, or the like. This process allows 2,971,879 Patented F eb, 14, 1961 excellent control of the deposition of rubber on fibers in a papermaking slurry.
However, it has been found that aluminum hydroxide, because of its highly gelatinous nature, is a dispersing agent as Well as a precipitating agent for rubber latices under the conditons described in the Pretzel process. The result of this situation is that a slow-draining stock sometimes results from use of the Pretzel process, particularly where higher amounts of aluminum hydroxide are formed in the slurry. Thus there is often a need for a modification of the Pretzel process which will produce a faster draining stock.
It is the primary object of the present invention to supply such a modification. It is a further object of the present invention to produce a papermaking furnish prepared by the Pretzel process which has a higher Canadian freeness than would normally be expected.
These objects are accomplished in a surprisingly straightforward and eflfective manner. The invention contemplates the addition of finely divided zinc oxide subsequent to the step of adding the ammonium hydroxide to form the metal hydroxide in the Pretzel process and prior to the step of adding the'synthetic rubber latex. The result of the addition of zinc oxide at this point in the Pretzel process is that the stock possesses a higher Canadian freeness, presents a more clumpy appearance to the eye, and enables the formation of a thicker sheet.
The fibers contemplated for treatment by the present invention are cellulosic fibers such as kraft, rags, soda. pulp, wood pulp, cotton linters, and the like. The fibers may be present in the slurry along with additional, sheetforming materials such as finely divided cork or finely divided scrap foam rubber; use of finely divided cork with fibers is fully described in US. Patent 2,613,190Feigley. The fibers and additional material, if any, aretaken up in water in the usual manner to form a slurry which will generally be in the consistency range of about 0.5-5%. This slurry may then be subjected to mechanical refining in the usual refiners such as Jordan engines, beaters, disc refiners, and the like. When the desired degree of refinement has been achieved, the consistency-may be adjusted to that desired for further treatment. Generally this consistency will be in the range of about l3%.
To the slurry there is then added a water-soluble salt of a suitable electrolyte such as papermakers alum, aluminum chloride, aluminum sulphate, magnesium chloride, magnesium sulphate, zinc chloride, and the like. For convenience the salt may be added in the form of its water solution. The amount of the electrolyte to be added will generally be in the range of about 25-75% I by weight based on the amount of rubber to be deposited on the fibers subsequently. 1
After the electrolyte has been added to the slurryfand dissolved therein, sufficient ammonium hydroxide is added to establish a substantially neutral pH. To state it another way, sutficient ammonium hydroxide is added to react with and form the hydroxide of substantially all of the metal ion present in the aqueous phase of the slurry.
The reaction proceeds rapidly, and gentle agitation for-' a few minutes is all that is needed.
Instead of adding next the synthetic rubberlatex as contemplated by the Pretzel process, the presentinvention calls for the addition of zinc water; the slurry is simply poured into the papermaking slurry with gentle agitation. The zinc oxide is added as finely divided zinc oxide commonly known as pigment grade or filler grade zinc oxide; these are readily available incommerce. The amount of zinc oxide to be added 1 of aluminum hydroxide which has been formed in the papermaking slurry. Since will be controlled by the amount the amount of aluminum hydroxide is controlled to some oxide at this point. The zinc oxide is preferably added in the form of a slurryin- :acrnere r extent by the amount of rubber to be "deposited on "ihe fibers, it can be seen that the amount of rubber ultimately controls the amount of zinc oxide to be added. Generally speaking, the zinc oxide will be added in an amount of about 3-50% j by" weight based on the total weight of rubber to be deposited on the fibers.
Upon the addition of'zinc oxide to the paperrnaking slurry, some of thelinc oxide apparently immediatelyde positson the aluminum hydroxide-treated-fibersand some stays suspended in the water phase of thepaper-making slurry. Once the zinc oxide has been thoroughly dispersed throughout thepaperrnaking-slurry, the synthetic rubber latex may be added. V
V The synthetic rubber latices contemplated for, use in thepre sent invention'arejthose latices widely media the beater saturation processes. Typical of these synthetic rubbers arethe products *known as; GR+S, which is a copolymer of butadiene and-styrene containing about 50% to about 70% butadiene. There may also be used those products known ,as l lycars, which are copolymers of'butadiene-and acrylonitrile containing about 50% to about 80% butadiene. The polychloroprenes may also be'used. The polychloroprenes, often called neoprenes,
at'aaia 'Eiheto ihe "zinc bate seamen. we
pared according to the progess of the present invention find use as a backing for linoleum composition and plastic surface coverings. Additionally, gaskets may be cut from the sheets, which gaskets find wide use in the automotive and airplane industries.
The following examples illustrate several embodiments of the invention. All parts are' by weight unless otherwise stated.
Example 1 mm 3,750 parts of water there was asse-1" kraft fiber, and 20 parts "Of finelydi'vide'd foam rubber scrap. There was then added 10 -parts papermakers are polymers'of-Z-chlordbutadiene-1,3. If desired homop'olyin'erso'f 'butadiene may begemployed as well as homopolymers and/or copolymers of butadiene homologues snchasisoprene. T hese materials can be vgenerally designated as "synthetic rubbers and more specifically designated asrubberlike polymers of butadiene, isoprene,
and chlorop're ne, and rubberlike copolymers of butadiene or isoprene with copolynierizable vinyl compoundssuch as styrene and acrylonitrile. As is well known in beater saturation 'niethodsgthe'sesynthetic rubbers are added to the slurry in the form of a :latex. The rubber particles therein constitutean electrone gatively charged organic binding material. ,These latices normally contain about 25 to about 50% by weight solids and'contain additional compounding ingredients such as stabilizers and thelike which'arewell known to the art and which {form no part of this invention. The latices are added in an amount suflicie'nt 'to introduce the required amount of r'ubberto be deposited on the fib ers. Normally this will bein'the range; of about 10-1 00% iby weight rubber based on the dry Weight of'the fiber s. v V U V I Theselected latexis simplypoured into the zinc oxide treated slurry withgentle agitation. Therubber content or the latex coagulats and evenly deposits upon the fibers. Since'zinc oxide is subst'antiallyiinsoluble in water under the beater saturation conditions of the Pretzel process, the rubber particles carry with-them all the zinc-oxide which is suspended in the whitewater. The resulting coatedfibers carrfyaninner coating of Zinc oxide and an outer'coating'of a synthetic rubber binder, which binder distributed throughout additional particles of zinc 0x1 e.
Agitation is maintaineduntil rubber precipitation is complete. Normally the necessary period oftime runs less than 20 minutes and often less than 10 minutes. Complete'preci'pitation'is indicated by the fact that the water phaseof thepapermaking'slurry is water white and alum dissolved in 100 parts 'of water, with gentle agitation. There was then added "8' parts aimrhonium hydroxide (28%) with continuing agitation.
A butadiene-styrene latex containing styrene, 40% by weight solids (FRS-ZOOO was added to the resulting slurry in anamount of 45 parts. 7 Antioxidantstofstabilize the rubber against oxidation were "also added, ifria 1.34 partsof a 45% dispersion ofainixtureoff I and 'di-heptyl'diphenyl amines, and 0,75 part .poly merized l,2-dihydro'-2,2,4-trimethyl quinolijne. 'rreeipi: tation of the rubber was 'complete'in 5 minutes,
A slurry identical to that described jjabove pared save for the addition of ninc'oxidesubs n the addition of the ammonium hydroxide and pribrto the addition, of the synthetic rubber --latex. The zinc oxide was addedin the form of a 48% dispersionin' waten and 1.56 parts of the dispersion was added. M m V The Canadian f r'eeriess of the stock containing no zinc oxide was 650 and the stock was only very slightly clumpy. The Canadian 'fre'eness Gfthe stock containing the zinc oxide was 750 an}; fthe stock had a definite clumpy appearance to 'HE eye;
Sheets were prepared fromboth stocks in a 12" x 12" laboratory mold and werefsubse'cfintly dried in an aircirculating oven maintained at "195 F. The zinc oxide treated stock drained faster and allowed the production of a thicker sheet than did the stock not treated with zinc oxide.
Example Two slurries were prepared having'the ingredients listed below. The various ingredients were added in the order given.
Ingredients Run 1, Run 2,
7 parts parts Kraft Fibers 7. 5 7.5 Cotton Linters 7. 5 7. 5 Aluminum Sulphate"--. 6. 5 6.5 NHrOH, 23% 5 6 Zinc Oxide 1 5.8 Butariiene-Styrene Copolymer Latex, 50%
Styrene, 40% Solids 22. 5 22. 5
Canadian Freeness 530 760 clear containing jno suspended particles either o=rubber or zinc oxide; The slurry itself "will possess 'a more clumpy appearantx': to the eye than an identical slurry prepared without the use of. zinc oxide. The Canadian freeness .of the zinc oxide treated slurry will .be higher than an identical slurry not treated with 'zinc'oxide.
"The specificity 'o'f zihc oxide as a means of improving drainage rate is unexpected and surprising. Aseries of similar compounds gives no improvement whatsoever. Zinc oxide appears to stand alone in this respect, the
reasons for which are not understood.
The completed slurryi's next form ed into a sh eet 'on the usual papermaking machine such as -a Fourdrinier wire, cylinder machine, or the like. The resulting sheet on the wire, especially in heavier gauges, will befaster (65% dispersion in water.) v The slurry prepared in -run 1 was smooth while the slurry prepared in run 2 was very-clumpy. 60
nesium oxide, zinc sulphide, iron foxi'de '(1=e, or), f miumoxide (Q 0 1,and'zinc'sulphate. lfloch'ange;was,
noted in the drainage rate or clumpiness "of'fthe "final slurry. 1 I
I claim: 7 1. -In the process or producing" by suspending fibers ma-salaries containing thedis solveiif salt of the metal of the group consisting of aluminum, magnesium, and zinc, mixing with said solution and the fibers suspended therein an aqueous solution of am monium hydroxide to a substantially neutral pH, and thereafter mixing with the thus treated fibers in suspension a latex of a synthetic rubber to form a papermaking slurry of rubber-coated fibers, the step of improving the drainage rate of said slurry by adding finely divided zinc oxide thereto subsequent to the addition of said ammonium hydroxide and prior to the addition of said synthetic rubber latex.
2. A process according to claim 1 wherein said zinc oxide is added in an amount of about 350% by weight based on the dry weight of said synthetic rubber.
3. A process according to claim 1 wherein said zinc oxide is added in the form of a dispersion.
4. A water-laid fibrous sheet comprising cellulosic fibers having an inner coating of zinc oxide and an outer coating of a synthetic rubber containing zinc oxide dispersed therethrough.
5. A sheet according to claim 4 containing zinc oxide in an amount of about 3-50% by weight based on the dry weight of said rubber.
6. A sheet according to claim 4 wherein said synthetic rubber comprises a butadiene-styrene copolymer.
7. A sheet according to claim 4 wherein said synthetic rubber comprises a butadiene-acrylonitrile copolymer.
8. A sheet according to claim 4 wherein said synthetic rubber comprises a polychloroprene.
9. A sheet according to claim 4 wherein said synthetic rubber is present in an amount of about 10-100% by weight based on the dry weight of said fibers.
References Cited in the file of this patent UNITED STATES PATENTS 1,947,104 Plumstead Feb. 13, 1934 2,375,245 Pretzel May 8, 1945 2,666,699 McQuiston et a1 Jan. 19, 1954 2,930,106 Wrotnowski Mar. 29, 1960
Claims (1)
1. IN THE PROCESS OF PRODUCING FELTED FIBER PRODUCTS BY SUSPENDING FIBERS IN A SOLUTION CONTAINING THE DISSOLVED SALT OF THE METAL OF THE GROUP CONSISTING OF ALUMINUM, MAGNESIUM, AND ZINC, MIXING WITH SAID SOLUTION AND THE FIBERS SUSPENDED THEREIN AN AQUEOUS SOLUTION OF AMMONIUM HYDROXIDE TO A SUBSTANTIALLY NEUTRAL PH, AND THEREAFTER MIXING WITH THE THUS TREATED FIBERS IN SUSPENSION A LATEX OF A SYNTHETIC RUBBER TO FORM A PAPERMAKING SLURRY OF RUBBER-COATED FIBERS, THE STEP OF IMPROVING THE DRAINAGE RATE OF SAID SLURRY BY ADDING FINELY DIVIDED ZINC OXIDE THERETO SUBSEQUENT TO THE ADDITION OF SAID AMMONIUM HYDROXIDE AND PRIOR TO THE ADDITION OF SAID SYNTHETIC RUBBER LATEX.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US695520A US2971879A (en) | 1957-11-12 | 1957-11-12 | Water-laid fibrous sheets |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US695520A US2971879A (en) | 1957-11-12 | 1957-11-12 | Water-laid fibrous sheets |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2971879A true US2971879A (en) | 1961-02-14 |
Family
ID=24793342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US695520A Expired - Lifetime US2971879A (en) | 1957-11-12 | 1957-11-12 | Water-laid fibrous sheets |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2971879A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3144379A (en) * | 1961-10-17 | 1964-08-11 | Du Pont | Process of precipitating chloroparene polymer latex onto chrysotile asbestos fibers in a slurry using magnesium chloride as sole precipitating agent |
| US4121966A (en) * | 1975-02-13 | 1978-10-24 | Mitsubishi Paper Mills, Ltd. | Method for producing fibrous sheet |
| DE3132841A1 (en) * | 1980-10-22 | 1982-06-03 | Penntech Papers, Inc., 10016 New York, N.Y. | FINE PAPER AND METHOD FOR THE PRODUCTION THEREOF |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1947104A (en) * | 1932-09-09 | 1934-02-13 | Jessup & Moore Paper Co | Fibrous felting or felted paper product and process of making same |
| US2375245A (en) * | 1941-08-25 | 1945-05-08 | Paul W Pretzel | Manufacture of rubberized fibers and sheets |
| US2666699A (en) * | 1947-01-06 | 1954-01-19 | Minnesota Mining & Mfg | Precipitating size with chromium and aluminum salts |
| US2930106A (en) * | 1957-03-14 | 1960-03-29 | American Felt Co | Gaskets |
-
1957
- 1957-11-12 US US695520A patent/US2971879A/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1947104A (en) * | 1932-09-09 | 1934-02-13 | Jessup & Moore Paper Co | Fibrous felting or felted paper product and process of making same |
| US2375245A (en) * | 1941-08-25 | 1945-05-08 | Paul W Pretzel | Manufacture of rubberized fibers and sheets |
| US2666699A (en) * | 1947-01-06 | 1954-01-19 | Minnesota Mining & Mfg | Precipitating size with chromium and aluminum salts |
| US2930106A (en) * | 1957-03-14 | 1960-03-29 | American Felt Co | Gaskets |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3144379A (en) * | 1961-10-17 | 1964-08-11 | Du Pont | Process of precipitating chloroparene polymer latex onto chrysotile asbestos fibers in a slurry using magnesium chloride as sole precipitating agent |
| US4121966A (en) * | 1975-02-13 | 1978-10-24 | Mitsubishi Paper Mills, Ltd. | Method for producing fibrous sheet |
| DE3132841A1 (en) * | 1980-10-22 | 1982-06-03 | Penntech Papers, Inc., 10016 New York, N.Y. | FINE PAPER AND METHOD FOR THE PRODUCTION THEREOF |
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