EP0000620A1 - Procédé et dispositif pour la fabrication de fibrilles en matière polymère - Google Patents

Procédé et dispositif pour la fabrication de fibrilles en matière polymère Download PDF

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Publication number
EP0000620A1
EP0000620A1 EP19780300087 EP78300087A EP0000620A1 EP 0000620 A1 EP0000620 A1 EP 0000620A1 EP 19780300087 EP19780300087 EP 19780300087 EP 78300087 A EP78300087 A EP 78300087A EP 0000620 A1 EP0000620 A1 EP 0000620A1
Authority
EP
European Patent Office
Prior art keywords
impeller
blades
cylindrical cavity
polymer
plane
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.)
Granted
Application number
EP19780300087
Other languages
German (de)
English (en)
Other versions
EP0000620B1 (fr
Inventor
Robert E. Boehme
Clarence R. Murphy
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Champion International Corp
Gulf Oil Corp
Original Assignee
Champion International Corp
Gulf Oil Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Champion International Corp, Gulf Oil Corp filed Critical Champion International Corp
Publication of EP0000620A1 publication Critical patent/EP0000620A1/fr
Application granted granted Critical
Publication of EP0000620B1 publication Critical patent/EP0000620B1/fr
Expired legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/40—Formation of filaments, threads, or the like by applying a shearing force to a dispersion or solution of filament formable polymers, e.g. by stirring
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/18—Formation of filaments, threads, or the like by means of rotating spinnerets
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/47—Processes of splitting film, webs or sheets

Definitions

  • This invention relates to a process and apparatus for the manufacture of fibrils.
  • the Parrish patent U. S. 2, 988, 782 discloses the manufacture of very fine polymer filaments that can be employed to manufacture water- laid sheets of synthetic paper. These synthetic filaments are of such a small diameter that they behave quite differently from spun filaments and have been characterized in the art as "fibrils" or “fibrids”.
  • the Parrish process for preparing such fibrils involves preparing a solution of a polymer in a suitable solvent and adding the polymer solution to a vigorously-agitated solution of a liquid, which is a nonsolvent for the polymer of interest. As the polymer solution is added to the vigorously-stirred nonsolvent liquid, the droplets of the polymer solution are subjected to sheer forces and attenuated while simultaneously being precipitated. Parrish discloses that the precipitation step is carried out in a high intensity mixer such as a Waring blender, While the Parrish process is suitable for making small laboratory quantities of such fibrils, the process is not well suited to make substantial quantities of the fibrils at an acceptable cost.
  • the Davis, et al, patent U. S. 4, 013, 751 discloses an alternate process for preparing fibrils by modified methods in which a hot polymer solution is passed through a hammermill and suds cooled as the streams of polymer solution are thrown free of the rotating plate of the hammermill. While this process provides; good quality fibrils, the process is capital intensive and has higher manufacturing costs than is desired.
  • Novel centrifugal spinning apparatus has been developed for the manufacture of fibrils from hot viscous hydrocarbon solutions of olefin polymers having an inherent viscosity of at least 3. 5.
  • the apparatus consists of an impeller which rotates at high speed in a cylindrical cavity having a discharge port.
  • the impeller has a plurality of blades whose narrow dimensions lie substantially in the plane of the impeller's rotation and whose tips come in close proximity to the inner peripheral surface of the cylindrical cavity.
  • the blades are arranged in at least two substantially-identical sets. Within each set, the blades are offset substantially equidistant from one another; both in the rotational plane of the impeller and in the plane transverse thereto.
  • Two inlet ports are provided in the peripheral surface of the cylindrical cavity to feed hot polymer solution and coolant liquid to the cylindrical cavity, each of which port is narrow in a plane transverse to the plane of the impeller's rotation and extends over substantially the entire peripheral surface.
  • the inlet ports are positioned near the discharge port of the cylindrical cavity and upstream thereof viewed with respect to the impeller's rotation, so that the bulk of the liquids entering the cavity from the inlet ports are swept away from the discharge port by the impeller's rotation.
  • the hot polymer solution fed to the appratus is broken up into droplets by the rotating impeller blades. Individual droplets impinge upon the surface of the impeller blades and are attenuated into thin streams. In a like manner, the coolant liquid impinges upon the impeller blades and cools the attenuated polymer streams to precipitate the solute polymer in the form of fibrils.
  • the centrifugal spinning apparatus includes a housing 20 having a cavity 30 machined therein and having a downwardly and outwardly extending lower discharge port 22 which terminates at its lowermost end in an opening 24.
  • the ratio of diameter to depth in cavity 30 preferably is at least 5.0:1.0.
  • Cavity 30 normally is covered and sealed by a removable front plate 32,Front plate 32 is held in position on the front of housing 20 by means of a plurality of nuts 34 secured to the ends of bolts 36 which are pivotally mounted to housing 20 and extend through U-shaped slots 38.
  • An impeller is mounted within cavity 30 on shaft 40 and consists of four blades 42, 44, 46 and 48.
  • the impeller blades are separated from each other by washers not shown and are locked in fixed positions by suitable keys not shown.
  • the two halves of each blade are shown as, respectively, 42a and 42b, 44a and 44b, 46a and 46b, and 48a and 48b.
  • the blades are offset from each other in fixed positions so that the blades 42a, 44a, 46a and 48a constitute one set of blades, each of which is offset substantially equidistant from each other, both in the rotational. plane of the impeller and in the plane transverse thereto.
  • the blades 42b, 44b, 46b and 48b constitute a second substantially-identical set of blades, with these blades also being offset substantially equidistant from each other, both in the rotational plane of the impeller and in the plane transverse thereto.
  • the impeller rotates in the direction of the arrow at high speed so that the tip speed of each of the blades is at least about 200 feet per second and preferably greater than 500 feet per second.
  • Two inlet ports 50 and 52 of rectangular cross section are provided in the inner peripheral surface of cavity 30, and extend over substantially the entire inner peripheral surface in a plane transverse to the rotational plane of the impeller. Tapped openings in the peripheral surface communicate with inlet ports 50 and 52 and are, threaded to receive liquid feed tubes 54 and 56.
  • Fig . 5 illustrates three units being ganged together for operation off one drive shaft.
  • the apparatus illustrated in the drawings represents the preferred embodiment of the invention as presently perceived by the applicants, a number of modifications can be made therein,
  • the apparatus illustrated contains four impeller blades which constitute two separate sets of blades. By increasing the ratio of the cylindrical cavity's depth to its diameter, it is possible to mount a significantly greater number of blades on the shaft. While the illustrated apparatus is mounted so that the impeller blades rotate in the earth's gravitational field, the apparatus can be rotated 90° so that the impeller rotates in a plane perpendicular to the earth's gravitational field. When operated in this mode, the product discharge port is in one side of the apparatus and the centrifugal force of the impeller blades transfers product into the discharge port.
  • the impeller In operation the impeller is rotated by an external motor at high speed to provide tip speeds in excess of 200 ft. /sec. At these speeds, the two tips of each blade, e. g. 42a and 42b, 44a and 44b, etc. , function essentially as one continuous knife blade. This action is shown in Fig. 3 in which rotation of the impeller blades is shown in an extended, flattened plane.
  • a polymer solution consisting of about 4 weight % of a high molecular weight olefin polymer having an intrinsic viscosity of at least 3.5 dissolved in a kerosene-type hydrocarbon, heated to a temperature of about 190°C, is fed to cavity 30 through inlet port 50.
  • the polymer solution Upon entering cavitty 30, the polymer solution impinges upon the impeller blades and is broken up into a multiplicity of droplets which are carried by centrifugal forces around the periphery of cavity 30 until they reach discharge port 22. Virtually all of the droplets of polymer solution will come into contact with the face of an impeller blade. When this occurs the droplets as indicated by 60 and 62 in Fig 4 are attenuated by centrifugal force to form thin polymer streams as shown, this action having the effect of orienting the solute polymer molecules in the direction of the applied centrifugal force.
  • a coolant liquid preferably water
  • the coolant liquid impinges upon the impeller blades and is carried to discharge port 22 by centrifugal forces in the manner previously described.
  • the coolant liquid removes heat from the blades which cools the polymer solution in contact therewith and causes the polymer to precipitate from the solution in the form of fibrils.
  • the product will be treated and recovered in the manner as illustrated and discussed in U.S. 4, 013, 751. Specifically, the product will be passed through a wringer to express the bulk of the liquid from the polymer solids which then wil be beat one or more times in isopropanol to remove the remainder of the solvent and coolant liquid from the fibrils. The fibrils then are filtered and dried for use.
  • the process of the invention can be employed to prepare fibrils from essentially any polymer solution in which the difference in polymer solubility between the two operating temperatures is sufficient large.
  • the quality of the fibrils produced will be importa influenced by the polymer from which they are prepared.
  • Fibrils of optimum properties are prepared from olefin polymers having a very high molecular weight such that the polymer has an intrinsic viscosity of at least 3. 5.
  • One species of such polymers consists of ethylene polymers containing, on a weight basis, at least 9 0% of polymerized ethylene.
  • Such ethylene polymers will be ethylene homopolymers or ethylene copolymers containing small quantities of C 4 or higher olefin comonomer such as butene, hexene, styrene, a conjugated diene such as butadiene, or the like.
  • a second species of such olefin polymers consists of propylene polymers containing, on a weight basis, at least 50% of polymerized propylene.
  • propylene polymers will be propylene homopolymers, or propylene copolymers containing up to 50% of copolymerized ethylene.
  • fibrils having a highly satisfactory combination of overall properties are obtained when the polymer employed in the process consists entirely of an olefin polymer as described above. It has been observed, however, that fibrils of generally satisfactory properties can be cb tained when a mixture of polymers is employed in the process, provided that the olefin polymer as described above, constitutes at least about 20 weight % and preferably at least 35 weight % of the total polymer employed in the fibril-manufacturing process.
  • the other polymers employed may be employed for either of two principal purposes.
  • such other polymers can be employed principally to lower the raw material cost of the fibrils to be prepared.
  • such other polymers can be employed to modify specific properties of the fibrils themselves, or the water-laid, paper-like sheets prepared therefrom.
  • the polymers employed in the fibril-manufacturing process, in addition to the olefin polymers described above will be referred to as "diluent polymers".
  • Diluent polymers suitable for this purpose are those set forth in U. S. 4, 013, 751.
  • the solvent to be employed in the process of the invention may be any liquid which will completely dissolve the olefin polymer employed in the process at an elevated temperature. It is highly desirable that the solvent employed have a significantly different capacity to dissolve the olefin polymer at different temperatures.
  • the ideal solvents are those having a very low solubility for the olefin polymer at ambient temperature, but having a high degree of solvent power for the olefin polymer at temperatures above 140 C.
  • Hydrocarbon solvents such as kerosene, mineral spirits, tetraline and aromatic hydrocarbons such as xylenes, have excellent characteristics for use in the invention and are the preferred solvents to be employed in the invention. Other solvents, however, such as certain of the chlorinated hydrocarbons, also can be employed if desired.
  • the solvents employed should be liquids at ambient temperature and preferably should have atmosphe boiling points above 150°C and preferably above 180 C .
  • the polymer solutions employed in the process should be heated to temperatures of at least 100°C and preferably 150°C or higher. Polymer concentrations of 2 weight % or higher should be employed.
EP19780300087 1977-07-01 1978-06-27 Procédé et dispositif pour la fabrication de fibrilles en matière polymère Expired EP0000620B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US812031 1977-07-01
US05/812,031 US4125584A (en) 1977-07-01 1977-07-01 Process for the manufacture of fibrils

Publications (2)

Publication Number Publication Date
EP0000620A1 true EP0000620A1 (fr) 1979-02-07
EP0000620B1 EP0000620B1 (fr) 1981-11-11

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP19780300087 Expired EP0000620B1 (fr) 1977-07-01 1978-06-27 Procédé et dispositif pour la fabrication de fibrilles en matière polymère

Country Status (6)

Country Link
US (1) US4125584A (fr)
EP (1) EP0000620B1 (fr)
JP (1) JPS5434417A (fr)
CA (1) CA1101163A (fr)
DE (1) DE2861309D1 (fr)
NO (1) NO782282L (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51103196A (fr) * 1975-03-07 1976-09-11 Ishikawa Takashi
US4237081A (en) * 1978-04-03 1980-12-02 Gulf Oil Corporation Method for preparation of fibrils
SE438874B (sv) * 1983-09-19 1985-05-13 Moelnlycke Ab Forfarande for kontinuerlig framstellning av fibrost, bundet material direkt ur en polymerlosning
US5030403A (en) * 1989-01-17 1991-07-09 Ppg Industries, Inc. Method for making polymeric fibrils
CN112048774A (zh) * 2020-09-04 2020-12-08 郭元松 一种湿法无纺布喷丝防堵塞设备

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1205509A (en) * 1967-12-16 1970-09-16 Voith Gmbh J M Precipitating device
US4013751A (en) * 1971-10-29 1977-03-22 Gulf Research & Development Company Fibrils and processes for the manufacture thereof

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2021837A (en) * 1933-10-31 1935-11-19 Viscose Co Method and apparatus for precipitating cellulose acetate
GB849935A (en) * 1957-10-22 1960-09-28 Arthur Abbey Improvements in or relating to the treatment of thermo-plastic materials
US3070835A (en) * 1960-01-12 1963-01-01 Standard Oil Co Pump quenching of polymer solvent mixtures
US3400189A (en) * 1964-09-14 1968-09-03 Dow Chemical Co Process for centrifugally spinning hollow or filled filaments
GB1071325A (en) * 1965-02-18 1967-06-07 Rhodiatocae S P A Method of and apparatus for the precipitation of cellulose esters from solutions thereof
US3846529A (en) * 1971-10-26 1974-11-05 Grace W R & Co Extrusion cutting device
FR2199015A2 (en) * 1971-10-29 1974-04-05 Gulf Research Development Co Polymeric fibre paper - or non-woven fibre web, from polyolefins (co)poly-mers

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1205509A (en) * 1967-12-16 1970-09-16 Voith Gmbh J M Precipitating device
US4013751A (en) * 1971-10-29 1977-03-22 Gulf Research & Development Company Fibrils and processes for the manufacture thereof

Also Published As

Publication number Publication date
DE2861309D1 (en) 1982-01-14
US4125584A (en) 1978-11-14
EP0000620B1 (fr) 1981-11-11
JPS5434417A (en) 1979-03-13
CA1101163A (fr) 1981-05-19
NO782282L (no) 1979-01-03

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