US1952038A - Process of extruding sheet material - Google Patents
Process of extruding sheet material Download PDFInfo
- Publication number
- US1952038A US1952038A US235611A US23561127A US1952038A US 1952038 A US1952038 A US 1952038A US 235611 A US235611 A US 235611A US 23561127 A US23561127 A US 23561127A US 1952038 A US1952038 A US 1952038A
- Authority
- US
- United States
- Prior art keywords
- sheet
- edges
- center
- extruding
- heated
- 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.)
- Expired - Lifetime
Links
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J1/00—Fibreboard
-
- 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
- Y10S264/66—Processes of reshaping and reforming
-
- 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
- Y10S425/00—Plastic article or earthenware shaping or treating: apparatus
- Y10S425/123—Repress
-
- 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
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T156/00—Adhesive bonding and miscellaneous chemical manufacture
- Y10T156/10—Methods of surface bonding and/or assembly therefor
- Y10T156/1002—Methods of surface bonding and/or assembly therefor with permanent bending or reshaping or surface deformation of self sustaining lamina
- Y10T156/1043—Subsequent to assembly
-
- 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
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T24/00—Buckles, buttons, clasps, etc.
- Y10T24/14—Bale and package ties, hose clamps
- Y10T24/1498—Plastic band
Definitions
- A. c. FISCHER PROCESS OF EXTRUDING SHEET MATERIAL Filed NOV. 25, 1927 Patented 20, 1934 UNITED STATES PATEN T OFFICE PROCESS OF EXTBUDING SHEET MATERIAL Albert C. Fischer, Chicago, IlL, assignor to The Philip Carey Manufacturing Company, a corporation of Ohio My process relates to the formation of sheet material composed of a mixture of a waterproofed binder and fibrous material.
- the waterproofed binder would preferably be blown asphalt, or any suitable pitch, tar, bituminous material, asphalts or other waterproofing material which is of a ductile, plastic nature rather than a hard brittle nature, and which is suitable for waterproofing purposes.
- the sheet material has a preponderance of waterproofing material.
- the waterproofing material may likewise have a rubber content in an unvulcanized state, preferably of a cut back or reclaimed type.
- the fibrous material is preferably ina coarse condition, that is, it is incorporated in considerable length if it so comes, or in considerable width, and may be felt fibers or cotton fibers, hemp, sisal,
- the fibrous material may be excelsior in coarse or fine condition, the inner bark of trees, which shreds to fiat thin strips of fibrous material, or it may consist of large pieces of shavings, or fiake material of various kinds, either vegetable or mineral.
- the sheet material is primarily for the purpose of manufacturing expansion joints, but it might likewise be used for roofing, flooring or other constructional uses.
- the binder must be ductile, must have a fairly high melting point, at least over 200 F. and must not be brittle in cold temperatures. This is the requirement of the art for proper functioning. It must be as resilient and elastic as possible, and this process of incorporating the coarse material in the waterproofed binder aids such resiliency very materially.
- the prior art discloses fiber incorporated in a manner so that it is broken up into small pieces, and it loses much of its value. Likewise in the breaking up of thisfiber into small pieces a thin sheet can be prepared, whereas by mixing the material in a coarse manner and preserving in as near a natural state as possible a; thin sheet can.- not be prepared without a great deal of breaking.
- the fibrous material may either be previously waterproofed or not, as-desired. If it is previously waterproofed it will not require as much new waterproofed binder as if it were not waterproofed.
- the mixing operation is done in a steam-:heated 56 mixer.
- the liquid binder is heated and poured In the expansion joint art into the mixer, and the fibrous material is incorporated in the liquid binder in a short rapid mix, thus preventing the breaking up of the fiber to any appreciable degree.
- a fourth process comprises the manufacture of sewer pipe belt, which comprises extruding a sheet having its edges thicker than its center, and by cutting thru the center manufacturing a wedge-shapedbelt for sewer pipe caulking.
- the primary process is the formation of a sheet having thicker edges and then rolling said sheet to obtain a uniformly thick sheet without breaking the edges, and this is my preferred form, but I do not wish to be limited to this particular process, as the process may apply in other ways and for the manufacture. of different constructional materials, as described.
- the main process is the rapid mixing of a waterproof material and coarse fibrous material, introduced into a steam-heated extrusion machine, and extruding the sheet so that the edges are thicker than the center, for the purpose of rolling the sheet to obtain a sheet of uniform thickness with its edges comparatively free of breaks.
- Figure 1 represents a uniform sheet of material; (n) represents the material.
- a represents the material reduced to sheet form.
- Figures 1a and 2a represent cross sections and face views of a blown sheet of ductile material extruded and rolled in the same manner as Figures 1 and 2, the diiferencebeing that in Figures 1a and 2a the sheet has no fiber content.
- Figure 3 shows a sheet b extruded so that the edges are thicker than the center.
- Figure 4 shows the result of the sheet b, in which the edges are practically perfect, due to the fact that it has been extruded with thickened edges, presented to pressure rolls, and by reason of the thick edges is produced practically free from breaks.
- Figure 5 shows an extruder head provided for steam-heat, 0 represents, the head, at the steam conveyance, e the valve, ,f the slot in the extruder. If the slot in the extruder, as at f, is left undisturbed it will extrude a uniform sheet. If a slide interference is arranged in the center of the opening then the sheet will be thickerat the center and thicker at the sides.
- Figure 6 shows an interference placed in the groove of the extruder, in which g represents the interference. This will cause two strips to flow from either side of the interference.
- Figure 7 shows a sheet in which the material I) is introduced between the two strips hh, which are run alongside of the introduced strip b, and the edges hh being formed by the extruder head.
- strip 12 is introduced and strip h is run along one edge thereof.
- Figure 10 illustrates the sheet b, which when cut in the center results in the strip shown in Figure 11.
- Figure 11 indicates the strip b suitable for sewer pipe caulking.
- Figure 12 illustrates an extruder head c, provided with steam conveyance d and a'valve e.
- the-process will work equally well where the sheet is formed with a homogeneous mixture into a single thickness, or where the sheet b with'the heavy edges is pressed between sheets of saturated felt. In either case it will fill out the edges and save waste.
- construction sheet material consisting in forming a plastic mass. feeding same to an extruding device, extruding the material into sheets, applying a reenforcing layer to the face of the sheet, and thereafter subjecting the composite structure to pressure to reduce same to the desired thickness.
- construction sheet material consisting in forming a plastic mass, feeding same to an extruding device, extruding the material into sheets, applying a reenforcing layer to both faces of the sheet, and thereafter subjecting the composite structure to pressurev to reduce same to the desired thickness.
- the method of making constructional material comprising mixing a warm plastic mass, feeding same to an extruding device, extruding the mass into a sheet of tapering transverse thickness, and dividing the sheet into strips.
- the method'of making constructional material comprising mixing a warm plastic mass, feeding same to an extruding device, extruding the mass into a sheet of tapering transverse thickness, and dividing the sheet longitudinally intostrips.
- the method of making constructional material comprising mixing a warm plastic mass, feeding same to a forming device, forming the mass into a sheet of tapering transverse thickness, and dividing the sheet along the longitudinal medial plane into uniform strips.
- the method of making constructional material comprising mixing a warm plastic mass, feeding same to a forming device, forming the mass into a sheet of increasing thickness from the center to the side edges, and dividing the sheet longitudinally along the line of its minimum ALBERT C. FISCHER.
Description
March 20, 1934. A. c. FISCHER PROCESS OF EXTRUDING SHEET MATERIAL Filed NOV. 25, 1927 Patented 20, 1934 UNITED STATES PATEN T OFFICE PROCESS OF EXTBUDING SHEET MATERIAL Albert C. Fischer, Chicago, IlL, assignor to The Philip Carey Manufacturing Company, a corporation of Ohio My process relates to the formation of sheet material composed of a mixture of a waterproofed binder and fibrous material. The waterproofed binder would preferably be blown asphalt, or any suitable pitch, tar, bituminous material, asphalts or other waterproofing material which is of a ductile, plastic nature rather than a hard brittle nature, and which is suitable for waterproofing purposes. The sheet material has a preponderance of waterproofing material. The waterproofing material may likewise have a rubber content in an unvulcanized state, preferably of a cut back or reclaimed type. I
The fibrous material is preferably ina coarse condition, that is, it is incorporated in considerable length if it so comes, or in considerable width, and may be felt fibers or cotton fibers, hemp, sisal,
flax, jute, cocoanut, istle, or in fact any linear fiber having length. The fibrous material may be excelsior in coarse or fine condition, the inner bark of trees, which shreds to fiat thin strips of fibrous material, or it may consist of large pieces of shavings, or fiake material of various kinds, either vegetable or mineral.
The sheet material is primarily for the purpose of manufacturing expansion joints, but it might likewise be used for roofing, flooring or other constructional uses. the binder must be ductile, must have a fairly high melting point, at least over 200 F. and must not be brittle in cold temperatures. This is the requirement of the art for proper functioning. It must be as resilient and elastic as possible, and this process of incorporating the coarse material in the waterproofed binder aids such resiliency very materially.
The prior art discloses fiber incorporated in a manner so that it is broken up into small pieces, and it loses much of its value. Likewise in the breaking up of thisfiber into small pieces a thin sheet can be prepared, whereas by mixing the material in a coarse manner and preserving in as near a natural state as possible a; thin sheet can.- not be prepared without a great deal of breaking.
One of the features of my invention is the reduction of the mixing operation, which previously required an hour's time to fabricate a sheet, but which by my process is reduced to fifteen or twenty minutes or even less. The fibrous material may either be previously waterproofed or not, as-desired. If it is previously waterproofed it will not require as much new waterproofed binder as if it were not waterproofed.
The mixing operation is done in a steam-:heated 56 mixer. The liquid binder is heated and poured In the expansion joint art into the mixer, and the fibrous material is incorporated in the liquid binder in a short rapid mix, thus preventing the breaking up of the fiber to any appreciable degree.
I have found that it is impossible to roll such a mixture to sheet form unless same is mixed for some length of time. Ordinarily the mixture should be run for an hour or more. If the fibrous material ran too coarse the sheet would tear apart in rolling. In my present process my object is to mix the ingredients only a short period and keep the fibrous material in as coarse a condition in the mix as possible, thereby gaining tensile strength and body.
I find a satisfactory sheet can be made by tak ing this mixture and' introducing it into an extruding machine in a heated plastic state, and extending thru a steam-heated extruder, having a steam-heated die or head, into a sheet and then rolling the sheet between rollers. The mixture can be extruded into sheets as wide as 26 inches, and down to of an inch in thickness.
If provision is not properly made in the die for the preparation of this sheet so that it will be thicker on the edges than it is at the center, the g0 sheet will tear apart at the edges and much waste material will be obtained. I, therefore, arrange the die by padding the center so that the edges of the sheet are' thicker than the center. When a sheet of uniform dimension is pressed between pressure rolls the friction at the edges forces the edges apart and the center is not affected, with the result that the edges are badly torn. If, however, I arrange to have the edges taper inward to the center and then make the center "over a given distance uniform I will receive a sheet of increased dimension, with little if any breaking of the edges. This is very important in manufacturing constructional material of various kinds and obviates extruding in a-heavy slab section and reducing it under pressure by rolling. In fact a heavy slab rolled down under pressure, containing coarse material, pulls apart, that is, a coarse section travels forward and leaves a ragged hole I in the reduced material, but by extruding as previ- 100 ously described, and when rolling so that inch compression is obtained or more, I find the sheet V is not damaged but kept practically perfect, and
that a very strong sheet containing coarse fibrous material can be formed. Likewise, by extruding a sheet with thicker edges for certain purposes, for instance, sewer pipe belts, tapered shingles, or the like I can extrude a sheet or strip of a given width, having heavy edges and tapering to the center. By cutting thru the center of the strip I obtain two strips of sewer pipe belt suitable for caulking sewer pipes. Likewise in this same process I find that by locking the center of the extruder opening I can obtain two strips and introduce a third strip in the center, uniting the two strips on either side of the third strip, so that my invention relates to, first, a process of mixing,
second, a process of extruding a sheet that is thicker at its edges than at its center, third, the process of extruding strips and introducing an intervening section, and uniting the extruded strips to the intervening section. A fourth process comprises the manufacture of sewer pipe belt, which comprises extruding a sheet having its edges thicker than its center, and by cutting thru the center manufacturing a wedge-shapedbelt for sewer pipe caulking. The primary process is the formation of a sheet having thicker edges and then rolling said sheet to obtain a uniformly thick sheet without breaking the edges, and this is my preferred form, but I do not wish to be limited to this particular process, as the process may apply in other ways and for the manufacture. of different constructional materials, as described.
The main process is the rapid mixing of a waterproof material and coarse fibrous material, introduced into a steam-heated extrusion machine, and extruding the sheet so that the edges are thicker than the center, for the purpose of rolling the sheet to obtain a sheet of uniform thickness with its edges comparatively free of breaks.
Referring to the drawing. Figure 1 represents a uniform sheet of material; (n) represents the material.
In Figure 2, a represents the material reduced to sheet form. Where the sheet has beenintroduced into a steam-heated extruder and where the sheet has been extruded to a uniform thickness and then subjected to pressure rolls, it can be readily seen that the sheet is an economic loss.
Figures 1a and 2a represent cross sections and face views of a blown sheet of ductile material extruded and rolled in the same manner as Figures 1 and 2, the diiferencebeing that in Figures 1a and 2a the sheet has no fiber content.
Figure 3 shows a sheet b extruded so that the edges are thicker than the center.
Figure 4 shows the result of the sheet b, in which the edges are practically perfect, due to the fact that it has been extruded with thickened edges, presented to pressure rolls, and by reason of the thick edges is produced practically free from breaks.
Figure 5 shows an extruder head provided for steam-heat, 0 represents, the head, at the steam conveyance, e the valve, ,f the slot in the extruder. If the slot in the extruder, as at f, is left undisturbed it will extrude a uniform sheet. If a slide interference is arranged in the center of the opening then the sheet will be thickerat the center and thicker at the sides.
Figure 6 shows an interference placed in the groove of the extruder, in which g represents the interference. This will cause two strips to flow from either side of the interference.
Figure 7 shows a sheet in which the material I) is introduced between the two strips hh, which are run alongside of the introduced strip b, and the edges hh being formed by the extruder head.
In Figure 8 strip 12 is introduced and strip h is run along one edge thereof.
In Figure 9 an extruder head is shown provided with steam-heat, in which the groove is formed the center.
Figure 10 illustrates the sheet b, which when cut in the center results in the strip shown in Figure 11. Figure 11 indicates the strip b suitable for sewer pipe caulking. Figure 12 illustrates an extruder head c, provided with steam conveyance d and a'valve e.
forming a plastic sheet b, introducing said plastic sheet between rollers i'-i. said rollers having belts 12, in that the extruded sheet I: is fed between two sheets of saturated felt ll unrolled from rollers -46, the lower sheet traveling upon a belt :i around rolls ii, the sheet 11 finally resting thereon, the upper sheet 1 passing below the rolle1 1, and said saturated sheets being pressed against the sheet 12 without seriously breaking the edges of the sheet, thus preventing waste forming a finished sheet.
It can be readily understood that the-process will work equally well where the sheet is formed with a homogeneous mixture into a single thickness, or where the sheet b with'the heavy edges is pressed between sheets of saturated felt. In either case it will fill out the edges and save waste.
I am the first to extrude a bituminous, fibratedsheet 26 inches in width, and introduce said sheet to a set of rolls, producing a sheet of lesserdimension with unbroken edges.
I am not claiming a two or three inch thick slab of uniform dimension reduced to a thinner dimension in which the edges of the sheet are broken. I do claim any slab formed of bituminous material and fiber, in which the slab is thicker at the edges than the center and reduced to a thinner dimension, in which the entire sheet becomes uniform in thickness and is free from broken edges.
I likewise claim a bituminous sheet formed with thicker edges and tapered to the center, in which the center is later cut and used as strips for caulking pipes, tapered shingles or the like.
I claim:
1. The process of forming sheet material characterized by mixing a heated waterproofed binder and coarse fibrous material, presenting said heated mixture to a steam heated extrusion machine and extruding said mixture thru a steam heated die, with the edges of the sheet so extruded thicker than the center, and reducing said sheet to uniform thickness.
2. The process of forming sheet material char acterized by mixing a heated waterproofed binder and coarse fibrous material, presenting said heated mixture to a steam heated extrusion machine and extruding said mixture thru a steam heated die, with the edges of the sheet so exedges, as shown truded heavier than the center, presenting said er and coarse fibrous material, presenting said heated mixture to a steam heated extrusion machine and extruding said mixture thru a steam heated die, with the edges of the sheet so extruded thicker than the'center, presenting said sheet between upper and lower saturated felt sheets, running said saturated felt sheet containing the plastic sheet with thicker edges and uniform center between pressure rolls, and forming a sheet of uniform thickness without unfilled edges.
4. The method of making construction sheet material consisting in forming a plastic mass. feeding same to an extruding device, extruding the material into sheets, applying a reenforcing layer to the face of the sheet, and thereafter subjecting the composite structure to pressure to reduce same to the desired thickness.
5. The method of making construction sheet material consisting in forming a plastic mass, feeding same to an extruding device, extruding the material into sheets, applying a reenforcing layer to both faces of the sheet, and thereafter subjecting the composite structure to pressurev to reduce same to the desired thickness.
thickness.
' 6. The method of making constructional material comprising mixing a warm plastic mass, feeding same to an extruding device, extruding the mass into a sheet of tapering transverse thickness, and dividing the sheet into strips.
7. The method'of making constructional material comprising mixing a warm plastic mass, feeding same to an extruding device, extruding the mass into a sheet of tapering transverse thickness, and dividing the sheet longitudinally intostrips.
8. The method of making constructional material comprising mixing a warm plastic mass, feeding same to a forming device, forming the mass into a sheet of tapering transverse thickness, and dividing the sheet along the longitudinal medial plane into uniform strips.
9. The method of making constructional material comprising mixing a warm plastic mass, feeding same to a forming device, forming the mass into a sheet of increasing thickness from the center to the side edges, and dividing the sheet longitudinally along the line of its minimum ALBERT C. FISCHER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US235611A US1952038A (en) | 1927-11-25 | 1927-11-25 | Process of extruding sheet material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US235611A US1952038A (en) | 1927-11-25 | 1927-11-25 | Process of extruding sheet material |
Publications (1)
Publication Number | Publication Date |
---|---|
US1952038A true US1952038A (en) | 1934-03-20 |
Family
ID=22886231
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US235611A Expired - Lifetime US1952038A (en) | 1927-11-25 | 1927-11-25 | Process of extruding sheet material |
Country Status (1)
Country | Link |
---|---|
US (1) | US1952038A (en) |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2451986A (en) * | 1943-05-25 | 1948-10-19 | Extruded Plastics Inc | Thermoplastic extrusion method |
US2452884A (en) * | 1945-07-07 | 1948-11-02 | Werner Co Inc R D | Method and device for molding |
US2572833A (en) * | 1945-07-30 | 1951-10-30 | Balzarini Martin Louis | Apparatus for making edible products |
US2671041A (en) * | 1952-01-11 | 1954-03-02 | Gen Tire & Rubber Co | Method of forming plastic weather stripping and windlaces |
US2682292A (en) * | 1950-08-29 | 1954-06-29 | Reliance Steel Prod Co | Continuous system for forming fiber and plastic shapes |
US2723933A (en) * | 1950-01-31 | 1955-11-15 | Hans D Isenberg | Method of making preformed insulation for high voltage transformer |
US2788051A (en) * | 1953-01-02 | 1957-04-09 | Honeycomb Structures Company I | Apparatus for applying a coating to sheet material |
US2920352A (en) * | 1954-04-23 | 1960-01-12 | Du Pont | Process of casting and stretching film |
US2960425A (en) * | 1955-09-02 | 1960-11-15 | Owens Illinois Glass Co | Method of integrally uniting thermoplastic sheets with extruded plastic material |
US2974360A (en) * | 1957-06-07 | 1961-03-14 | Continental Oil Co | Slab molding machine |
US3109196A (en) * | 1959-12-17 | 1963-11-05 | Schmidt Max | Extruder having an interchangeable injector head |
US3168509A (en) * | 1965-02-02 | figure | ||
US3267518A (en) * | 1961-02-09 | 1966-08-23 | Great Lakes Carbon Corp | Apparatus for making carbon electrodes or neutronic reactor core bars |
US4093487A (en) * | 1976-11-15 | 1978-06-06 | Dayco Corporation | Method of continuously making a printing blanket construction |
US4123490A (en) * | 1975-11-20 | 1978-10-31 | Fiber Industries Inc. | Production of a high tenacity, low denier poly(ethylene terephthalate) fibrillated tape yarn |
US4182606A (en) * | 1975-11-20 | 1980-01-08 | Fiber Industries, Inc. | Slit extrusion die |
US4789514A (en) * | 1985-12-09 | 1988-12-06 | Aluminum Company Of America | Methods of producing biaxially oriented polymer sheet |
US4826560A (en) * | 1985-08-24 | 1989-05-02 | Kurt Held | Device for continuous production of thermoplastic webs |
US4877393A (en) * | 1985-12-09 | 1989-10-31 | Aluminum Company Of America | Apparatus for producing biaxially oriented polymer sheet |
US6071110A (en) * | 1997-09-11 | 2000-06-06 | Mikkelsen; Oeystein | Polishing roll and method for making same |
US6074192A (en) * | 1997-09-11 | 2000-06-13 | Mikkelsen; Oeystein | Lenticular pattern forming roll and method for making the roll |
-
1927
- 1927-11-25 US US235611A patent/US1952038A/en not_active Expired - Lifetime
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3168509A (en) * | 1965-02-02 | figure | ||
US2451986A (en) * | 1943-05-25 | 1948-10-19 | Extruded Plastics Inc | Thermoplastic extrusion method |
US2452884A (en) * | 1945-07-07 | 1948-11-02 | Werner Co Inc R D | Method and device for molding |
US2572833A (en) * | 1945-07-30 | 1951-10-30 | Balzarini Martin Louis | Apparatus for making edible products |
US2723933A (en) * | 1950-01-31 | 1955-11-15 | Hans D Isenberg | Method of making preformed insulation for high voltage transformer |
US2682292A (en) * | 1950-08-29 | 1954-06-29 | Reliance Steel Prod Co | Continuous system for forming fiber and plastic shapes |
US2671041A (en) * | 1952-01-11 | 1954-03-02 | Gen Tire & Rubber Co | Method of forming plastic weather stripping and windlaces |
US2788051A (en) * | 1953-01-02 | 1957-04-09 | Honeycomb Structures Company I | Apparatus for applying a coating to sheet material |
US2920352A (en) * | 1954-04-23 | 1960-01-12 | Du Pont | Process of casting and stretching film |
US2960425A (en) * | 1955-09-02 | 1960-11-15 | Owens Illinois Glass Co | Method of integrally uniting thermoplastic sheets with extruded plastic material |
US2974360A (en) * | 1957-06-07 | 1961-03-14 | Continental Oil Co | Slab molding machine |
US3109196A (en) * | 1959-12-17 | 1963-11-05 | Schmidt Max | Extruder having an interchangeable injector head |
US3267518A (en) * | 1961-02-09 | 1966-08-23 | Great Lakes Carbon Corp | Apparatus for making carbon electrodes or neutronic reactor core bars |
US4123490A (en) * | 1975-11-20 | 1978-10-31 | Fiber Industries Inc. | Production of a high tenacity, low denier poly(ethylene terephthalate) fibrillated tape yarn |
US4182606A (en) * | 1975-11-20 | 1980-01-08 | Fiber Industries, Inc. | Slit extrusion die |
US4093487A (en) * | 1976-11-15 | 1978-06-06 | Dayco Corporation | Method of continuously making a printing blanket construction |
US4826560A (en) * | 1985-08-24 | 1989-05-02 | Kurt Held | Device for continuous production of thermoplastic webs |
US4789514A (en) * | 1985-12-09 | 1988-12-06 | Aluminum Company Of America | Methods of producing biaxially oriented polymer sheet |
US4877393A (en) * | 1985-12-09 | 1989-10-31 | Aluminum Company Of America | Apparatus for producing biaxially oriented polymer sheet |
US6071110A (en) * | 1997-09-11 | 2000-06-06 | Mikkelsen; Oeystein | Polishing roll and method for making same |
US6074192A (en) * | 1997-09-11 | 2000-06-13 | Mikkelsen; Oeystein | Lenticular pattern forming roll and method for making the roll |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1952038A (en) | Process of extruding sheet material | |
US2168218A (en) | Mastic shingle | |
EP1674224B1 (en) | Process for production of wood fiber insulating panels | |
EP0906480B1 (en) | Structural member | |
EP1674633B1 (en) | Wood fiber insulating panel or mat | |
US2168288A (en) | Extruding sheet material | |
DE3020641A1 (en) | THERMALLY INSULATING AND BITUMEN-CONTAINING WATERPROOF PANEL AND THEIR USE | |
US2241603A (en) | Roofing element | |
US2091125A (en) | Apparatus for making extruded products | |
DE102005026656A1 (en) | Production of a mineral fiber web with largely upright mineral fibers and use of the resulting waste | |
US2213249A (en) | Insulation board and method of making the same | |
US2091124A (en) | Method of and apparatus for making extruded products | |
US1344826A (en) | Process of making lath or the like | |
DD300115A5 (en) | WATERPROOFED LUBRICANT | |
US2156566A (en) | Building unit and method of manufacture thereof | |
US1831058A (en) | Building board and process of making same | |
US1952828A (en) | Method of making composition roofing | |
DE19906734C1 (en) | Insulation material, comprising binder and preferably rock wool fibres, contains binder free regions where fibres extend at right angles to material surfaces | |
US2452226A (en) | Laminated product and method of manufacture | |
US1886456A (en) | Method of making roofing | |
US1851300A (en) | Strip shingle and method of making the same | |
US1571667A (en) | Building board and method of making it | |
US1900940A (en) | Roofing and method of making same | |
US1314476A (en) | Frederick c | |
US1683881A (en) | Expansion joint |