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Production of artificial materials

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Publication number
US2517711A
US2517711A US68082846A US2517711A US 2517711 A US2517711 A US 2517711A US 68082846 A US68082846 A US 68082846A US 2517711 A US2517711 A US 2517711A
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Prior art keywords
jet
extrusion
orifices
material
plate
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Expired - Lifetime
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Pool William
Upton Edward James
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Celanese Corp
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Celanese Corp
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    • DTEXTILES; PAPER
    • D01NATURAL OR ARTIFICIAL THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00Spinnerette packs; Cleaning thereof

Description

Aug. 8, 1950 w. POOL EI'AL 2,517,711

PRODUCTION OF ARTIFICIAL MATERIALS Filed July 1, 1946 5/ \\\\\L&\\ VA mvsuroks Patented Aug. 8, 1950 PRQBUCTION F ARTIFICIAL MATERIALS WilliamPooland Edward James Upton, Spondon, 1 near Derby. England, assignors to Celanese Corporation of America, a corporation of Delaware Application July 1, 1M6, Serial No. 680,828 1 In Great Britain July 13, 1945 This invention relates to the production of ar- 1 1 tificial materials and particularly to the spinning by extrusion of artificial filaments and like products, and is especially concerned with the spinning jets and jet assemblies by means of which filament-forming materials are extruded to form such products.

.In the spinning of certain materials into filamentary form, and particularly of organic materials that require to be extruded at high temperatures, bubbles are liable to form in the material being extruded, giving rise to weak and irregular filaments and to frequent stoppages of spinning by the lodgment of bubbles in the extrusion orifices. In such cases it is desirable to maintain the pressure of the material on its Way to the spinning jet high enough to inhibit as far as possible the formation of bubbles in the material in spite of the fact that so high a pressure is more than is necessary, at the rates of flow of the material usually met within practice, to force the material through the extrusion orifices. This may be done in some measure by the insertion of filters immediately before the jet which, apart from their function of preventing the passage of any solid particles contained in the material, are designed to offer such a, resistance to the flow of the material as to ensure a high pressure in the material being extruded, up to a point shortly before the jet is reached. This pressure, however, gradually falls off across each filter and this gives an opportunity for bubble-formation, both in the later stages of filtering and between the last filter and the jet. It is the object of the present invention to provide a jet assembly in \which a high pressure is maintained right up to the jet itself, whereby this disadvantage is overcome or substantially reduced.

According to the present invention a jet as sembly for the extrusion of artificial filaments and like products comprises a jet having extrusion orifices therein, and a plate finely spaced from the inner surface of said jet, said plate being perforated at a distance across the face of the plate from any of said orifices for the passage of material to be extruded to the inner surface of said jet. By these means the extrusion material reaches the inner surface of the jet at a point removed from the extrusion orifices and, in order to reach the extrusion orifices, is forced to pass through a very thin flat space, the conformation of which offers a high resistance to its passage and gives rise to a high pressure in the material reaching and passing across the inner face of the jet.

5 Claims. (Cl. 18-8) The jet is conveniently in the form of a fiat circular disc with a concentric circle of extru- 'sion orifices, the plate behind the jet then being a circular plate coextensive with the jet and having a single central perforation, which is thus equally spaced from each of the extrusion orifices. A thin spacing washer can be interposed between the jet and the plate in order to space them accurately apart, the washer being exchangeable with other washers of different thickness in order to vary .or adjust the pressure .de veloped in the material being extruded. Alternatively, the spacing of the faces of the jet and plate may be effected by integral projections on one or other of said faces. The jet itself must, of course, be of a thickness sufficient to withstand the pressure developed on its inner surface, and since the thickness thus necessitated may be substantial the inner surface of the jet may be recessed at the points where the extrusion orifices are formed in order to reduce the length of the fine holes constituting theorifices.

The jet assembly according to the invention is applicable generally to the extrusion of filamentformin g materials which are liable to bubbleformation under the conditions of extrusion, and is particularly well suited for the spinning of molten material in. the form of filaments which harden by cooling after extrusion. Thus, for example, it may be employed in the melt-spinning of synthetic linear polyamides made, for instance, by the condensation of diamlnes with di-carboxylic acids.

By way of example one form of jet assembly in accordance with the invention and particularly adapted for the melt-spinning of such materials will now be described in greater detail with reference to the accompanying drawing which is a section through the jet assembly.

The assembly comprises a die steel disc I of 1% outside diameter, 4 mm. thick, drilled with six holes 2 each 3.5 mm. deep and diameter, on centres equally spaced round the disc at a distance of from the centre thereof. At the bottom of each hole, and coaxial therewith, is formed a spinning orifice 3 of 0.2 mm. diameter, 0.5 mm. long. After the formation of the orifices 3 the disc I is hardened, ground and lapped fiat. Over the disc is placed a washer 4, 0.003 thick, 1%" outside diameter and inside diameter, and above the Washer l is a hardened and ground die steel disc 5, 1%" diameter and 4 mm. thick, having a central hole 6 of 1 5" diameter. The three members I, 4 and 5 are clamped together by means of a heavy internally flanged nut I against the end of a flanged and screw-threaded pipe 8 by which the spinning material is supplied to the assembly. The spinning material so supplied is constrained to pass through the central hole 6 in the upper plate 5, and radially across from centre to edge of the flat space, 0.003" deep, enclosed between the jet I, the plate 5, and the separating washer 4. By these means a pressure of the order of 800 to 900 lbs/sq. inch can readily be built up in the material reaching the jet assembly. By changing the washer 4 for one of different thickness, the pressure may be altered when required.

Having described our invention, what we desire to secure by Letters Patent is:

1. A jet assembly for the extrusion of artificial filaments and other shaped products, which comprises a jet having extrusion orifices therein, and behind and finely spaced therefrom a plate adapted to cause a viscous filament-forming material to travel, laterally across and substantially parallel to the inner surface of the jet under a considerable pressure gradient, said plate having a perforation therein, the arrangement of the extrusion orifices in the jet in relation to the perforation in the plate being such that each orifice is at substantially the same distance normally to and laterally across the jet face from the perforation in the plate.

2. A jet assembly according to claim 1, wherein the perforated plate is spaced from the inner surface of the jet by means of a thin spacing washer.

3. A jet assembly for the extrusion of artificial filaments and other shaped products, which comprises a jet consisting of a flat disc provided with a number of extrusion orifices arranged in a circle concentric with the circumference of the disc, behind the jet a plate of substantially the same diameter as the jet having a single central perforation of diameter substantially less than that of the circle of extrusion orifices, the arrangement of the extrusion orifices in the jet in relation to the perforation in the plate being such that each orifice is at substantially the same distance normally to and laterally across the jet face from the perforation in the plate, and between the jet and the plate and in contact with both a spacing washer, the combination being adapted to cause a viscous filament-forming material to travel laterally across and substantially parallel to the inner surface of the jet under a considerable pressure gradient.

4. A jet assembly according to claim 1, wherein the inner surface of the jet is recessed at the points where the extrusion orifices are formed so as to reduce the length of the fine holes constituting the orifices.

5. A jet assembly according to claim 3, wherein the inner surface of the jet is recessed at the points where the extrusion orifices are formed so as to reduce the length of the fine holes constituting the orifices.

WILLIAM POOL. EDWARD JAMES UPTQN.

REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 304,901 Bowron et a1. Sept. 9, 1884 1,922,718 Tidmus et a1. Aug. 15, 1933 1,983,330 Welch Dec. 4, 1934 2,295,942 Fields Sept. 15, 1942 FOREIGN PATENTS Number Country Date 837,555 France Nov. 12, 1938

US2517711A 1945-07-13 1946-07-01 Production of artificial materials Expired - Lifetime US2517711A (en)

Priority Applications (1)

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GB1795045A GB596010A (en) 1945-07-13 1945-07-13 Improvements in the production of artificial filaments and the like

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US2517711A true US2517711A (en) 1950-08-08

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2731667A (en) * 1951-05-16 1956-01-24 Celanese Corp Wet spinning apparatus
US2892675A (en) * 1951-05-16 1959-06-30 Celanese Corp Method and apparatus for production of viscose rayon filamentary materials
US2936482A (en) * 1955-06-30 1960-05-17 Du Pont Spinneret assembly
US2970340A (en) * 1958-04-03 1961-02-07 American Viscose Corp Multi-jet couplings
US3006028A (en) * 1959-05-25 1961-10-31 Du Pont Spinning apparatus
US3070840A (en) * 1960-03-25 1963-01-01 Plastic Textile Access Ltd Extrusion of plastic sheeting or netting
US3095607A (en) * 1962-07-10 1963-07-02 Du Pont Spinneret assembly
US3516478A (en) * 1967-12-05 1970-06-23 Monsanto Co Apparatus for separation of impurities from metal melts in a filament spinning device
US5397227A (en) * 1990-12-26 1995-03-14 Basf Corporation Apparatus for changing both number and size of filaments
US5533883A (en) * 1992-10-29 1996-07-09 Basf Corporation Spin pack for spinning synthetic polymeric fibers
US5578330A (en) * 1989-02-16 1996-11-26 Conoco Inc. Pitch carbon fiber spinning apparatus
US5620644A (en) * 1992-10-29 1997-04-15 Basf Corporation Melt-spinning synthetic polymeric fibers

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1011428A (en) * 1949-02-05 1952-06-23 Rhodiaceta Apparatus and process for spinning high polymers solutions

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US304901A (en) * 1884-09-09 Dlesex
US1922718A (en) * 1929-09-05 1933-08-15 Celanese Corp Manufacture of artificial filaments, threads, and the like
US1983330A (en) * 1928-07-06 1934-12-04 Celanese Corp Manufacture of artificial filaments, threads, films, or the like
FR837555A (en) * 1937-05-11 1939-02-14 Ig Farbenindustrie Ag Method and device for the production of man-made fibers
US2295942A (en) * 1940-08-02 1942-09-15 Du Pont Manufacture of filaments

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US304901A (en) * 1884-09-09 Dlesex
US1983330A (en) * 1928-07-06 1934-12-04 Celanese Corp Manufacture of artificial filaments, threads, films, or the like
US1922718A (en) * 1929-09-05 1933-08-15 Celanese Corp Manufacture of artificial filaments, threads, and the like
FR837555A (en) * 1937-05-11 1939-02-14 Ig Farbenindustrie Ag Method and device for the production of man-made fibers
US2295942A (en) * 1940-08-02 1942-09-15 Du Pont Manufacture of filaments

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2731667A (en) * 1951-05-16 1956-01-24 Celanese Corp Wet spinning apparatus
US2892675A (en) * 1951-05-16 1959-06-30 Celanese Corp Method and apparatus for production of viscose rayon filamentary materials
US2936482A (en) * 1955-06-30 1960-05-17 Du Pont Spinneret assembly
US2970340A (en) * 1958-04-03 1961-02-07 American Viscose Corp Multi-jet couplings
US3006028A (en) * 1959-05-25 1961-10-31 Du Pont Spinning apparatus
US3070840A (en) * 1960-03-25 1963-01-01 Plastic Textile Access Ltd Extrusion of plastic sheeting or netting
US3095607A (en) * 1962-07-10 1963-07-02 Du Pont Spinneret assembly
US3516478A (en) * 1967-12-05 1970-06-23 Monsanto Co Apparatus for separation of impurities from metal melts in a filament spinning device
US5578330A (en) * 1989-02-16 1996-11-26 Conoco Inc. Pitch carbon fiber spinning apparatus
US5397227A (en) * 1990-12-26 1995-03-14 Basf Corporation Apparatus for changing both number and size of filaments
US5533883A (en) * 1992-10-29 1996-07-09 Basf Corporation Spin pack for spinning synthetic polymeric fibers
US5575063A (en) * 1992-10-29 1996-11-19 Basf Corporation Melt-spinning synthetic polymeric fibers
US5620644A (en) * 1992-10-29 1997-04-15 Basf Corporation Melt-spinning synthetic polymeric fibers

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Publication number Publication date Type
GB596010A (en) 1947-12-24 application

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