US1560965A - Process of spinning artificial silk and other filaments from cellulose materials - Google Patents
Process of spinning artificial silk and other filaments from cellulose materials Download PDFInfo
- Publication number
- US1560965A US1560965A US639655A US63965523A US1560965A US 1560965 A US1560965 A US 1560965A US 639655 A US639655 A US 639655A US 63965523 A US63965523 A US 63965523A US 1560965 A US1560965 A US 1560965A
- Authority
- US
- United States
- Prior art keywords
- cellulose
- spinning
- filaments
- artificial silk
- spinneret
- 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
- 239000000463 material Substances 0.000 title description 14
- 238000000034 method Methods 0.000 title description 13
- 238000009987 spinning Methods 0.000 title description 12
- 229920002678 cellulose Polymers 0.000 title description 10
- 239000001913 cellulose Substances 0.000 title description 10
- 229920002955 Art silk Polymers 0.000 title description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 16
- 239000000020 Nitrocellulose Substances 0.000 description 10
- 229920001220 nitrocellulos Polymers 0.000 description 10
- 229940079938 nitrocellulose Drugs 0.000 description 10
- 239000007788 liquid Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- FJWGYAHXMCUOOM-QHOUIDNNSA-N [(2s,3r,4s,5r,6r)-2-[(2r,3r,4s,5r,6s)-4,5-dinitrooxy-2-(nitrooxymethyl)-6-[(2r,3r,4s,5r,6s)-4,5,6-trinitrooxy-2-(nitrooxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-3,5-dinitrooxy-6-(nitrooxymethyl)oxan-4-yl] nitrate Chemical compound O([C@@H]1O[C@@H]([C@H]([C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O)O[C@H]1[C@@H]([C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@@H](CO[N+]([O-])=O)O1)O[N+]([O-])=O)CO[N+](=O)[O-])[C@@H]1[C@@H](CO[N+]([O-])=O)O[C@@H](O[N+]([O-])=O)[C@H](O[N+]([O-])=O)[C@H]1O[N+]([O-])=O FJWGYAHXMCUOOM-QHOUIDNNSA-N 0.000 description 5
- -1 acetyl nitro cellulose Chemical compound 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 229920002301 cellulose acetate Polymers 0.000 description 4
- 238000000578 dry spinning Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 241000585703 Adelphia <angiosperm> Species 0.000 description 1
- 241001233887 Ania Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000003307 slaughter Methods 0.000 description 1
Images
Classifications
-
- 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
- D01D5/04—Dry spinning methods
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/24—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives
- D01F2/28—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives from organic cellulose esters or ethers, e.g. cellulose acetate
- D01F2/30—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from cellulose derivatives from organic cellulose esters or ethers, e.g. cellulose acetate by the dry spinning process
Definitions
- cellulose materialin solution is forced from a spinneret and delivered through a body of a1rJto permit evaporation of the solvent in which the cellulose material is contained and is then wound on a bobbin or spool, Prac- 'tically all of the solvent is removed from the cellulose material by evaporation during its passage through the body of air.
- a spinneret surrounded by-a tube adapted to contain-a body of a suitable liquid and the cellulose material in. solution is forced through this liquid and then through a body of air for a distance considerably greater than the height of the body of liquid and then wound on the bobbin or spool.
- the reference numeral 1 designates the usual feed pipe through which the solution containing the cellulose material is delivered to the spinnerets.
- This pipe is provided with a suitable branch 2 having and about/1 inches long. As shown, the
- the reference numeral 9 designates the thread formed which is carried upwardly through a guide 10 and wound upon a bobs bin or spool 11.
- the distance from the top of the spinneret to the spool is from 2 to 3 feet and at least ten times the distance from the top of the spinneret to the top of the tube 6.
- the process may be advana'geously employed' in spinning threads or filaments from cellulosce material, in the form of acetyl nitro cellulose described and claimed A in our. copending application Serial No.
- the material passing through the feed pipe consists of a solution of acetyl nitro cellulose'in acetone in which the acetyl nitro cellulose forms from 20 to 30 per cent, by weight of the total.
- This material is passed from the spinneret through a body of diluted acetone 8'1". ranged in the tube 6. During its passage through the body of liquid, very little of t e solvent is removed from the acetyl nitrocellulose.
- the thread leaving the top of the tube is passed through the guide 10 and wound upon thebobbin or spool 11, substantially all of the solvent being evaporated during its passage through the am
- the distance from the top of the spinneret to the bottom of spool 1s at least ten times as greatas the distance from the tip of the spinneret to the top of the liquid.
- the thread or filament formed is of substantially uniform cylindrical cross section as distinguished from the non-uniform thread esS.
- Wehave also 1 found that the spinning strength of the thread is materially in c'reased and its elasticity during the spinning opei'ationis greater, permitting reater variation in tension with less possi 'ility of breaking the thread and "tlieresulting disadvant ges .a d inconvenience.
- other liquids may t-bejplacedin the tube 6, such as water, a weak solution of alcoholfand dilute acetic acid;
- cellulose materials such as nitro cellulose, and celulose acetate, may be formed into threads or filaments in the same manner.
- nitro cellulose a mixture of alcohol and Water may be substituted 'for the diluted acetone or a mixture of acetone and Water as described above may" e employed.
- the liquid'employed in the 't e 6 depends upon the solvent usedfor the cellulose acetate.'-Where the cellulose acetate is dissolved in a solution of acetone, a mixture of acetone and Water may be employed in the tube 6. I i
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Artificial Filaments (AREA)
Description
Nov.. 10 1925. 1,560,965-
H P. BASSETTV ET AL PROCESS OF ,SFINNINGkRTIFICIAL SILK AND OTHER FILAM ENTS FROM GELLULOSE MATERIAL Filed May. 1'7, 1:923
1 v HAPPY/ 954mm Patented Noy. 1 0, 1925.
UNITED STATES I v i 1,560,965 ATEN O F E- I HARRY 1 BASSETT, on CYNTHIANA, xsn'rucxr, AnnTHonAs r. BANIGAN, or'ririn- I .ADELPHIA, PE1\LNSYLV ANIA, ASSIGNORS TO MmesBAssET'r & SLAUGHTER, me,
1 orrmLAnELrmA, PENNSYLVANIA, A coaron'A'rxonor PENLLSYLVANIA.
raocsss ofsrmnme 'Aiat rxrrcrAL SILK AND ornnn FILAMn N'rs'FRon oELLULosE v MATERIALS. 1
Application filed May17, 192s. Serial No. 639,655,
l I J v To all whom it may concern: 1
Be it known that we, HARRY P. BASSETT and THOMAS F. BANIG N, citizens of the United States, residing at Cynthiana, in the countyof Harrison and State of Kentucky,
andiPhiladelphia, in the cdunty of Philadel- I "phia-and State of Pennsylvania, respectivehave invented certain new and useful Improvements in Processes. of Spinning 1 Artificial Silk and Other Filaments from Cellulose Materials, ofwhich the followingis a specification. This invention relates to processes of'spinning artificial silk and other filaments from cellulose material, and more particularly to a modification of the ordinary dry spinning process-- by meansof which nitro cellulose. cellulose acetate, acetyl nitro cellulose and similar materials are formed into threads or "I filaments. A 5
In the usual dry spinning processes, cellulose materialin solution is forced from a spinneret and delivered through a body of a1rJto permit evaporation of the solvent in which the cellulose material is contained and is then wound on a bobbin or spool, Prac- 'tically all of the solvent is removed from the cellulose material by evaporation during its passage through the body of air.
In the present invention, we provide a spinneret surrounded by-a tube adapted to contain-a body of a suitable liquid and the cellulose material in. solution is forced through this liquid and then through a body of air for a distance considerably greater than the height of the body of liquid and then wound on the bobbin or spool.
By thus modifying the usual dry spinning process, a filament or thread more regular in crosssection" is obtained and it possesses greater spinning strength and elasticity during the spinning ,operation, permitting a wider variation of the tension of the thread during the spinning operation, without breaking the thread.
A further advantage of our process is that much finer threads may be spun by it from the same spinneret than is possible in the ordinary dry spinning process. I In the accompanying drawings, we have diagrammatically shown ,an apparatus particularly suitable for use in practicing the .process.
In the drawings, the reference numeral 1 designates the usual feed pipe through which the solution containing the cellulose material is delivered to the spinnerets.
ably from to of an inch'in'diamcter This pipe is provided with a suitable branch 2 having and about/1 inches long. As shown, the
upper end of the spinneret is arranged in-;
termediate the ends of the tube and preferably :from 1 th 3 inches from the top of the tube. The bottom of the tube is closed by a support 7 and a body of liquid 8"is arranged therein. Y
The reference numeral 9, designates the thread formed which is carried upwardly through a guide 10 and wound upon a bobs bin or spool 11. The distance from the top of the spinneret to the spool is from 2 to 3 feet and at least ten times the distance from the top of the spinneret to the top of the tube 6.-
The process may be advana'geously employed' in spinning threads or filaments from cellulosce material, in the form of acetyl nitro cellulose described and claimed A in our. copending application Serial No.
638,391. filed May 11, 1923. The material passing through the feed pipe consists of a solution of acetyl nitro cellulose'in acetone in which the acetyl nitro cellulose forms from 20 to 30 per cent, by weight of the total. This material is passed from the spinneret through a body of diluted acetone 8'1". ranged in the tube 6. During its passage through the body of liquid, very little of t e solvent is removed from the acetyl nitrocellulose. The thread leaving the top of the tube is passed through the guide 10 and wound upon thebobbin or spool 11, substantially all of the solvent being evaporated during its passage through the am As stated, the distance from the top of the spinneret to the bottom of spool 1s at least ten times as greatas the distance from the tip of the spinneret to the top of the liquid. The thread or filament formed is of substantially uniform cylindrical cross section as distinguished from the non-uniform thread esS. Wehave also 1 found that the spinning strength of the thread is materially in c'reased and its elasticity during the spinning opei'ationis greater, permitting reater variation in tension with less possi 'ility of breaking the thread and "tlieresulting disadvant ges .a d inconvenience. In place of acetone, other liquids may t-bejplacedin the tube 6, such as water, a weak solution of alcoholfand dilute acetic acid;
Other cellulose materials such as nitro cellulose, and celulose acetate, may be formed into threads or filaments in the same manner. In spinning nitro cellulose according to the process, :a mixture of alcohol and Water may be substituted 'for the diluted acetone ora mixture of acetone and Water as described above may" e employed.
1 In spinning cellulose acetate acco'rdingtd the pr sent invention, the liquid'employed in the 't e 6 depends upon the solvent usedfor the cellulose acetate.'-Where the cellulose acetate is dissolved in a solution of acetone, a mixture of acetone and Water may be employed in the tube 6. I i
It is to be understood that the formof the neeoteee invention herewith shown and describedjs to'be taken as a preferred example of the same and thatvarious "changes in the shape, size, and arrangfement of parts may be resorted to without departing from the spirit of the. invention orf the"scope of the subjOlIiBCl claims. 9 3 q @We claim: r l. The process of spinningacetyl nitro cellulose Whichcomprises delivering a solution ofacetyl nitro cellulose i'nacetone from spinneret through ashallow body o f acetone and Water, and then delivering the thread formed through a body of air of 'appreciable depth. 2. The process of spinning'acetyl nitro tioii of acetyl nitro cellulose i'nac'etoneirom a spinneret through a body of acetoneand water, and then delivering the thread rformed through'a body of air of at least teiu timeshthed'epth of the liquid.
cellulose which comprises delivering a solu- In testimony 'vvhereof, We aflix our signatures HARRY P.'BAS'SETT;
THOMAS BANIGAN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US639655A US1560965A (en) | 1923-05-17 | 1923-05-17 | Process of spinning artificial silk and other filaments from cellulose materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US639655A US1560965A (en) | 1923-05-17 | 1923-05-17 | Process of spinning artificial silk and other filaments from cellulose materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1560965A true US1560965A (en) | 1925-11-10 |
Family
ID=24565017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US639655A Expired - Lifetime US1560965A (en) | 1923-05-17 | 1923-05-17 | Process of spinning artificial silk and other filaments from cellulose materials |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1560965A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE970677C (en) * | 1948-11-27 | 1958-10-16 | American Viscose Corp | Process for the production of artificial structures from acrylonitrile-containing polymerization products |
| US3448185A (en) * | 1967-03-28 | 1969-06-03 | Monsanto Co | Melt-spinning of filaments |
-
1923
- 1923-05-17 US US639655A patent/US1560965A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE970677C (en) * | 1948-11-27 | 1958-10-16 | American Viscose Corp | Process for the production of artificial structures from acrylonitrile-containing polymerization products |
| US3448185A (en) * | 1967-03-28 | 1969-06-03 | Monsanto Co | Melt-spinning of filaments |
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