US1188718A - Process for spinning solutions of nitrocellulose. - Google Patents
Process for spinning solutions of nitrocellulose. Download PDFInfo
- Publication number
- US1188718A US1188718A US84355614A US1914843556A US1188718A US 1188718 A US1188718 A US 1188718A US 84355614 A US84355614 A US 84355614A US 1914843556 A US1914843556 A US 1914843556A US 1188718 A US1188718 A US 1188718A
- Authority
- US
- United States
- Prior art keywords
- nitrocellulose
- alcohol
- spinning
- ether
- solutions
- 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
- 239000000020 Nitrocellulose Substances 0.000 title description 17
- 229920001220 nitrocellulos Polymers 0.000 title description 17
- 238000000034 method Methods 0.000 title description 14
- 238000009987 spinning Methods 0.000 title description 10
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 16
- 235000019441 ethanol Nutrition 0.000 description 14
- 239000000203 mixture Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 230000001376 precipitating effect Effects 0.000 description 5
- 229920002955 Art silk Polymers 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000001476 alcoholic effect Effects 0.000 description 3
- 230000001112 coagulating effect Effects 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000002166 wet spinning Methods 0.000 description 3
- 239000010902 straw Substances 0.000 description 2
- 101100369915 Drosophila melanogaster stas gene Proteins 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000578 dry spinning Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229960004756 ethanol Drugs 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
Classifications
-
- 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
Definitions
- a precipitating liquid composed of diluted alcohol conveniently heated, said liquid comprising preferably from 25 to 50 volumes of alcohol for 100 volumes of water.
- the expulsion of the ether from the products, after coagulation can be effected in particularly good conditions if the precipitating or coagulating liquid is maintained at a temperature corresponding approximately to the boiling temperature of the ether, consequently at about 355 C. If said conditions are observed it is possible to obtain transparent threads (the transparency of which may be compared with the transparency of glass) having acircular and regular section, said threads being produced at a spinning velocity which is not less than the velocity which is obtained in the dry'spinning process and which attains a rate of 40 to 50 m. per minute. It will be evident that by conducting the thread during a sufiiciently long time through the coagulating liquid, the main portion of the ether will be recovered; further approximately the total quantity of alcohol can be recovered if the products are subsequently treated with water.
- a high velocity of spinning can thus be used and the artificial silk which is produced, is particularly soft and nonadhesive.
- a further advantage of the new process consists in that the recuperation of the solventcan be very easily carried out.
- the possibility of using Wet nitrocellulose also constitutes a great advantage in view of the suppression of danger in the manufacture.
- a process for the spinning of solutions of nitrocellulose for the manufacture of artificial silk, lustrous threads, artificial horsehair and straw, films, bands and the like consisting in preparing a collodion with a nitrocellulose containlng from to 30% of water, then spinning said collodion and then coagulating said collodion,
- said coagulation beholic solution containing from 25 to 50% vol. of alcohol the temperature of said solution being maintained at about 35.5 C.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
- Materials For Medical Uses (AREA)
Description
UNIETED STAS PATENT @FIBIGE ERNST BERL AND MAX ISLER, OF TUIBIZE, NEAR BRUSSELS, BELGIUM.
PROCESS FOR SPINNING SOLUTIONS OF NITROCELLULOSE.
No Drawing.
To all whom it may concern:
Be it known that we, ERNEST BERL, a subject of the Emperor of Austria-Hungary, and MAX IsLnR, a citizen of Switzerland, residing at Tubize near Brussels, in theKingdom of Belgium, have invented certain new and useful Improvements in Processes for Spinning Solutions of Nitrocellulose, of which the following is a specification.
The processes which have hitherto been used for spinning solutions of nitrocellulose for the production of artificial silk, lustrous threads, artificial horse-hair, artificial straw, films, bands or the like from a collodion of nitrocellulose by means of what 13 termed the wet-spinning process have very 1mportant inconveniences. In the first place, it is necessary to employ dry nitrocellulose to secure its solution in the required solvents. It has been found, for instance, that if it is intended to spin in water a collodion which has been prepared with wet nitrocellulose as commonly used in the dry spinning process, the products which are finally obtained are opaque, unelastic and possess only a very low industrial value. The drying of the nitrocellulose, however, which has been considered hitherto asnecessary, requires a very great stability of the ntrocellulose in order to prevent the accldents due to the spontaneous decomposition of the nitrocellulose. Notwithstanding the said precautions, however, the danger of working with dry nitrocellulose remains very great. On the other hand, as it is well known, it is advisable, in the wet-spinning process, to substitute certain mixtures of solvents, which are relatively heavy, as for example a mixture comprising methyl alco hol, ethyl alcohol and a little proportion of ether to the usual and cheaper mixtures of ether and alcohol originally used.
-Now it has been found that the above stated inconveniences of the wet spinning process can be completely avoided if use is made of ordinary wet nitrocellulose such as that dried in a centrifugal machine and if said nitrocellulose, containing from 20 to 30% of water, is dissolved in a mixture of ether and alcohol, the usual proportions of the mixture of parts of ether and 40 parts of alcohol being replaced by a mixture in which alcohol prevails for example a mixture containing from 10 to 50 parts of ether and 60 to 50 parts of alcohol. Fur- Specification of Letters Patent.
Application filed June 6, 191a.
ther it has been found that very transparent and elastic threads, having an absolutely regular and uniform section can be obtained if, instead of the usual precipitating liquid of pure water, a precipitating liquid is employed composed of diluted alcohol conveniently heated, said liquid comprising preferably from 25 to 50 volumes of alcohol for 100 volumes of water.
It has been further found that the expulsion of the ether from the products, after coagulation, can be effected in particularly good conditions if the precipitating or coagulating liquid is maintained at a temperature corresponding approximately to the boiling temperature of the ether, consequently at about 355 C. If said conditions are observed it is possible to obtain transparent threads (the transparency of which may be compared with the transparency of glass) having acircular and regular section, said threads being produced at a spinning velocity which is not less than the velocity which is obtained in the dry'spinning process and which attains a rate of 40 to 50 m. per minute. It will be evident that by conducting the thread during a sufiiciently long time through the coagulating liquid, the main portion of the ether will be recovered; further approximately the total quantity of alcohol can be recovered if the products are subsequently treated with water.
We are aware that the use of concentrated alcohol is already known for the coagulation of threads obtained from solutions of nitrocellulose, said alcohol having been used in order to compensate the solvent capacity of the precipitating solution for the nitrocellulose. In this known process, however, in order that the precipitating solution be able to act rapidly, it is necessary to use alcohol from to If it was proposed to use alcoholic solutions of such a concentration in the new process as above described, in which the spinning velocity stands above 40 m. per minute, the threads would be adhesive and the products obtained, specially artificial silk, would be absolutely useless in practice. Said inconveniences are avoided when it is worked according to the above described process by using an alcoholic solution containing only from 25 to 50% of alcohol and having a temperature less than the temperature of ebullltion of the ether. A high velocity of spinning can thus be used and the artificial silk which is produced, is particularly soft and nonadhesive. A further advantage of the new process consists in that the recuperation of the solventcan be very easily carried out. The possibility of using Wet nitrocellulose also constitutes a great advantage in view of the suppression of danger in the manufacture.
Having thus described our invention, what we claim is:
1. A process for the spinning of solutions of nitrocellulose for the manufacture of artificial silk, lustrous threads, artificial horsehair and straw, films, bands and the like, said process consisting in preparing a collodion with a nitrocellulose containlng from to 30% of water, then spinning said collodion and then coagulating said collodion,
with alcoholic solutions containing from to'50% vol. of alcohol, said coagulation beholic solution containing from 25 to 50% vol. of alcohol the temperature of said solution being maintained at about 35.5 C.
In testimony whereof wehave afiixed our' I signatures in presence of two witnesses.
ERNEST BERL.
MAX ISLER.
Witnesses:
JACQUES BEDE, CHAS. Row. NASMITH.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US84355614A US1188718A (en) | 1914-06-06 | 1914-06-06 | Process for spinning solutions of nitrocellulose. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US84355614A US1188718A (en) | 1914-06-06 | 1914-06-06 | Process for spinning solutions of nitrocellulose. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1188718A true US1188718A (en) | 1916-06-27 |
Family
ID=3256675
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US84355614A Expired - Lifetime US1188718A (en) | 1914-06-06 | 1914-06-06 | Process for spinning solutions of nitrocellulose. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1188718A (en) |
-
1914
- 1914-06-06 US US84355614A patent/US1188718A/en not_active Expired - Lifetime
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2716049A (en) | Water-soluble yarn | |
| ES453845A1 (en) | Process for hygroscopic, fibres and filaments of synthetic polymers | |
| US2716586A (en) | Wet spinning of acrylonitrile polymers | |
| US1188718A (en) | Process for spinning solutions of nitrocellulose. | |
| US3235634A (en) | Process for producing microporous fibers and vinyl chloride spinning solutions therefor | |
| CN1422282A (en) | Methods of preparing and processing cellulose solutions | |
| GB1042305A (en) | Vinylidene fluoride yarns and process for producing them | |
| US625033A (en) | James frederick hoyne | |
| GB343062A (en) | Improvements in the production of artificial filaments, films and like materials | |
| US2145076A (en) | Method of preparing artificial threads | |
| US1028748A (en) | Filaments and other products obtained from cellulose compounds. | |
| US1936753A (en) | Method of making silk products | |
| US2858229A (en) | Preparation of spinning solutions | |
| DE743597C (en) | Process for the production of threads from solutions of polyvinyl resins | |
| US1996753A (en) | Artificial yarn and method of preparing the same | |
| US646351A (en) | Production of cellulose solution for manufacturing threads. | |
| GB328636A (en) | Improvements in or relating to the manufacture of filaments, films, and the like from cellulose derivatives | |
| US1566384A (en) | Manufacture of artificial silk and the like from cellulose derivatives | |
| US2267790A (en) | Treatment of textile materials | |
| US1296600A (en) | Process of producing an extract of proteolytic enzyms. | |
| US1883347A (en) | Process of making artificial filaments and product thereof | |
| US2070630A (en) | Manufacture of artificial filaments and other products containing organic derivatives of cellulose | |
| US2170752A (en) | Filament of rayon from viscose | |
| US1260508A (en) | Process for the production of articles from viscose. | |
| US1709513A (en) | Process of forming cellulose products |