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US888260A - Apparatus for the manufacture of collodion filaments. - Google Patents

Apparatus for the manufacture of collodion filaments. Download PDF

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Publication number
US888260A
US888260A US35374907A US1907353749A US888260A US 888260 A US888260 A US 888260A US 35374907 A US35374907 A US 35374907A US 1907353749 A US1907353749 A US 1907353749A US 888260 A US888260 A US 888260A
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Prior art keywords
filament
manufacture
collodion
sieve
receptacle
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Expired - Lifetime
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US35374907A
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Victor Planchon
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Individual
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Priority to US35374907A priority Critical patent/US888260A/en
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/088Cooling filaments, threads or the like, leaving the spinnerettes
    • D01D5/092Cooling filaments, threads or the like, leaving the spinnerettes in shafts or chimneys

Definitions

  • the filament descends on to the sieve a certain distance from the center of rotation, so that during the working of the apparatus the spirals formed by the collod ion at the mo- To all whom it. may concern:
  • the present invention relates to improvements In a paratus for the manufacture of ment of its contact with the coagulating liqcollodion aments and the object isto allow uid are not superposed on each other.
  • These of simultaneously producing the filament and of coiling it for the pur ose of producing regular cocoons, which a low of carrying out spirals overlap each other in the manner illustrated in Fig. 3 and after a certain length of time form a hollow, conical structure, as shown in Fig. 2.
  • This structure nearly fills the sieve-bottomed receptacle the latter is removed and replaced by a similar rece tacle of the same kind.
  • the filament can e very easily wound, being. perfectly continuous and arranged in t e manner of regular, overlapping rings.
  • the length of the filament is only restricted by the capacity of the receptacle, and may attain several thousand meters without a joint.
  • Figs. Zand 3 are an elevation res ectively of the cocoon obtained.
  • nozzle the col lodion descends by gravity in the form of a cylindrical thread j, which enters the receptacle r containing a suitable coagulating liquid.
  • the cylinder 9 is of metal and open The ament of liquid at 0th ends, and is lined with spong mate descends by gravity through the alcohol varial saturated with alcohol.
  • the filament por in the cylinder 9 and is solidified and coiled on the sieve as has been described.
  • a lurality of vessels and sieves may simul taneously used, with a single driving cord or belt.
  • the cover of the space betw tube contains alcohol, which enters the said s ace through the tube t and passes out t ough the tube t.
  • the si hon or si hons may merely consist of strips of fiibric, conduct alcohol to the spongy lining of the cylinder g.
  • the collodion filament c linder g does not become dry but is merely slightly expanded and hardened. It enters the vessel 1' in a erfectly cylindrical state.
  • the vessel 1 may e an ordinarybowl or the to evaporation.
  • the apparatus may be constructed of any suitable material, and the dimensions and details of construction may be varied indefinitely. In all cases, however, the collodion filament traverses by gravity a certain vertical distance before coming into contact with th lating agent, and descends on to a rotating sieve, so that it forms thereon a regular coil similar easy to unwind.
  • apparatus for the purpose set forth be effected by transferring the sieve-botthecombination with a discharge nozzle tomed vessel into successive baths, in which through which a filament is passed, of a rotait is placed with suitable care, or by successive, double, sieve-bottomed receptacle besively introducing the liquids into a single low said nozzle and adapted to contain a co vessel in which the sieve-bottomed receptaagulating substance, said vessel being so 10- cle is placed.
  • the filament descends thereinto What I claim as my at a distance from its center of rotation an to secure by Letters Patent of the open ended chamber intermediate the nozzle States is and receptacle through which the filament 1.
  • adapted to contain a coagulating substance In witness whereof I have signed this the fillamentl aforesaid desplending into said specification in the presence of two witnesses.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

PATENTED MAY 19, 1908. v
APPARATUS FOR THE MANUFACTURE OF OOLLODION FILAMENTS. APPLICATION FILED JAN.23,1907.
FIGJ
' s, which i with great facility the final chemical operapasses into the cylinder UNITED STATES PATENT OFFICE.
VICTOR PLAN CHON OF LYON, FRANCE. APPARATUS FOR THE MANUFACTURE OF COLLODION FILAMiEN TS.
Specification of Letters Patent. Application filed January 23, 1907. Serial No. 353,749;
No. 888,260. Patented May 19, 1908.
I liquid. During the entire operation the parts 11 and e are rotated by means of the horizontal pulley p and the cord i l; 11: is the axle of the pulley.
The filament descends on to the sieve a certain distance from the center of rotation, so that during the working of the apparatus the spirals formed by the collod ion at the mo- To all whom it. may concern:
Be it known that I, VICTOR PLANcnoN, a citizen of the Frencl1 Republ1c, residing at Apparatus for t e Manufacture 'of Collodion Filaments, of which the following is a specification.
The present invention relates to improvements In a paratus for the manufacture of ment of its contact with the coagulating liqcollodion aments and the object isto allow uid are not superposed on each other. These of simultaneously producing the filament and of coiling it for the pur ose of producing regular cocoons, which a low of carrying out spirals overlap each other in the manner illustrated in Fig. 3 and after a certain length of time form a hollow, conical structure, as shown in Fig. 2. When this structure nearly fills the sieve-bottomed receptacle the latter is removed and replaced by a similar rece tacle of the same kind. The filament can e very easily wound, being. perfectly continuous and arranged in t e manner of regular, overlapping rings. The length of the filament is only restricted by the capacity of the receptacle, and may attain several thousand meters without a joint.
he apparatus described is very easy to control. When the horizontal pulley has been started, and an empty sieve-bottomed receptacle has been placed liquid, the 0 eration can be started. by turnii which controls the flow of the c diodion solution.
tion of manufacture.
An; embodiment of the invention is illustrated in the annexed drawing, in which igure 1 is a sectional elevation thereof.
Figs. Zand 3 are an elevation res ectively of the cocoon obtained.
- ollodion from the pipe (1 is discharged at suitable pressure through the nozzle 0 connected to the ipe by the union 6. nozzle the col lodion descends by gravity in the form of a cylindrical thread j, which enters the receptacle r containing a suitable coagulating liquid.
va ors. The cylinder 9 is of metal and open The ament of liquid at 0th ends, and is lined with spong mate descends by gravity through the alcohol varial saturated with alcohol. The filament por in the cylinder 9 and is solidified and coiled on the sieve as has been described.
A lurality of vessels and sieves may simul taneously used, with a single driving cord or belt. he vessel 1 or the rotating 9 through the orifice 0 1n the cover of the space betw tube contains alcohol, which enters the said s ace through the tube t and passes out t ough the tube t. The si hon or si hons may merely consist of strips of fiibric, conduct alcohol to the spongy lining of the cylinder g.
The collodion filament c linder g does not become dry but is merely slightly expanded and hardened. It enters the vessel 1' in a erfectly cylindrical state. The vessel 1 may e an ordinarybowl or the to evaporation. The apparatus may be constructed of any suitable material, and the dimensions and details of construction may be varied indefinitely. In all cases, however, the collodion filament traverses by gravity a certain vertical distance before coming into contact with th lating agent, and descends on to a rotating sieve, so that it forms thereon a regular coil similar easy to unwind. This special arran ement to that illustrated in the rawing This arof the ament allows of effecting, wit great rangement com rises the cylindrical inner rel facility, all the final chemical operatlons of ceptacle v, whic is open at the to and con- J manufacture wlthout removing the filament talns the coa ulating liquid and tlie sieve e, from t e s1eve-bottomed receptacle. The the bottom 0 the latter consisting of widelatter, with the coil therein, is first dipped meshed fabric or metallic gauze. The filainto pure water to remove all the so uble ment enters the sieve-bottomed vessel and substances contained therein, these subthe latter serves for removing it from the ssazao the combination with a discharge nozzle through which a filament is passed, of a rotatable, double, sieve-bottomed receptacle bethe receptacle is placed in baths containing suitable denitratmg and decoloring agents of the kind commonly used. Then the filament is again dipped into water, and can be I low said nozzle and adapted to contain a coremoved in a clean and incombustible state. agulating substance, sai vessel being so 10- These operations are performed Without concated that the filament descends thereinto at tact between the filament and the operators a distance from its center of rotation, and hands. For commercial purposes the filameans intermediate the nozzle and receptament is wound into hanks, skeins, balls or cle aforesaid fortreating the filament with the like, which are dried by suitable means. alcohol vapor. The chemical operations described can either 3. In apparatus for the purpose set forth be effected by transferring the sieve-botthecombination with a discharge nozzle tomed vessel into successive baths, in which through which a filament is passed, of a rotait is placed with suitable care, or by succestable, double, sieve-bottomed receptacle besively introducing the liquids into a single low said nozzle and adapted to contain a co vessel in which the sieve-bottomed receptaagulating substance, said vessel being so 10- cle is placed. cated that the filament descends thereinto What I claim as my at a distance from its center of rotation an to secure by Letters Patent of the open ended chamber intermediate the nozzle States is and receptacle through which the filament 1. In apparatus for the purpose set forth passes, a lining of spongy material in said the combination with a discharge nozzle chamber and means for saturating said through which a filament is passed of a rotaspongy material with alcohol substantially table receptacle below said conduit and as described. adapted to contain a coagulating substance, In witness whereof I have signed this the fillamentl aforesaid desplending into said specification in the presence of two witnesses. vesse at a istance om t e center of rota- T tion thereof and means intermediate the noz- VICTOR PLAL OHON' zle and receptacle for treating the filament I with alcohol vapor.
2. In apparatus for the purpose set forth invention and desire United Witnesses:
THos. N. BROWNE, GASTON YEANNrANs.
US35374907A 1907-01-23 1907-01-23 Apparatus for the manufacture of collodion filaments. Expired - Lifetime US888260A (en)

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US35374907A US888260A (en) 1907-01-23 1907-01-23 Apparatus for the manufacture of collodion filaments.

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US35374907A US888260A (en) 1907-01-23 1907-01-23 Apparatus for the manufacture of collodion filaments.

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425782A (en) * 1944-03-04 1947-08-19 Celanese Corp Preparation of filaments
US2439034A (en) * 1944-03-16 1948-04-06 American Viscose Corp Process of forming porous artificial masses
US3088793A (en) * 1958-12-29 1963-05-07 Monsanto Chemicals Spinning of acrylonitrile polymers
US4724109A (en) * 1983-12-28 1988-02-09 Denki Kagaku Kogyo Kabushiki Kaisha Process for production of continuous inorganic fibers and apparatus therefor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425782A (en) * 1944-03-04 1947-08-19 Celanese Corp Preparation of filaments
US2439034A (en) * 1944-03-16 1948-04-06 American Viscose Corp Process of forming porous artificial masses
US3088793A (en) * 1958-12-29 1963-05-07 Monsanto Chemicals Spinning of acrylonitrile polymers
US4724109A (en) * 1983-12-28 1988-02-09 Denki Kagaku Kogyo Kabushiki Kaisha Process for production of continuous inorganic fibers and apparatus therefor

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