US677012A - Art of manufacturing celluloid. - Google Patents

Art of manufacturing celluloid. Download PDF

Info

Publication number
US677012A
US677012A US73706199A US1899737061A US677012A US 677012 A US677012 A US 677012A US 73706199 A US73706199 A US 73706199A US 1899737061 A US1899737061 A US 1899737061A US 677012 A US677012 A US 677012A
Authority
US
United States
Prior art keywords
mixture
pyroxylin
solvent
celluloid
materials
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
Application number
US73706199A
Inventor
George Hillard Benjamin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US73706199A priority Critical patent/US677012A/en
Application granted granted Critical
Publication of US677012A publication Critical patent/US677012A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals

Definitions

  • My invention relates to the manufacture of celluloid, and has for its object to avoid the possibility of explosion during treatment of the materials and to bring about an intimate mechanical mixture of the materials in the required proportions unaccompanied by an excess of the solvent used, which, according to the processes nowin use, has to be removed by the application of heat and hot and cold rolling before the compound sought to be obtained is ready for commercial use.
  • Celluloid consists of pyroxylin'i. e., tetra or penta nitrated cellulose(sometimes hexa-nitrated cellulose is used. The latter, however, is seldom employed on account of its explosive properties) gum-camphor and a solvent-such, for in; stance, as alcohol, ether, nitrobenzene, &c.
  • the usual process of manufacturing celluloid consists in effecting a mechanical mixture of pyroxylin and camphor,- then introducing a liquid solvent, such as alcohol or other suitable fluid, and subjecting the mixture to pressure and heat, and, if a solid is required,- to hot and cold rolling to remove the excess of alcohol or other solvent employed.
  • a liquid solvent such as alcohol or other suitable fluid
  • This process is both costly and defective, owing to the fact that explosions are liable to occur in effecting the mechanical mixture of the materials and that long-continued heating and expensive rolling and other manipulations are requisite to eliminate the excess of solvent where a solid is to be made and bring about an intimate mixture of the materials to produce a homogeneous compound.
  • liquid solvent may be brought to a solid state, and all solids may, by mechanical means and without danger of explosion, be reduced to a very fine state of division, and, further, that if the various materials are thoroughly mixed in proper proportions while in such intensely cold and divided state they will, upon regaining the temperature of the atmosphere, have combined mechanically or coacted to form a homogeneous compound having the form of asolid or a liquid, depending upon the amount of solvent employed.
  • pyroxylin one part in any one of its forms2'. 6., tetra, penta, or hexa nitrate-and subject it to the action of intensecold. This,lfind,oanbeconveniently done by immersing the pyroxylin in liquid air and allowing it to remain therein for from six to ten minutes. Upon withdrawing the frozen pyroxylin from the mixture it is placed in an ordinary iron mill, the metal of which is preserved at a low temperature through the means of liquid air, and ground to a fine state of division. The second solid material, camphor, (two parts,) is treated in a precisely similar manner.
  • the solvent alcohol, ether, &c. (usually from ten to thirty per cent., by weight, of the combined mass of pyroxylin and camphor and depending upon whether a solid, semisolid, or liquid celluloid is required, although I do not limit myself to these proportions,) is introduced into an open-mouthed glass jar and the jar immersed from fifteen to eighteen minutes in liquid air. The solvent is then ground in a mill, as described for the treatment of the pyroxylin and camphor.
  • I may only freeze and grind the pyroxylin and camphor.
  • the alcohol or other solvent is introduced in its normal state at the temperature of the atmosphere, or where a fluid or sernifluid is required
  • I may only freeze and grind the pyroxylin, in which case the camphor and solvent are mixed together, preferably under the influence of heat, to form a fluid, to which the frozen and comminuted pyroxylin is added in the required proportions and the mixture stirred together.
  • This last-described process requires carein manipulation and that the solution of camphor be quite cold, as otherwise there is liability of explosion.
  • the best results and mixture are obtained by freezing and grinding all of the materials and mixing while such materials are in a frozen state.
  • Any loading or coloring material can be advantageously introduced at the time when the mixture of frozen materials is effected. It is preferable to also chill these materials.
  • claim- 1 The herein-described process of manufacturing celluloid, which consists in reducing the materials to a frozen state, then grinding, and finally mixing.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

UNITED STATES PATENT QEEIQE.
GEORGE HILLARD BENJAMIN, OF NEIV YORK, N. Y.
ART OF MANUFACTURING CELLULOID SPECIFICATION forming part of Letters Patent N o. 677,012, dated June 25, 1901.
Application filed November 15,1899.
To all whom it may concern;
Be it known that I, GEORGE HILLARD BEN- JAMIN, a citizen of the United States, residing at New York city, county and State of New York, have invented certain new and useful Improvements in the Art of Manufacturing Celluloid, of which the following is a specification.
My invention relates to the manufacture of celluloid, and has for its object to avoid the possibility of explosion during treatment of the materials and to bring about an intimate mechanical mixture of the materials in the required proportions unaccompanied by an excess of the solvent used, which, according to the processes nowin use, has to be removed by the application of heat and hot and cold rolling before the compound sought to be obtained is ready for commercial use.
Celluloid,- as is well understood, consists of pyroxylin'i. e., tetra or penta nitrated cellulose(sometimes hexa-nitrated cellulose is used. The latter, however, is seldom employed on account of its explosive properties) gum-camphor and a solvent-such, for in; stance, as alcohol, ether, nitrobenzene, &c.
The usual process of manufacturing celluloid consists in effecting a mechanical mixture of pyroxylin and camphor,- then introducing a liquid solvent, such as alcohol or other suitable fluid, and subjecting the mixture to pressure and heat, and, if a solid is required,- to hot and cold rolling to remove the excess of alcohol or other solvent employed. This process is both costly and defective, owing to the fact that explosions are liable to occur in effecting the mechanical mixture of the materials and that long-continued heating and expensive rolling and other manipulations are requisite to eliminate the excess of solvent where a solid is to be made and bring about an intimate mixture of the materials to produce a homogeneous compound.
In order to overcome the objections stated, I have devised the process which I will now proceed to describe.
I will premise by stating that I have found by experiment that if pyroxylin,camphor,and a suitable solvent-such as alcohol or ether, &c.are subjected for a sufficient time to the action of intense cold--such, for instance as Serial No. 737,061. (No specimens.)
may be applied through the agency of liquid airthe liquid solvent will be brought to a solid state, and all solids may, by mechanical means and without danger of explosion, be reduced to a very fine state of division, and, further, that if the various materials are thoroughly mixed in proper proportions while in such intensely cold and divided state they will, upon regaining the temperature of the atmosphere, have combined mechanically or coacted to form a homogeneous compound having the form of asolid or a liquid, depending upon the amount of solvent employed.
To carry my invention into effect, I take a definite quantity of pyroxylin (one part) in any one of its forms2'. 6., tetra, penta, or hexa nitrate-and subject it to the action of intensecold. This,lfind,oanbeconveniently done by immersing the pyroxylin in liquid air and allowing it to remain therein for from six to ten minutes. Upon withdrawing the frozen pyroxylin from the mixture it is placed in an ordinary iron mill, the metal of which is preserved at a low temperature through the means of liquid air, and ground to a fine state of division. The second solid material, camphor, (two parts,) is treated in a precisely similar manner. The solvent alcohol, ether, &c., (usually from ten to thirty per cent., by weight, of the combined mass of pyroxylin and camphor and depending upon whether a solid, semisolid, or liquid celluloid is required, although I do not limit myself to these proportions,) is introduced into an open-mouthed glass jar and the jar immersed from fifteen to eighteen minutes in liquid air. The solvent is then ground in a mill, as described for the treatment of the pyroxylin and camphor. All of the ground materials while in an intensely-cold condition are then thoroughly mixed (almost perfect mixture can thus be obtained) and set aside in a suitable vessel, preferably of stoneware, to acquire heat, or, if it is desired to hasten the process, gentle heat may be applied to the mixture by means of a water-bath. When the mixture has acquired the temperature of the atmosphere, it will be found that the various materials have combined mechanically or coacted to form a homogeneous mixture of the required physical condition.
Instead of freezing and grinding all of the ingredients I may only freeze and grind the pyroxylin and camphor. In such case the alcohol or other solvent is introduced in its normal state at the temperature of the atmosphere, or where a fluid or sernifluid is required I may only freeze and grind the pyroxylin, in which case the camphor and solvent are mixed together, preferably under the influence of heat, to form a fluid, to which the frozen and comminuted pyroxylin is added in the required proportions and the mixture stirred together. This last-described process, however, requires carein manipulation and that the solution of camphor be quite cold, as otherwise there is liability of explosion. The best results and mixture, however, are obtained by freezing and grinding all of the materials and mixing while such materials are in a frozen state.
Any loading or coloring material can be advantageously introduced at the time when the mixture of frozen materials is effected. It is preferable to also chill these materials.
Having thus described my invention, I
claim- 1. The herein-described process of manufacturing celluloid, which consists in reducing the materials to a frozen state, then grinding, and finally mixing.
2. The herein-described process of manufacturing celluloid, which consists in reducing the pyroxylin and camphor to a frozen state, then grinding, then adding the liquid solvent.
3. The herein-described process of manufacturing celluloid, which consists in first freezing the pyroxylin andcamphor, then grinding and intimately mixing these two bodies, then introducing the liquid solvent into the mixture, and finally increasing the temperature of the mixture.
In testimony whereof I affix my signature in the presence of two witnesses.
GEORGE HILLARD. BENJAMIN.
\Vitnesses:
J. E. PEARSON, ARTHUR O. BLA'r'z.
US73706199A 1899-11-15 1899-11-15 Art of manufacturing celluloid. Expired - Lifetime US677012A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US73706199A US677012A (en) 1899-11-15 1899-11-15 Art of manufacturing celluloid.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US73706199A US677012A (en) 1899-11-15 1899-11-15 Art of manufacturing celluloid.

Publications (1)

Publication Number Publication Date
US677012A true US677012A (en) 1901-06-25

Family

ID=2745559

Family Applications (1)

Application Number Title Priority Date Filing Date
US73706199A Expired - Lifetime US677012A (en) 1899-11-15 1899-11-15 Art of manufacturing celluloid.

Country Status (1)

Country Link
US (1) US677012A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2665850A (en) * 1950-07-25 1954-01-12 Sol B Wiczer Comminuted product and method of grinding

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2665850A (en) * 1950-07-25 1954-01-12 Sol B Wiczer Comminuted product and method of grinding

Similar Documents

Publication Publication Date Title
US677012A (en) Art of manufacturing celluloid.
US2384730A (en) Method of preparing cast explosive charges
US1204709A (en) Coating process.
US2006184A (en) Treatment of rubber
US1139470A (en) Process for coating porous substances.
US652455A (en) Process of making smokeless powder.
SU94258A1 (en) The way to protect metal surfaces from corrosion
US520600A (en) Acid-proof composition
Hailes The thermal decomposition of lead styphnate
US496752A (en) Otto schweissinger
US1631113A (en) Bond for elastic grinding wheels and method of applying the same
US673377A (en) Colloid explosive and process of making the same.
US341239A (en) Fining composition
US601091A (en) Process of devulcanizing rubber
US2031659A (en) Process for making smokeless powder
US617434A (en) Adolph brougier
US2990389A (en) Superior polyethylene emulsions
US317389A (en) Charles s
US280483A (en) adams
US1990460A (en) Manufacture of sponge rubber from latex or rubber solutions
US1335757A (en) Rust-preventing composition
US1913776A (en) Bleaching of flour
US1219286A (en) Food product and method of manufacturing and preparing the same.
US1330444A (en) Process of manufacturing electric insulating molded articles
US701429A (en) Process of hardening copper.