US2176903A - Manufacture of nonfibrous film - Google Patents

Manufacture of nonfibrous film Download PDF

Info

Publication number
US2176903A
US2176903A US107054A US10705436A US2176903A US 2176903 A US2176903 A US 2176903A US 107054 A US107054 A US 107054A US 10705436 A US10705436 A US 10705436A US 2176903 A US2176903 A US 2176903A
Authority
US
United States
Prior art keywords
film
casting
amine
stearylamine
solution
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
US107054A
Inventor
Emmette F Izard
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US107054A priority Critical patent/US2176903A/en
Application granted granted Critical
Publication of US2176903A publication Critical patent/US2176903A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties

Definitions

  • This invention relates to the production of nonfibrous film, such as by casting a film-forming solution onto a surface, forexample, a metal casting wheel. More particularly, it relates to the production of such film. by dry or evaporative methods. 1 e
  • a suitable solution of a film-former is spread or flowed upon a casting surface and the solvents removed therefrom by evaporation.
  • One of the most commonly employed methods is to .dissolve a sufficient amount'of film-former in appropriate solvents to secure a solution or dope of the proper composition and viscosity and to feed this dope from a hopper, regulated to give the desired thickness, upon the surface of a slowly rotating casting wheel.
  • the dope flows out upon the surface of the wheel as the latter rotates a current of air or other suitable evaporative medium is brought in contact with the film thus formed to evaporate the solvent therefrom.
  • the film Before the wheel has rotated through a complete revolution most of the solvents have evaporated "and the film is sufficiently self-sustaining to be stripped from the surface of the wheel and to be subjected to a curing treatment to further reduce its residual solvent content and to bring its shrinkage characteristics within the desired range.
  • the cured film is finally wound on a mandrel to form a mill roll of suitable size.
  • strip chattering is a termemployed to denote a type of film defect distinguished by 5 characteristic transverse markings or lines appearing at regularly or irregularly spaced intervals along the length of the film. Strip chattering naturally detracts from the appearance of the film and renders it undesirable as a first 10 quality product. Strip chattering is apparently caused in a great many cases by the film being stripped from the casting surface in a jerky or spasmodic manner due to the above mentioned strong adhesive power of the film for the cast- 15 ing surface.
  • Another object is to improve the stripping quality of the film to the extent that strip chattering defects are substantially eliminated.
  • a further object of the invention is to improve the stripping characteristics of films with- 25 out substantially impairing the transparency, gloss and clarity thereof.
  • Example I Twenty-five grams of octadecyl amine (commonly called stearylamine) are thoroughly and uniformly incorporated into a casting dope of 40 the following composition:
  • the hopper may be provided with an extrustion orifice in the shape of an elongated slit of adjustable width, serving to deposit a predetermined 5 amount of casting composition on the surface of the wheel, which is caused to rotate at a peripheral speed commensurate to the linear extrusion speed. In either case, the wheel surface is maintained at a temperature of about 32 to 35 C.
  • the smooth uniform layer of casting composition emerges from the casting chamber into a drying chamber which encloses the casting wheel.
  • Air passing through the drying chamber at a temperature of about 70--80 C. or higher removes the solvents from the composition so that after approximately fourfifths of a revolution of the wheel, a film is secured which is fairly well set.
  • the cellulose acetate film containing approximately 1.72.0% by weight of stearylamine, is stripped with considerable ease from the wheel surface and is carried over suitable rolls to a conditioning chamber through which air is passed at a suitably elevated temperature and relative humidity to effect substantially complete removal of any residual solvent.
  • the illm' is led from the conditioning chamber over one or more rolls and wound on a suitable core or mandrel. Optionally, it may be cut off at predetermined intervals to produce a cut-to-size" sheeted stock.
  • Example II One kg. of polymerized vinyl acetate inthe form of a colorless resin is introduced into a container provided with an agitation system. To this is added one liter of water, 200 grams of ethyl alcohol, and 2 kg. of hydrochloric acid of 22-23" Baum. The mixture is permitted to set for a period of approximately 5 hours, at the end of which time the mass becomes thoroughly homogeneous. Five hundred grams of paraldehyde are then added and the thickened mass is rendered homogeneous by agitation. The mass is again permitted to set for approximately 5 hours, after which the polyvinyl acetal condensation product is precipitated by the gradual addition of water. The precipitated product is washed in the cold and dried in the open air at low temperature. The product may be bleached if necessary and is soluble in the usual solvents, particularly alcohol, methyl acetate and chloroform.
  • the thoroughly mixed solution is converted into film by a procedure analogous to that of Example I, except the casting surface is maintained at a temperature of about 40 to 60 C.
  • the resulting film contains approximately 0.3 to 0.4% by weight of stearylamine and strips readily from the casting surface.
  • Example III Six hundred grams of potassium hydroxide are dissolved in 500 grams of ethyl alcohol in a vessel equipped. with a stirrer. To this solution are added, with thorough agitation, 800 grams of ground polymerized vinyl acetate prepared by polymerizing vinyl acetate with the aid of benzoyl peroxide. After agitating about hour, the polyvinyl acetate saponifies and precipitates as polyvinyl alcohol, which is separated on a filter, washed with ethyl alcohol, and dried. TWO thousand grams of polyvinyl alcohol, prepared in the above manner, and 13 grams of stearylamine acetate are added to a composition consisting of 8,000
  • the solution is converted into film by a method comparable to that of Example I, except that the casting surface is maintained at a temperature of to C. while the air passing through the drying chamber is kept at a temperature of approximately 200 C.
  • the resulting film contains approximately 0.40.5% by weight of stearylamine acetate, and strips without difliculty from the casting surface.
  • the presence of stearylamine acetate also facilitates wetting of the casting surface by the aqueous film-former and thereby enhances the ease of securing a thin film of uniform gage.
  • the films have been formed by what is commonly known as a wheel casting method.
  • a continuous band casting method can be used if appropriate consideration is given to the required casting conditions and similarly, a discontinuous plate casting method can be utilized advantageously for certain purposes.
  • polyvinyl acetal compounds and cellulose acetate have been cited as typical examples of the incorporation of a waxy amine in a film-forming dope, wherein a volatile, organic liquid is employed as the solvent. It will, however, be recognized by those skilled in the art that the process is broadly applicable to the dry casting of any film-former dissolved 4 in a volatile, organic solvent wherein it is desired to facilitate the stripping operation by the incorporation of a waxy amine that does not react detrimentally with the film-former and is soluble in the solvent or mixture of solvents employed.
  • the process may be applied in casting'cellulose propionate, cellulose aceto-propionate, cellulose a'ceto-butyrate, cellulose aceto-stearate, cellulose crotonate, or other simple and mixed cellulose esters; also in casting ethyl, butyl, benzyl, or other cellulose ethers, and in casting resinous films, such as ether resins, polymerized vinyl compounds, interpolymerized vinyl chloride-vi "v1 acetate compounds, and polymerized acrylat nd/or methacrylate compounds.
  • the condit. is of casting and conditioning the film will, of course, be suitably regulated and adjusted to meet the needs of the individual case.
  • the stearylamine may be incorporated in a chloroform solution of cellulose acetate having a'combined acetic acid contentof 62.5% or in an acetone solution of cellulose acetate having a combined acetic acid content of 54% or less, with equal advantage.
  • stearylamine may be utilized in the case of any polyvinyl acetaf condensation product that is soluble in an organic solvent.
  • the polyvinyl acetal film-former may be one obtained by the reaction of other aldehydes, such as formaldehyde, propionaldehyde, butaldehyde, or benzaldehyde with a partially or completely hydrolyzed 4 ride.
  • aldehydes such as formaldehyde, propionaldehyde, butaldehyde, or benzaldehyde with a partially or completely hydrolyzed 4 ride.
  • polyvinyl alcohol has been given as a.
  • the w xy amine derivative will produce comparably good results'when incorporated into aqueous lutions of gelatin, casein, lowly etherified me hyl cellulose, or other lowly etherified or esterified cellulose derivatives such as cellulose acetophthalate, cellulose acetotartrate, or other water-soluble film-formers.
  • the conditions of casting and conditioning the film are of course suitably regulated to fit the peculiarities of the given film-former.
  • stearylamine is employed as the free base.
  • the stearylamine is conveniently employed in the form of a water-soluble salt derivative, such as the acetate, lactate, or hydrochlo- It is thought probable that the stearylamine salt decomposes partially or completely to stearylamine during the casting and/or conditioning of the water-soluble film.
  • the amount of stearylamine or derivative thereof necessary for good stripping varies according to the particular nature of the filmformer to be cast and the particular casting conditions to be followed. In the preferred embodiment. of the invention, only a relatively small amount of a waxy amine or salt thereof is employed. Large amounts will unduly increase the cost of the product, will tend to cause haze or opacity when the film-forming material is not completely compatible with the waxy amine, may impart odor and taste to the film, and may cause the film to strip from the support in advance of the time desired. In general, amounts less than based on the weight of the film are desired.
  • an amount of stearylamine corresponding to 1.5-3.0% by weight of the film is preferably incorporated in the casting dope, but quantities of 4% or more of stearylamine may be added, if desired.
  • an amount of stearylamine corresponding to 0.25-0.50% by weight of the film is preferably incorporated in the casting dope, but quantities of 1% or more may be added, if desired.
  • an amount of stearylamine corresponding to 0.25-0.50% by weight'of the film is preferably incorporated in the casting dope, but quantities of 1% or more may be added, depending on the ease of stripping desired.
  • waxy amines and salts thereof may be used as strip agents with satisfactory results.
  • cetyl amine and lauryl amine (dodecyl amine) and their'water-soluble salts may be substituted.
  • any waxy amine, particularly aliphatic amines may be used satisfactorily as a strip agent provided its molecular weight is not so high that the amine is insoluble in the casting dope, nor so low that the amine is not solid at ordinary temperatures (25 0.).
  • the film-forming dopes in addition to stearylamine or its salts may have also present other modifying agents such as plasticizers, pigments and dyes.
  • the dyes may be selected either for the puropse of coloring the films or for the purpose of improving the transparency of the films by neutralization of any coloration that may be present.
  • suitable deodorizing substances may be'added to mask any undesirable odor that may be present.
  • polyvinyl 5 alcohol water soluble dimethylolurea or urea formaldehyde in an amount of 15 to 20% by weight of the finished film may be incorporated in the film-former, with beneficial results.
  • the waxy amine or salt thereof may be applied directly to the casting surface, such as by means of a brush or other spreading device. Care must be taken, however, that uniform distribution in the proper quantity is secured and that proper precautions be taken to replenish the supply of strip agent as it is removed from the support.
  • a solution comprising polyvinyl alcohol, water and a salt of octodecyl amine.
  • a solution comprising a polyvinyl alcohol, water, and octodecyl amine acetate.
  • a solution comprising essentially 2,000 parts polyvinyl alcohol, 8,000 parts water, 260 parts glycerin, 3 parts acetic acid and 13 parts octodecyl amine acetate.
  • a solution comprising cellulose acetate, an organic solvent and octodecyl amine.
  • a solution comprising essentially 1,000 parts cellulose acetate, 3,750 parts acetone, 250 parts dibutyl phi-halate, '75 parts water and 25 parts octodecyl amine.
  • a solution comprising polyvinyl acetal, an organic solvent, and octodecyl amine.
  • a solution comprising essentially 1785 parts polyvinyl acetal, 9000 parts organic solvent therefor consisting of methylene chloride, benzene and methyl alcohol, 200 parts dibutyl phthalate, and 9 parts octodecyl amine.
  • a solution capable of being dry-cast to form a solid self-sustaining film said solution containing a substance taken from the class consisting of normally solid primary alkyl amines of high molecular weight hydrocarbons and salts thereof, said substance being soluble in said solution, said substance being present in sufficient quantity to improve the stripping characteristics of the film, but in insufiicient quantity to materially affect the transparency of the resultant film.
  • An aqueous solution capable of being dry- 75 cast to form a solid self-sustaining film said solution containing a water-soluble salt 01. a nor-- mally solid primary alkyl amine ot a high molecular weight hydrocarbon, said salt being present in suificient quantity to improve the stripping characteristics of the film, but in insufiicient quantity to materially afi'ect the transparency 11
  • An organic solvent solution capable of being dry-cast to form a solid se1i'-sustaining film, said solution containing a normally solid primary alkyl amine of a high molecular weight hydro-' carbon, said amine being soluble in saidsolvent, said amine being present in sufiicient quantity to improve the stripping characteristics of the film, but in insuflicient quantity to materially aflect the transparency oi the resultant film;

Description

Patented Oct. 24, 1939 PATENT OFFICE 2,176,903 I MANUFACTURED! NONFIBROUS FILM- I i'nmmttfi' F- 113111, Kenmore, N. Y., assignor to j H E. '1. du' Pont de Nemours & Company, Wilmington, Del., a corporation of Delaware Nol Drawing.
Application October 22,1936, Serial No. 107.05;
12 Claims. (Cl. 260-32) This invention relates to the production of nonfibrous film, such as by casting a film-forming solution onto a surface, forexample, a metal casting wheel. More particularly, it relates to the production of such film. by dry or evaporative methods. 1 e
In the dry method ofcasting film, a suitable solution of a film-former is spread or flowed upon a casting surface and the solvents removed therefrom by evaporation. One of the most commonly employed methods is to .dissolve a sufficient amount'of film-former in appropriate solvents to secure a solution or dope of the proper composition and viscosity and to feed this dope from a hopper, regulated to give the desired thickness, upon the surface of a slowly rotating casting wheel. The dope flows out upon the surface of the wheel as the latter rotates a current of air or other suitable evaporative medium is brought in contact with the film thus formed to evaporate the solvent therefrom. Before the wheel has rotated through a complete revolution most of the solvents have evaporated "and the film is sufficiently self-sustaining to be stripped from the surface of the wheel and to be subjected to a curing treatment to further reduce its residual solvent content and to bring its shrinkage characteristics within the desired range. The cured film is finally wound on a mandrel to form a mill roll of suitable size.
In dry casting, however, depending upon the character of the particular film-former and upon the nature of the given casting surface, a film is formed which adheres relatively tenaciously to the casting surface. In commercial casting, this adherence or cohesion of the film to the casting surface, which is particularly tenacious in the case of certain film-formers, has been the source of a number of direct and indirect difficulties. Thus, this cohesion makes it somewhat difiicult to strip the films from the casting surface and often necessitates the exertion of a strong pull which produces an excessive strain on the films to such an extent that sometimes thin films tear and interrupt the casting operation. In the case of thick film or relatively thick plastic sheets, the resistance to stripping exerts a stretching action which produces undesirable irregularities in the thickness of the film. Again, the tenacious adherence in certain cases has a tendency to tear off minute particles of metal from the casting surface which eventually results in the formation of irregularities on the castingsurface with corresponding imperfections in the films cast thereon, However, of all the difficulties caused bythe adhesive tendency of'the film towards the casting surface, strip chattering is probably the most important and of the most concern. "Strip chattering is a termemployed to denote a type of film defect distinguished by 5 characteristic transverse markings or lines appearing at regularly or irregularly spaced intervals along the length of the film. Strip chattering naturally detracts from the appearance of the film and renders it undesirable as a first 10 quality product. Strip chattering is apparently caused in a great many cases by the film being stripped from the casting surface in a jerky or spasmodic manner due to the above mentioned strong adhesive power of the film for the cast- 15 ing surface.
It is therefore an object of the present invention to secure films which may be stripped from a casting surface without marring the films or said casting surface.
Another object is to improve the stripping quality of the film to the extent that strip chattering defects are substantially eliminated.
A further object of the invention is to improve the stripping characteristics of films with- 25 out substantially impairing the transparency, gloss and clarity thereof.
Other objects are disclosed hereinafter.
These objects are accomplished by incorporating into a film-forming dope a suitable amount 30 of a waxy amine or salt thereof.
To facilitate clear understanding of the invention a few examples will now be given, but it is to be understood that they are illustrative only and are not to be considered limitative.
Example I Twenty-five grams of octadecyl amine (commonly called stearylamine) are thoroughly and uniformly incorporated into a casting dope of 40 the following composition:
Grams Cellulose acetate 1,000 Dibutyl phfhalafP 250 Acetone 3,750 45 Water '15 one of the edges of the hopper. Alternatively, the hopper may be provided with an extrustion orifice in the shape of an elongated slit of adjustable width, serving to deposit a predetermined 5 amount of casting composition on the surface of the wheel, which is caused to rotate at a peripheral speed commensurate to the linear extrusion speed. In either case, the wheel surface is maintained at a temperature of about 32 to 35 C.
As the wheel revolves, the smooth uniform layer of casting composition emerges from the casting chamber into a drying chamber which encloses the casting wheel. Air passing through the drying chamber, at a temperature of about 70--80 C. or higher removes the solvents from the composition so that after approximately fourfifths of a revolution of the wheel, a film is secured which is fairly well set. The cellulose acetate film, containing approximately 1.72.0% by weight of stearylamine, is stripped with considerable ease from the wheel surface and is carried over suitable rolls to a conditioning chamber through which air is passed at a suitably elevated temperature and relative humidity to effect substantially complete removal of any residual solvent. The illm' is led from the conditioning chamber over one or more rolls and wound on a suitable core or mandrel. Optionally, it may be cut off at predetermined intervals to produce a cut-to-size" sheeted stock.
Example II One kg. of polymerized vinyl acetate inthe form of a colorless resin is introduced into a container provided with an agitation system. To this is added one liter of water, 200 grams of ethyl alcohol, and 2 kg. of hydrochloric acid of 22-23" Baum. The mixture is permitted to set for a period of approximately 5 hours, at the end of which time the mass becomes thoroughly homogeneous. Five hundred grams of paraldehyde are then added and the thickened mass is rendered homogeneous by agitation. The mass is again permitted to set for approximately 5 hours, after which the polyvinyl acetal condensation product is precipitated by the gradual addition of water. The precipitated product is washed in the cold and dried in the open air at low temperature. The product may be bleached if necessary and is soluble in the usual solvents, particularly alcohol, methyl acetate and chloroform.
Seventeen hundred eighty-five grams of a polyvinyl acetal condensation product, prepared as above, are thoroughly agitated with 9 grams of stearylamine, 200 grams of dibutyl phthalate, and
9,000 grams of a solvent mixture consisting of methylene chloride, benzene and methyl alcohol.
The thoroughly mixed solution is converted into film by a procedure analogous to that of Example I, except the casting surface is maintained at a temperature of about 40 to 60 C. The resulting film contains approximately 0.3 to 0.4% by weight of stearylamine and strips readily from the casting surface.
Example III Six hundred grams of potassium hydroxide are dissolved in 500 grams of ethyl alcohol in a vessel equipped. with a stirrer. To this solution are added, with thorough agitation, 800 grams of ground polymerized vinyl acetate prepared by polymerizing vinyl acetate with the aid of benzoyl peroxide. After agitating about hour, the polyvinyl acetate saponifies and precipitates as polyvinyl alcohol, which is separated on a filter, washed with ethyl alcohol, and dried. TWO thousand grams of polyvinyl alcohol, prepared in the above manner, and 13 grams of stearylamine acetate are added to a composition consisting of 8,000
grams of water, 260 grams of glycerin and 3 grams of acetic acid. The mixture is heated to a temperature of 90-97 C. and while at that temperature, is thoroughly agitated for a period of 3 hours. The solution is filtered and delivered by means of a metering pump to a casting hopper which is maintained at a suitable temperature.
The solution is converted into film by a method comparable to that of Example I, except that the casting surface is maintained at a temperature of to C. while the air passing through the drying chamber is kept at a temperature of approximately 200 C. The resulting film contains approximately 0.40.5% by weight of stearylamine acetate, and strips without difliculty from the casting surface. The presence of stearylamine acetate also facilitates wetting of the casting surface by the aqueous film-former and thereby enhances the ease of securing a thin film of uniform gage.
In the above examples, the films have been formed by what is commonly known as a wheel casting method. A continuous band casting method can be used if appropriate consideration is given to the required casting conditions and similarly, a discontinuous plate casting method can be utilized advantageously for certain purposes.
In the above examples, polyvinyl acetal compounds and cellulose acetate have been cited as typical examples of the incorporation of a waxy amine in a film-forming dope, wherein a volatile, organic liquid is employed as the solvent. It will, however, be recognized by those skilled in the art that the process is broadly applicable to the dry casting of any film-former dissolved 4 in a volatile, organic solvent wherein it is desired to facilitate the stripping operation by the incorporation of a waxy amine that does not react detrimentally with the film-former and is soluble in the solvent or mixture of solvents employed. Thus, the process may be applied in casting'cellulose propionate, cellulose aceto-propionate, cellulose a'ceto-butyrate, cellulose aceto-stearate, cellulose crotonate, or other simple and mixed cellulose esters; also in casting ethyl, butyl, benzyl, or other cellulose ethers, and in casting resinous films, such as ether resins, polymerized vinyl compounds, interpolymerized vinyl chloride-vi "v1 acetate compounds, and polymerized acrylat nd/or methacrylate compounds. The condit. is of casting and conditioning the film will, of course, be suitably regulated and adjusted to meet the needs of the individual case.
Furthermore, in the case of cellulose acetate, it is immaterial whether the combined acetic vicid content of the ester is relatively high or relatively low as long as the ester is soluble in organic solvents. Thus, the stearylamine may be incorporated in a chloroform solution of cellulose acetate having a'combined acetic acid contentof 62.5% or in an acetone solution of cellulose acetate having a combined acetic acid content of 54% or less, with equal advantage. Likewise, stearylamine may be utilized in the case of any polyvinyl acetaf condensation product that is soluble in an organic solvent. Thus, the polyvinyl acetal film-former may be one obtained by the reaction of other aldehydes, such as formaldehyde, propionaldehyde, butaldehyde, or benzaldehyde with a partially or completely hydrolyzed 4 ride.
polyvinyl acetate ester as exemplified in Patents Nos. 2,036,092 and 2,035,939.
In the above examples, polyvinyl alcohol has been given as a. typical application of the incorporation of a stearylamine derivative in a film-forming dope wherein the solvent is water or aqueous in nature. The w xy amine derivative will produce comparably good results'when incorporated into aqueous lutions of gelatin, casein, lowly etherified me hyl cellulose, or other lowly etherified or esterified cellulose derivatives such as cellulose acetophthalate, cellulose acetotartrate, or other water-soluble film-formers. The conditions of casting and conditioning the film are of course suitably regulated to fit the peculiarities of the given film-former.
In the case of film-formers dissolved in organic solvents, it will be noted that stearylamine is employed as the free base. -In the case of film-formers dissolved in aqueous media, on the other hand, the stearylamine is conveniently employed in the form of a water-soluble salt derivative, such as the acetate, lactate, or hydrochlo- It is thought probable that the stearylamine salt decomposes partially or completely to stearylamine during the casting and/or conditioning of the water-soluble film.
The amount of stearylamine or derivative thereof necessary for good stripping varies according to the particular nature of the filmformer to be cast and the particular casting conditions to be followed. In the preferred embodiment. of the invention, only a relatively small amount of a waxy amine or salt thereof is employed. Large amounts will unduly increase the cost of the product, will tend to cause haze or opacity when the film-forming material is not completely compatible with the waxy amine, may impart odor and taste to the film, and may cause the film to strip from the support in advance of the time desired. In general, amounts less than based on the weight of the film are desired. In the case of cellulose acetate, an amount of stearylamine corresponding to 1.5-3.0% by weight of the film is preferably incorporated in the casting dope, but quantities of 4% or more of stearylamine may be added, if desired. In the polyvinyl acetal type of filmformer, an amount of stearylamine corresponding to 0.25-0.50% by weight of the film is preferably incorporated in the casting dope, but quantities of 1% or more may be added, if desired. In the case of polyvinyl alcohol, an amount of stearylamine corresponding to 0.25-0.50% by weight'of the film is preferably incorporated in the casting dope, but quantities of 1% or more may be added, depending on the ease of stripping desired.
While stearylamine (octadecyl amine) or its salts are preferred, other waxy amines and salts thereof may be used as strip agents with satisfactory results. Thus, cetyl amine and lauryl amine (dodecyl amine) and their'water-soluble salts may be substituted. Generally speaking, depending of course upon the nature of the particular film-former, any waxy amine, particularly aliphatic amines, may be used satisfactorily as a strip agent provided its molecular weight is not so high that the amine is insoluble in the casting dope, nor so low that the amine is not solid at ordinary temperatures (25 0.).
The film-forming dopes in addition to stearylamine or its salts may have also present other modifying agents such as plasticizers, pigments and dyes. The dyes may be selected either for the puropse of coloring the films or for the purpose of improving the transparency of the films by neutralization of any coloration that may be present. In certain cases, suitable deodorizing substances may be'added to mask any undesirable odor that may be present. With polyvinyl 5 alcohol, water soluble dimethylolurea or urea formaldehyde in an amount of 15 to 20% by weight of the finished film may be incorporated in the film-former, with beneficial results.
The advantages of the invention are obviously many. The fact that the film strips easily and readilyfrom the casting surface means that the highly undesirable strip chattering defects are substantially eliminated. 'In the dry casting of thick film at relatively high rates of speed, the film peels so readily from the casting surface that substantially no undesirable stretching occurs, even though the film retains considerable solvent and is plastic. Film, and particularly thick film, can be cast at higher rates of speed. Another distinct advantage of the invention is that waxy amines are soluble in most organic solvents customarily used to dissolve film-forming compositions. Likewise, waxy amine salts are soluble in water, and can therefore be used as strip agents for film cast from aqueous solution. Furthermore, these waxy amines and salts thereof do not interfere with the good transparency, gloss and clarity of the film, which are essential requirements for a commercial article.
Under certain conditions, the waxy amine or salt thereof may be applied directly to the casting surface, such as by means of a brush or other spreading device. Care must be taken, however, that uniform distribution in the proper quantity is secured and that proper precautions be taken to replenish the supply of strip agent as it is removed from the support.
Any other variation or modification of the invention as described, which conforms to the spirit of the invention, is intended to be included within the scope of the claims.
I claim:
1. A solution comprising polyvinyl alcohol, water and a salt of octodecyl amine.
2. A solution comprising a polyvinyl alcohol, water, and octodecyl amine acetate.
3. A solution comprising essentially 2,000 parts polyvinyl alcohol, 8,000 parts water, 260 parts glycerin, 3 parts acetic acid and 13 parts octodecyl amine acetate.
4. A solution comprising cellulose acetate, an organic solvent and octodecyl amine.
5. A solution comprising essentially 1,000 parts cellulose acetate, 3,750 parts acetone, 250 parts dibutyl phi-halate, '75 parts water and 25 parts octodecyl amine.
6. A solution comprising polyvinyl acetal, an organic solvent, and octodecyl amine.
7. A solution comprising essentially 1785 parts polyvinyl acetal, 9000 parts organic solvent therefor consisting of methylene chloride, benzene and methyl alcohol, 200 parts dibutyl phthalate, and 9 parts octodecyl amine.
8. A solution capable of being dry-cast to form a solid self-sustaining film, said solution containing a substance taken from the class consisting of normally solid primary alkyl amines of high molecular weight hydrocarbons and salts thereof, said substance being soluble in said solution, said substance being present in sufficient quantity to improve the stripping characteristics of the film, but in insufiicient quantity to materially affect the transparency of the resultant film.
9. An aqueous solution capable of being dry- 75 cast to form a solid self-sustaining film, said solution containing a water-soluble salt 01. a nor-- mally solid primary alkyl amine ot a high molecular weight hydrocarbon, said salt being present in suificient quantity to improve the stripping characteristics of the film, but in insufiicient quantity to materially afi'ect the transparency 11 An organic solvent solution capable oi being dry-cast to form a solid self-sustaining film,
said solution containing octodecyl amine, said amine being soluble in said solvent, said amine being present in suificient quantity to improve the stripping characteristics of the film, but in insumcient quantity to materially airect the transparency of the resultant film.
12. An organic solvent solution capable of being dry-cast to form a solid se1i'-sustaining film, said solution containing a normally solid primary alkyl amine of a high molecular weight hydro-' carbon, said amine being soluble in saidsolvent, said amine being present in sufiicient quantity to improve the stripping characteristics of the film, but in insuflicient quantity to materially aflect the transparency oi the resultant film;
EMME'I'IE F. IZARD.
US107054A 1936-10-22 1936-10-22 Manufacture of nonfibrous film Expired - Lifetime US2176903A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US107054A US2176903A (en) 1936-10-22 1936-10-22 Manufacture of nonfibrous film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US107054A US2176903A (en) 1936-10-22 1936-10-22 Manufacture of nonfibrous film

Publications (1)

Publication Number Publication Date
US2176903A true US2176903A (en) 1939-10-24

Family

ID=22314596

Family Applications (1)

Application Number Title Priority Date Filing Date
US107054A Expired - Lifetime US2176903A (en) 1936-10-22 1936-10-22 Manufacture of nonfibrous film

Country Status (1)

Country Link
US (1) US2176903A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2423761A (en) * 1943-07-09 1947-07-08 Standard Oil Dev Co Coating composition comprising polybutene, an organic solvent and an amine acetate wetting agent
US2491642A (en) * 1944-09-02 1949-12-20 Du Pont Polyvinyl alcohol casting solution
US2749312A (en) * 1952-05-23 1956-06-05 Exxon Research Engineering Co Modified polymeric pour point depressants

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2423761A (en) * 1943-07-09 1947-07-08 Standard Oil Dev Co Coating composition comprising polybutene, an organic solvent and an amine acetate wetting agent
US2491642A (en) * 1944-09-02 1949-12-20 Du Pont Polyvinyl alcohol casting solution
US2749312A (en) * 1952-05-23 1956-06-05 Exxon Research Engineering Co Modified polymeric pour point depressants

Similar Documents

Publication Publication Date Title
US2239718A (en) Composition of matter and pellicles of polyvinyl alcohol
US2607704A (en) Cellulose acetate solution and a film formed therefrom
US2419281A (en) Polyvinyl alcohol film
US2319052A (en) High speed method of making cellulose organic derivative film and sheeting
DE728445C (en) Overlay on photographic elements and method of manufacture
US2201747A (en) Method of producing moistureproof cellulosic pellicles
US2271468A (en) Water soluble polyvinyl alcohol softened with beta-hydroxy-alkyl ammounium salt
US2176903A (en) Manufacture of nonfibrous film
US2316274A (en) Coating and production of coated structures
US2327765A (en) Manufacture of vinyl resin film and sheeting
US2379236A (en) Plasticization of plastics
US2306790A (en) Film
US2119702A (en) Film manufacture
US2235516A (en) Plastic sheet material and process for making the same
US2476976A (en) Plasticized cellulose derivative
US2276305A (en) Film
US2119727A (en) Manufacture of resin films
US2284100A (en) Nonfibrous films
US2459927A (en) Process of manufacturing regenerated cellulose sheet material
DE1055949B (en) Process for the pretreatment of film bases for the application of hydrophilic colloid layers
DE1035472B (en) Process for the production of antihalation layers
US2409986A (en) Coating compositions for moistureproofing by hot melt coating
US2099341A (en) Colored cellulose ester sheeting
US2950504A (en) Process for molding hard polyvinyl chloride
US2419277A (en) Process for the production of polyamide compositions