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US2156929A - Zein filaments - Google Patents

Zein filaments Download PDF

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Publication number
US2156929A
US2156929A US38977A US3897735A US2156929A US 2156929 A US2156929 A US 2156929A US 38977 A US38977 A US 38977A US 3897735 A US3897735 A US 3897735A US 2156929 A US2156929 A US 2156929A
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Prior art keywords
zein
solutions
filaments
filament
employed
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Expired - Lifetime
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US38977A
Inventor
Lloyd C Swallen
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Corn Products Refining Co
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Corn Products Refining Co
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Priority to US38977A priority Critical patent/US2156929A/en
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    • 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
    • D01F4/00Monocomponent artificial filaments or the like of proteins; Manufacture thereof

Definitions

  • My invention relates to the production of protein filaments suitable for use in the manufacture of fabrics and the like. More specifically, my inventionrelates to the production of artificial protein fibres having improved strength and water-resistance. 1
  • One embodiment of my invention comprises the use of solutions of zein in organic solvents containing free formaldehyde or other reactive aldehyde.
  • solutions of zein are described in copending application Ser. No. 41,776, filed Sept. 23, 1935.
  • the zein solutions may be prepared simply by adding the desired amount of formaldehyde or other aldehyde to a solution of zein in aqueous ethyl alcohol or a similar solvent such as methyl alcohol, carbitol (di-ethylene glycol), cellosolve are (mono-ethylv ether of ethylene glycol), diacetone alcohol or the like.
  • the zein concentration of the solution may be adjusted to any suitable value for extrusion, depending upon the size'and nature of the orifice, the pressure to be employed, etc. of free formaldehyde, based on the weight of the zein, is usually required to give satisfactory strength and water-resistance to the product. Larger amounts, for example up to 50% by weight, can usually be satisfactorily employed, but I prefer, generally, to use from 2-5% by weight. J
  • plasticizer in order to obtain the desired degree of flexibility and resilience in the product.
  • Any suitable plasticizer for zein such as dibutyl tartrate, monobutyl phthalate, or ptoluene methyl sulfonamide, may be used.
  • Suitable zein solutions containing plasticizers are disclosed in copending application Ser. No. 38,976, filed Sept. 3, 1935. Such solutions may be prepared by any satisfactory procedure such as simply incorporating the desired amount of plasticizer into the solutions previously described. Amounts of plasticizer up to 20% or more, based on the weight of the zein, will generally be suitable, and for most purposes from satisfactory.
  • the zein solutions described above may be extruded in any type of apparatus suitable for use with cellulose acetate or other cellulose solutions.
  • the standard spinnerettes may be used and the degree of pressure may be adjusted to correspond to the size of the orifice and the viscosity of the solution in accordance with known practice in this regard.
  • the solution may be extruded into air, in which case the coagulation will take due to the evaporation of solvents, or it may be extruded into water or other liquid coagulating medium.
  • Any suitable means may be employed for this purpose and the heat treatment may be effected
  • the heating could be eflected in a Vertical tower through which heated air is passed counter-current to the travel of the filament.
  • the heating should be effected at temperatures not substantially above 100 C. in view of the water content of the material and the possible deleterious eifect of higher temperatures upon proteins. Temperatures of 60-90" C. will be found to be quite satisfactory and at such temperatures a treatment of approximately 5 minutes will usually impart sufficient strength to the material.
  • the reaction between zein and the aldehyde will continue to completion upon storage at atmospheric temperatures. However, at such temperatures the reaction is relatively slow and I therefore prefer to subject the filament to further heating to impart initial water-resistance.
  • the material may be baked at temperatures of 60-90- 0. for a period of 8-10 hours. This operation may be carried out at any suitable stage of the processing, for example, when the filament is first spooled, but is preferably effected when the material is in a loose form, as in skeins. V
  • a second modification of my invention comprises the use of solutions of zein in aqueous formaldehyde without organic solvents. It' is disclosed in copending application Ser. No. 38,971. filed Sept. 3, 1935 that aqueous formaldehyde exerts a solvent and plastifying eifect upon zein. According to the process of this application, zein is kneaded with aqueous formaldehyde to obtain a mass suitable for the production of plastics. Such solutions will usually be too viscous for satisfactory extrusion, so that for the present purpose a more dilute solution should be prepared. By the use of suitable apparatus, additional plasticizers the solution and these will generally be found to be beneficial from the standpoint of reducing viscosity and aiding extrusion. Solutions of this type may be employed in the same manner as the solutions in aqueous organic solvents discussed above.
  • the coagulating fluid may comprise either a liquid or a gaseous medium and the procedures discussed above will apply to these alternative procedures.
  • a further modification of my invention comprises the use of zein solutions without aldehydes, in which case the solution is extruded into a medium containing the desired concentration of formaldehyde or the like.
  • solutions of zein in aqueous organic solvents such as the alcoholic solutions obtained by the process of my copending application Ser. No. 20,402 filed May 8, 1935, may be employed and, as in the preceding examples, plasticizing agents may be incorporated if desired.
  • Such solutions may be extruded into aqueous formaldehyde or a solution of other may be incorporated may be incorporated into reactive aldehyde, or they may be extruded into a gaseous medium containing formaldehyde vapor or the like.
  • the same general procedure as to extrusion and heat treatment previously described applies equally to the present modification.
  • Process for the production of zein filaments which comprises: extruding a solution of zein through a filament forming orifice into an aqueous coagulating medium containing formaldehyde; withdrawing the filament and heating the same to evaporate water and promote reaction between the formaldehyde and zein.
  • Process for the production of zein filaments which comprises: extruding an alcohol solution of zein containing formaldehyde through a, filament forming orifice into an aqueous coagulating medium; withdrawing the filament from said medium, and subjecting it for a short time to .a current of air heated to a temperature not in excess of 100 C., skeining the filament and ball;- 8 for about 8-10 hours.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Artificial Filaments (AREA)

Description

Patented May 2, 1939 znm FILAMEN'IS Lloyd G. Swallen, 'Terre Haute, Ind., assignor, by mesne assignments, to Corn Products Refining Company, New York, N. Y., a corporation of e, New Jersey No Drawing. Application September 3, 1935, Serial No. 38,977
2 Claims. (oi. l8-54) My invention relates to the production of protein filaments suitable for use in the manufacture of fabrics and the like. More specifically, my inventionrelates to the production of artificial protein fibres having improved strength and water-resistance. 1
It is well known that artificial fibres can be produced 'from regenerated cellulose or from cellulose esters, and such fibres have now come into extensive commercial use. However, the processes for the production .of such fibres relatively expensive and have certain disadvantages, particularly in difficulty of producing uniform products. In all of the methods now in use it has been found necessaryto rip'en the cellulose solutions prior to extrusion and even then it is necessary to blend a number of different batches in order to secure approximate uniformity. The processes previously employed have various other disadvantages, particularly with regard to dyeing and obtaining suitable lustre. In view of the proteinaceous nature of real silk, it has been attempted to produce artificial silk fibres from proteins, but up to the present time such attempts have been entirely unsuccessful. It has been impossible to secure solutions of the proteins previously employed without undesirably changing their chemical nature and the products obtained have lacked strength and water-resistance.
I have now discovered that very satisfactory filaments may be secured by extruding zein solutions into a coagulating fluid while simultaneously contacting the zein with a reactive aldehyde, and subsequently subjecting the resulting filament to elevated temperatures. It will be apparent that my invention is capable of various modifications depending upon the nature of the zein solutions employed and upon the nature of the coagulating fluid. For example, the latter may comprise either a liquid or a gas and the reactive aldehyde may be incorporated in the zein solution, in the coagulating fluid, or in both. A number of these modifications will be discussed in more detail below.
One embodiment of my invention comprises the use of solutions of zein in organic solvents containing free formaldehyde or other reactive aldehyde. Such solutions are described in copending application Ser. No. 41,776, filed Sept. 23, 1935. According to the process of this application, the zein solutions may be prepared simply by adding the desired amount of formaldehyde or other aldehyde to a solution of zein in aqueous ethyl alcohol or a similar solvent such as methyl alcohol, carbitol (di-ethylene glycol), cellosolve are (mono-ethylv ether of ethylene glycol), diacetone alcohol or the like. The zein concentration of the solution may be adjusted to any suitable value for extrusion, depending upon the size'and nature of the orifice, the pressure to be employed, etc. of free formaldehyde, based on the weight of the zein, is usually required to give satisfactory strength and water-resistance to the product. Larger amounts, for example up to 50% by weight, can usually be satisfactorily employed, but I prefer, generally, to use from 2-5% by weight. J
Although the solutions described above are satisfactory from the standpoint of extrusion to form suitable filaments, I generally prefer to incorporate a plasticizer in order to obtain the desired degree of flexibility and resilience in the product. Any suitable plasticizer for zein, such as dibutyl tartrate, monobutyl phthalate, or ptoluene methyl sulfonamide, may be used. Suitable zein solutions containing plasticizers are disclosed in copending application Ser. No. 38,976, filed Sept. 3, 1935. Such solutions may be prepared by any satisfactory procedure such as simply incorporating the desired amount of plasticizer into the solutions previously described. Amounts of plasticizer up to 20% or more, based on the weight of the zein, will generally be suitable, and for most purposes from satisfactory.
The zein solutions described above may be extruded in any type of apparatus suitable for use with cellulose acetate or other cellulose solutions. The standard spinnerettes may be used and the degree of pressure may be adjusted to correspond to the size of the orifice and the viscosity of the solution in accordance with known practice in this regard. The solution may be extruded into air, in which case the coagulation will take due to the evaporation of solvents, or it may be extruded into water or other liquid coagulating medium. After solidification of the filament and before winding, it is necessary to apply heat in An amount of aldehyde equivalent to 2% 5 10-29% will be place order to obtain satisfactory initial strength. It 5 is used, the filament should pass through a heated 5 chamber prior to winding. Any suitable means may be employed for this purpose and the heat treatment may be effected simultaneously with other treatments such as imparting the desired heated amount of tension or twist to the filament. For
example, in either of the cases mentioned above, the heating could be eflected in a Vertical tower through which heated air is passed counter-current to the travel of the filament. The heating should be effected at temperatures not substantially above 100 C. in view of the water content of the material and the possible deleterious eifect of higher temperatures upon proteins. Temperatures of 60-90" C. will be found to be quite satisfactory and at such temperatures a treatment of approximately 5 minutes will usually impart sufficient strength to the material.
It will be found that the reaction between zein and the aldehyde will continue to completion upon storage at atmospheric temperatures. However, at such temperatures the reaction is relatively slow and I therefore prefer to subject the filament to further heating to impart initial water-resistance. For this purpose, the material may be baked at temperatures of 60-90- 0. for a period of 8-10 hours. This operation may be carried out at any suitable stage of the processing, for example, when the filament is first spooled, but is preferably effected when the material is in a loose form, as in skeins. V
A second modification of my invention comprises the use of solutions of zein in aqueous formaldehyde without organic solvents. It' is disclosed in copending application Ser. No. 38,971. filed Sept. 3, 1935 that aqueous formaldehyde exerts a solvent and plastifying eifect upon zein. According to the process of this application, zein is kneaded with aqueous formaldehyde to obtain a mass suitable for the production of plastics. Such solutions will usually be too viscous for satisfactory extrusion, so that for the present purpose a more dilute solution should be prepared. By the use of suitable apparatus, additional plasticizers the solution and these will generally be found to be beneficial from the standpoint of reducing viscosity and aiding extrusion. Solutions of this type may be employed in the same manner as the solutions in aqueous organic solvents discussed above. The coagulating fluid may comprise either a liquid or a gaseous medium and the procedures discussed above will apply to these alternative procedures.
A further modification of my invention comprises the use of zein solutions without aldehydes, in which case the solution is extruded into a medium containing the desired concentration of formaldehyde or the like. For this purpose solutions of zein in aqueous organic solvents, such as the alcoholic solutions obtained by the process of my copending application Ser. No. 20,402 filed May 8, 1935, may be employed and, as in the preceding examples, plasticizing agents may be incorporated if desired. Such solutions may be extruded into aqueous formaldehyde or a solution of other may be incorporated may be incorporated into reactive aldehyde, or they may be extruded into a gaseous medium containing formaldehyde vapor or the like. The same general procedure as to extrusion and heat treatment previously described applies equally to the present modification.
The products obtained by any of the above procedures will be found to have satisfactory strength and to have excellent water-resistance after final cure. It will be seen that no ripening processes are necessary and that a uniform product may be secured in accordance with any of the procedures specified. Filaments of desirably low denier may readily be obtained and any'of the standard types of yarns may be produced. The materials will be found to have excellent appearance and satisfactory elasticity and resilience. The filaments will generally be found to have wet strength, elastic recovery and abrasion resistance superior to the artificial cellulose fibres previously employed. These properties and other advantages previously pointed out make the products of this invention especially suited for use in the textile industry for any of the purposes for which artificial cellulose fibres have previously been employed.
It will be apparent to those skilled in the art that further modifications of my invention are possible and that various equivalent materials may be employed. Various modifying agents into the solutions and any of the known procedures may be applied to the extrusion and subsequent treatment of the filaments. Spirit-soluble dyes may be incorporated into the organic solvent solutions or the final products may be dyed according to known procedures for protein plastics. In general it may be said that any equivalents or any modifications of procedure which would naturally occur to those skilled in the art may be employed without departing from the scope of my invention.
My invention now having been described, what I claim is:
1. Process for the production of zein filaments which comprises: extruding a solution of zein through a filament forming orifice into an aqueous coagulating medium containing formaldehyde; withdrawing the filament and heating the same to evaporate water and promote reaction between the formaldehyde and zein.
2. Process for the production of zein filaments which comprises: extruding an alcohol solution of zein containing formaldehyde through a, filament forming orifice into an aqueous coagulating medium; withdrawing the filament from said medium, and subjecting it for a short time to .a current of air heated to a temperature not in excess of 100 C., skeining the filament and ball;- 8 for about 8-10 hours.
LLOYD C. SWALLEN.
the same at a temperature of 60-90 C.
US38977A 1935-09-03 1935-09-03 Zein filaments Expired - Lifetime US2156929A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2521704A (en) * 1944-03-28 1950-09-12 Cyril D Evans Fibers from zein
US2852812A (en) * 1954-04-14 1958-09-23 Freudenberg Carl Manufacture of artificial sausage casings
US2864663A (en) * 1954-11-01 1958-12-16 Virginia Carolina Chem Corp Process for the production of vegetable protein fibers
US5750064A (en) * 1996-01-19 1998-05-12 E. I. Du Pont De Nemours And Company Dry spinning process for producing zein fibers
US20060282958A1 (en) * 2005-06-17 2006-12-21 Yiqi Yang Process for the production of high quality fibers from wheat proteins and products made from wheat protein fibers

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2521704A (en) * 1944-03-28 1950-09-12 Cyril D Evans Fibers from zein
US2852812A (en) * 1954-04-14 1958-09-23 Freudenberg Carl Manufacture of artificial sausage casings
US2864663A (en) * 1954-11-01 1958-12-16 Virginia Carolina Chem Corp Process for the production of vegetable protein fibers
US5750064A (en) * 1996-01-19 1998-05-12 E. I. Du Pont De Nemours And Company Dry spinning process for producing zein fibers
US20060282958A1 (en) * 2005-06-17 2006-12-21 Yiqi Yang Process for the production of high quality fibers from wheat proteins and products made from wheat protein fibers

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