US2324529A - Manufacture of paper and board - Google Patents
Manufacture of paper and board Download PDFInfo
- Publication number
- US2324529A US2324529A US277453A US27745339A US2324529A US 2324529 A US2324529 A US 2324529A US 277453 A US277453 A US 277453A US 27745339 A US27745339 A US 27745339A US 2324529 A US2324529 A US 2324529A
- Authority
- US
- United States
- Prior art keywords
- board
- lecithin
- pine
- stock
- starch
- 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
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/10—Phosphorus-containing compounds
Definitions
- This invention relates to retarding the deterioration and the development of ofi and cardboard odors in paper and board and particularly in secondary stock board.
- the board after manufacture is readily subject to the development of objectionable odors that are transmitted to packaged compositions and particularly when used for the packaging of food products such as for eggs, whole wheat biscults, cakes, cookies and other bakery goods, corn flakes, whole wheat flakes, bacon, and other meat products, butter, lard, margarine, ice cream, milk, etc.
- the objectionable oiT odor penetrates the liner to contaminate the packaged composition and frequently renders it unsalable. Then develops what is known as cardboard or papery flavors in eggs, whole wheat biscuits, etc.
- An object of this invention is therefore the retardation of cardboard and papery oil-odors andthe substantial stabilization of papers and boards and particularly of pine stock boards.
- a further object is to overcome the absorption of objectionable board odors into packaged organic food compositions, this being accomplished cheaply and simply.
- lecithin is applied to the surface of pine stock board, for
- the lecithin employed may be of any origin such as from crude corn germ oil, cottonseed oil, etc., and obtained by the segregation of the phosphatides from the crude oil.
- the lecithin may be in its crude unrefined state or more, highly refined and substantially oil free.
- the desirable method for the application of lecithin to the board is to place the lecithin in a finely divided powdery condition so that it may be readily stirred into an aqueous bath for application at the calendar stacks.
- a carrier such as starch, flour, sugar, powdered skim milk, charcoal, or similar material.
- the carrier for example, a mixture is made comprising from 50% to 98% by weight of the starch with the balance of lecithin,thoroughly admixing the lecithin in r the powdered starch to obtain a powdery product and one that will readily mix with water even though the lecithin is itself not water soluble.
- lecithin is more highly refined and freer of associated oil, less of the starch or other carrier need be used to obtain the powdery combination.
- the lecithin itself may not readily be applied to the surface of the board because of its insolubility in water so that if it were added to water for sizing on board, it would not become example, at the calendar stacks and the board tions of the heat treatment, the lecithin at the surface or the board becomes "activated and develops marked stabilizing characteristics.
- the lecithinis desirably present in the water I used for sizing in an amount ranging from 0.3% to 10% against the weight of the water and other materials in the sizing bath, and good results are obtained by using as'little as 2% of lecithin.
- a lecithin starch mixture is prepared, comprising, for example, starch and 15% lecithin, that mixture may be added to the water tub at the calendar stacks in an amount of 8% to give desirable improvement to the manufactured board.
- Example I Pine stock board after forming an the board making machine contained 70% total moisture.
- the board was passed through a trough contain- I lecithin thoroughly dispersed therethrough.
- starch lecithin mixture was added to the water and the mixture agitated tohold the combination in suspension while the board passed through, it
- the amount of lecithin to apply to the board may vary from 0.01% to 2%--but generally less than 0.7% and desirably under 0.3% is applied.
- the heating of the board after the addition thereto of the lecithin is important to obtain the desired results.
- Example II 7 Waste paper stocks used in the manufacture of secondary grade stock board and containing about 60% total moisture were prepared by adding thereto and thoroughly mixing therein 0.25% against the solids weight of the board of a mixture comprising 75% lecithin extracted from corn germ oil and ,.25% powdered anhydrous dextrose.
- One sample of the stock thus prepared was heated under 28 pounds of steam pressure for 5 minutes.
- Another sample was heated under 18 pounds steam pressure for 5. minutes. Both lots were then dried in a vacuum oven at 60 C.
- Thestocks thus prepared were placed into sealed glass bottles and observed for objectionable odor'development at daily intervals. At the end of 12 days the stock which had been heated under 18 pounds pressure was 011 in odor whereas the stock that was heated under 28 pounds pressure remained in good condition for about 26 days.
- Pine stock board develops ofi odors rapidly and the lecithin treatment described in accordance with this invention is particularly valuable for application to board made of pine stock and preferably to board made of pine stock which has not been aged or seasoned" for any long period of time.
- the lecithin treatment desirably applies to pine stock board which has been stored and held for less than a 5 month period prior to use.
- the treatment described will very materially retard and in many cases prevent the objectionable oiT odors which so seriously depreciate the value of that board by contaminating products .packaged in it even though the packaged product is not in intimate or direct contact with the board.
- the lecithin is desirably prepared for addition to the paper or board stock as anoii emulsion and emulsifying agents other than starch or glucose may beused such as gum acacia,
- gum tragacanth blackstrap molasses. etc.
- the lecithin is emulsified in this manner, it may be put through a colloid mill or an emulsifying machine, in order to reduce the particle size of the lecithin to as small as possible, so that the lecithin will exert greater effectiveness when utilized in accordance with this invention.
- the aqueous phase of such an emulsion may desirably include glucose, blackstrap molasses, dextrlnes or gums, and there may also be presentin that aqueous phase boiled or unboiled starch. 1 g;
- a powdered mixture is prepared first comprising lecithin and starch, or lecithin and powdered anhydrous dextrose, sucrose or similar sugar, sumcient cf the starch or sugar serving as the carrier should be utilized so that the finished combination including the lecithin is substantially in powdered form. In this way it' may be more readily added to the size trough or used as a heater application in the manufacture of the board.
- Desirable combinations for use are, for example, any of the following:
- lecithin A. 98 parts'of starch and 2 parts lecithin B. 70 parts powdered anhydrous dextrose and 30 parts lecithin C. 65 parts black strap molasses lecithin D. 50 parts glucose, 25 parts starch, and 25 parts lecithin.
- the lecithin is added to a petroleum oil or to paraflln or other wax used for sizing or impregnation in the paper or board, the desired effectiveness of the lecithin is not obtained and, in addition, moisture-proofness is very materially reduced.
- the lecithin is added to the board without dissolving in the oil or parailin and where ofled and waxed papers and boards are normally employed.
- The'increased paraflin or paraflin oil penetration is oiconsiderable importance in permitting minimum quantities of the oil or paraflin to be employed while getting maximum moisture prooiness and retarding freezer-burn" and 'dessication.
- the leeithin may be added in the beaters, provided that the paper or board is subsequently subjected to the elevated temperature of 180 F. to 212 F. and preferably to in excess of 220 F.
- the lecithin may be added along with rosin, starches or other materials that are normally employed in the heaters and must be thoroughly admixed in the stock material in the heaters in order to obtain a thorough dispersion of the lec- 'ithin with the paper pulp material.
- pine board stock is particularly to be treated in accordance with this invention
- other boards may also be treated and also otherpapers, and particularly kraft, although greaseproof, sulphite, and similar papers may be treated in accordance with this invention as well.
- lecithin may be employed for direct addition to the pine board, either as a tub-sizing or less preferably to the heaters, and such lecithin may be utilized without the co-addition of starch, sugar or similar material, it is most preferable for the lecithin to be added with sugar andconsiderably improved results will be obtained when the lecithin-sugar combination is used for addition to the paper stock bei'or'e subjecting it to the elevated temperature as against adding lecithin alone or'even as against a mixture comprising lecithin and starch.
- Each of the boards was heated to 220 F. for 10 minutes, and then placed in a vacuum oven at 160 F. until dried.
- the board stocks were then placed in sealed glass bottles andobserved daily for aft odor developments.
- Other materials that may less preferably be employed for utilization particularly in retarding the development of off odors in pine board, include combinations of sugars or water-soluble carbohydrates, such as dextrins, with any one of the following groups: 1
- pine stock themselves or in combination with other materials previously mentioned, and particularly to pine stock in an amount of under 2% include black strap molasses and the residues and mother liquors obtained from thereiining of crude cane and crude beet sugars and less desirably the crude cane and beet sugars themselves.
- the water and alcohol soluble extracts from the cereals and de-oiled or expressed seeds may also be utilized such as the concentrated water extract of finely divided dry milled maize, oats or barley, and also and less preferably 'of the seeds such as of peanut, cottonseed, sunflower seed, olives, etc., and preferably in their de-oiled or de-i'atted condition and after the glyceride oil contained therein has been expressed or extracted therefrom.
- the water and alcohol soluble extracts of the de-oiled cereal germs may also be employed such as of de-oiled rice germ, corn germ, etc.
- pine board stock may be employed in an amount ranging from 0.005% to 2% against the weight of and for addition to the pine board stock. In any event, it is important that the pine board stockbe subjected to the elevated temperature in order to obtain the desired interaction whereby stabilization is secured.
- tannic acid which appears to be unusual in'having the property of becoming markedly increased in stabilizing effect when added to an oxidizable organic compound and particularly to a glyceride, essential or hydrocarbon oil-containing oxidizable organic compound and then subjected to an elevated temperature in the presence of that oxidizable organic compound, such increase in eflectiveness being entirely out of proportion from what would be expected by comparison to similarly constituted are subject to the development of off odors resulting from the components of'those textiles being subject to rapid deterioration under conditlons of storage.
- the board may be somewhat improved in keeping quality by subjecting the pulp to between 30 and 35 pounds steam pressure or more. Where less than 30 pounds steam pressure is applied to the pulp, the deteriorative changesoccur with extreme rapidity but these changes .can be somewhat reduced by subjecting the pulp to between 30 and 35 pounds steam pressure, this treatment being given to the entire pulp before the,
- the pine fiber board of this application relates to the paper and paperboard made of pine stock base, par-'- ticularly by the use of slash pine from which paper and paperboard of great susceptibility to oxidative deterioration and to the development of off-odors is obtained.
- the slash pine used in the manufacture of paper and paperboard becomes more readily subject to oil-odors when it has not been aged or seasoned for a period of three to six months, and the process described herein is particularly of value for paper and paper board made from slash pine and other pine stock which has not been properly aged or seasoned.
- a process of treating a pine fiberboard subject to oxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of about 93% water and 7% of a starch-lecithin mixture, said mixture consisting of about 1 ,part by weight of crude lecithin and about 5 parts by weight of starch, and then passing the board over heated rolls at an elevated temperature above 1''. until dry,-the final board containing about between 0.01% and 2% oi lecithin.
- A'process of treating a paperboard subject to oxidative deterioration to render the same resistant tooxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of a major proportion of water and a minor proportion of a starch lecithin mixture, said mixture consisting'of a minor proportion of lecithin anda major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the final board containing between about 0.01% and 2% of lecithin.
- a process of treating a pine fibre board subject to oxidative deterioration to render the same resistant to oxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of a major proportion of water and a minor proportion of a starch lecithin mixture, said mixture consisting of a minor proportion of lecithin and a major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the flnal board containing between about 0.01% and 2% of lecithin.
- a process of treatinga pine fibre board subject to oxidative deterioration to render the same resistant to oxidative deterioration' which comprises passing the board through a trough containing an aqueous bath composed of about 93% water and 7% of astarch lecithin mixture, said mixture consisting of a minor proportion of lecithin and a major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the final board containing between about 0.01% and 2% oi lecithin.
Landscapes
- Paper (AREA)
Description
Patented July 20, 1943 MANUFACTURE ormrrn AND noiu'm Sidney Musher, New York, N. Y., assignor to Musher Foundation, Incorporated, New York, N. Y., a corporation of New York No Drawing. Application June 5, 1939, Serial No. 277,453
4 Claims. (Cl. a-nas) This invention relates to retarding the deterioration and the development of ofi and cardboard odors in paper and board and particularly in secondary stock board.
In the field of the secondary stock board made of crude and not too highly refined raw materials, the board after manufacture is readily subject to the development of objectionable odors that are transmitted to packaged compositions and particularly when used for the packaging of food products such as for eggs, whole wheat biscults, cakes, cookies and other bakery goods, corn flakes, whole wheat flakes, bacon, and other meat products, butter, lard, margarine, ice cream, milk, etc.
Even thoughthere is used an inner paper liner,
the objectionable oiT odor penetrates the liner to contaminate the packaged composition and frequently renders it unsalable. Then develops what is known as cardboard or papery flavors in eggs, whole wheat biscuits, etc.
The problem is particularly serious in the utilization of pine stock, and pine board will, within a few days of manufacture and particularly if fresh stock is employed, develop very objectionable and readily penetratable oiT-cdors.
An object of this invention is therefore the retardation of cardboard and papery oil-odors andthe substantial stabilization of papers and boards and particularly of pine stock boards.
A further object is to overcome the absorption of objectionable board odors into packaged organic food compositions, this being accomplished cheaply and simply.
Still further objectsand advantages will appear from the more detailed description setforth below, it being understood, however, that this more detailed description is given by way of illustration and explanation only, and not by way of limitation, since various changes therein may be made by those skilled in the art without departing from the scope and spirit of the present invention.
In accordance with this invention, lecithin is applied to the surface of pine stock board, for
stock board, for example, is subjected after adding lecithin thereto, the greater is the stabilizing efiect. It is not known as to how this stabilizing action occurs because it would normally be expected that an elevated temperature decreases rather than increases stability. It is believed, however; that some chemical action occurs whereo by marked stabilization is eflected.
The lecithin employed may be of any origin such as from crude corn germ oil, cottonseed oil, etc., and obtained by the segregation of the phosphatides from the crude oil. The lecithin may be in its crude unrefined state or more, highly refined and substantially oil free.
The desirable method for the application of lecithin to the board is to place the lecithin in a finely divided powdery condition so that it may be readily stirred into an aqueous bath for application at the calendar stacks. This is accomplished by the use of a carrier such as starch, flour, sugar, powdered skim milk, charcoal, or similar material.
Where starch is employed as, the carrier, for example, a mixture is made comprising from 50% to 98% by weight of the starch with the balance of lecithin,thoroughly admixing the lecithin in r the powdered starch to obtain a powdery product and one that will readily mix with water even though the lecithin is itself not water soluble.
Where the lecithin is more highly refined and freer of associated oil, less of the starch or other carrier need be used to obtain the powdery combination.
The lecithin itself may not readily be applied to the surface of the board because of its insolubility in water so that if it were added to water for sizing on board, it would not become example, at the calendar stacks and the board tions of the heat treatment, the lecithin at the surface or the board becomes "activated and develops marked stabilizing characteristics.
The higher the temperature to which the pine tain a dispersion of the lecithin in the water which may then be used as a sizing.
The lecithinis desirably present in the water I used for sizing in an amount ranging from 0.3% to 10% against the weight of the water and other materials in the sizing bath, and good results are obtained by using as'little as 2% of lecithin. Where a lecithin starch mixture is prepared, comprising, for example, starch and 15% lecithin, that mixture may be added to the water tub at the calendar stacks in an amount of 8% to give desirable improvement to the manufactured board.
Example I Pine stock board after forming an the board making machine contained 70% total moisture.
The board was passed through a trough contain- I lecithin thoroughly dispersed therethrough. The
starch lecithin mixture was added to the water and the mixture agitated tohold the combination in suspension while the board passed through, it
j beingestimated that 0.1% by weight of the lecithin adhered to the board (against the solids weight of the board). The treated board was then passed over heated rolls at a temperature of about 220 F. until dried. The board thus obtained was tested alongside of pine stock board similarly prepared but without the lecithin addition by allowing to remain exposed to the air at room temperature and in the dark. A distinct objectionable cardboard odor developed in the untreated board within 8 days whereas the treated board did not'show the same objectionable characteristics until days had elapsed.
The amount of lecithin to apply to the board may vary from 0.01% to 2%--but generally less than 0.7% and desirably under 0.3% is applied.
The heating of the board after the addition thereto of the lecithin is important to obtain the desired results.
Example II 7 Waste paper stocks used in the manufacture of secondary grade stock board and containing about 60% total moisture were prepared by adding thereto and thoroughly mixing therein 0.25% against the solids weight of the board of a mixture comprising 75% lecithin extracted from corn germ oil and ,.25% powdered anhydrous dextrose. One sample of the stock thus prepared was heated under 28 pounds of steam pressure for 5 minutes. Another sample was heated under 18 pounds steam pressure for 5. minutes. Both lots were then dried in a vacuum oven at 60 C. Thestocks thus prepared were placed into sealed glass bottles and observed for objectionable odor'development at daily intervals. At the end of 12 days the stock which had been heated under 18 pounds pressure was 011 in odor whereas the stock that was heated under 28 pounds pressure remained in good condition for about 26 days. t
Pine stock board develops ofi odors rapidly and the lecithin treatment described in accordance with this invention is particularly valuable for application to board made of pine stock and preferably to board made of pine stock which has not been aged or seasoned" for any long period of time. For example, the lecithin treatment desirably applies to pine stock board which has been stored and held for less than a 5 month period prior to use.
The treatment described will very materially retard and in many cases prevent the objectionable oiT odors which so seriously depreciate the value of that board by contaminating products .packaged in it even though the packaged product is not in intimate or direct contact with the board.
The lecithin is desirably prepared for addition to the paper or board stock as anoii emulsion and emulsifying agents other than starch or glucose may beused such as gum acacia,
gum tragacanth, blackstrap molasses. etc.
Where the lecithin is emulsified in this manner, it may be put through a colloid mill or an emulsifying machine, in order to reduce the particle size of the lecithin to as small as possible, so that the lecithin will exert greater effectiveness when utilized in accordance with this invention.
The aqueous phase of such an emulsion may desirably include glucose, blackstrap molasses, dextrlnes or gums, and there may also be presentin that aqueous phase boiled or unboiled starch. 1 g;
Where a powdered mixture is prepared first comprising lecithin and starch, or lecithin and powdered anhydrous dextrose, sucrose or similar sugar, sumcient cf the starch or sugar serving as the carrier should be utilized so that the finished combination including the lecithin is substantially in powdered form. In this way it' may be more readily added to the size trough or used as a heater application in the manufacture of the board.
Desirable combinations for use are, for example, any of the following:
A. 98 parts'of starch and 2 parts lecithin B. 70 parts powdered anhydrous dextrose and 30 parts lecithin C. 65 parts black strap molasses lecithin D. 50 parts glucose, 25 parts starch, and 25 parts lecithin.
The cruder forms of-lecithin are even more desirable to use in accordance with this invenand 35 parts tion than the more refined lecithins. For examdeterioration of pine stock board when particularly subjected to the elevated temperature is most unusual in view of the fact that lecithin is normally recognized as becoming substantially inactivated as an antioxidant when heated to a temperature in excess of 65 0., but in accordance with this invention, it has been observed that unless the high heat treatment is applied, the desired improvement in keeping quality is not obtained. g,
Where the lecithin is added to a petroleum oil or to paraflln or other wax used for sizing or impregnation in the paper or board, the desired effectiveness of the lecithin is not obtained and, in addition, moisture-proofness is very materially reduced.
Where, however, the lecithin is added to the board without dissolving in the oil or parailin and where ofled and waxed papers and boards are normally employed. The'increased paraflin or paraflin oil penetration is oiconsiderable importance in permitting minimum quantities of the oil or paraflin to be employed while getting maximum moisture prooiness and retarding freezer-burn" and 'dessication. As a less preferable alternative to adding the .lecithin as ,a tubsizing operation on the board or paper, the leeithin may be added in the beaters, provided that the paper or board is subsequently subjected to the elevated temperature of 180 F. to 212 F. and preferably to in excess of 220 F.
The lecithin may be added along with rosin, starches or other materials that are normally employed in the heaters and must be thoroughly admixed in the stock material in the heaters in order to obtain a thorough dispersion of the lec- 'ithin with the paper pulp material.
Although pine board stock is particularly to be treated in accordance with this invention, other boards may also be treated and also otherpapers, and particularly kraft, although greaseproof, sulphite, and similar papers may be treated in accordance with this invention as well.
Although lecithin may be employed for direct addition to the pine board, either as a tub-sizing or less preferably to the heaters, and such lecithin may be utilized without the co-addition of starch, sugar or similar material, it is most preferable for the lecithin to be added with sugar andconsiderably improved results will be obtained when the lecithin-sugar combination is used for addition to the paper stock bei'or'e subjecting it to the elevated temperature as against adding lecithin alone or'even as against a mixture comprising lecithin and starch.
Eoample III Pine board stock, containing approximately 60%moisture, was treated by adding thereto and thoroughly mixing therein the following materials:
A. 0.1% soya lecithin B. 0.1% powdered anhydrous dextrose C. A combination comprising 0.05% soya lecithin and 0.05% powdered anhydrous dextrose D. No addition.
Each of the boards was heated to 220 F. for 10 minutes, and then placed in a vacuum oven at 160 F. until dried. The board stocks were then placed in sealed glass bottles andobserved daily for aft odor developments.
Oil odor observed after--.
A 18 days B 5 days C 29 days D 4 days Other materials, that may less preferably be employed for utilization particularly in retarding the development of off odors in pine board, include combinations of sugars or water-soluble carbohydrates, such as dextrins, with any one of the following groups: 1
A. Phospholipins, ."phosphoric acid and phos-' D. Polyhydroxy-aryl compounds such as hydroquinone, pyrogallol, pyrocatechol, resorcinol, phloroglucinol, and other polyhydroxy phenols, guaiacoi, eugenol, aromatic hydroxy aldehydes, the naphthols including alphanaphthol, and substituted naphthols, tannic acid, etc.;
E. Other substituted aromatic compounds such as thymol.
Other materials that may be desirably em-fl ployed for addition to paper or board stock, by
themselves or in combination with other materials previously mentioned, and particularly to pine stock in an amount of under 2% include black strap molasses and the residues and mother liquors obtained from thereiining of crude cane and crude beet sugars and less desirably the crude cane and beet sugars themselves.
The water and alcohol soluble extracts from the cereals and de-oiled or expressed seeds may also be utilized such as the concentrated water extract of finely divided dry milled maize, oats or barley, and also and less preferably 'of the seeds such as of peanut, cottonseed, sunflower seed, olives, etc., and preferably in their de-oiled or de-i'atted condition and after the glyceride oil contained therein has been expressed or extracted therefrom. The water and alcohol soluble extracts of the de-oiled cereal germs may also be employed such as of de-oiled rice germ, corn germ, etc.
These materials may be employed in an amount ranging from 0.005% to 2% against the weight of and for addition to the pine board stock. In any event, it is important that the pine board stockbe subjected to the elevated temperature in order to obtain the desired interaction whereby stabilization is secured.
Among the materials that may particularly be employed for addition to pine board stock before subjecting to the elevated temperature heating is tannic acid which appears to be unusual in'having the property of becoming markedly increased in stabilizing effect when added to an oxidizable organic compound and particularly to a glyceride, essential or hydrocarbon oil-containing oxidizable organic compound and then subjected to an elevated temperature in the presence of that oxidizable organic compound, such increase in eflectiveness being entirely out of proportion from what would be expected by comparison to similarly constituted are subject to the development of off odors resulting from the components of'those textiles being subject to rapid deterioration under conditlons of storage.
In the treatment of pine stock board the board may be somewhat improved in keeping quality by subjecting the pulp to between 30 and 35 pounds steam pressure or more. Where less than 30 pounds steam pressure is applied to the pulp, the deteriorative changesoccur with extreme rapidity but these changes .can be somewhat reduced by subjecting the pulp to between 30 and 35 pounds steam pressure, this treatment being given to the entire pulp before the,
finished board is actually formed, and the pressures indicated is apparently critical in this regard.
The present application is a continuationln part of application, Serial No. 69,296 filed March 1'7, 1936. i
The pine fiber board of this application, and as referred to in the claims, relates to the paper and paperboard made of pine stock base, par-'- ticularly by the use of slash pine from which paper and paperboard of great susceptibility to oxidative deterioration and to the development of off-odors is obtained. The slash pine used in the manufacture of paper and paperboard becomes more readily subject to oil-odors when it has not been aged or seasoned for a period of three to six months, and the process described herein is particularly of value for paper and paper board made from slash pine and other pine stock which has not been properly aged or seasoned. I
Having described my invention, what I claim is l. A process of treating a pine fiberboard subject to oxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of about 93% water and 7% of a starch-lecithin mixture, said mixture consisting of about 1 ,part by weight of crude lecithin and about 5 parts by weight of starch, and then passing the board over heated rolls at an elevated temperature above 1''. until dry,-the final board containing about between 0.01% and 2% oi lecithin.
2. A'process of treating a paperboard subject to oxidative deterioration to render the same resistant tooxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of a major proportion of water and a minor proportion of a starch lecithin mixture, said mixture consisting'of a minor proportion of lecithin anda major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the final board containing between about 0.01% and 2% of lecithin.
3. A process of treating a pine fibre board subject to oxidative deterioration to render the same resistant to oxidative deterioration which comprises passing the board through a trough containing an aqueous bath composed of a major proportion of water and a minor proportion of a starch lecithin mixture, said mixture consisting of a minor proportion of lecithin and a major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the flnal board containing between about 0.01% and 2% of lecithin.
4. A process of treatinga pine fibre board subject to oxidative deterioration to render the same resistant to oxidative deterioration'which comprises passing the board through a trough containing an aqueous bath composed of about 93% water and 7% of astarch lecithin mixture, said mixture consisting of a minor proportion of lecithin and a major proportion of starch, and then passing the board over heated rolls at an elevated temperature above 180 F. until dry, the final board containing between about 0.01% and 2% oi lecithin.
SIDNEY uusrmn.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US277453A US2324529A (en) | 1939-06-05 | 1939-06-05 | Manufacture of paper and board |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US277453A US2324529A (en) | 1939-06-05 | 1939-06-05 | Manufacture of paper and board |
Publications (1)
Publication Number | Publication Date |
---|---|
US2324529A true US2324529A (en) | 1943-07-20 |
Family
ID=23060937
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US277453A Expired - Lifetime US2324529A (en) | 1939-06-05 | 1939-06-05 | Manufacture of paper and board |
Country Status (1)
Country | Link |
---|---|
US (1) | US2324529A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3413190A (en) * | 1964-12-30 | 1968-11-26 | Continental Can Co | Process for manufacturing paperboard with high grease resistance by applying a plurality of starch coatings to a wet board |
US4828650A (en) * | 1985-08-23 | 1989-05-09 | International Paper Company | Heat treatment of paper products having milk and other additives |
US5034097A (en) * | 1989-09-25 | 1991-07-23 | Borden, Inc. | Epoxidized polyamide wet strength resins containing lecithin |
US20070102129A1 (en) * | 2005-11-04 | 2007-05-10 | Ki-Oh Hwang | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
WO2007055912A1 (en) * | 2005-11-04 | 2007-05-18 | Cargill, Incorporated | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
WO2007055911A1 (en) * | 2005-11-04 | 2007-05-18 | Cargill, Incorporated | Lecithin-containing starch compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
US8192845B2 (en) | 2005-11-04 | 2012-06-05 | Cargill, Incorported | Lecithin-containing starch compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
-
1939
- 1939-06-05 US US277453A patent/US2324529A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3413190A (en) * | 1964-12-30 | 1968-11-26 | Continental Can Co | Process for manufacturing paperboard with high grease resistance by applying a plurality of starch coatings to a wet board |
US4828650A (en) * | 1985-08-23 | 1989-05-09 | International Paper Company | Heat treatment of paper products having milk and other additives |
US5034097A (en) * | 1989-09-25 | 1991-07-23 | Borden, Inc. | Epoxidized polyamide wet strength resins containing lecithin |
US20070102129A1 (en) * | 2005-11-04 | 2007-05-10 | Ki-Oh Hwang | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
WO2007055912A1 (en) * | 2005-11-04 | 2007-05-18 | Cargill, Incorporated | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
WO2007055911A1 (en) * | 2005-11-04 | 2007-05-18 | Cargill, Incorporated | Lecithin-containing starch compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
US7931778B2 (en) * | 2005-11-04 | 2011-04-26 | Cargill, Incorporated | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
CN101365745B (en) * | 2005-11-04 | 2011-06-08 | 嘉吉有限公司 | Lecithin-containing starch compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
CN101326233B (en) * | 2005-11-04 | 2012-05-16 | 嘉吉有限公司 | Lecithin-starches compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
US8192845B2 (en) | 2005-11-04 | 2012-06-05 | Cargill, Incorported | Lecithin-containing starch compositions, preparation thereof and paper products having oil and grease resistance, and/or release properties |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2324529A (en) | Manufacture of paper and board | |
US3506447A (en) | Method for preparing a fruit cereal product | |
US3050437A (en) | Manufacture of sized paper | |
US2377359A (en) | Manufacture of antioxygenic paper | |
US2758032A (en) | Antioxidant wrapper for foods | |
US3524796A (en) | Starch phosphate-ketene dimer emulsion as internal paper size | |
US2342162A (en) | Extraction of food and similar antioxygens from cane and beet molasses | |
US2155731A (en) | Paper treatment | |
US2233142A (en) | Paper packaging material and method of making the same | |
US2325624A (en) | Treatment of paper and paperboard | |
US2431498A (en) | Shortening | |
US2282800A (en) | Stabilization against oxidation by use of caramelized milk solids | |
US2233141A (en) | Antioxidant for packaging materials | |
US2162585A (en) | Aerated products | |
DE2758941A1 (en) | NEW APPLICATIONS OF STARCH PRODUCTS AND METHODS FOR MANUFACTURING THEM | |
US2186609A (en) | Method of removing wax from waxed paper stock | |
US3052562A (en) | Stable emulsions | |
US2181765A (en) | Preservation of organic substances | |
US2198212A (en) | Stabilization of oils | |
US2198218A (en) | Wheat germ preparation | |
US2273063A (en) | Paper container | |
US2830916A (en) | Sized paper and method of making | |
US2193695A (en) | Treatment of paper and board | |
US1863867A (en) | Paper size and process of making same | |
US2309079A (en) | Treatment of paper |