US1939404A - Manufacture of pressed cellulose articles - Google Patents
Manufacture of pressed cellulose articles Download PDFInfo
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- US1939404A US1939404A US642819A US64281932A US1939404A US 1939404 A US1939404 A US 1939404A US 642819 A US642819 A US 642819A US 64281932 A US64281932 A US 64281932A US 1939404 A US1939404 A US 1939404A
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- Prior art keywords
- sulfur
- pulp
- product
- peptizing
- paper
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- 229920002678 cellulose Polymers 0.000 title description 16
- 239000001913 cellulose Substances 0.000 title description 16
- 238000004519 manufacturing process Methods 0.000 title description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 102
- 239000011593 sulfur Substances 0.000 description 99
- 229910052717 sulfur Inorganic materials 0.000 description 99
- 239000003795 chemical substances by application Substances 0.000 description 38
- 239000000047 product Substances 0.000 description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 27
- 238000000034 method Methods 0.000 description 15
- 229920001131 Pulp (paper) Polymers 0.000 description 14
- 239000000123 paper Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 11
- 239000005871 repellent Substances 0.000 description 9
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 8
- 238000001035 drying Methods 0.000 description 8
- 230000002940 repellent Effects 0.000 description 8
- 239000002699 waste material Substances 0.000 description 8
- 239000000080 wetting agent Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 238000000227 grinding Methods 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- 229920003043 Cellulose fiber Polymers 0.000 description 3
- 239000001263 FEMA 3042 Substances 0.000 description 3
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 3
- 238000010410 dusting Methods 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 239000000417 fungicide Substances 0.000 description 3
- 238000007731 hot pressing Methods 0.000 description 3
- 238000005470 impregnation Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 3
- 229940033123 tannic acid Drugs 0.000 description 3
- 235000015523 tannic acid Nutrition 0.000 description 3
- 229920002258 tannic acid Polymers 0.000 description 3
- 238000001238 wet grinding Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000011111 cardboard Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000010908 decantation Methods 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000000855 fungicidal effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 229920001864 tannin Polymers 0.000 description 2
- 235000018553 tannin Nutrition 0.000 description 2
- 239000001648 tannin Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 235000017709 saponins Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 150000003463 sulfur Chemical class 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J1/00—Fibreboard
- D21J1/08—Impregnated or coated fibreboard
Definitions
- This invention relates to manufacture of pressed cellulose articles; and it comprises a fine dry, fragmental sulfur having a fineness of the order of 200 mesh, being immiscible in water,
- a product having a purity of the order of 99.5 per cent and being substantially. free from insoluble, amorphous sulfur, said product being made by wet grinding sulfur in the presencepf a peptizing agent, such as a colloidal tanning agent,
- the fine sulfur of commerce usually occurs in 5 one of two forms.
- flowers of sulfur is at times loosely applied to cover both types. Strictly speaking this term applies only to sulfur which has been sublimed and condensed in finely divided form.
- the other type of fine sulfur is merely a ground product obtained by'grinding rock f, roll or lump sulfur, as the coarser particles produced by various processes are called. Both of these forms are immiscible in water and neither is much finer than about 50 mesh. There is a considerable demand for a sulfur of greater fineness. For some purposes it is desired to have such a product miscible with water while in other cases a water repellent product is desired.
- Fine sulfur is also used to some extent for impregnating paper and carboard. $urface impregnation is usually employed. It has been proposed to mix fine sulfur with paper pulp before making the same into paper, cardboard and the like. Here again it is found that the fine sulfur of commerce 'does not possess the requisite adhesiveness for best results. It does not readily stick to the cellulose fibres. This method has not been developed commercially due to the large losses caused by this lack of adhesiveness.
- the present application is directed more particularly to an immiscible fine sulfur product which may be obtained from the above described miscible product by removing any peptizing agent and then drying. Drying destroys the property of miscibility. I have found that such a dry product has many highly valuable properties.
- miscible sulfur of my acknowledged copending application is valuable for a large number of industrial uses, I have found that the property of miscibility of this product is not always desired. Moreover the presence of the wetting or peptizing agent in the sulfur is disadvantageous for some purposes. For example,
- the immiscible sulfur product of the present invention can be readily produced from that of my acknowledged application merely by washing and drying.
- one method of making a miscible sulfur is to take a pound of tannic acid (or 4 pounds of dry sulfite waste liquor solids or 8 pounds of a commercial preparation of sulfite waste liquor containing 50 per cent solids) add 0.75 ton of water and a ton of sulfur and run the mixture through some sort of fine grinding device to form a'sulfur pulp.
- the sulfur can then be allowed to settle out. It may be washed while wet and will still retain its miscibility with water. With the dispersing agent washed out, the wet pulp of sulfur and water is still miscible with water and with wet paper pulp.
- the sulfur pulp containing peptizing agent is washed, usually by decantation, to remove this agent down to a concentration of say 0.005 per cent.
- the washed sulfur pulp is then dried. Drying destroys its miscibility with water.
- This new product is water repellent, it has a composition usually ranging from 99.5 to 99.9 per cent sulfur, it has a fineness of the order of 200 mesh and is considerably finer than flowers of sulfur or than sulfur ground in the absence of peptizing agents.
- Its solubility in carbon disulfide is substantially 95 r cent showing the substantial absence of amorphous sulfur, it has a fragmental particle structure and readily adheres to foliage and other objects when dusted thereon.
- peptizing agents having tanning properties such as tannic acid and sulfite waste liquor. These peptizing agents are better for producing the desired results than any others with which I am acquainted.
- other peptizing or wetting agents may be employed in making the products of the present invention. These include saponin, gelatin, casein and the like. When sulfur is wet ground in the presence of these agents and the resulting sulfur pulp is washed for their removal and then dried, a highly valuable new sulfur product is produced having the descriped properties.
- these peptizing agents are employed instead of tannin or sulfite waste liquor moisture, of high insulating value and proof their use disadvantageous from an economic standpoint.
- sulfur in. miscible form containing peptizing agent can be incorporated with wet cellulose pulp in the manufacture of paper; being simply added to the pulp and stirred.
- Pulp board or paper can, for example, be made by suspending sulfur in the water used for paper or pulp board making and otherwise proceeding exactly as usual. The wet sheet or board can then be washed with water. This removes the peptizing agent and restores the sulfur to its normal water-repellent condition. After the paper or board is thus man-' ufactured and dried, the sulfur can then be fused in place.
- a better method of producing a cellulose article impregnated with the sulfur of my invention and free from peptizing agents is to wash the mixture of sulfur pulp and wetting agent for removal of the latter prior to admixture with the paper pulp. Washing by decantation is usually satisfactory but a fine filter may be employed if desired. Special solvents may be used ,for removal of the peptizing agents.
- One method ofproceeding tomake the cellulose pulp articles of the present invention is to take ordinary ground sulfur of commerce. mix it with a peptizing or wetting agent in order to make it readily wet with water, then wash out the wetting agent and add the still miscible product to paper pulp.
- the use of the wetting agent in this process overcomes the difliculties involved in mixing untreated sulfur with water and with paper pulp.
- sulfur particles In order to stick to wet cellulose fibres sulfur particles must be readily wet with water.
- untreated ground sulfur is highly water repellent. It does not effectively stick to the fibres; hence the value of my treatment.
- I hotpress the pulp articles in order to melt the sulfur in place This can be accomplished by the use of calender rolls through which the impregnated sheet maybe passed or by the use of heated molds, etc.
- the impregnated paper pulp may be pressed into any shape desired;
- I prepared a sulfur pulp free from peptizing agent by grinding a one ton batch of commercial pulverulent sulfur in a so-called colloid mill. Prior to grinding there was mixed with the sulfur approximately 0.75 ton of water and 1 gallon of a 30 B. commercial preparation of sulfite waste liquor containing about 50 per cent of solids. This mixture was run through the colloid mill and into a large settling tank equipped with an agitator. The ground sulfur pulp was allowed to settle for 1 hour and the supernatant liquor was drawn off. About 1500 pounds of water were run into the tank, the agitator was started to thoroughly mix the material and then the mix was allowed to settle for 1 hour, after which the supernatant liquor was again decanted off.
- This washing process was repeated 3 times until the proportion of sulfite waste liquor remaining in the sulfur pulp was reduced to less than .01 per cent by weight of solids based on the sulfur.
- This sulfur pulp was then introduced into the Jordans of a paper mill in amount to give about 25 per cent by weight in the finished product.
- the sulfur and paper pulp mixture was then passed to the Fourdrinier machine where it was made into sheet card board. After passing the drying rolls the sheet was passed through a pair of corrugated calender rolls maintained at a temperature of about 260 F. or sufiicient to melt the sulfur in situ. To the corrugated sheet thus formed there was applied on both sides sheets of non-impregnated paper in the usual manner.
- the resulting composite sheet was found to have a strength of about double a similar sheet without a sulfur impregnated core.
- the impregnated sheet was also waterproof. It was made into a carton suitable for transporting fish or other like materials.
- a hot-pressed cellulose product having uniformly dispersed therethrough from 5 to 200 per cent of sulfur in water repellent form and having a fineness of the order of 200' mesh, the said product being substantially free from peptizing agents for sulfur.
- a hot-pressed cellulose product having uniformly dispersed therethrough from 15 to 50 per cent of fine, water repellent sulfur, the said fine sulfur being substantially free from amorphous sulfur and having a fineness of the order of 200 mesh, the said product being substantialy free from peptizing
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- Paper (AREA)
Description
Patented Dec. 12, 1933 MANUFACTURE OF PRESSED CELLULOSE ARTICLES Adriaan Nagelvoort, Wilmington, Del., assignor to Delaware Chemical Engineering Company, Wilmington, Del., a corporation of Delaware No Drawing. Application November 15, 1932 Serial No. 642,819
7 Claims. (CI. 92-21) This invention relates to manufacture of pressed cellulose articles; and it comprises a fine dry, fragmental sulfur having a fineness of the order of 200 mesh, being immiscible in water,
having a purity of the order of 99.5 per cent and being substantially. free from insoluble, amorphous sulfur, said product being made by wet grinding sulfur in the presencepf a peptizing agent, such as a colloidal tanning agent,
10 washing to remove such agent and drying; and it also comprises, as a new article, a hot-pressed cellulose product having uniformly dispersed therethrough from 5 to 200 per cent of sulfur in water repellent form and having a fineness of the order of 200 mesh, the said product being substantially free from peptizing agents for sulfur; and it further comprises a process of making such. an article wherein a dispersed paper pulp is mixed with the above described sulfur preparation, (usually before drying the same) the mixture of paper pulp and sulfur is formed into final shape and is then hot pressed; all as more fully hereinafter set forth and as claimed.
The fine sulfur of commerce usually occurs in 5 one of two forms. The term flowers of sulfur is at times loosely applied to cover both types. Strictly speaking this term applies only to sulfur which has been sublimed and condensed in finely divided form. The other type of fine sulfur is merely a ground product obtained by'grinding rock f, roll or lump sulfur, as the coarser particles produced by various processes are called. Both of these forms are immiscible in water and neither is much finer than about 50 mesh. There is a considerable demand for a sulfur of greater fineness. For some purposes it is desired to have such a product miscible with water while in other cases a water repellent product is desired.
An important use for fine sulfur is in the socalled dusting powders used as fungicides for fruit and other trees. The fine sulfur of commerce has not proved entirely satisfactory for' this purposesince it does not readily stick to the foliage. It is usually necessary to employ a socalled sticker in the dusting powder to supply the necessary adhesiveness.
Fine sulfur is also used to some extent for impregnating paper and carboard. $urface impregnation is usually employed. It has been proposed to mix fine sulfur with paper pulp before making the same into paper, cardboard and the like. Here again it is found that the fine sulfur of commerce 'does not possess the requisite adhesiveness for best results. It does not readily stick to the cellulose fibres. This method has not been developed commercially due to the large losses caused by this lack of adhesiveness.
It has been proposed to overcome this difliculty by the use of certain agents whose alleged purpose is to precipitate on and to stick to the fibre, dragging the sulfur along with them. But such agentsdo not form advantageous components of cellulose pulp articles.
In a prior and copending application, Serial No. 608,866, filed May 2, 1932, of which the pres- 85 ent application is a continuation in part, I have described and claimed a fine sulfur product miscible with water; the said product being obtained by wet grinding sulfur in the presence of a peptizing agent having tanning properties. This product, as described in the acknowledged application, can be washed to remove the peptizing agent and, while still wet, will retain its miscibility with water. A dry miscible preparation can be obtained by drying the product without removing the peptizing agent.
The present application is directed more particularly to an immiscible fine sulfur product which may be obtained from the above described miscible product by removing any peptizing agent and then drying. Drying destroys the property of miscibility. I have found that such a dry product has many highly valuable properties.
I have also found that the process of making cellulose pulp articles, described but not claimed in my acknowledged copending application, can be improved by removing peptizing agents from the ground sulfur pulp prior to admixture with cellulose pulp.
While the miscible sulfur of my acknowledged copending application is valuable for a large number of industrial uses, I have found that the property of miscibility of this product is not always desired. Moreover the presence of the wetting or peptizing agent in the sulfur is disadvantageous for some purposes. For example,
I have found that, in making sulfur and oil emulsions for spraying fruit trees, the presence of a peptizing agent such as tannic acid or sulfite waste liquor causes the sulfur pulp to be precipi- 10o tated in curds when added to the oil emulsions. If the peptizing agent is removed by washing prior to addition to the oil emulsion, in accordance with my present process, the sulfur mixes with the oil and remains suspended.
I have also found that the dry immiscible preparation -of my present invention is especially valuable when used in fungicide dusting powders. The new product sticks to the leaves whereas the miscible product is easily washed off. In fact 1 the sticking properties of my new product are so great that the use of the stickers in such products may usually be dispensed with. As previously mentioned the commercial flowers of sulfur" does not show sufiicient adhesiveness without the use of stickers. A possible explanation of this phenomenon is that the particles of my product are fragmentary or granular in shape while those of flowers of sulfur are spherical.
I have also found that, in the manufacture of paper products, the presence of a peptizing agent is disadvantageous for several reasons. In the presence of such an agent the sulfur particles do not stick readily to the paper fibres. A large proportion of the sulfur is washed off and lost during the process. Moreover, the presence of such agents largely destroys the water repellent properties of the sulfur and hence impairs the final products from the standpoint of waterproofness. If tannin is used as peptizing agent it is likely to impart a slight color to the paper product, especially if the water used contains any iron.
The immiscible sulfur product of the present invention can be readily produced from that of my acknowledged application merely by washing and drying. As described in the prior application one method of making a miscible sulfur is to take a pound of tannic acid (or 4 pounds of dry sulfite waste liquor solids or 8 pounds of a commercial preparation of sulfite waste liquor containing 50 per cent solids) add 0.75 ton of water and a ton of sulfur and run the mixture through some sort of fine grinding device to form a'sulfur pulp. The sulfur can then be allowed to settle out. It may be washed while wet and will still retain its miscibility with water. With the dispersing agent washed out, the wet pulp of sulfur and water is still miscible with water and with wet paper pulp.
In the present invention the sulfur pulp containing peptizing agent is washed, usually by decantation, to remove this agent down to a concentration of say 0.005 per cent. The washed sulfur pulp is then dried. Drying destroys its miscibility with water. This new product is water repellent, it has a composition usually ranging from 99.5 to 99.9 per cent sulfur, it has a fineness of the order of 200 mesh and is considerably finer than flowers of sulfur or than sulfur ground in the absence of peptizing agents. Its solubility in carbon disulfide is substantially 95 r cent showing the substantial absence of amorphous sulfur, it has a fragmental particle structure and readily adheres to foliage and other objects when dusted thereon.
In my acknowledged copending application I described the use of peptizing agents having tanning properties, such as tannic acid and sulfite waste liquor. These peptizing agents are better for producing the desired results than any others with which I am acquainted. However, for certain purposes, other peptizing or wetting agents may be employed in making the products of the present invention. These include saponin, gelatin, casein and the like. When sulfur is wet ground in the presence of these agents and the resulting sulfur pulp is washed for their removal and then dried, a highly valuable new sulfur product is produced having the descriped properties. When these peptizing agents are employed instead of tannin or sulfite waste liquor moisture, of high insulating value and proof their use disadvantageous from an economic standpoint.
In my acknowledged copending application I have described the making of a cellulose pulp article containing immiscible sulfur uniformly distributed within the article. -As there stated, sulfur in. miscible form containing peptizing agent can be incorporated with wet cellulose pulp in the manufacture of paper; being simply added to the pulp and stirred. Pulp board or paper can, for example, be made by suspending sulfur in the water used for paper or pulp board making and otherwise proceeding exactly as usual. The wet sheet or board can then be washed with water. This removes the peptizing agent and restores the sulfur to its normal water-repellent condition. After the paper or board is thus man-' ufactured and dried, the sulfur can then be fused in place. It is a convenient operation to incorporate sulfur in wet paper pulp, making dry pulp board and then hot stamp to make finished articles. The sulfur melts in stamping and sets in cooling. In this way, it is possible to make articles of waterproof nature, non-absorbent of against mildew, bacterial action, etc. The porosity of the product is not necessarily destroyed.
A better method of producing a cellulose article impregnated with the sulfur of my invention and free from peptizing agents is to wash the mixture of sulfur pulp and wetting agent for removal of the latter prior to admixture with the paper pulp. Washing by decantation is usually satisfactory but a fine filter may be employed if desired. Special solvents may be used ,for removal of the peptizing agents.
One method ofproceeding tomake the cellulose pulp articles of the present invention is to take ordinary ground sulfur of commerce. mix it with a peptizing or wetting agent in order to make it readily wet with water, then wash out the wetting agent and add the still miscible product to paper pulp. The use of the wetting agent in this process overcomes the difliculties involved in mixing untreated sulfur with water and with paper pulp. In order to stick to wet cellulose fibres sulfur particles must be readily wet with water. But untreated ground sulfur is highly water repellent. It does not effectively stick to the fibres; hence the value of my treatment.
As long as the sulfur pulp remains wet it retains its miscibility with water. It is therefore added to the paper pulp in the wet state. The sulfur particles, freed from the peptizing agent, tend to cling to the cellulose fibres. When the peptizing agent is present this adhesiveness is greatly reduced. The adhesiveness of my present product is an important factor in overcoming the losses of sulfur usually encountered when fine sulfur is added in the paper making operation. In mafing pulp articleslgenerally add the washed sulfur pulp eithento the heaters or in the Jordans where it can be thoroughly mixed with the paper pulp prior to passing to the Fourdrinier ma chine. The sulfur is usually added in amounts equal to from about 5 to 200 per cent by weight of the finished product.
When the pulp article is dried during the finishing steps the sulfur recovers its normal water repellent state. The article is then thoroughly waterproof. Containers made of pulp board can be employed even for carrying liquids. When a wetting agent is present in the pulp board it is only partially waterproof.
I have found that, if sheeted pulp articles are made of laminated structure, that is of several plies, only one of these plies requires impregnation with the sulfur to produce substantial waterproofness. There is another important advantage gained by impregnating only part of a multi-ply sheet. I have found that, if one or more of the plies is free from sulfur the structure as a whole retains a considerable degree of flexibility even after hot-pressing, while if all plies are impregnated the sheet is stiff and more subject to fracture upon bending. In making a multi-ply article I therefore usually leave at least one of the plies free from sulfur. One desirable structure is an article the outer plies of which are impregnated while at least one of the interior plies or the core is free from sulfur. Another advantageous structure is a compound sheet having a corrugated core impregnated with sulfur while the outside sheets are free from sulfur. These structures are, of course, advantageous even though the sulfur is not free from peptizing agents and is not of 200 mesh fineness.
impregnation with sulfur makes a corrugated structure of about double the strength it would otherwise have. The strength of an impregnated pulp article increases rapidly with sulfur content up to about 15 per cent and more gradually from there on up to about 50 per cent by weight. Above 50 per cent the increase in strength is practically negligible. I therefore usually employ a sulfur content ranging between 15 to 50 per cent and usually not above 25 per cent.
In all cases except those applications wherein the sulfur is used mainly as a fungicide, I hotpress the pulp articles in order to melt the sulfur in place. This can be accomplished by the use of calender rolls through which the impregnated sheet maybe passed or by the use of heated molds, etc. The impregnated paper pulp may be pressed into any shape desired;
In one specific operation I prepared a sulfur pulp free from peptizing agent by grinding a one ton batch of commercial pulverulent sulfur in a so-called colloid mill. Prior to grinding there was mixed with the sulfur approximately 0.75 ton of water and 1 gallon of a 30 B. commercial preparation of sulfite waste liquor containing about 50 per cent of solids. This mixture was run through the colloid mill and into a large settling tank equipped with an agitator. The ground sulfur pulp was allowed to settle for 1 hour and the supernatant liquor was drawn off. About 1500 pounds of water were run into the tank, the agitator was started to thoroughly mix the material and then the mix was allowed to settle for 1 hour, after which the supernatant liquor was again decanted off. This washing process was repeated 3 times until the proportion of sulfite waste liquor remaining in the sulfur pulp was reduced to less than .01 per cent by weight of solids based on the sulfur. This sulfur pulp was then introduced into the Jordans of a paper mill in amount to give about 25 per cent by weight in the finished product. The sulfur and paper pulp mixture was then passed to the Fourdrinier machine where it was made into sheet card board. After passing the drying rolls the sheet was passed through a pair of corrugated calender rolls maintained at a temperature of about 260 F. or sufiicient to melt the sulfur in situ. To the corrugated sheet thus formed there was applied on both sides sheets of non-impregnated paper in the usual manner. The resulting composite sheet was found to have a strength of about double a similar sheet without a sulfur impregnated core. The impregnated sheet was also waterproof. It was made into a carton suitable for transporting fish or other like materials.
While I have described several embodiments and in some detail, various modifications in the.
procedure outlined may be made without departing from the spirit and scope of my invention. In making the sulfur product of my present invention any of the peptizing agents mentioned may be utilized in the grinding step. It is also possible to employ any of these sulfur products in the production of the cellulose articles of my invention. Various proportions of sulfur may be used in making these articles. Other modifications which fall within the scope of the following claims will be immediately evident to those skilled in the art.
What I claim is:
1. As a new material, a hot-pressed cellulose product having uniformly dispersed therethrough from 5 to 200 per cent of sulfur in water repellent form and having a fineness of the order of 200' mesh, the said product being substantially free from peptizing agents for sulfur.
2. In the manufacture of cellulose pulp articles, the process which comprises wet grinding sulfur in the presence of a peptizing agent having tanning properties to an extreme degree of fineness, removing the peptizing agent from the resulting sulfur pulp, mixing the sulfur with paper pulp, forming the pulp mixture into shape and hot pressing.
3. The process of claim 2 wherein the peptizing agent is one having tanning properties.
4. The process of claim 2 wherein the peptizing agent is sulfite waste liquor.
5. The process of claim 2 wherein the sulfur is ground to a fineness of the order of 200 mesh.
6. In the manufacture of cellulose pulp articles the process which comprises mixing ground sulfur with a wetting agent, washing out the wetting agent, mixing the resulting miscible product while still wet with paper pulp, forming the pulp mixture into shape and hot pressing.
7. As a new material, a hot-pressed cellulose product having uniformly dispersed therethrough from 15 to 50 per cent of fine, water repellent sulfur, the said fine sulfur being substantially free from amorphous sulfur and having a fineness of the order of 200 mesh, the said product being substantialy free from peptizing
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US642819A US1939404A (en) | 1932-11-15 | 1932-11-15 | Manufacture of pressed cellulose articles |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US642819A US1939404A (en) | 1932-11-15 | 1932-11-15 | Manufacture of pressed cellulose articles |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1939404A true US1939404A (en) | 1933-12-12 |
Family
ID=24578157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US642819A Expired - Lifetime US1939404A (en) | 1932-11-15 | 1932-11-15 | Manufacture of pressed cellulose articles |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1939404A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2486601A (en) * | 1946-04-27 | 1949-11-01 | Jesse M Irwin | Process of producing a molding powder |
| US2675312A (en) * | 1950-09-29 | 1954-04-13 | Lammers Gerald James | Loaded paper |
-
1932
- 1932-11-15 US US642819A patent/US1939404A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2486601A (en) * | 1946-04-27 | 1949-11-01 | Jesse M Irwin | Process of producing a molding powder |
| US2675312A (en) * | 1950-09-29 | 1954-04-13 | Lammers Gerald James | Loaded paper |
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