US1866917A - Manufacture of cellulose material from hemp fibers - Google Patents
Manufacture of cellulose material from hemp fibers Download PDFInfo
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- US1866917A US1866917A US347728A US34772829A US1866917A US 1866917 A US1866917 A US 1866917A US 347728 A US347728 A US 347728A US 34772829 A US34772829 A US 34772829A US 1866917 A US1866917 A US 1866917A
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- United States
- Prior art keywords
- cellulose
- fibers
- hemp
- fiber
- cellulosic
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- Expired - Lifetime
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- 239000000835 fiber Substances 0.000 title description 50
- 229920002678 cellulose Polymers 0.000 title description 46
- 239000001913 cellulose Substances 0.000 title description 36
- 244000025254 Cannabis sativa Species 0.000 title description 25
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 title description 25
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 title description 25
- 235000009120 camo Nutrition 0.000 title description 25
- 235000005607 chanvre indien Nutrition 0.000 title description 25
- 239000011487 hemp Substances 0.000 title description 25
- 238000004519 manufacturing process Methods 0.000 title description 13
- 239000000463 material Substances 0.000 title description 10
- 235000010980 cellulose Nutrition 0.000 description 38
- 238000011282 treatment Methods 0.000 description 16
- 229920000297 Rayon Polymers 0.000 description 14
- 238000000034 method Methods 0.000 description 13
- 238000005406 washing Methods 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000000126 substance Substances 0.000 description 9
- 229920000742 Cotton Polymers 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 8
- 239000012535 impurity Substances 0.000 description 8
- 239000002964 rayon Substances 0.000 description 8
- 239000002904 solvent Substances 0.000 description 8
- 230000032050 esterification Effects 0.000 description 7
- 238000005886 esterification reaction Methods 0.000 description 7
- 229920003043 Cellulose fiber Polymers 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- 235000019198 oils Nutrition 0.000 description 6
- 238000004061 bleaching Methods 0.000 description 5
- 230000007935 neutral effect Effects 0.000 description 5
- 239000002023 wood Substances 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 229920002488 Hemicellulose Polymers 0.000 description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- RGCKGOZRHPZPFP-UHFFFAOYSA-N alizarin Chemical compound C1=CC=C2C(=O)C3=C(O)C(O)=CC=C3C(=O)C2=C1 RGCKGOZRHPZPFP-UHFFFAOYSA-N 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 241000234295 Musa Species 0.000 description 2
- 239000000020 Nitrocellulose Substances 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 230000003292 diminished effect Effects 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 229920001220 nitrocellulos Polymers 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000557626 Corvus corax Species 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 229920002522 Wood fibre Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- -1 alkali metal salts Chemical class 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229920003086 cellulose ether Polymers 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 150000002895 organic esters Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002195 soluble material Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
- 239000002025 wood fiber Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S162/00—Paper making and fiber liberation
- Y10S162/03—Wetting agent
Definitions
- This invention relates to the industrial treatment and utilization of the fibers for the production of purified cellulose therefrom, of various kinds, species or'grades of hemp said cellulose in the purified state,
- rayon or artificial filaments is understood to comprise those esters and ethers of cellulose, which, after being placed. in solution, are afterwards forced through minute orifices into a liquid or other medium whereby they are precipitated into a hydrated cellulose with decomposition of the cellulose compound or cellulose ester, or deposited as the cellulose ester by the volatilization of a volatile solvent.
- rayon produced from viscose and cuprammonium cellulose would be included from the second group, would be included the nitrocellulose filaments which are afterwards denitrated, the organic esters of cellulose such as acetated cellulose, and the alkyland aryl-celluloses,
- hemp fibers there appears to be a looseness in the use of the word hemp by some writers. Hemp in this invention is intended to cover hemp fibers, as stated on page 190 of Report No. 9, U. S. Department of Agriculture, A descriptive catalogue of useful fiber plants of the world, by Charles Richards Dodge, published at the Government Printing Oflice, Washington, D. C., 1897. Of these hemp fibers therein listed, I have obtained especially useful cellulosic fibers for the production of rayon and artificial filaments by the use of fibers and other components from the hotanical group Musa, of which Mum temtz'lz's and Musa sapz'en-tum are perhaps most well known. the partially purified state, whether that pu- Hemp fibers in general, when in Application filed March 16, 1929. Serial No. 347,728.
- a relatively long fiber cotton upon nitration will produce a cellulose ester, which when dissolved and the solvent removed therefrom, forms a film or filament of greater tensile strength and other desirable physical qualities than will a relative ly much shorter cotton fiber (such as linters or-fiy).
- This difference has been found to be due in a measure to the greater length and strength of the individual cellulose cell in the longer fiber cotton.
- hemp fiber possesses unusual strength when compared with wood fiber or cott-oncellulose fiber, all in the purified state.
- cotton cellulose is more obdurate to treatment than is wood cellulose, and purified hemp fiber cellulose than is cotton cellulose, especially when subjected to the various steps involved in esterification primarily for rayon production, and corresponding variations ,and adJustment in chemicals, concentration,
- This invention is primarily concerned with the respective steps in treatment of the fibers commercially classified under the general heading of hemp as heretofore indicated, for the preparation therefrom of a cellulosic material high in alphacellulose, and relatively low in hemicellulose and other inferior cellulosic bodies, and admirably adapted for the transformation into ravens and other artificial filaments, films, etc. by virtue of its high alphacellulose or resistant cellulose content, and virtue of practical absence of inferior of cellulose and cellulosic bodies.
- the hemp has been submitted to a retting operation, is scutched or homeled, or a combination of two or more of the operations has been applied to it.
- the boiloif operation is continued from 3 to 8 hours depending upon the comparative amounts of impurities in the fibers or fibrous aggregates, after which the boil-off liquor is allowed to drain oil, and clear Water added, and heat applied, and this alternate addition of water, heating, and discarding of the wash water is continued until the wash waters are practically colorless, and a sample of material when extracted in a Soxhlet'or other suitable apparatus with a chemical-such as ether, gives practically no extractive.
- the fibers are, stillxin the Wet condition, passed through friction rollers which tend to break down and disintegrate the fibrous bundles 'orimasses, the fibers being subjected in an ,elutriating manner, whereby intercellular and encrusting'material is disintegrated, and floats off in the water. fibers are then hydro-extracted, and submitted to an electrolytic (preferably) chlorine bleach, care being taken that the fibers are not exposedto the atmospheretduring the bleaching and subsequent acidifying operation, to minimize formation of oxycellulose and other oxidation cellulosic compounds.
- electrolytic preferably
- One or more of the foregoing steps may be prolonged, shortened or repeated, depending upon the comparative refractoriness of i the hemp fiber to be purified, or the concen- The trations of the baths may be increased or diminished, as conditions may arise.
- the absorption of the cellulose is shown by the fact that a pledget of the same placed upon the surface of water at room temperature will be immersed by its own weight, usually in less than 30 seconds.
- Alphacellulose determinations made on various samples indicated that it was practically pure alphaor resistant cellulose, and with but negligible amounts of other cellulosic materials present, while the original tensile strength of the fiber was substantially conserved.v
- the color of the-individual fibers varies from a light straw color to pure White, depending upon the thoroughness and care exercised in the purification treatments.
- a process for treating hemp fibers for the isolation therefrom of alphacellulose in a highly purified condition comprising mechanically disintegrating said fibers, removing impurities therefrom by treatment with a hot solution of alkalinehydi'oxide, alkaline silicate and a softening body, removing reac'tants and products of decomposition by Washing, bleaching the same in the absence o'fthe air, and Washing free from chemicals, substantially as herein set forth.
- a process for treating hemp fibers comprising mechanically disintegrating the same, removing therefrom alkali-soluble matter by boiling in Water, removing water-soluble components by Washing and bleaching, finally removing reacting chemicals by washing until a neutral mass is obtained, as herein described.
- a process for the production of cellulosic material relatively high in alpha-cellulose and relatively low in hemicellulosicand other inferior cellulosic bodies from hemp .fiber comprising boiling the original fibers in an aqueous solution containing the hydroxide and silicate of an alkali metal until all alkali-soluble material has become water soluble, washing until neutral, and removing coloring matter therefrom by Ways now known, as herein set forth.
- a process for the treatment of hemp fibers to obtain therefrom cellulose of maximum suitability for esterification purposes comprising treating the hemp fiber suitably subdivided with a saponified vegetable oil containing an excess of alkali until non-cellulosic bodies have been saponified, emulsified or otherwise rendered water-soluble or removable by washing, eliminating said impurities by a washing treatment, decolorizing the purified cellulose, and washing to a neutral reaction, substantially as herein set forth.
- a process for the treatment 'of hemp fibers to obtain therefrom purified resistant cellulose comprising treating the finely subdivided fibers with a non-solvent of cellulose containing alkali hydroxide and silicate which is at the same time a solvent or emulsifier of the non-cellulosic impurities therein, removing said non-cellulosic bodies by a Washing process in water with the minimum of'degradation of the cellulosic portion, then bleaching and washing to a neutral reaction the purified cellulose so obtained, asrset forth herein.
- a process for the purificationof hemp fibers from the non-cellulosic 'bodies normally contained therein comprising treating said fibers preferably in a fine state ofsubdivision with an emulsifying and saponifying agent containing alkaline metal 40 hydroxide and silicate, and which; is at the same time a solvent of hemicelluloses and a non-solvent of alphacellulose, continuing said treatment in a hot aqueous solution until the alphacellulose has been separated from its impurities, washing to remove said impurities, bleaching the alphacellulose thus formed to increase its porosity and receptiveness for esterifying chemicals, then washing until neutral, substantially as herein set forth.
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
Patented July 12, 1932 UNITED STATES PATENT OFFICE EDWAJRD GHAUNCEY WORDEN, 151, OF MILIBURN, NEW JERSEY, ASSIGNOR TO HANSON 03TH N YORK, N. Y. A FIRM GOMPOSED or GEARLESD. ORTH, sn, AND CHARLES 1). 0mm, an, AND MICHAEL J. smrrn: 1
MANUFACTURE OF CELL'ULOSE MATERIAL FROM IEEMP FIBERS 1T0 Drawing.
This invention relates to the industrial treatment and utilization of the fibers for the production of purified cellulose therefrom, of various kinds, species or'grades of hemp said cellulose in the purified state,
having een found highly advantageous forthe manufacture of rayon, as more specifically set forth in my co-pending application, Serial No. 347,457 of March 15, 1929, for manufacture of rayon from hemp fiber. By rayon or artificial filaments is understood to comprise those esters and ethers of cellulose, which, after being placed. in solution, are afterwards forced through minute orifices into a liquid or other medium whereby they are precipitated into a hydrated cellulose with decomposition of the cellulose compound or cellulose ester, or deposited as the cellulose ester by the volatilization of a volatile solvent. Of the first group would be included rayon produced from viscose and cuprammonium cellulose. From the second group, would be included the nitrocellulose filaments which are afterwards denitrated, the organic esters of cellulose such as acetated cellulose, and the alkyland aryl-celluloses,
{.ypified by ethylcellulose and benzyl-celluose.
There appears to be a looseness in the use of the word hemp by some writers. Hemp in this invention is intended to cover hemp fibers, as stated on page 190 of Report No. 9, U. S. Department of Agriculture, A descriptive catalogue of useful fiber plants of the world, by Charles Richards Dodge, published at the Government Printing Oflice, Washington, D. C., 1897. Of these hemp fibers therein listed, I have obtained especially useful cellulosic fibers for the production of rayon and artificial filaments by the use of fibers and other components from the hotanical group Musa, of which Mum temtz'lz's and Musa sapz'en-tum are perhaps most well known. the partially purified state, whether that pu- Hemp fibers in general, when in Application filed March 16, 1929. Serial No. 347,728.
rification be entirelymechanical or not, are distmgulshed by their great tensile strength, and also by their resistance to-chemical treatment with the minimum of degradation, de-
phacellulose or resistant cellulose, and con-- taining but small amounts of hemicelluloses and other inferior celluloses or cellulosic bodies, which renders purified hemp cellulose, peculiarly adapted to the formation of high strengthartificial filaments, provided the series of treatments or steps to which the cellulosic material is subjected in transformation from. cellulose toartificial filaments, is carried on without serious weakening of the hemp cellulosic structure or strength. 1
In the cellulose ester and cellulose ether art in general, and. the nitrocellulose industry in particular, those who have lived the art, and not merely worked in it, have been aware that in an identical method and procedure of esterification, the initial length and strength of the cellulose fiber to be esterified bears a definite relation tothe strength of the esterified cellulose made therefrom, and this relationship of strength and tenacity is especially exemplified when the esterized cellulose is dissolved and placed in filament or film form from an evaporation therefrom of the volatile solvents contained therein. In other words, where thetensile strength and length offiber of the initial purified cellulose is relatively high, other conditions of treatment being the same, the esterified prod not will be correspondingly high in tensile strength and other desirable characteristics.
That is, they are increased with an increase in strength of the original cellulose from which produced by the esterifying or other process towhich the cellulosic fibers are sub jected, and that the stronger the original purified cellulosic fiber, other conditions remaining substantially the same, the stronger will films and filaments be when the cellulose is transformed into ester form, dissolved and deposited either as a filnrby the removal of solvent, or as a filament by the same procedure, by precipitation, setting, coagulation or otherwise.
That is, a relatively long fiber cotton upon nitration, for example, will produce a cellulose ester, which when dissolved and the solvent removed therefrom, forms a film or filament of greater tensile strength and other desirable physical qualities than will a relative ly much shorter cotton fiber (such as linters or-fiy). This difference has been found to be due in a measure to the greater length and strength of the individual cellulose cell in the longer fiber cotton.
Furthermore, in the production of those cellulose esters represented by the Xanthated celluloses (viscose) it has been noted that the relatively shorter wood cellulose fibers do not admit of the production of a rayon filament of as high tensile strength and other desirable physical characteristics as when the relatively longer purified cotton cellulose fibers have been submitted to the same esterification steps under comparable conditions, and cotton cellulose fiber is being admixed with wood cellulose fiber at the present time for viscose rayon manufacture, in order to increase the tensile strength both in the wet and dry state and other qualities, over that which would normally result if wood cellulose alone be used.
There appears to be a well defined relationship between the length and strength of the original cellulose fiber used for esterification purposes and the tensile strength and other qualities of filaments and films producible therefrom, irrespective of whether the final product is the cellulose ester in the solid form or whether the final product is .a de-esterified filament or film as in viscose and nitrocellulose rayon.
It is conceded that hemp fiber possesses unusual strength when compared with wood fiber or cott-oncellulose fiber, all in the purified state.
Coincidental with an increase in tensile strength of initial purified cellulosic-fiber as used for esterification purposes, usually comes a diminished reactivity, especially to chen'ncal treatments, and adjustments of concentration, avidity ofreactiveness, time factor, temperature, etc. are usually necessary d e to this property, when operating upon celluloses from various origins. This is readily seen at the present time, in endeavors to supplant a portion of the wood cellulose here- I tofore used in viscose rayon production, with an equivalent amount of purified cotton fiber,
usually linters on account of its inexpensiveness.
In general, from a chemical reactive point of view, cotton cellulose is more obdurate to treatment than is wood cellulose, and purified hemp fiber cellulose than is cotton cellulose, especially when subjected to the various steps involved in esterification primarily for rayon production, and corresponding variations ,and adJustment in chemicals, concentration,
product, whether that product be an ester or an ester which has been de-esterified, usually with the production of hydrated cellulose.
This invention. therefore, is primarily concerned with the respective steps in treatment of the fibers commercially classified under the general heading of hemp as heretofore indicated, for the preparation therefrom of a cellulosic material high in alphacellulose, and relatively low in hemicellulose and other inferior cellulosic bodies, and admirably adapted for the transformation into ravens and other artificial filaments, films, etc. by virtue of its high alphacellulose or resistant cellulose content, and virtue of practical absence of inferior of cellulose and cellulosic bodies.
In the illustrative example to follow, it is to be understood that the method of procedure will necessarily vary, as well as the amounts and nature of chemicals used, time, temperature, pressure and concentration factors, depending upon the source from which the hemp was obtained whether from the male or female plant, and the physical condition as to disintegration of the fibers or bundles of fibers, at the time the treatment of purification is commenced.
It is immaterial whether the hemp has been submitted to a retting operation, is scutched or heckled, or a combination of two or more of the operations has been applied to it. I prefer as the first chemical operation (the fiber previously having been placed in physical condition to make it of maximum receptivity to chemical treatment) to boil the fibers or fiber bundles or aggregates with an excess of water containing 3%7% free sodium hydroxide, Q.5%3% alkali silicate and 0.5%- 4% cottonseed oil or other readily saponifiable vegetable or animal oil, or an equivalent amount of the oil already saponified. Satisfactory results have also been obtained by substituting for the saponified oil, the alkali metal salts of the sulfonated oils (i. e. Turkey red oil, alizarin assistant, saponified-sulfonated corn oil, etc.). The fiber is placed in s to a running cold water washing treatment.
a pressure kier, and submitted to heat, preferably at a temperature of around 110 C. circulation being aided, if desired, by means of a circulatory arrangement for pumping continuously the boil-off liquor over the mass of fibers. It has been found that the addition to the boil-off liquor of an amount of soluble water glass is especially beneficial in scouring and removal of intercellular and cementitious material, fats, oil,= wax and similar encrusting and adhering impurities, and tends to leave the fiber in an especially porous and absorptive condition for quick and complete penetration of reagents used in normal esterifying and etherifying processes. The boiloif operation is continued from 3 to 8 hours depending upon the comparative amounts of impurities in the fibers or fibrous aggregates, after which the boil-off liquor is allowed to drain oil, and clear Water added, and heat applied, and this alternate addition of water, heating, and discarding of the wash water is continued until the wash waters are practically colorless, and a sample of material when extracted in a Soxhlet'or other suitable apparatus with a chemical-such as ether, gives practically no extractive.
, The fibers are, stillxin the Wet condition, passed through friction rollers which tend to break down and disintegrate the fibrous bundles 'orimasses, the fibers being subjected in an ,elutriating manner, whereby intercellular and encrusting'material is disintegrated, and floats off in the water. fibers are then hydro-extracted, and submitted to an electrolytic (preferably) chlorine bleach, care being taken that the fibers are not exposedto the atmospheretduring the bleaching and subsequent acidifying operation, to minimize formation of oxycellulose and other oxidation cellulosic compounds.
The'now nearly white fibers are washed until all traces of reactants are removed, and dried at a comparatively low temperature. For ease in manipulation during esterification, and the steps preceding and succeeding it, it is advisable to make the fibers into sheet paper, either along or with admixture thereto.
One or more of the foregoing steps may be prolonged, shortened or repeated, depending upon the comparative refractoriness of i the hemp fiber to be purified, or the concen- The trations of the baths may be increased or diminished, as conditions may arise.
The purified hemp cellulose, as the mean of determinations of several runs, gave figures as follows Per cent Molsture (drying at 105 C.) 6.1 Ether extractive 0.12
Hemicellulose and similar bodies (less than) 1. Ash (inorganic impurities) 0.14
The absorption of the cellulose is shown by the factthat a pledget of the same placed upon the surface of water at room temperature will be immersed by its own weight, usually in less than 30 seconds. Alphacellulose determinations made on various samples indicated that it was practically pure alphaor resistant cellulose, and with but negligible amounts of other cellulosic materials present, while the original tensile strength of the fiber was substantially conserved.v The color of the-individual fibers varies from a light straw color to pure White, depending upon the thoroughness and care exercised in the purification treatments. Inasmuch, however, as rayon filaments are usually bleached, I prefer to submit the cellulose to what is known in the trade as between a threequarters and full bleach, in order to conserve to the maximum, the tensile strength of the individual cellulosic fibers.
I am aware that it is proposed to produce paper from hemp fibers by the addition thereto in a partially purified state of varying amounts of filling and loading materials, sizes, albuminous and other organic and inorganic products to induce specific surface and interior effects in the paper so produced. I lay no claim to this.
But what I do claim and desire to secure by Letters Patent is:
1. A process for treating hemp fibers for the isolation therefrom of alphacellulose in a highly purified condition, comprising mechanically disintegrating said fibers, removing impurities therefrom by treatment with a hot solution of alkalinehydi'oxide, alkaline silicate and a softening body, removing reac'tants and products of decomposition by Washing, bleaching the same in the absence o'fthe air, and Washing free from chemicals, substantially as herein set forth.
2. A process for treating hemp fibers comprising mechanically disintegrating the same, removing therefrom alkali-soluble matter by boiling in Water, removing water-soluble components by Washing and bleaching, finally removing reacting chemicals by washing until a neutral mass is obtained, as herein described.
3. A process for the production of cellulosic material relatively high in alpha-cellulose and relatively low in hemicellulosicand other inferior cellulosic bodies from hemp .fiber, comprising boiling the original fibers in an aqueous solution containing the hydroxide and silicate of an alkali metal until all alkali-soluble material has become water soluble, washing until neutral, and removing coloring matter therefrom by Ways now known, as herein set forth.
4. A process for the treatment of hemp fibers to obtain therefrom cellulose of maximum suitability for esterification purposes, comprising treating the hemp fiber suitably subdivided with a saponified vegetable oil containing an excess of alkali until non-cellulosic bodies have been saponified, emulsified or otherwise rendered water-soluble or removable by washing, eliminating said impurities by a washing treatment, decolorizing the purified cellulose, and washing to a neutral reaction, substantially as herein set forth.
5. A process for the treatment 'of hemp fibers to obtain therefrom purified resistant cellulose, comprising treating the finely subdivided fibers with a non-solvent of cellulose containing alkali hydroxide and silicate which is at the same time a solvent or emulsifier of the non-cellulosic impurities therein, removing said non-cellulosic bodies by a Washing process in water with the minimum of'degradation of the cellulosic portion, then bleaching and washing to a neutral reaction the purified cellulose so obtained, asrset forth herein.
6. A process for the purificationof hemp fibers from the non-cellulosic 'bodies normally contained therein, comprising treating said fibers preferably in a fine state ofsubdivision with an emulsifying and saponifying agent containing alkaline metal 40 hydroxide and silicate, and which; is at the same time a solvent of hemicelluloses and a non-solvent of alphacellulose, continuing said treatment in a hot aqueous solution until the alphacellulose has been separated from its impurities, washing to remove said impurities, bleaching the alphacellulose thus formed to increase its porosity and receptiveness for esterifying chemicals, then washing until neutral, substantially as herein set forth.
In witness whereof I attach my signature hereto.
EDWARD CHAUNCEY woman, 1a.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US347728A US1866917A (en) | 1929-03-16 | 1929-03-16 | Manufacture of cellulose material from hemp fibers |
US420018A US1814106A (en) | 1929-03-16 | 1930-01-10 | Manufacture of cellulose material from musa fibers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US347728A US1866917A (en) | 1929-03-16 | 1929-03-16 | Manufacture of cellulose material from hemp fibers |
Publications (1)
Publication Number | Publication Date |
---|---|
US1866917A true US1866917A (en) | 1932-07-12 |
Family
ID=23364994
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US347728A Expired - Lifetime US1866917A (en) | 1929-03-16 | 1929-03-16 | Manufacture of cellulose material from hemp fibers |
Country Status (1)
Country | Link |
---|---|
US (1) | US1866917A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2651571A (en) * | 1948-06-26 | 1953-09-08 | Howard E St John | Alkaline treating method for obtaining ramie and other fibers |
US2700608A (en) * | 1950-12-27 | 1955-01-25 | Procedes Lourd Soc D Expl Des | Process for degumming vegetable textile fibers |
US4851082A (en) * | 1987-04-22 | 1989-07-25 | Director General Of Agency Of Industrial Science And Technology | Pulping process |
-
1929
- 1929-03-16 US US347728A patent/US1866917A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2651571A (en) * | 1948-06-26 | 1953-09-08 | Howard E St John | Alkaline treating method for obtaining ramie and other fibers |
US2700608A (en) * | 1950-12-27 | 1955-01-25 | Procedes Lourd Soc D Expl Des | Process for degumming vegetable textile fibers |
US4851082A (en) * | 1987-04-22 | 1989-07-25 | Director General Of Agency Of Industrial Science And Technology | Pulping process |
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