US2558066A - Production of alkali cellulose - Google Patents
Production of alkali cellulose Download PDFInfo
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- US2558066A US2558066A US692108A US69210846A US2558066A US 2558066 A US2558066 A US 2558066A US 692108 A US692108 A US 692108A US 69210846 A US69210846 A US 69210846A US 2558066 A US2558066 A US 2558066A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B1/00—Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
- C08B1/08—Alkali cellulose
- C08B1/10—Apparatus for the preparation of alkali cellulose
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- This invention relates to the preparation of alkali cellulose. More particularly, the invention relates to an efficient process, which may be carried out continuously, for the preparation of a uniform alkali cellulose which is suitable for conversion into cellulose derivative, such as sodium cellulose xanthate for use in the viscose process of producting filaments and yarns.
- Alkali cellulose for use in the viscose process should be uniformly reactive with carbon disulfide to form a uniformly xanthated sodium cellulose, and should have a press weight ratio not in excess of 3:1, and preferably of about 2.511, the press weight ratio being the ratio of the weight of the final mass of alkali cellulose to the weight of the original unreacted air-dry cellulose forming that mass.
- the alkali cellulose is obtained by steeping cel lulose material in the form of cut sheets of pressed pulp of definite size, strength and surface characteristics, or as a continuous web supplied in roll form, in an aqueous sodium hydroxide solution, and then pressing the steeped material to remove excess steeping liquor therefrom, after which the alkali cellulose is aged for a period during which it undergoes several changes which are manifested chiefly in an increase in alkalisolubility and a decrease in solution viscosity.
- alkali celluloses produced by usual methods often yield cellulose xanthates of indifferent uniformity characterized by the existence therein of appreciable amounts of partially xanthated cellulosic material commonly referred to as gels.
- the non-uniformity of mercerization and press weight ratio of the alkali celluloses may be considered as due, in large part, to variations in the rate of penetration of the alkali liquor to different parts of the sheet or web of cellulosic material in a given time period, and the tendency of the fibers to absorb the liquid alkali ata slower rate than remaining portions of the pressed pulp, so that the mercerization reaction is not completed simultaneously at all portions of the material.
- the present invention in accordance with which the cellulosic material, in contact with the liquid alkali, is subjected to the radiations of high frequency longitudinal or compressional waves, herein called high frequency sound waves, that is sound waves having frequencies in the upper sonic and ultrasonic frequency ranges, say, frequencies of from abeut'lOOO to a million or more cycles per second.
- the sound waves may be applied to the liquid alkali in which the cellulosic material is im mersed in either sheet form or in the form of a continuous web, or in shredded or disintegrated form, as for instance the waves may be applied directly to the surface of the steeping liquor containing the cellulosic material, to a wall of the steeping vat or vessel, or to both, or
- the cellulosic material may be impregnated with the liquid alkali, and then moved through one or more fields of high frequency sound waves after withdrawal thereof from the steeping vat or immersion vessel before or after, but preferably prior to pressing thereof to separate the excess alkali liquor therefrom, and prior to or subsequent to disintegration into relatively small particles to complete the penetration of the alkali solution uniformly to all portions of the cellulosic pulp,
- the cellulosic material such as wood or cotton pulp in sheet or shredded form, may be deposited on a screen conveyor or the like, sprayed with the caustic, and thereafter moved through a field of high frequency sound waves, or the cellulosic material, in torn or disintegrated condition may be slurried in the alkali liquor and the slurry thus...
- the sheet being continuously passed through a field of high frequency sound waves as it is conveyed through the solution or after its withdrawal from the solution. It is within the scope of this invention to subject the cellulosic material and alkali liquor simultaneously or successively to the radiations of sound waves having different frequencies in the range previously stated, and of diiierent magnitudes while the cellulosic material is passing through the alkali liquor or after it has been withdrawn from the liquor.
- any suitable transducer may be used for converting high frequency electrical waves to sound waves.
- the transducer may be a piezo-electric crystal, a magnetostriction device, or an electromagnetic device.
- Figure 1 is a sectional diagrammatic side elevation of an apparatus suitable for carrying out one embodiment of the invention
- Figure 2 is a similar view illustrating another embodiment-of the invention
- Figure 3 is a diagrammatic side elevation of a further embodiment.
- a sheet of cellulosic fibers 3 is continuously unwound from a supply roll 2 over guide roll I, and is led, at a controlled predetermined rate of speed into and through an aqueous sodium hydroxide solution of appropriate concentration and contained in vessel 5.
- the cellulosic sheet 3 passes under guide rolls 6 and 1 and thence out of the solution.
- the period of contact between the sheet 3 and the solution may be increased by passing the sheet under guide roll 6, over guide roll 8 under roll 1, and thence out of the bath.
- Roller 6 is adjustable vertically so that the length of the path of the sheet through the solution may be altered, as desired.
- a sound generator ll having an associated transmission tube I21 which extends into the alkali liquor in the vessel.
- the bath and the web travelling therethrough, are continuously subjected to the high frequency sound wave radiations.
- the cellulosic sheet is withdrawn from the bath over guide roll 8, through the pressure rollers 9, excess adhering liquid alkali being pressed out of the sheet by rollers 9 and returned to the bath.
- the web withdrawn from the bath may be forwarded directly to a disintegrator or shredder and then aged, or it may be further irradiated with high frequency sound waves, if desired.
- the web impregnated with the liquid alkali is subjected to the high frequency sound wave radiations after it leaves vessel containing the aqueous alkali solution.
- the sound generator II is supported in bracket III on the side of the tank, and transmission tube l2 extends into the path of the web so that the web passes thereover and is subjected directly to the high frequency sound wave radiations.
- the tube l2 also serves to guide Alternatively, the fibrous material may in conventional batch procedures for the production of alkali cellulose.
- Belt I2 is supported by rotating rollers l5, II, and I! and belt H is supported by rotating rollers l8, I9, 20, and 2!, the belts being driven (by means not shown) to travel at the same speed.
- Roller I6 is submerged in the liquid alkali contained in a vat or tank 22.
- Supported above the vat is a sound generator 24 having an associated transmission tube 25 which projects into the bath above roller IE to transmit the high frequency vibrations to the bath.
- the cellulosic material, in torn or disintegrated condition, is carried, by a conveyor belt 28 and fed into the nip of the rolls l5 and IS.
- the cellulosic material is thus carried, between the foraminous belts l3 and I4 through the sound wave field maintained continuously in the bath, and whereby it absorbs the liquid alkali uniformly and at an accelerated rate.
- the liquid treated material leaves the vat through rollers l1 and 2
- a method of producing alkali cellulose of substantially uniform composition which comprises impregnating pressed cellulosic pulp with an aqueous alkali solution while subjecting the pressed pulp and solution to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as such from the sound wave field.
- Method of producing alkali cellulose of substantially uniform composition which comprises immersing pressed cellulosic pulp in an aqueous alkali solution, subjecting the immersed material and solution to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as such from the sound wave field.
- Method of producing alkali cellulose of substantially uniform composition which comprises treating pressed cellulosic pulp with aqueous alkali, thereafter subjecting the treated pulp to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as'such from the sound wave field.
- Method of producing alkali cellulose of substantially uniform composition which comprises continuously moving a mass of pressed cellulosic pulp in contact with an aqueous alkali solution through a field of sound waves having a irequency of at least 1000 cycles per second, and
- Method of producing alkali cellulose of substantially uniform composition which comprises maintaining a field of sound waves having a frequency of at least 1000 cycles per second in an aqueous alkali solution, passing a sheet of pressed cellulosic pulp through said field, and then removing the sheet of impregnated pulp as such from the sound wave field.
- Method of producing alkali cellulose of substantially uniform composition which comprises treating pressed cellulosic pulp with an aqueous alkali solution, continuously moving the treated pulp through a field of sound waves having a frequency of at least 1000 cycles per second and then removing the impregnated pulp as such from the sound wave field.
- Method of producing alkali cellulose of substantially uniform composition which comprises forming a slurry of pressed cellulosic pulp in an aqueous alkali solution, passing the slurry through a field of sound waves having a frequency of at least 1000 cycles per second and then removing the impregnated pulp as such from the sound wave field.
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Description
INVENTOR. FREDERICK C WEDLER Filed Aug. 21, 1946 F C WEDLER PRODUCTION OF ALKALI vCELLULOSE 'June 26, 1951 Patented June 26, 1951 PRODUCTION OF ALKALI CELLULOSE Frederick C. Wedler, Swarthmore, Pa., assignor to American Viscose Corporation, Wilmington, Del., a corporation of Delaware Application August 21, 1946, Serial No. 692,108
7 Claims. (01. 26o 233)' This invention relates to the preparation of alkali cellulose. More particularly, the invention relates to an efficient process, which may be carried out continuously, for the preparation of a uniform alkali cellulose which is suitable for conversion into cellulose derivative, such as sodium cellulose xanthate for use in the viscose process of producting filaments and yarns.
Alkali cellulose for use in the viscose process should be uniformly reactive with carbon disulfide to form a uniformly xanthated sodium cellulose, and should have a press weight ratio not in excess of 3:1, and preferably of about 2.511, the press weight ratio being the ratio of the weight of the final mass of alkali cellulose to the weight of the original unreacted air-dry cellulose forming that mass.
The alkali cellulose is obtained by steeping cel lulose material in the form of cut sheets of pressed pulp of definite size, strength and surface characteristics, or as a continuous web supplied in roll form, in an aqueous sodium hydroxide solution, and then pressing the steeped material to remove excess steeping liquor therefrom, after which the alkali cellulose is aged for a period during which it undergoes several changes which are manifested chiefly in an increase in alkalisolubility and a decrease in solution viscosity.
It is well recognized that, under the usual conditions of manufacture, it is difficult to insure the required uniform mercerization of the cellulose material and the desired constant press weight ratio of the alkali cellulose. The alkali celluloses produced by usual methods often yield cellulose xanthates of indifferent uniformity characterized by the existence therein of appreciable amounts of partially xanthated cellulosic material commonly referred to as gels. The non-uniformity of mercerization and press weight ratio of the alkali celluloses may be considered as due, in large part, to variations in the rate of penetration of the alkali liquor to different parts of the sheet or web of cellulosic material in a given time period, and the tendency of the fibers to absorb the liquid alkali ata slower rate than remaining portions of the pressed pulp, so that the mercerization reaction is not completed simultaneously at all portions of the material.
It is an object of the presentinvention. to provide an improved process for the manufacture of alkali cellulose which is characterized by a uniform composition. Another object is the pro vision of a method for speeding up the rate at which the fibers present in the pressed collulosic pulp absorb the liquid alkali. A further object is the production of an alkali cellulose which, on reaction with carbon disulfide yields a more uniformly xanthated sodium cellulose. A further object is to provide a process for producing alkali cellulose of uniform composition in a comparatively short time.
These and other objectsare accomplished by the present invention, in accordance with which the cellulosic material, in contact with the liquid alkali, is subjected to the radiations of high frequency longitudinal or compressional waves, herein called high frequency sound waves, that is sound waves having frequencies in the upper sonic and ultrasonic frequency ranges, say, frequencies of from abeut'lOOO to a million or more cycles per second. I
The sound waves may be applied to the liquid alkali in which the cellulosic material is im mersed in either sheet form or in the form of a continuous web, or in shredded or disintegrated form, as for instance the waves may be applied directly to the surface of the steeping liquor containing the cellulosic material, to a wall of the steeping vat or vessel, or to both, or
the cellulosic material may be impregnated with the liquid alkali, and then moved through one or more fields of high frequency sound waves after withdrawal thereof from the steeping vat or immersion vessel before or after, but preferably prior to pressing thereof to separate the excess alkali liquor therefrom, and prior to or subsequent to disintegration into relatively small particles to complete the penetration of the alkali solution uniformly to all portions of the cellulosic pulp, Alternatively the cellulosic material such as wood or cotton pulp in sheet or shredded form, may be deposited on a screen conveyor or the like, sprayed with the caustic, and thereafter moved through a field of high frequency sound waves, or the cellulosic material, in torn or disintegrated condition may be slurried in the alkali liquor and the slurry thus...
kali bath, the sheet being continuously passed through a field of high frequency sound waves as it is conveyed through the solution or after its withdrawal from the solution. It is within the scope of this invention to subject the cellulosic material and alkali liquor simultaneously or successively to the radiations of sound waves having different frequencies in the range previously stated, and of diiierent magnitudes while the cellulosic material is passing through the alkali liquor or after it has been withdrawn from the liquor.
In carrying out the invention, any suitable transducer may be used for converting high frequency electrical waves to sound waves. The transducer may be a piezo-electric crystal, a magnetostriction device, or an electromagnetic device.
In the annexed drawing illustrative of the invention, Figure 1 is a sectional diagrammatic side elevation of an apparatus suitable for carrying out one embodiment of the invention, and Figure 2 is a similar view illustrating another embodiment-of the invention, and Figure 3 is a diagrammatic side elevation of a further embodiment.
Referring to Figure l, a sheet of cellulosic fibers 3 is continuously unwound from a supply roll 2 over guide roll I, and is led, at a controlled predetermined rate of speed into and through an aqueous sodium hydroxide solution of appropriate concentration and contained in vessel 5. The cellulosic sheet 3 passes under guide rolls 6 and 1 and thence out of the solution. The period of contact between the sheet 3 and the solution may be increased by passing the sheet under guide roll 6, over guide roll 8 under roll 1, and thence out of the bath. Roller 6 is adjustable vertically so that the length of the path of the sheet through the solution may be altered, as desired. Mounted above the vessel 5, in a bracket i0, is a sound generator ll having an associated transmission tube I21 which extends into the alkali liquor in the vessel. The bath and the web travelling therethrough, are continuously subjected to the high frequency sound wave radiations. The cellulosic sheet is withdrawn from the bath over guide roll 8, through the pressure rollers 9, excess adhering liquid alkali being pressed out of the sheet by rollers 9 and returned to the bath. The web withdrawn from the bath may be forwarded directly to a disintegrator or shredder and then aged, or it may be further irradiated with high frequency sound waves, if desired.
In the embodiment illustrated in Figure 2, the web impregnated with the liquid alkali is subjected to the high frequency sound wave radiations after it leaves vessel containing the aqueous alkali solution. The sound generator II is supported in bracket III on the side of the tank, and transmission tube l2 extends into the path of the web so that the web passes thereover and is subjected directly to the high frequency sound wave radiations. The tube l2 also serves to guide Alternatively, the fibrous material may in conventional batch procedures for the production of alkali cellulose.
Referring to Figure 3 there are shown two endless foraminous belts II and II. Belt I2 is supported by rotating rollers l5, II, and I! and belt H is supported by rotating rollers l8, I9, 20, and 2!, the belts being driven (by means not shown) to travel at the same speed. Roller I6 is submerged in the liquid alkali contained in a vat or tank 22. Supported above the vat is a sound generator 24 having an associated transmission tube 25 which projects into the bath above roller IE to transmit the high frequency vibrations to the bath. The cellulosic material, in torn or disintegrated condition, is carried, by a conveyor belt 28 and fed into the nip of the rolls l5 and IS. The cellulosic material is thus carried, between the foraminous belts l3 and I4 through the sound wave field maintained continuously in the bath, and whereby it absorbs the liquid alkali uniformly and at an accelerated rate. The liquid treated material leaves the vat through rollers l1 and 2| and is discharged into a hopper 23 from which it drops onto a conveyor belt 21 on which it is carried from the vicinity of the bath. Excess liquid is squeezed out of the material by the action of rollers l1 and 2! and is returned to the vessel 22.
Under the influence of the extremely rapid longitudinal alternate waves of compression and rareiaction to which the cellulosic material and liquid alkali are subjected, and due to the cavitation eifect of the waves, the rate of diffusion of the alkali solution through the material is greatly accelerated, with consequent increase in the rate at which the fibers present in the, pulp absorb the alkali solution, so that, in a given time of contact between the cellulosic material and alkali solution, all portions of the pulp absorb and react chemically with a sufficient quantity of sodium hydroxide to produce the desired reaction which is uniform at all portions of the material treated.
Variations and modifications may be made in carrying out the invention, without departing from the spirit and scope thereof, as defined by the appended claims.
I claim:
1. A method of producing alkali cellulose of substantially uniform composition which comprises impregnating pressed cellulosic pulp with an aqueous alkali solution while subjecting the pressed pulp and solution to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as such from the sound wave field.
2. Method of producing alkali cellulose of substantially uniform composition which comprises immersing pressed cellulosic pulp in an aqueous alkali solution, subjecting the immersed material and solution to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as such from the sound wave field.
3. Method of producing alkali cellulose of substantially uniform composition which comprises treating pressed cellulosic pulp with aqueous alkali, thereafter subjecting the treated pulp to sound wave radiations having a frequency of at least 1000 cycles per second, and then removing the impregnated pulp as'such from the sound wave field.
4. Method of producing alkali cellulose of substantially uniform composition which comprises continuously moving a mass of pressed cellulosic pulp in contact with an aqueous alkali solution through a field of sound waves having a irequency of at least 1000 cycles per second, and
then removing the impregnated pulp as such from the sound wave fleld.
5. Method of producing alkali cellulose of substantially uniform composition which comprises maintaining a field of sound waves having a frequency of at least 1000 cycles per second in an aqueous alkali solution, passing a sheet of pressed cellulosic pulp through said field, and then removing the sheet of impregnated pulp as such from the sound wave field.
6. Method of producing alkali cellulose of substantially uniform composition which comprises treating pressed cellulosic pulp with an aqueous alkali solution, continuously moving the treated pulp through a field of sound waves having a frequency of at least 1000 cycles per second and then removing the impregnated pulp as such from the sound wave field.
7. Method of producing alkali cellulose of substantially uniform composition which comprises forming a slurry of pressed cellulosic pulp in an aqueous alkali solution, passing the slurry through a field of sound waves having a frequency of at least 1000 cycles per second and then removing the impregnated pulp as such from the sound wave field.
FREDERICK C. WEDLER.
REFERENCES CITED The following references. are of record in the flle of this patent:
UNITED STATES PATENTS Number Name Date 1,858,017 Lilienfeld May 10, 1932 2,005,811 Steimmig June 25, 1935 2,079,313 Clary May 4, 1937 2,138,051 Williams Nov. 29, 1938 2,163,649 Weaver June 27, 1939 2,293,840 Lignian Aug. 25, 1942 FOREIGN PATENTS Number Country Date 423,382 Canada Got. 24, 1944 OTHER REFERENCES a Marinesco, Eflects Thermiques et chimiques des Ultra-Sons?
Claims (1)
- 7. METHOD OF PRODUCING ALKALI CELLULOSE OF SUBSTANTIALLY UNIFORM COMPOSITION WHICH COMPRISES FORMING A SLURRY OF PRESSED CELLULOSIC PULP IN AN AQUEOUS ALKALI SOLUTION, PASSING THE SLURRY THROUGH A FIELD OF SOUND WAVES HAVING A FREQUENCY OF AT LEAST 1000 CYCLES PER SECOND AND THEN REMOVING THE IMPREGNATED PULP AS SUCH FROM THE SOUND WAVE FIELD.
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Application Number | Priority Date | Filing Date | Title |
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US692108A US2558066A (en) | 1946-08-21 | 1946-08-21 | Production of alkali cellulose |
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US692108A US2558066A (en) | 1946-08-21 | 1946-08-21 | Production of alkali cellulose |
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US2558066A true US2558066A (en) | 1951-06-26 |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2699592A (en) * | 1950-08-30 | 1955-01-18 | Du Pont | Treatment of fabrics |
US2742773A (en) * | 1952-03-21 | 1956-04-24 | Kroy Unshrinkable Wools Ltd | Method and apparatus for treating textile goods, loose fibers and like materials |
US2899201A (en) * | 1959-08-11 | Guide and tensioning device for processing | ||
US2967765A (en) * | 1955-11-07 | 1961-01-10 | Wasagchemie Ag | Treatment of cellulosic materials |
US3090666A (en) * | 1959-06-16 | 1963-05-21 | Elastic Fabric Co Inc | Alkaline shrinkage of cotton fabric on vibratory conveyor |
US3211159A (en) * | 1962-04-30 | 1965-10-12 | Engineering & Dev Company Of C | Ultrasonic method for treating natural and synthetic fibers |
US3254424A (en) * | 1963-07-23 | 1966-06-07 | Engineering & Dev Company Of C | Apparatus for drying and treating hair or other fibers via ultrasonics |
US4163840A (en) * | 1975-05-09 | 1979-08-07 | Fiber Associates, Inc. | Process and apparatus for making alkali cellulose in sheet form |
US4269973A (en) * | 1975-05-09 | 1981-05-26 | Fiber Associates, Inc. | Process and apparatus for making alkali cellulose in sheet form |
US4275195A (en) * | 1975-05-09 | 1981-06-23 | Fiber Associates | Process and apparatus for expediting the mercerization of alkali cellulose |
US4591485A (en) * | 1983-12-22 | 1986-05-27 | International Paper Company | Method and apparatus for sonicating articles |
US20100279019A1 (en) * | 2009-05-01 | 2010-11-04 | Stephanie Beck | Control of nanocrystalline cellulose film iridescence wavelength |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1858017A (en) * | 1919-08-01 | 1932-05-10 | Lilienfeld Leon | Process of making alkali cellulose |
US2005811A (en) * | 1932-03-07 | 1935-06-25 | Steimmig Franz | Method of preparing and maturing alkali cellulose |
US2079313A (en) * | 1933-10-31 | 1937-05-04 | Paul D Clary | Method for making alkali-cellulose and products therefrom |
US2138051A (en) * | 1933-06-02 | 1938-11-29 | Submarine Signal Co | Means for treating liquids |
US2163649A (en) * | 1935-11-25 | 1939-06-27 | Chester E Weaver | Method and apparatus for utilizing high frequency compressional waves |
US2293840A (en) * | 1939-07-13 | 1942-08-25 | Gen Motors Corp | Impregnating apparatus |
CA423382A (en) * | 1944-10-24 | Philip Ham Garnet | Cellulose disintegration method |
-
1946
- 1946-08-21 US US692108A patent/US2558066A/en not_active Expired - Lifetime
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA423382A (en) * | 1944-10-24 | Philip Ham Garnet | Cellulose disintegration method | |
US1858017A (en) * | 1919-08-01 | 1932-05-10 | Lilienfeld Leon | Process of making alkali cellulose |
US2005811A (en) * | 1932-03-07 | 1935-06-25 | Steimmig Franz | Method of preparing and maturing alkali cellulose |
US2138051A (en) * | 1933-06-02 | 1938-11-29 | Submarine Signal Co | Means for treating liquids |
US2079313A (en) * | 1933-10-31 | 1937-05-04 | Paul D Clary | Method for making alkali-cellulose and products therefrom |
US2163649A (en) * | 1935-11-25 | 1939-06-27 | Chester E Weaver | Method and apparatus for utilizing high frequency compressional waves |
US2293840A (en) * | 1939-07-13 | 1942-08-25 | Gen Motors Corp | Impregnating apparatus |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2899201A (en) * | 1959-08-11 | Guide and tensioning device for processing | ||
US2699592A (en) * | 1950-08-30 | 1955-01-18 | Du Pont | Treatment of fabrics |
US2742773A (en) * | 1952-03-21 | 1956-04-24 | Kroy Unshrinkable Wools Ltd | Method and apparatus for treating textile goods, loose fibers and like materials |
US2967765A (en) * | 1955-11-07 | 1961-01-10 | Wasagchemie Ag | Treatment of cellulosic materials |
US3090666A (en) * | 1959-06-16 | 1963-05-21 | Elastic Fabric Co Inc | Alkaline shrinkage of cotton fabric on vibratory conveyor |
US3211159A (en) * | 1962-04-30 | 1965-10-12 | Engineering & Dev Company Of C | Ultrasonic method for treating natural and synthetic fibers |
US3254424A (en) * | 1963-07-23 | 1966-06-07 | Engineering & Dev Company Of C | Apparatus for drying and treating hair or other fibers via ultrasonics |
US4163840A (en) * | 1975-05-09 | 1979-08-07 | Fiber Associates, Inc. | Process and apparatus for making alkali cellulose in sheet form |
US4269973A (en) * | 1975-05-09 | 1981-05-26 | Fiber Associates, Inc. | Process and apparatus for making alkali cellulose in sheet form |
US4275195A (en) * | 1975-05-09 | 1981-06-23 | Fiber Associates | Process and apparatus for expediting the mercerization of alkali cellulose |
US4591485A (en) * | 1983-12-22 | 1986-05-27 | International Paper Company | Method and apparatus for sonicating articles |
US20100279019A1 (en) * | 2009-05-01 | 2010-11-04 | Stephanie Beck | Control of nanocrystalline cellulose film iridescence wavelength |
US8530005B2 (en) * | 2009-05-01 | 2013-09-10 | Fpinnovations | Control of nanocrystalline cellulose film iridescence wavelength |
US9394481B2 (en) | 2009-05-01 | 2016-07-19 | Fpinnovations | Control of nanocrystalline cellulose film iridescence wavelength |
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