CA1110404A - Process for making a precursor of a solution of cellulose - Google Patents
Process for making a precursor of a solution of celluloseInfo
- Publication number
- CA1110404A CA1110404A CA308,113A CA308113A CA1110404A CA 1110404 A CA1110404 A CA 1110404A CA 308113 A CA308113 A CA 308113A CA 1110404 A CA1110404 A CA 1110404A
- Authority
- CA
- Canada
- Prior art keywords
- cellulose
- amine oxide
- solvent
- tertiary amine
- solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/09—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids
- C08J3/091—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in organic liquids characterised by the chemical constitution of the organic liquid
- C08J3/096—Nitrogen containing compounds
-
- 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
- C08B1/003—Preparation of cellulose solutions, i.e. dopes, with different possible solvents, e.g. ionic liquids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2301/00—Characterised by the use of cellulose, modified cellulose or cellulose derivatives
- C08J2301/02—Cellulose; Modified cellulose
Abstract
PROCESS FOR MAKING A PRECURSOR
OF A SOLUTION OF CELLULOSE
Abstract of the Disclosure A process is provided for making a solid precursor of a solution of cellulose in a tertiary amine oxide by suspending cellulose in a mixture containing a tertiary amine oxide and water under conditions where the amine oxide will dissolve the cellulose and cooling the resulting product to ambient tempera-ture to provide a solid solution of cellulose in amine oxide.
The product may be comminuted to form chips which are adapted to be fed to an extruder or other apparatus for shaping it into a cellulosic article. An organic liquid which is miscible with the tertiary amine oxide and is a non-solvent for the cellulose may be included with the amine oxide-water mixture to improve the up-take of the tertiary amine oxide by the cellulose.
OF A SOLUTION OF CELLULOSE
Abstract of the Disclosure A process is provided for making a solid precursor of a solution of cellulose in a tertiary amine oxide by suspending cellulose in a mixture containing a tertiary amine oxide and water under conditions where the amine oxide will dissolve the cellulose and cooling the resulting product to ambient tempera-ture to provide a solid solution of cellulose in amine oxide.
The product may be comminuted to form chips which are adapted to be fed to an extruder or other apparatus for shaping it into a cellulosic article. An organic liquid which is miscible with the tertiary amine oxide and is a non-solvent for the cellulose may be included with the amine oxide-water mixture to improve the up-take of the tertiary amine oxide by the cellulose.
Description
4~3~
This invention relates generally to regenerated cellulose and more particularly to a process for preparing a solid cellulosic-amine oxide material which can be used for making shaped cellulosic articles such as fibers and filaments.
A process for dissolving cellulose in a tertiary amine oxide is disclosed by Graenacher et al in U.S. Patent No.
This invention relates generally to regenerated cellulose and more particularly to a process for preparing a solid cellulosic-amine oxide material which can be used for making shaped cellulosic articles such as fibers and filaments.
A process for dissolving cellulose in a tertiary amine oxide is disclosed by Graenacher et al in U.S. Patent No.
2,179,181. In accordance with the disclosed process from 7 to 10% by weight of cellulose is dissolved in 93 to 90% by weight of a tertiary amine oxide to form a viscous solution which is poured or spun into an aqueous precipitating bath to precipitate the cellulose. The tertiary amine oxides suitable for practic-ing the disclosed process con-ta.in fourteen or less carbon atoms and may be an oxide o~ a tri~lkyl am:ine or of an alkylcyclo-~ll:Lphatic tertiary amine. As :Ls apparent Erom the working ex-amples of the patent, the resulting solution has the disadvant-age of having a low solids content and a high viscosity.
Another process for dissolving cellulose or other com-pounds having strong intermolecular hydrogen bonding in a tertiary amine oxide is disclosed by Johnson in U.S. Patent No.
Another process for dissolving cellulose or other com-pounds having strong intermolecular hydrogen bonding in a tertiary amine oxide is disclosed by Johnson in U.S. Patent No.
3,447,939. A cyclic mono (N-methylamine-N-oxide) compound such as N-methylmorpholine-N-oxide is used as the solven-t. The solu-tion can be used in chemical reactions involving the dissolved compound or to precipitate the cellulose to form a film or fila-ment. In accordance with the process the solution is maintained as a liquid until it is used. The resulting solutions have much the same disadvantages of those prepared by the process disclosed in U.S. Patent No. 2,179,181 because they are also of low solids content and have a high viscosity.
In accordance with the process disclosed in U.S. Patent No. 3,508,941, two or more diEferent polymers are dissolved in a cyclic mono (N-methylamine-N-oxide) compound and are precipi-tated together to produce a bi-component polymer mixture. A
diluent such as dimethyl sulfoxide, N-methyl-pyrrolidone or sulfo-lane may be added to the solution to reduce its-viscosity. As indicated by the examples set forth in the patent, only solid solutions having low percentages of oollulose can be prepared when cellulose is one of the compounds used in the preparation of the solution.
It is an object of this invention to provide a process for making a solid cellulosic product which is adapted to be heated to prepare a solution of cellulose in a tertiary amine oxide. Another object of -the invention is -to provide a chip or similar granular cellulosic product which can be heatecl alone to Eorm a solut:ion of cellulose in an amine oxide which iE~ suitable ~or shaping and coayulating the cellulose. Another object of the invention is to provide a process for making a cellulosic product which can be comminuted, stored and otherwise treated as a solid material and can be heated later to convert the product into a solution of cellulose which is adapted Eor shaping into a cellu-losic article such as by extrusion or spinning. A more specificobject of the invention is to provide a cellulos:ic product which can be converted into a solution of cellulose in a tertiary amine oxide which has a higher solids content than the amine oxide solutions of the above-discussed prior art. A still more speci-fic object of the invention is to provide a precursor of a solu-tion of cellulose in a tertiary amine oxide which is a solid at ambient temperatures but becomes a solution adapted to be ex-truded or spun when heated to a temperature above ambient.
The foregoing objects and others are accomplished in accordance with this invention, generally speaking, by providing a process wherein cellulose is mixed with a liquid containing ..
a tertiary amine oxide and a liquid non-solvent containing water which assists in intimately associating the tertiary amine ox-ide with the fibers of the cellulose to facilitate absorption of the tertiary amine oxide, the resulting mixture is maintained ~:
at a temperature where the cellulose dissolves in the tertiary amine oxide until a solution is obtained and is cooled to form a solid solution suitable for shaping into a cellulosic article such as by spinning or extrusion. The non-solvent may be water -.
alone or a mixture of water and an organic non-solvent which is compatible with the tertiary amine oxide, water and cellulose.
It is preEerred to use only the calculated amount oE tertiary amine oxide necessary to complete the dissolution of the cellu-lose under extrusion conditions of heat and pressure. However, an excess of water, say 18-30% by weight of the amine oxide sol-vent-non-solvent system is desirable in forming a solid solution because the excess enhances the uniformity of distribution of the solvent throughout the cellulose and reduces the time neces-sary to complete the dissolution. If an organic non-solvent is used, dissolution i9 brought about in an evacuated vessel with removal of the organic non-solvent and any excess water that may be present. The solid solution may be comminuted to Eorm chips or other particles suitable for feeding to an extruder or other device for redissolving the chip by the application of heat and/or pressure and shaping the melt into a cellulosic article.
In one embodiment of the invention, cellulose is mixed with a liquid solution of a tertiary amine oxide and liquid non-solvent for cellulose in such proportions and at a temperature where the cellulose absorbs tertiary amine oxide and non-solvent and substantially completely swells in the tertiary amine oxide.
?9~
It is believed that the water and non-solvent cause the fibers of the cellulose to swell and thereby facilitate uniform and rapid wetting of the cellulose throughout its mass by the liquid con-taining the tertiary amine oxide prior to dic,solution of the cellulose which takes place on removal of the non-solvent. The non-solvent may be water or it may be a mixture of water and organic non-solvent. A slurry of the cellulose, amine oxide solvent and non-solvent is made and a portion of the non-solvent is removed therefxom by mixing under vacuum at an elevated tem-perature until solution occurs. Preferably, the cellulose-amine oxide-non-solvent mixture is heated to a temperature oE about 70C. or higher during mixing to accelerate swelling and dis-solution of the cellulose. At low concentrations of cellulose, e.g. 10~, solution will occur when the water content (based on total cellulose, solvent and water) reaches the range of about 10-15% (depending upon the amine oxide employed) (all of an organic non-solvent will have been first removed). At higher concentrations of cellulose, e.g. 20-30~, solution will occur when the water content, after removal of any organic amine non-solvent, reaches about 2-9%.
The resulting solution is cooled until solid and may then be comminuted such as by grinding or chopping to form fragments or chips which are suitable for extrusion, spinning, molding or the like. They may be stored for later conversion into a solution or they may be heated immediately to form a solution of cellulose in a tertiary amine oxide and water and shaped.
The chip product of the invention may be used for mak-ing a shaped cellulose product by heating the solid cellulose con-taining absorbed tertiary amine oxide and water to a tempera-ture where the cellulose dissolves in the tertiary amine oxideand removing the tertiary amine oxide while shaping the solution.
The solid solution produced by the process of the inven-tion is a solid cellulosic product containing amine oxide and some water which, when heated, will produce a melt adapted for shaping. One of the advantages of the process of this invention is that the water or water-organic non-solvent mixture mixed with the tertiary amine oxide assists in transpoxting the tertiary amine oxide to the fibers and assists in uniformly dispersing the amine oxide in the cellulose. The use of the non-solvent reduces the time necessary to transport and uniEormly d:isperse the am:ine oxide throughout the cellulose. The chip pxoduct can be shaped by merely he~ting it su~ficiently to provide an ex-trudable solid raw material. The invention thus provides a method for making a solid raw material which is complete in it-self for the extrusion of cellulose film or for spinning cellu-lose fibers and yarns. The use of a non-solvent, whether water alone or a water-organic non-solvent system, assists in achieving a homogeneous solution by slowing down the dissolution so that amine oxide is absorbed uniformly.
It has been found that cellulose sheet or shreads sus-pended in a tertiary amine oxide and water or tertiary amine ox-ide, water and organic non-solvent will dissolve when the sus-pension is heated with simultaneous removal of any organic non-solvent and any excess water present in the suspension to form a high solids solution which can be cooled to form a solid solution adapted to be comminuted to form chips or the like.
l'he organic non-solvent is removed during mixing or dissolution at any temperature which permits efEicient and rapid removal of the solvent under vacuum. With most non-solvents the -temperature may be from about 70C. to about 95C. during non-solvent removal. The non-solvent may be removed under vacuum at a pressure of as low as 0.01 mm of mercury.
The solid product obtained by cooling down the solwtion can be transferred immediately to suitable equipment for shaping it into a regenerated cellulose product or it can be stored until some later date. The solid solution is substantially free from unabsorbed liquid when it is cornminuted to form chips or the like.
The relative proportions of cellulose, water, amine oxide and liquid organic non-solvent for cellulose wh:ich are mlxed together may be ~aried broacll~ depending upon the composi-tion desired for the product as :long as suf~icient amine oxide-water mixture will remain in the solid solution to dissolve the cellulose after the non-solvent has been removed. Preferably, the ratio of liquid phase to cellulose in -the slurry should be such that the cellulose completely dissolves bu-t the excess of liquid phase is not so great that unnecessary separation oE large volumes of liquid is required.
The water content of the liquid mixture oE am:ine oxide-water or amine oxide-water-organlc non-solvent mixed with the cellulose should be as low as possible to avoid removing large volumes of water during the dissolving step. However, in the embodiment using an organic non-solvent, -the ratio of organic non-solvent and water to cellulose must be such that sufficient water remains after the organic non-solvent is removed -that the melting point of the cellulose will be below the decomposi-tion point of -the tertiary amine oxide. When the percentage by weight cellulose in the solid solution is to be low (say about 10~) the ratio of organic non-solvent plus water to the cellulose at the beginning of the process should be about 0.5 par-ts or more by weight non-solvent plus water per part of cellulose. When the product (cellulose containing tertiary amine oxide) is to contain a high percentage of cellulose, say bout 35% by weight, the ratio at the beginning of the process should be more than about 0.15 parts by weight non-solvent-water mixture per part of cellulose and less than about 2.0 parts by weight non-so]vent-water mix-ture per parts of cellulose. With the pre~erred solvents, par-ticularly N-methylmorpholine oxide and dimethylethanol amine oxide, a higher percentage of water is desirable, say 18-30%, in order to achieve a uniform solution in a cons:iderably shorter t:ime.
The dissolut:ion oE the cellulose appears to be inde-pendent of the ratio of non-solvent to water. However, as men-tioned previously, the ratio must be such that the desired ter-tiary amine oxide-water ratio will remain in the cellulose after ~ !
the non-solvent is removed. For best results, the amine oxide should contain from about 10% to about 25% by weight water and the amount of non-solvent in the slurry should be Erom about 20%
by weight to about 50% based on the weight of amine oxide-water mixture.
Best results are obtained for the dried product af-ter excess water and/or organic non-solvent have been removed con-tains from about 10% to about 35% by weight cellulose, 2 to 15~
by weight water and the remainder i.e. about 50-8~%, preferably 63-75% by weight, tertiary amine oxide.
The solid product, after the organic non-solvent has been removed and the water content has been reduced to from 2 to about 15% by weight water based on the weight of the product, may be heated to a temperature of, say, 120~C. or higher where the cellulose is dissolved by the amine oxide-water mixture remain-ing in the solid product without further addition of amine oxide, water or other material and the resulting solution may be spun or otherwise shaped into a useful cellulosic product.
Any suitable cellulose may be used in the process such as, for example, cotton linters or various kinds of wood cellu-lose, but it is preferred to use a rayon grade wood pulp.
Any suitable tertiary amine oxide which is a solvent for cellulose and is compatible with water and the organic liquid non-solvent, if an organic liquid non-solven-t is used, may be used such as, Eor ex~mple, those di~clo~ed in th~ aEo:resa.id pat-ent~. ~low~ver, the pr~eerrcd tert.iary am:inc ox:ides ~re d:Lmethy.l-ethanol amine oxide, triethylamine oxide, ce:rta:in cyclic mono-tn-methylamine-N-oxide) compounds such as, for example, N-methyl-morpholine-N-oxide, N-methylpiperidine-N-oxide, N-methylhomopiperi-dine-N-oxide, n-methylpyrollidine-N-oxide, other cyclic amine oxides where the amine oxide functionality is exo to the cyclic functionality such as di-N-methylcyclohexylamine-N-oxide and dime-thylbenzylamine-N-oxide, ancl the like.
~ny suitable li~uid non-so:Lvent for cellulose may be used such as, for example, an alcohol, n-propyl alcohol, iso-propyl alcohol, butanol and the like or an aprotic solvent such as toluene, xylene, dimethylformamide, dimethyl acetamide or the like.
In the following examples all parts and percentages are by weight unless otherwise stated.
EXAMPLE I
About 209 grams of dry rayon grade wood pulp containing about 6% water is soaked ~or about 5 minutes at 90C. in about 829 grams dimethylcyclohexyl~amine oxide containing about: 14.6%
water, about 4 milliliters dimethyl-coco-amine oxide surfactant aids spinning and 80 ml of methanol. The wood pulp absorbs amine oxide, water and methanol with swelling of the fibers.
The resulting mixture is stirred at 210 RPM for 10 minutes at 75C. and then at 250 RPM for 15 minutes at 75C. under a vacuum of 25 inches of mercury, removing the methanol and a portion of the water. The wood pulp dissolved, the solution containlng about 8.9% by weight water and had a viscosity of [n] = 3.02.
Upon cooling, a solid solution of cellulose in amine oxide was obtained. The product contained about 20.3% of cellulose.
EX~MPI,E II
___ About 150 ~rams clry woocl pu:Lp is soaked about 1() m:in-utes at 70C. in a mixture prepared b~ mixing about 899 yrams N-methylmorpholine oxide containing about 18.7% water, 13 milli-liters water and 100 ml toluene. The resulting suspension is stirred about 10 minutes at 97C. at 210 RPM. It is then sitrred about 250 RPM at 97C. under a vacuum of 25 inches of mercury resulting in the removal of toluene and a portion of the water.
The solution crystallized slightly as it cooled to room tempera-ture. The solid product thus obtai.necl was cut into p:ieces andspun to form a yarn. The spinning solution contained about 12.6%
water and had a viscosity of [n] = 4.14.
About 10 grams rayon grade wood cellulose is soaked in a mixture prepared from about 90 grams dimethyl ethanol-amine oxide con-taining about 14.7% water, and 5 ml toluene at about 95-97C. for 10 minutes. The mixture is then stirred at 210 RPM
about 10 minutes at 95-97C. and at 250 RPM at 97C. for 55-60 minutes under vacuum at about 26 inches of mercury, removing the toluene and a portion of the water. The resulting solulion is
In accordance with the process disclosed in U.S. Patent No. 3,508,941, two or more diEferent polymers are dissolved in a cyclic mono (N-methylamine-N-oxide) compound and are precipi-tated together to produce a bi-component polymer mixture. A
diluent such as dimethyl sulfoxide, N-methyl-pyrrolidone or sulfo-lane may be added to the solution to reduce its-viscosity. As indicated by the examples set forth in the patent, only solid solutions having low percentages of oollulose can be prepared when cellulose is one of the compounds used in the preparation of the solution.
It is an object of this invention to provide a process for making a solid cellulosic product which is adapted to be heated to prepare a solution of cellulose in a tertiary amine oxide. Another object of -the invention is -to provide a chip or similar granular cellulosic product which can be heatecl alone to Eorm a solut:ion of cellulose in an amine oxide which iE~ suitable ~or shaping and coayulating the cellulose. Another object of the invention is to provide a process for making a cellulosic product which can be comminuted, stored and otherwise treated as a solid material and can be heated later to convert the product into a solution of cellulose which is adapted Eor shaping into a cellu-losic article such as by extrusion or spinning. A more specificobject of the invention is to provide a cellulos:ic product which can be converted into a solution of cellulose in a tertiary amine oxide which has a higher solids content than the amine oxide solutions of the above-discussed prior art. A still more speci-fic object of the invention is to provide a precursor of a solu-tion of cellulose in a tertiary amine oxide which is a solid at ambient temperatures but becomes a solution adapted to be ex-truded or spun when heated to a temperature above ambient.
The foregoing objects and others are accomplished in accordance with this invention, generally speaking, by providing a process wherein cellulose is mixed with a liquid containing ..
a tertiary amine oxide and a liquid non-solvent containing water which assists in intimately associating the tertiary amine ox-ide with the fibers of the cellulose to facilitate absorption of the tertiary amine oxide, the resulting mixture is maintained ~:
at a temperature where the cellulose dissolves in the tertiary amine oxide until a solution is obtained and is cooled to form a solid solution suitable for shaping into a cellulosic article such as by spinning or extrusion. The non-solvent may be water -.
alone or a mixture of water and an organic non-solvent which is compatible with the tertiary amine oxide, water and cellulose.
It is preEerred to use only the calculated amount oE tertiary amine oxide necessary to complete the dissolution of the cellu-lose under extrusion conditions of heat and pressure. However, an excess of water, say 18-30% by weight of the amine oxide sol-vent-non-solvent system is desirable in forming a solid solution because the excess enhances the uniformity of distribution of the solvent throughout the cellulose and reduces the time neces-sary to complete the dissolution. If an organic non-solvent is used, dissolution i9 brought about in an evacuated vessel with removal of the organic non-solvent and any excess water that may be present. The solid solution may be comminuted to Eorm chips or other particles suitable for feeding to an extruder or other device for redissolving the chip by the application of heat and/or pressure and shaping the melt into a cellulosic article.
In one embodiment of the invention, cellulose is mixed with a liquid solution of a tertiary amine oxide and liquid non-solvent for cellulose in such proportions and at a temperature where the cellulose absorbs tertiary amine oxide and non-solvent and substantially completely swells in the tertiary amine oxide.
?9~
It is believed that the water and non-solvent cause the fibers of the cellulose to swell and thereby facilitate uniform and rapid wetting of the cellulose throughout its mass by the liquid con-taining the tertiary amine oxide prior to dic,solution of the cellulose which takes place on removal of the non-solvent. The non-solvent may be water or it may be a mixture of water and organic non-solvent. A slurry of the cellulose, amine oxide solvent and non-solvent is made and a portion of the non-solvent is removed therefxom by mixing under vacuum at an elevated tem-perature until solution occurs. Preferably, the cellulose-amine oxide-non-solvent mixture is heated to a temperature oE about 70C. or higher during mixing to accelerate swelling and dis-solution of the cellulose. At low concentrations of cellulose, e.g. 10~, solution will occur when the water content (based on total cellulose, solvent and water) reaches the range of about 10-15% (depending upon the amine oxide employed) (all of an organic non-solvent will have been first removed). At higher concentrations of cellulose, e.g. 20-30~, solution will occur when the water content, after removal of any organic amine non-solvent, reaches about 2-9%.
The resulting solution is cooled until solid and may then be comminuted such as by grinding or chopping to form fragments or chips which are suitable for extrusion, spinning, molding or the like. They may be stored for later conversion into a solution or they may be heated immediately to form a solution of cellulose in a tertiary amine oxide and water and shaped.
The chip product of the invention may be used for mak-ing a shaped cellulose product by heating the solid cellulose con-taining absorbed tertiary amine oxide and water to a tempera-ture where the cellulose dissolves in the tertiary amine oxideand removing the tertiary amine oxide while shaping the solution.
The solid solution produced by the process of the inven-tion is a solid cellulosic product containing amine oxide and some water which, when heated, will produce a melt adapted for shaping. One of the advantages of the process of this invention is that the water or water-organic non-solvent mixture mixed with the tertiary amine oxide assists in transpoxting the tertiary amine oxide to the fibers and assists in uniformly dispersing the amine oxide in the cellulose. The use of the non-solvent reduces the time necessary to transport and uniEormly d:isperse the am:ine oxide throughout the cellulose. The chip pxoduct can be shaped by merely he~ting it su~ficiently to provide an ex-trudable solid raw material. The invention thus provides a method for making a solid raw material which is complete in it-self for the extrusion of cellulose film or for spinning cellu-lose fibers and yarns. The use of a non-solvent, whether water alone or a water-organic non-solvent system, assists in achieving a homogeneous solution by slowing down the dissolution so that amine oxide is absorbed uniformly.
It has been found that cellulose sheet or shreads sus-pended in a tertiary amine oxide and water or tertiary amine ox-ide, water and organic non-solvent will dissolve when the sus-pension is heated with simultaneous removal of any organic non-solvent and any excess water present in the suspension to form a high solids solution which can be cooled to form a solid solution adapted to be comminuted to form chips or the like.
l'he organic non-solvent is removed during mixing or dissolution at any temperature which permits efEicient and rapid removal of the solvent under vacuum. With most non-solvents the -temperature may be from about 70C. to about 95C. during non-solvent removal. The non-solvent may be removed under vacuum at a pressure of as low as 0.01 mm of mercury.
The solid product obtained by cooling down the solwtion can be transferred immediately to suitable equipment for shaping it into a regenerated cellulose product or it can be stored until some later date. The solid solution is substantially free from unabsorbed liquid when it is cornminuted to form chips or the like.
The relative proportions of cellulose, water, amine oxide and liquid organic non-solvent for cellulose wh:ich are mlxed together may be ~aried broacll~ depending upon the composi-tion desired for the product as :long as suf~icient amine oxide-water mixture will remain in the solid solution to dissolve the cellulose after the non-solvent has been removed. Preferably, the ratio of liquid phase to cellulose in -the slurry should be such that the cellulose completely dissolves bu-t the excess of liquid phase is not so great that unnecessary separation oE large volumes of liquid is required.
The water content of the liquid mixture oE am:ine oxide-water or amine oxide-water-organlc non-solvent mixed with the cellulose should be as low as possible to avoid removing large volumes of water during the dissolving step. However, in the embodiment using an organic non-solvent, -the ratio of organic non-solvent and water to cellulose must be such that sufficient water remains after the organic non-solvent is removed -that the melting point of the cellulose will be below the decomposi-tion point of -the tertiary amine oxide. When the percentage by weight cellulose in the solid solution is to be low (say about 10~) the ratio of organic non-solvent plus water to the cellulose at the beginning of the process should be about 0.5 par-ts or more by weight non-solvent plus water per part of cellulose. When the product (cellulose containing tertiary amine oxide) is to contain a high percentage of cellulose, say bout 35% by weight, the ratio at the beginning of the process should be more than about 0.15 parts by weight non-solvent-water mixture per part of cellulose and less than about 2.0 parts by weight non-so]vent-water mix-ture per parts of cellulose. With the pre~erred solvents, par-ticularly N-methylmorpholine oxide and dimethylethanol amine oxide, a higher percentage of water is desirable, say 18-30%, in order to achieve a uniform solution in a cons:iderably shorter t:ime.
The dissolut:ion oE the cellulose appears to be inde-pendent of the ratio of non-solvent to water. However, as men-tioned previously, the ratio must be such that the desired ter-tiary amine oxide-water ratio will remain in the cellulose after ~ !
the non-solvent is removed. For best results, the amine oxide should contain from about 10% to about 25% by weight water and the amount of non-solvent in the slurry should be Erom about 20%
by weight to about 50% based on the weight of amine oxide-water mixture.
Best results are obtained for the dried product af-ter excess water and/or organic non-solvent have been removed con-tains from about 10% to about 35% by weight cellulose, 2 to 15~
by weight water and the remainder i.e. about 50-8~%, preferably 63-75% by weight, tertiary amine oxide.
The solid product, after the organic non-solvent has been removed and the water content has been reduced to from 2 to about 15% by weight water based on the weight of the product, may be heated to a temperature of, say, 120~C. or higher where the cellulose is dissolved by the amine oxide-water mixture remain-ing in the solid product without further addition of amine oxide, water or other material and the resulting solution may be spun or otherwise shaped into a useful cellulosic product.
Any suitable cellulose may be used in the process such as, for example, cotton linters or various kinds of wood cellu-lose, but it is preferred to use a rayon grade wood pulp.
Any suitable tertiary amine oxide which is a solvent for cellulose and is compatible with water and the organic liquid non-solvent, if an organic liquid non-solven-t is used, may be used such as, Eor ex~mple, those di~clo~ed in th~ aEo:resa.id pat-ent~. ~low~ver, the pr~eerrcd tert.iary am:inc ox:ides ~re d:Lmethy.l-ethanol amine oxide, triethylamine oxide, ce:rta:in cyclic mono-tn-methylamine-N-oxide) compounds such as, for example, N-methyl-morpholine-N-oxide, N-methylpiperidine-N-oxide, N-methylhomopiperi-dine-N-oxide, n-methylpyrollidine-N-oxide, other cyclic amine oxides where the amine oxide functionality is exo to the cyclic functionality such as di-N-methylcyclohexylamine-N-oxide and dime-thylbenzylamine-N-oxide, ancl the like.
~ny suitable li~uid non-so:Lvent for cellulose may be used such as, for example, an alcohol, n-propyl alcohol, iso-propyl alcohol, butanol and the like or an aprotic solvent such as toluene, xylene, dimethylformamide, dimethyl acetamide or the like.
In the following examples all parts and percentages are by weight unless otherwise stated.
EXAMPLE I
About 209 grams of dry rayon grade wood pulp containing about 6% water is soaked ~or about 5 minutes at 90C. in about 829 grams dimethylcyclohexyl~amine oxide containing about: 14.6%
water, about 4 milliliters dimethyl-coco-amine oxide surfactant aids spinning and 80 ml of methanol. The wood pulp absorbs amine oxide, water and methanol with swelling of the fibers.
The resulting mixture is stirred at 210 RPM for 10 minutes at 75C. and then at 250 RPM for 15 minutes at 75C. under a vacuum of 25 inches of mercury, removing the methanol and a portion of the water. The wood pulp dissolved, the solution containlng about 8.9% by weight water and had a viscosity of [n] = 3.02.
Upon cooling, a solid solution of cellulose in amine oxide was obtained. The product contained about 20.3% of cellulose.
EX~MPI,E II
___ About 150 ~rams clry woocl pu:Lp is soaked about 1() m:in-utes at 70C. in a mixture prepared b~ mixing about 899 yrams N-methylmorpholine oxide containing about 18.7% water, 13 milli-liters water and 100 ml toluene. The resulting suspension is stirred about 10 minutes at 97C. at 210 RPM. It is then sitrred about 250 RPM at 97C. under a vacuum of 25 inches of mercury resulting in the removal of toluene and a portion of the water.
The solution crystallized slightly as it cooled to room tempera-ture. The solid product thus obtai.necl was cut into p:ieces andspun to form a yarn. The spinning solution contained about 12.6%
water and had a viscosity of [n] = 4.14.
About 10 grams rayon grade wood cellulose is soaked in a mixture prepared from about 90 grams dimethyl ethanol-amine oxide con-taining about 14.7% water, and 5 ml toluene at about 95-97C. for 10 minutes. The mixture is then stirred at 210 RPM
about 10 minutes at 95-97C. and at 250 RPM at 97C. for 55-60 minutes under vacuum at about 26 inches of mercury, removing the toluene and a portion of the water. The resulting solulion is
4'~9L
cooled to room temperature to form a solid solution of cellulose.
It is later stored. Following heating to above the melting point, the solution is extruded into a non-solvent bath to coagulate the cellulose.
EXAMPLE IV
About 100 grams bone dry wood pulp is soaked in a mix-ture containing about 900 grams dimethyl-ethanol-amine oxide containing about 14.7~ water and about 50 ml toluene 10 minutes at 90C. About 150 grams of the mixture is transferred to a vessel equipped with a stirrer and 5 ml toluene are added there-to. The mixture is stirred for 25 minutes at 97C. under a vacuwm Of 26 to 27 inches mercury removing the toluene and a portion oE the water. ~ clear, highly viscous solution is ob-tained. A~ter cooling and standing overnigh-t, the solution be-comes a crystalline solid. The melting point of the solid solu-tion is about 75-80C. The solution eontained about 8.7% water and has a viscosity before spinning of [n] = 3.54 and yarn [nJ = 2.2. Slight decomposition occurred during spinning at 105C, The amine oxide used in practicing the inven~ion may be prepared by oxidizing the amine as described in U.S. Patent No.
3,333,000, U.S. Patent No. 3,447,939 or other suitable process.
For convenience, the amine oxide has been referred to herein as simply "amine oxide" but it is to be understood that the amine oxide is always a tertiary amine oxide.
Although the invention is described in detail for the purpose of illustration, it is to be understood that such de-tail is solely for that purpose and that variations can be made therein by those skilled in the art without departing Erom the spirit and scope of the invention except as it may be limited by the claims.
:"' In each of the examples hereinabove, intrinsic vis-cosity [n] is determined with 0.5~ cellulose concentration in cupriethylenediamone.
cooled to room temperature to form a solid solution of cellulose.
It is later stored. Following heating to above the melting point, the solution is extruded into a non-solvent bath to coagulate the cellulose.
EXAMPLE IV
About 100 grams bone dry wood pulp is soaked in a mix-ture containing about 900 grams dimethyl-ethanol-amine oxide containing about 14.7~ water and about 50 ml toluene 10 minutes at 90C. About 150 grams of the mixture is transferred to a vessel equipped with a stirrer and 5 ml toluene are added there-to. The mixture is stirred for 25 minutes at 97C. under a vacuwm Of 26 to 27 inches mercury removing the toluene and a portion oE the water. ~ clear, highly viscous solution is ob-tained. A~ter cooling and standing overnigh-t, the solution be-comes a crystalline solid. The melting point of the solid solu-tion is about 75-80C. The solution eontained about 8.7% water and has a viscosity before spinning of [n] = 3.54 and yarn [nJ = 2.2. Slight decomposition occurred during spinning at 105C, The amine oxide used in practicing the inven~ion may be prepared by oxidizing the amine as described in U.S. Patent No.
3,333,000, U.S. Patent No. 3,447,939 or other suitable process.
For convenience, the amine oxide has been referred to herein as simply "amine oxide" but it is to be understood that the amine oxide is always a tertiary amine oxide.
Although the invention is described in detail for the purpose of illustration, it is to be understood that such de-tail is solely for that purpose and that variations can be made therein by those skilled in the art without departing Erom the spirit and scope of the invention except as it may be limited by the claims.
:"' In each of the examples hereinabove, intrinsic vis-cosity [n] is determined with 0.5~ cellulose concentration in cupriethylenediamone.
Claims (12)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for making a solid precursor of a solu-tion of cellulose in a tertiary amine oxide which comprises dis-solving cellulose in a tertiary amine oxide solvent for cellulose containing a non-solvent for the cellulose compatible with said amine oxide solvent at a temperature where a liquid solution is obtained and cooling the solution until it solidifies to form a solid cellulosic product containing absorbed amine oxide and non-solvent.
2. The process of Claim 1 where in the said solid solution is comminuted to form cellulose chips adapted to be fed to an extruder.
3. The process of Claim 1 wherein the non-solvent is water.
4. The process of Claim 1 wherein the non-solvent is a water-organic non-solvent mixture.
5. The process of Claim 1 wherein the tertiary amine oxide is N-methylmorpholine oxide.
6. The process of Claim 1 wherein the tertiary amine oxide is dimethylcyclohexylamine oxide.
7. The process of Claim 1 wherein the tertiary amine oxide is dimethylethanolamine oxide.
8 The process of Claim 1 wherein the product contains from about 90% to about 50% by weight tertiary amine oxide, from 2% to 15% by weight water and from about 10% to about 35% by weight cellulose.
9. A process for making a precursor of a solution of cellulose in a tertiary amine oxide which comprises suspending cellulose in a mixture containing a tertiary amine oxide, water, and an organic liquid, which is miscible with the tertiary amine oxide and water and is a non-solvent for cellulose at a temperature at which the cellulose dissolves, until a solution of cellulose is obtained, removing the organic liquid therefrom, and thereafter cooling the solution to provide a solid solution containing cellulose and absorbed tertiary amine oxide and water which is capable of becoming a solution of cellulose when heated without further addition of solvent for the cellulose.
10. A method for making a solid chip containing cellu-lose adapted to be melted and shaped comprising preparing a slurry containing cellulose and a mixture of a tertiary amine oxide solvent for the cellulose and a non-solvent for the cellulose containing water in an amount which improves the intimate association of the tertiary amine oxide and cellulose fibers, heating the slurry to dissolve the cellulose in the tertiary amine oxide and applying vacuum to remove any non-aqueous non-solvent, thereafter cooling the solution to form a solid solution of cellulose in tertiary amine oxide and water, and comminuting the product to form chips adapted for feeding to an extruder or similar processing equipment.
11. The method of Claim 10 wherein the non-solvent is a mixture of an organic non-solvent and water and the organic non-solvent is removed as the cellulose dissolves in the tertiary amine oxide.
12. A process for making a solid cellulose product which is adapted to form a solution of cellulose by heating the said product alone, said process comprising dispersing cellulose in a liquid containing a tertiary amine oxide solvent for cellulose and a non-solvent for cellulose, dissolving the cellulose in said liquid mixture, and cooling the resulting solution until solidi-fication to form a solid cellulosic product containing absorbed tertiary amine oxide solvent and non-solvent in an amount which will not dissolve the cellulose at ambient temperatures but is adapted to dissolve the cellulose when heated to form a shapeable solution.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US819,081 | 1977-07-26 | ||
| US05/819,081 US4142913A (en) | 1977-07-26 | 1977-07-26 | Process for making a precursor of a solution of cellulose |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1110404A true CA1110404A (en) | 1981-10-13 |
Family
ID=25227152
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA308,113A Expired CA1110404A (en) | 1977-07-26 | 1978-07-25 | Process for making a precursor of a solution of cellulose |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US4142913A (en) |
| JP (1) | JPS5424962A (en) |
| AR (1) | AR225003A1 (en) |
| BE (1) | BE868736A (en) |
| BR (1) | BR7804791A (en) |
| CA (1) | CA1110404A (en) |
| DD (1) | DD140258A5 (en) |
| DE (1) | DE2830683C3 (en) |
| FR (1) | FR2398759A1 (en) |
| GB (1) | GB2001321B (en) |
| IT (1) | IT1099563B (en) |
| NL (1) | NL7807423A (en) |
| SE (1) | SE7808038L (en) |
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| US4246221A (en) * | 1979-03-02 | 1981-01-20 | Akzona Incorporated | Process for shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent |
| US4416698A (en) * | 1977-07-26 | 1983-11-22 | Akzona Incorporated | Shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent and a process for making the article |
| US4324593A (en) * | 1978-09-01 | 1982-04-13 | Akzona Incorporated | Shapeable tertiary amine N-oxide solution of cellulose, shaped cellulose product made therefrom and process for preparing the shapeable solution and cellulose products |
| US4261943A (en) * | 1979-07-02 | 1981-04-14 | Akzona Incorporated | Process for surface treating cellulose products |
| US4290815A (en) * | 1980-01-28 | 1981-09-22 | Akzona Incorporated | Use of co-solvents in amine N-oxide solutions |
| DE3021943A1 (en) * | 1980-06-12 | 1982-01-21 | Akzo Gmbh, 5600 Wuppertal | CELLULOSE DIALYSIS MEMBRANE |
| DE3034685C2 (en) * | 1980-09-13 | 1984-07-05 | Akzo Gmbh, 5600 Wuppertal | Cellulose molding and spinning mass with low proportions of low molecular weight breakdown products |
| JPH0431248Y2 (en) * | 1986-04-18 | 1992-07-28 | ||
| US5330567A (en) * | 1988-08-16 | 1994-07-19 | Lenzing Aktiengesellschaft | Process and arrangement for preparing a solution of cellulose |
| US5277857A (en) * | 1992-01-17 | 1994-01-11 | Viskase Corporation | Method of making a cellulose food casing |
| USH1592H (en) * | 1992-01-17 | 1996-09-03 | Viskase Corporation | Cellulosic food casing |
| WO1994019405A1 (en) * | 1993-02-16 | 1994-09-01 | Mitsubishi Rayon Co., Ltd. | Cellulose molding solution and process for molding therefrom |
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| US5891375A (en) * | 1997-07-24 | 1999-04-06 | Alfacel S.A. | Processes for precipitating tertiary amine oxide cellulose solutions containing esters and products made therefrom |
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| US6773648B2 (en) | 1998-11-03 | 2004-08-10 | Weyerhaeuser Company | Meltblown process with mechanical attenuation |
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| AU2003273104A1 (en) * | 2003-06-30 | 2005-01-13 | Hyosung Corporation | A solution containing cellulose dissolved in n-methylmorpholine-n-oxide and high tenacity lyocell multifilament using the same |
| JP4104596B2 (en) * | 2003-06-30 | 2008-06-18 | ヒョスング コーポレーション | Highly homogeneous cellulose solution and high strength lyocell fiber using the same |
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| KR100488604B1 (en) * | 2003-07-25 | 2005-05-11 | 주식회사 효성 | Lyocell multi-filament |
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| DE102004024030A1 (en) * | 2004-05-13 | 2005-12-08 | Zimmer Ag | Lyocell process with polymerization-degree-dependent adjustment of the processing time |
| DE102004024028B4 (en) * | 2004-05-13 | 2010-04-08 | Lenzing Ag | Lyocell method and apparatus with press water return |
| DE102004024029A1 (en) * | 2004-05-13 | 2005-12-08 | Zimmer Ag | Lyocell method and apparatus with metal ion content control |
| KR100575378B1 (en) * | 2004-11-10 | 2006-05-02 | 주식회사 효성 | Process for preparing a cellulose fiber |
| KR100575388B1 (en) * | 2004-12-30 | 2006-05-03 | 주식회사 효성 | A highly homogeneous cellulose solution and fiber produced by using the same |
| KR100674670B1 (en) * | 2006-04-27 | 2007-01-25 | 주식회사 효성 | Cellulose raw cord for rubber reinforcement |
| KR100721443B1 (en) * | 2006-04-27 | 2007-05-23 | 주식회사 효성 | Cellulose dipped cord for rubber reinforcement |
| US7815741B2 (en) * | 2006-11-03 | 2010-10-19 | Olson David A | Reactor pump for catalyzed hydrolytic splitting of cellulose |
| US7815876B2 (en) | 2006-11-03 | 2010-10-19 | Olson David A | Reactor pump for catalyzed hydrolytic splitting of cellulose |
| KR100949556B1 (en) | 2006-12-26 | 2010-03-25 | 주식회사 코오롱 | Method for production of cross-linked composite fiber of cellulose-polyvinylalcohol and the cross-linked composite fiber |
| US8029260B2 (en) * | 2008-04-11 | 2011-10-04 | Reifenhauser Gmbh & Co. Kg Maschinenfabrik | Apparatus for extruding cellulose fibers |
| US8303888B2 (en) * | 2008-04-11 | 2012-11-06 | Reifenhauser Gmbh & Co. Kg | Process of forming a non-woven cellulose web and a web produced by said process |
| US8029259B2 (en) * | 2008-04-11 | 2011-10-04 | Reifenhauser Gmbh & Co. Kg Maschinenfabrik | Array of nozzles for extruding multiple cellulose fibers |
| CN103619886B (en) | 2011-06-29 | 2016-09-14 | 柯惠Lp公司 | The dissolving of oxidized cellulose |
| DE102012103296A1 (en) * | 2012-04-17 | 2013-10-17 | List Holding Ag | Process for the production of moldings |
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| US10413566B2 (en) | 2013-03-15 | 2019-09-17 | Covidien Lp | Thixotropic oxidized cellulose solutions and medical applications thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH191822A (en) * | 1936-04-21 | 1937-07-15 | Chem Ind Basel | Process for the preparation of a new cellulose solution. |
| CH194638A (en) * | 1936-04-21 | 1937-12-15 | Chem Ind Basel | Process for the preparation of a new cellulose solution. |
| US3447956A (en) * | 1966-09-02 | 1969-06-03 | Eastman Kodak Co | Process for strengthening swellable fibrous material with an amine oxide and the resulting material |
| US3447939A (en) * | 1966-09-02 | 1969-06-03 | Eastman Kodak Co | Compounds dissolved in cyclic amine oxides |
-
1977
- 1977-07-26 US US05/819,081 patent/US4142913A/en not_active Expired - Lifetime
-
1978
- 1978-06-30 IT IT25209/78A patent/IT1099563B/en active
- 1978-07-04 BE BE189076A patent/BE868736A/en unknown
- 1978-07-10 NL NL7807423A patent/NL7807423A/en not_active Application Discontinuation
- 1978-07-11 AR AR272907A patent/AR225003A1/en active
- 1978-07-12 DE DE2830683A patent/DE2830683C3/en not_active Expired
- 1978-07-21 SE SE7808038A patent/SE7808038L/en unknown
- 1978-07-25 BR BR7804791A patent/BR7804791A/en unknown
- 1978-07-25 CA CA308,113A patent/CA1110404A/en not_active Expired
- 1978-07-25 DD DD78206922A patent/DD140258A5/en unknown
- 1978-07-25 FR FR7821984A patent/FR2398759A1/en not_active Withdrawn
- 1978-07-26 GB GB787829894A patent/GB2001321B/en not_active Expired
- 1978-07-26 JP JP9203878A patent/JPS5424962A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| IT7825209A0 (en) | 1978-06-30 |
| AR225003A1 (en) | 1982-02-15 |
| BE868736A (en) | 1978-11-03 |
| IT1099563B (en) | 1985-09-18 |
| BR7804791A (en) | 1979-04-10 |
| DD140258A5 (en) | 1980-02-20 |
| US4142913A (en) | 1979-03-06 |
| JPS5541692B2 (en) | 1980-10-25 |
| DE2830683C3 (en) | 1982-04-01 |
| DE2830683A1 (en) | 1979-02-15 |
| FR2398759A1 (en) | 1979-02-23 |
| GB2001321B (en) | 1982-08-04 |
| DE2830683B2 (en) | 1980-12-11 |
| JPS5424962A (en) | 1979-02-24 |
| SE7808038L (en) | 1979-01-27 |
| NL7807423A (en) | 1979-01-30 |
| GB2001321A (en) | 1979-01-31 |
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