Producing method of cellulose polymer

FIELD OF THE INVENTION

The present invention relates to a producing method of a cellulose series polymer. Specifically, the present invention relates to a producing method of cellulose series polymer powder which is soluble in an organic solvent and a producing method of an organic solvent solution wherein a cellulose series polymer is dissolved in high concentration.

BACKGROUND OF THE INVENTION

Cellulose series polymers, in particular, cellulose esters have high dimensional stability and heat resistance, and sticky as compared with synthetic resins for general use. Due to these characteristics, cellulose esters are formed to various products, e.g., films and fibers as well as used as the materials of plastics and lacquers. A cellulose ester film is representative of the support of photographic materials, and they are also used as the members of liquid crystal display (e.g., a protective film of a polarizing plate, a support of an optical compensation sheet, and a color filter) due to their optical isotropy. Moreover, a demand for biodegradable polymers has been increasingly raised in recent years from the viewpoint of the environmental protection and, as a result, the importance of cellulose series polymers have been appreciated anew.

Thus, it is thought that the importance of cellulose series polymers represented by cellulose esters will increase hereafter. On the other hand, chlorine-based solvents, such as methylene chloride, have been widely used as the solvent to make the solution of cellulose series polymers for forming films and the like, because they have a high solubility and can be easily removed at low boiling point. However, chlorine-based solvents are toxic substances such as having carcinogen or environmentally deleterious substances represented by ozone layer depletion, therefore, the use of chlorine-based solvents has been restricted very much. The discharge of methylene chloride into the air is severely restricted for the latter reason.

Accordingly, studies for solving these problems have been actively pursued in these years and some techniques have been disclosed. For example, methods of using cyclic diethers such as 1,3-dioxane and 1,3-dioxolan (e.g., JP-A-8-143708 (the term “JP-A” as used herein means an “unexamined published Japanese patent application”) and JP-A-8-323785), and methods of using fluoro-alcohols such as trifluoroethanol (e.g., JP-A-8-143709 and JP-A-11-60807) are disclosed. However, cyclic diethers of the former case are not necessarily perfect in safety and have a drawback that they are highly flammable. On the other hand, fluoro-alcohols of the latter case is expensive and it is not practicable to be used in a large quantity as the solvent for polymer formation.

Accordingly, the use of safe and inexpensive solvents such as acetone, ethanol, methyl acetate and ethyl acetate has been examined but it is difficult to dissolve cellulose series polymers, such as cellulose ester, in these solvents in concentrations required in the production of films, etc., by merely a mixing means. Therefore, a variety of means for increasing solubility are now under investigation. Specific examples of these methods include (1) a method of using a means of cooling dissolution (

Makromol. Chem.,

143, 105 (1971) (e.g., JP-A-9-95538 and JP-A-9-95544), (2) a method of applying extra-high pressure (e.g., JP-A-11-21379), (3) a method of using ultrasonic wave (e.g., JP-A-11-71463), and (4) a method according to a means of a two-component system mixed fluid under high pressure of acetone, triacetin, methanol or ethanol and carbon dioxide (e.g., U.S. Pat. No. 5,512,231 and

Journal of Supercritical Fluids,

13, 135 (1998)).

The above methods (1) to (4) are certainly effective for improving solubility but there are big problems in every of them from the viewpoint of an industrial producing method. That is, for obtaining sufficient solubility according to method (1), an extremely low temperature such as −70° C. is necessary, which requires a vast sum of facility investment. For obtaining sufficient solubility according to method (2), extra-high pressure of almost 100 MPa is necessary, hence the realization of practical use is also industrially difficult in view of facilities. In method (3), it is necessary to develop an ultrasonic wave generating apparatus which can be used in an industrial scale and it is considerably practicably difficult at this point of time. In method (4), a sufficient amount of cellulose series polymers cannot be dissolved, and the stability of the solution with the lapse of time is low, and partial gelation is occur.

Thus, it can be said that an industrially practicable technique of dissolving cellulose series polymers without using environmentally deleterious chlorine-based solvents to form films with small facility investment has not yet been found. Therefore, such is the state of things that the development of a novel method is strongly desired.

SUMMARY OF THE INVENTION

Accordingly, an object of the present invention is to provide a producing method of cellulose series polymers, in particular, cellulose ester powder or the organic solvent solution of cellulose ester which is high in safety, small in environmental load, and light in imposition of facility investment (i.e., inexpensive).

The present inventors have repeated examinations for solving the above problems. As a result, the present inventors have found that when a cellulose polymer is dispersed and stirred in an organic solvent other than chlorine-based polymers and liquid carbon dioxide is added to the dispersion in an appropriate weight ratio and stirred, the polymer is dissolved, and the polymer once dissolved does not precipitate and dissolved in the organic solvent after the carbon dioxide is removed, and that the powder obtained by removing the organic solvent has excellent solubility as compared with polymers not subjected to this treatment. The present invention has been attained based on the above finding.

That is, the present invention provides the following.

(1) A process for producing a cellulose polymer powder which comprises the steps of dissolving a cellulose polymer by exposure to an organic solvent containing, as the main component, an ester-based solvent having from 2 to 8 carbon atoms, a ketone-based solvent having from 4 to 10 carbon atoms, or an alcohol-based solvent having from 3 to 6 carbon atoms, and carbon dioxide, and then removing the carbon dioxide and the organic solvent from the solution.

(2) A process for producing an organic solvent solution of a cellulose polymer which comprises dissolving a cellulose polymer by exposure to an organic solvent containing, as the main component, an ester-based solvent having from 2 to 8 carbon atoms, a ketone-based solvent having from 4 to 10 carbon atoms, or an alcohol-based solvent having from 3 to 6 carbon atoms, and carbon dioxide.

(3) The process as described in the above item (1) or (2), wherein the cellulose polymer is dissolved at the temperature and the pressure not lower than the critical temperature and the critical pressure of carbon dioxide.

(4) The process as described in the above item (1) or (2), wherein the cellulose polymer is cellulose acetate having the degree of acetylation of 55.0% or more and the concentration of the polymer in the organic solvent solution is 10 mass % or more.

As the preferred embodiments of the above-described present invention, the followings can be exemplified.

(5) The process as described in the above item (1) or (2), wherein said cellulose polymer is cellulose ester.

(6) The process as described in the above item (5), wherein said cellulose ester is acetyl cellulose.

(7) The process as described in the above item (6), wherein said acetyl cellulose has the acetylation degree of 58% or more.

DETAILED DESCRIPTION OF THE INVENTION

The present invention will be described in detail below.

As the cellulose polymers for use in the present invention, for example, cellulose ester and cellulose ether can be exemplified. Specifically, cellulose ester includes aliphatic carboxylic acid esters such as cellulose acetate, cellulose butyrate, and cellulose propionate, aromatic carboxylic acid esters such as phthalic acid ester, inorganic acid esters such as cellulose nitrate, cellulose sulfate, and cellulose phosphate, mixed acid esters such as cellulose acetate propionate, cellulose acetate butyrate, cellulose acetate phthalate, and cellulose nitrate acetate, and cellulose ester derivatives such as polycaprolactone grafted cellulose acetate. Specifically, cellulose ether includes methyl cellulose, ethyl cellulose, benzyl cellulose and carboxymethyl cellulose.

A preferred cellulose series polymer is cellulose ester, and cellulose acetate (acetyl cellulose) is especially preferred.

The average degree of substitution of cellulose ester is preferably from about 1 to 3. The average degree of polymerization of cellulose ester is preferably from 10 to 1,000, more preferably from 50 to 900, and most preferably from 200 to 800.

The degree of acetylation of cellulose ester is preferably from 30 to 62.5%, more preferably 55% or more, and particularly preferably 58% or more.

The organic solvents for use in the present invention are described below. The organic solvents for use in the present invention do not substantially contain a chlorine-based solvent such as methylene chloride. The terminology “do not substantially contain” means that the ratio of the chlorine-based solvent in the organic solvent is less than 5 mass % (preferably less than 2 mass %, more preferably does not contain at all).

In the present invention, “the main component” of a solvent means that the solvent is a single solvent (having purity of 99 mass % or more), or that the solvent has the highest ratio (mass % in a mixed solvent) in a mixed solvent of two or more solvents. In the case of a mixed solvent, the solvents other than the main component may be the solvents restricted in the present invention or may be the solvents other than the solvents restricted in the present invention. When a part of a mixed solvent is water, the ratio of water is preferably 5 mass % or less, particularly preferably 2 mass % or less.

When the organic solvent for use in the present invention is a mixed solvent of two or more organic solvents, the ratio of the solvent as the main component is preferably 30 mass % or more, particularly preferably 80 mass % or more. The organic solvents which can be used in the present invention are an ester-based solvent having from 2 to 8 carbon atoms, a ketone-based solvent having from 4 to 10 carbon atoms, and an alcohol-based solvent having from 3 to 6 carbon atoms, preferably an ester-based solvent having from 2 to 4 carbon atoms, a ketone-based solvent having from 4 to 6 carbon atoms, and an alcohol-based solvent having 3 or 4 carbon atoms. These solvents may have cyclic structure.

More specifically, the examples of the organic solvents which can be used in the present invention include ester-based solvents, e.g., methyl formate, ethyl formate, propyl formate, pentyl formate, methyl acetate, ethyl acetate, butyl acetate and hexyl acetate, ketone-based solvents, e.g., methyl ethyl ketone, diethyl ketone, diisobutyl ketone, cyclopentanone, cyclohexanone and methylcyclohexanone, and alcohol-based solvents, e.g., n-propanol, isopropanol, n-butanol, n-pentanol, n-hexanol, ethoxyethanol and ethylene glycol.

Preferred organic solvents which are used in the present invention include ester-based solvents alone and mixed solvents containing ester-based solvents as the main component, and particularly preferably a single solvent of methyl acetate alone and a mixed solvent containing methyl acetate as the main component and an alcohol-based solvent and/or a ketone-based solvent.

The amount of the organic solvents for use for cellulose polymers is generally such that the concentration of the dissolved polymer in an organic solvent solution becomes 1 mass % or more, preferably from 2 to 80 mass %, and especially preferably from 10 to 70 mass %. The amount of carbon dioxide to be used is preferably from 0.1 to 50, particularly preferably from 0.5 to 30, with the polymer as 1 in mass ratio.

When the powder or solution of a cellulose polymer is produced according to the method of the present invention, a plasticizer, a deterioration-preventing agent, an ultraviolet absorber and/or a light piping-preventing dye may be added. As the plasticizer, phosphate or carboxylate is mainly used. Specific examples of the plasticizers include phosphate, e.g., triphenyl phosphate, tricresyl phosphate, and biphenyldiphenyl phosphate, and carboxylate, e.g., diethyl phthalate, dioctyl phthalate, diethylhexyl phthalate, acetyltriethyl citrate, tributyl citrate, butyl oleate, and dibutyl sebacate.

The specific examples of the deterioration-preventing agents are the compounds disclosed in JP-A-5-197073. The specific examples of the ultraviolet absorbers are the compounds disclosed in JP-A-7-11056. The light piping-preventing dye is a dye soluble in an organic solvent which can prevent light piping by coloring a film base, and the specific examples include Spirit Black (manufactured by Chuo Kagaku Co., Ltd.) and Nigrosine Base EX (manufactured by Orient Kagaku Kogyo Co., Ltd.).

In the next place, the step of exposing the organic solvent having dispersed therein a cellulose polymer to carbon dioxide is described. The reaction apparatus is required to be resistant to high pressure and heating. Apparatuses called autoclaves are generally used, and a variety of apparatuses are easily commercially available according to the pressure and the solvents to be used. Although generally used autoclaves made of stainless steel that are resistant to internal pressure of 30 MPa (about 300 atm) are sufficient as the apparatuses for use in the present invention, it is convenient and preferable to use a volume-variable type autoclave in the experiment for finding out the optimum conditions.

The present invention is described below by specific procedure. A necessary amount of cellulose polymer to be dissolved is put in an autoclave and the lid of the autoclave is closed. The oxygen in the autoclave is purged by carbon dioxide or nitrogen gas, and then the necessary amount of the solvent to be used is introduced into the apparatus by pumping. The method of introducing carbon dioxide into the apparatus is generally performed by any of the following three methods.

That is, 1) a method of weighing the amount of carbon dioxide to be introduced by another weighing vessel and introducing by pumping, 2) a method of determining the amount of carbon dioxide to be introduced from the flow rate and the introducing time of carbon dioxide, and 3) a method of determining the amount of carbon dioxide introduced from the internal pressure.

The internal pressure of an autoclave is decided by the capacity of the autoclave, the amount of the solvent introduced, the amount of carbon dioxide and the temperature. For achieving the objective temperature and pressure, it is necessary to select an autoclave having an appropriate capacity in accordance with the amounts of the solvent and carbon dioxide to be used. When the size of the autoclave is limited, it is necessary to use corresponding amounts of the solvent and carbon dioxide. For obtaining high internal pressure with a small use amount of carbon dioxide, a volume-variable type autoclave is used, or an auxiliary means is used, such as pressure application by other high pressure gases, e.g., nitrogen gas. Pressure is generally from 0.1 to 100 MPa, preferably from 7.4 to 60 MPa. Since a special pressure-resisting autoclave is necessary when pressure of 30 MPa or more is applied, pressure is especially preferably from 8 to 30 MPa at which ordinary autoclaves can be used.

The temperature for dissolution after introduction of carbon dioxide is from 20 to 300° C., preferably from 31 to 200° C., and particularly preferably from 40 to 180° C.

The time required for dissolution is generally 100 hours or less, preferably from 1 minute to 30 hours, and particularly preferably from 30 minutes to 10 hours.

In the present invention, it is preferred to dissolve the cellulose polymer at the temperature and the pressure not lower than the critical temperature and the critical pressure of carbon dioxide. Further, the critical point of carbon dioxide is 31° C. (7.4 MPa).

A method of obtaining the organic solvent solution of a cellulose polymer by exposing the cellulose polymer to an organic solvent and carbon dioxide is described below. When carbon dioxide is introduced and heated, the temperature is restored to room temperature, and carbon dioxide is discharged by opening the valve little by little so as not to cause vigorous bubbling until the internal pressure of the autoclave becomes atmospheric pressure. It is preferred to scavenge carbon dioxide to another cooled vessel at this time. When the internal pressure is reached to atmospheric pressure, the carbon dioxide in the organic solvent is thoroughly removed by means of an aspirator, etc., by reducing the pressure a little. It is preferred at this time to take out some organic solvent from the system to make the system a little concentrated. Thus, an organic solvent solution containing the polymer in high concentration can be obtained.

The methods of obtaining the powder of a cellulose polymer is described below. Generally used methods of powdering can be arbitrarily selected according to purpose in the present invention, e.g., a method of drying the above-obtained organic solvent solution of a cellulose polymer with a band drier and removing the solvent thoroughly, and then powdering the dried product with a pulverizer, and a method of atomizing the organic solvent solution of a cellulose polymer by high pressure injection from a nozzle.

EXAMPLE

The present invention will be illustrated with referring to examples below but it should not be construed as the present invention is limited thereto.

Example 1

Twenty (20) grams of cellulose acetate each having different degree of acetylation and degree of polymerization was weighed and put into a volume-variable type autoclave having a content volume of 200 ml, and 80 g of the organic solvent shown in Table 1 defined in the present invention was added thereto. The lid was closed, a nitrogen gas bomb was connected and the oxygen in the autoclave was purged off, the valve of the air exit was closed, subsequently 20 g of liquefied carbon dioxide was charged by a feeding pump. The external temperature was then adjusted to 100° C., the volume of the inside of the autoclave was adjusted, the internal pressure was made 10.0 MPa and the content was stirred for 1 hour. The temperature was then lowered to room temperature, the original volume of the inside of the autoclave was restored, and then the valve was opened to get the carbon dioxide out of the autoclave. Thus, Sample Nos. 1 to 5 were obtained.

Comparative Sample Nos. 1 to 4 were produced in the same manner as above except for using acetone, triacetin, ethanol or methanol as the organic solvent.

The results obtained are shown in Table 1. All of Sample Nos. 1 to 5 according to the present invention were transparent and homogeneous solutions. This shows that cellulose acetate is completely dissolved. Comparative Sample Nos. 1 to 4 were swollen and in slurry state. This shows that cellulose acetate is only partially dissolved.

TABLE 1

Cellulose Acetate

Acetylation

Polymerization

Sample No.

Degree

Degree

Solvent

Solubilit

Sample 1

60.9

299

Methyl acetate

Homogeneous and

transparent

solution

Sample 2

60.9

299

Methyl ethyl ketone

Homogeneous and

transparent

solution

Sample 3

60.2

323

Butanol

Homogeneous and

transparent

solution

Sample 4

59.2

395

Methyl acetate/ethanol

Homogeneous and

(85/15)

transparent

solution

Sample 5

59.5

350

Cyclohexanone

Homogeneous and

transparent

solution

Comparative

60.9

299

Acetone

Swollen and in

Sample 1

slurry state

(partially

dissolved)

Comparative

60.9

299

Triacetin

Swollen and in

Sample 2

slurry state

(partially

dissolved)

Comparative

60.2

323

Ethanol

Swollen and in

Sample 3

slurry state

(partially

dissolved)

Comparative

59.2

395

Methanol

Swollen and in

Sample 4

slurry state

(partially

dissolved)

(Temperature: 100° C., Internal pressure: 10.0 MPa, Cellulose acetate: 20.0 g, Solvent: 80 g, CO

2

:20 g)

Example 2

Sample Nos. 1 to 5 and Comparative Sample Nos. 1 to 4 were dried with a band drier to remove the solvent, and then pulverized with a crasher. The thus-obtained powders were designated as Sample Nos. 6 to 10 and Comparative Sample Nos. 5 to 8, respectively. The solubility of these samples in the same solvents used in Example 1 respectively was examined under atmospheric pressure. The results obtained are shown in Table 2. Each of Sample Nos. 6 to 10 according to the present invention showed the solubility in the solvent (10 mass % or more) but Comparative Sample Nos. 5 to 8 showed only low solubility.

TABLE 2

Solubility

Sample No.

Powder

Solvent

(mass %)

Sample 6

Powder coming

Methyl acetate

14

from Sample 1

Sample 7

Powder coming

Methyl ethyl ketone

13

from Sample 2

Sample 8

Powder coming

Butanol

10

from Sample 3

Sample 9

Powder coming

Methyl acetate/

13

from Sample 4

ethanol (85/15)

Sample 10

Powder coming

Cyclohexanone

15

from Sample 5

Comparative

Powder coming from

Acetone

6

Sample 5

Comparative Sample 1

Comparative

Powder coming from

Triacetin

5

Sample 6

Comparative Sample 2

Comparative

Powder coming from

Ethanol

3

Sample 7

Comparative Sample 3

Comparative

Powder coming from

Methanol

3

Sample 8

Comparative Sample 4

Example 3

Twenty (20) grams of cellulose acetate each having different degree of acetylation and degree of polymerization was weighed and put into an autoclave having a content volume of 200 ml, and 90 g of the organic solvent shown in Table 3 was added thereto. The lid was closed, a nitrogen gas bomb was connected and the oxygen in the autoclave was purged off, the valves of the air exit and the liquid inlet were closed, the valve of other inlet was opened and 10 g of liquefied carbon dioxide was charged by a feeding pump, and then the valve was closed. Subsequently, the valve of the inlet of nitrogen gas was opened again, and nitrogen gas was charged with a pressure pump until the internal pressure became 10.0 MPa. The external temperature was then adjusted to 90° C., and the content was stirred for 1 hour. The internal pressure was 13.5 MPa. The temperature was then lowered to room temperature, and then the valve was opened to get the carbon dioxide and the nitrogen gas out of the autoclave. Thus, Sample Nos. 11 to 15 were obtained.

Comparative Sample Nos. 9 to 12 were produced in the same manner as above except for using acetone, triacetin, ethanol or methanol as the organic solvent.

The results obtained are shown in Table 3. All of Sample Nos. 11 to 15 according to the present invention were transparent and homogeneous solutions. This shows that cellulose acetate is completely dissolved. Comparative Sample Nos. 9 to 12 were swollen and in slurry state. This shows that cellulose acetate is only partially dissolved.

TABLE 3

Cellulose Acetate

Acetylation

Polymerization

Sample No.

Degree

Degree

Solvent

Solubility

Sample 11

60.9

299

Methyl acetate

Homogeneous and

transparent

solution

Sample 12

60.9

299

Methyl ethyl ketone

Homogeneous and

transparent

solution

Sample 13

60.2

323

Butanol

Homogeneous and

transparent

solution

Sample 14

59.2

395

Methyl acetate/ethanol

Homogeneous and

(85/15)

transparent

solution

Sample 15

59.5

350

Cyclohexanone

Homogeneous and

transparent

solution

Comparative

60.9

299

Acetone

Swollen and in

Sample 9

slurry state

(partially

dissolved)

Comparative

60.9

299

Triacetin

Swollen and in

Sample 10

slurry state

(partially

dissolved)

Comparative

60.2

323

Ethanol

Swollen and in

Sample 11

slurry state

(partially

dissolved)

Comparative

59.2

395

Methanol

Swollen and in

Sample 12

slurry state

(partially

dissolved)

(Temperature: 90° C., Internal pressure: 13.5 MPa, Cellulose acetate: 20.0 g, Solvent: 90 g, CO

2

: 10 g)

Example 4

Sample Nos. 11 to 15 and Comparative Sample Nos. 9 to 12 were dried with a band drier to remove the solvent, and then pulverized with a crasher. The thus-obtained powders were designated as Sample Nos. 16 to 20 and Comparative Sample Nos. 13 to 16, respectively. The solubility of these samples in the same solvents used in Example 3 respectively was examined under atmospheric pressure. The results obtained are shown in Table 4. Each of Sample Nos. 16 to 20 according to the present invention showed the solubility in the solvent (10 mass % or more) but Comparative Sample Nos. 13 to 16 showed only low solubility.

TABLE 4

Solubility

Sample No.

Powder

Solvent

(mass %)

Sample 16

Powder coming

Methyl acetate

15

from Sample 11

Sample 17

Powder coming

Methyl ethyl ketone

13

from Sample 12

Sample 18

Powder coming

Butanol

10

from Sample 13

Sample 19

Powder coming

Methyl acetate/

14

from Sample 14

ethanol (85/15)

Sample 20

Powder coming

Cyclohexanone

14

from Sample 15

Comparative

Powder coming from

Acetone

7

Sample 13

Comparative Sample 9

Comparative

Powder coming from

Triacetin

6

Sample 14

Comparative Sample 10

Comparative

Powder coming from

Ethanol

4

Sample 15

Comparative Sample 11

Comparative

Powder coming from

Methanol

4

Sample 16

Comparative Sample 12

Example 5

Ten (10) grams of cellulose acetate each having different degree of acetylation and degree of polymerization was weighed and put into an autoclave having a content volume of 200 ml, and 100 g of the organic solvent shown in Table 5 was added thereto. The lid was closed, a nitrogen gas bomb was connected and the oxygen in the autoclave was purged off, the valve of the air exit was closed, subsequently carbon dioxide gas was charged by a feeding pump until the internal pressure became 7.0 MPa. The introduced carbon dioxide was about 20 g, although a little uneven due to the solvent used. The external temperature was then adjusted to 90° C., and the content was stirred for 1 hour. The internal pressure was about 8.7 MPa. The temperature was then lowered to 50° C., and then the valve was opened to get the carbon dioxide out of the autoclave. Thus, Sample Nos. 21 to 25 were obtained.

Comparative Sample Nos. 17 to 20 were produced in the same manner as above except for using a nitrogen gas bomb in place of a carbon dioxide gas bomb.

All of Sample Nos. 21 to 25 and Comparative Sample Nos. 17 to 20 were transparent and homogeneous solutions at 50° C. Each sample was cooled to 25° C. and allowed to stand at 25° C. for 2 days. The results obtained are shown in Table 5.

All of Sample Nos. 21 to 25 remained transparent and homogeneous but all of Comparative Sample Nos. 17 to 20 were gelated partially and became white turbid.

TABLE 5

Solubility

Cellulose Acetate

After Being

Acetyla-

Polymeri-

Allowed to

tion

zation

Just After

Stand at 25° C.

Sample No.

Degree

Degree

Solvent

Coating

for 2 Days

Sample 21

60.9

299

Methyl

Homogeneous and

Homogeneous and

acetate

transparent

transparent

solution

solution

Sample 22

60.9

299

Ethyl acetate/

Homogeneous and

Homogeneous and

butanol

transparent

transparent

(85/15)

solution

solution

Sample 23

60.2

323

Isopropyl

Homogeneous and

Homogeneous and

methyl ketone

transparent

transparent

solution

solution

Sample 24

59.2

395

Methyl acetate/

Homogeneous and

Homogeneous and

ethanol/butanol

transparent

transparent

(85/10/5)

solution

solution

Sample 25

59.5

350

Cyclo-

Homogeneous and

Homogeneous and

hexanone

transparent

transparent

solution

solution

Comparative

60.9

299

Acetone

Homogeneous and

Partially

Sample 17

transparent

gelled,

solution

white

turbid

Comparative

60.9

299

Triacetin

Homogeneous and

Partially

Sample 18

transparent

gelled,

solution

white

turbid

Comparative

60.2

323

Ethanol

Homogeneous and

Partially

Sample 19

transparent

gelled,

solution

white

turbid

Comparative

59.2

395

Methanol

Homogeneous and

Partially

Sample 20

transparent

gelled,

solution

white

turbid

(Temperature: 90° C., Internal pressure: 8.7 MPa, Cellulose acetate: 10.0 g, Solvent: 100 g, CO

2

: about 20 g)

According to the present invention, the powders of cellulose polymers which are safe, inexpensive, and excellent in solubility in an organic solvent can be produced and, further, a highly concentrated and stable organic solvent solution of cellulose polymers can be produced. Thus, according to the present invention, it is possible to produce materials for forming films, etc., inexpensively without using chlorine-based solvents, e.g., methylene chloride, which are high in environmental load and toxicity. Accordingly, the present invention also widens the possibility of the use of cellulose polymers in biodegradable polymers and the like

While the invention has been described in detail and with reference to specific examples thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope thereof.

This application is based on Japanese patent applications No. Hei-11-349534 filed on Dec. 8, 1999, No. 2000-245916 filed on Aug. 14, 2000, and No. 2000-313651 fled on Oct. 13, 2000, the entire contents of which incorporated herein by reference.

Number	Date	Country
11-349534	Dec 1999	JP
2000-245916	Aug 2000	JP
2000-313651	Oct 2000	JP

Number	Name	Date	Kind
5512231	Thies et al.	Apr 1996	A
5962667	Murakami et al.	Oct 1999	A

Producing method of cellulose polymer

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