GB2152936A - Porous spherical cellulose acetate particles - Google Patents

Abstract

Porous, spherical particles consist substantially of cellulose acetate, having an acetylation degree of 49 to 60% (i.e. an esterification degree of 2.0 to 2.8), a particle diameter of 0.05 to 10 mm, a sphericity of at least 0.7, a pore volume of at least 0.4cc/g and a collapsing strength of at least 9 kg or higher. The particles are made using a dope comprising a solution formed by dissolving a cellulose acetate of the above degree of esterification in an acetic acid/water (80/20 to 90/10, by weight) solvent so that the concentration of the cellulose acetate is 25+/-7 wt.%, feeding said dope through a supply pipe to a coagulation bath comprising an acetic acid/water (30/70 to 42/58, by weight) solvent and having a temperature of 40+/-5 DEG C; operating an agitator having blades passing near a discharge port on the end of said supply pipe; effecting precipitation and granulation while adding water so that the acetic acid to water ratio of the coagulation bath may be maintained at a substantially constant value during said operation; centrifugally separating precipitate particles from the solution; washing these particles with water and drying the particles.

Description

SPECIFICATION Porous spherical cellulose acetate particles The invention relates to particles of cellulose acetate and a process for preparing them. Cellulose acetate which the invention especially concerns has a content of combined acetic acid, or an acetylation degree, of 49 to 60 %, which corresponds to an esterification degree of 2.0 to 2.8.

Cellulose acetate is known to have mouldability and solubility in common organic solvents, e.g. acetone, acetic acid or ethyl acetate. For this reason it has been used in the form of chips, flakes, powder, fiber, film or mould articles.

While moldings of cellulose acetate are excellent in properties such as for example transparency, dyeability, touch, and impact strength, the material itself exhibits properties such as adsorptivity, liquid retentivity, and easy wettability of its surface. Therefore, if particles that are both porous and spherical can be obtained from it, these particles will be useful as enzyme carriers, chromatographic packings, slow-releasing adsorbents for perfuming agents, deodorants, medicines or agricultural chemicals, and ion exchangers. The reason why spherical particles are advantageous is that they have good fluidity as compared with particles of other shapes. For example, spherical particles carrying an enzyme give a good efficiency of contact with a reaction solution when they are used in a packed bed, a fluidized bed, or an agitation tank.In these cases, it is desirable that disintegration or deformation of particles does not occur even when the height of the packed bed is increased or when a pressure or the impact of the blade of an agitation tank is exerted on the particles. The disintegration or deformation of the particles in a packed bed results in the formation of unevenly dense portions and causes an uneven flow of a reaction solution and a lowered reaction efficiency. Therefore, the particles must be those which are tough enough to withstand compression or impact.

On the other hand, the particles must have a large pore volume because the amount of an enzyme or a drug fixed or adsorbed thereon is proportional to the pore volume within the particles. Particles of a large pore volume necessarily have a small specific gravity. In general, the requirement that particles should have a small specific gravity or density is contrary to the requirement that they should have sufficient toughness and, therefore, none of the prior art has succeeded in meeting both of these requirements.

As a result of extensive studies, the inventors of the present invention have succeeded in producing porous spherical particles having a good sphericity, a toughness, and a large pore volume by using cellulose acetate as a starting material.

According to the present invention there is provided porous spherical particles substantially of cellulose acetate having an acetylation degree of 49 to 60 %, a particle diameter of 0.05 to 10 mm, a sphericity of at least 0.7, a pore volume of at least 0.4 cc;g, and a collapsing strength of at least 9 kg.

In a preferred embodiment, the sphericity is at least 0.8, the pore volume is at least 0.65 cc/g.

In a further preferred embodiment of the invention the surface of the above defined particles have been saponified. More preferably the surface, of the surface-saponified particles consists substantially of cellulose and the core of the particles consists essentially of cellulose acetate, having an acetylation degree of 48 to 59 %, a particle diameter of 0.05 to 10 mm, a sphericity of at least 0.7, a pore volume of at least 0.4 cc/g and a collapsing strength of at least 10 kg.

In an even more preferred embodiment of the surface-saponified particles, they have an acetylation degree of 50 to 58 % and a particle diameter of 0.5 to 10 mm.

The invention further provides a process for producing porous spherical cellulose acetate particles using a dope comprising a solution formed by dissolving a cellulose acetate of a degree of esterification of 2.0 to 2.8 in an acetic acid/water (80X20 to 90;10, by weight) solvent so that the concentration of the cellulose acetate is 25 t 7 wt. %, feeding said dope through a supply pipe to a coagulation bath comprising an acetic acid/water (30/70 to 42/58, by weight) solvent and having a temperature of 40 + 5'C; operating an agitator having blades passing near a discharge port on the end of said supply pipe; effecting precipitation and granulation while adding water so that the acetic acid to water ratio of the coagulation bath may be maintained at a substantially constant value during said operation; centrifugally separating precipitate particles from the solution; washing these particles with water and drying the particles.

According to the present invention there is also provided a process for preparing surface-saponified, porous, spherical particles of cellulose acetate, which comprises the step of soaking the porous, spherical particles as defined in Claim 1 or 2 in an aqueous sodium hydroxide solution having a concentration of 0.2 to 2 wt. % for 1 to 6 minutes at a ratio of liquid to soiid in the range from 3 to 10.

The process for producing spherical particles according to the present invention is the so-called "precipitation process". This process consists using a solution of a high-molecular substance as a dope; adding said dope to a bath comprising a medium in which the high-molecular substance is not soluble but the solvent of said dope sulution is soluble, that is, a coagulation bath; and applying thereto a shearing force to form particles while precipitating the high-molecular substance by solvent removal.

In the present invention, acetic acidiwater mixture are used as the solvent for a cellulose acetate solution, that is, a dope, and the medium for a coalgulation bath. The solvent for the dope has a composition of an acetic acid to water ratio of 80/20 to 90/10 by weight, and the medium for the coagulation bath has a composition of an acetic acid to water ratio of 30!70 to 4258 by weight.

The dope is prepared by dissolving a cellulose acetate of a degree of acetylation of 49 to 60 % in the above solvent for the dope so that the concentration of the cellulose acetate is 25 + 7 % by weight, preferably about 25%. It is preferable that the viscosity of the dope is about 2,000 poises 40"C. A supply pipe leads from a dope tank to a coagulation bath, and a discharge port such as a nozzle on one end of the supply pipe is submerged in the coagulation bath, and a discharge port such as a nozzle on one end of the supply pipe is submerged in the coagulation bath. The coagulation bath is provided with an agitator having blades thereon.Each of the blades has a cutting edge on the front side to pass near the holes of the nozzle and to cut a rod-like continuous body of the dope which is extruded from the holes of the nozzle and is coagulating. The cut fine pieces form spherical particles while they are precipitating and coagulating.

Since the acetic acid concentration of the acetic acid/water solution brought in by the dope during continued performance of the precipitation and coagulation is higher than the initial acetic acid concentration of the coagulation bath, it is necessary to maintain the acetic acid to water ratio of the coagulation bath substantially constant by adding such an amount of water as to counterbalance the acetic acid brought in. This addition of water makes it possible to keep the concentration gradient of particle/medium constant to thereby afford uniform particles continuously.

The size of particles obtained by this process depends for example on the nozzle hole diameter, the feed rate of the dope, and the agitator speed, and the sphericity is improved when the feed rate and the agitator speed are set such that the length of the cut pieces of dope is nearly equal to the nozzle hole diameter.

Particles having a particle diameter in the range of 0.05 to 10 mm are practical. Those having a particle diameter of less than 0.05 mm show a poor efficiency of production, while those having a particle diameter exceeding 10 mm acquire an excellent sphericity or a pore volume only with difficulty.

In the process of the present invention, it is also possible to use an aged dope, formed in the step of producing a cellulose acetate having a degree of esterification of 2.0 to 2.8, directly as the dope for the precipitation step. This cellulose acetate is one which is obtained by saponifying and aging cellulose triacetate by treatment with an acetic acid/water solvent, and the reaction solution at the time of completion of the aging is called aged dope, because it is in a state in which the cellulose acetate of a degree of acetylation of 49 to 60 %, is dissolved in a highly concentrated aqueous acetic acid solution, and has a viscosity of as high as about 1,000 to 3,000 poises. The separating and recovering step of cellulose acetate from the aged dope is the so-called "precipitation step".It is to be noted that the aged dope usually contains a water-soluble inorganic salt, e.g., magnesium sulfate, which is a product of neutralization of a catalyst (usually sulfuric acid) used in the acetylation reacton. If such a water-soluble inorganic salt is present in a large amount, the size of the internal pores will tend to increase in the precipitation step, thus reducing the pore volume. Therefore, it is preferable that the water-soluble inorganic salt content of the aged dope when it is sent to the precipitation step is 1.5 % or below. The water-soluble inorganic salt content depends on the conditions of the acetylation step, that is, on the amount of catalyst used, so that it is necessary to choose conditions including the use of a smaller amount of catalyst.Such a process for the acetyltion under conditions of a smaller amount of a catalyst is described, for example, in Japanese Patent Laid-Open No.

5980111981.

The particles according to the process of the present invention are thought to be formed in such a manner that a tough shell portion is formed during a relatively early period of the precipitation step and then a thick aqueous acetic acid solution held within the particles is replaced with the relatively thin aqueous acetic acid solution from the coagulation bath, during which time the internal pores are formed. It may be presumed that the tough shell is formed on an interface of a relatively large concentration gradient and, thereafter, the replacement of the solvents at a relatively smaller concentration difference proceeds within the particles, and passages left after the highly concentrated aqueous acetic acid solution has passed form internal pores.

Although, as can be seen from the above, the structure of a particle is established almost completely in the precipitation step, the particles still contain a large amount of acetic acid within them. These particles are centrifugally separated from the solution, subjected to a washing treatment in a water bath and then dried.

The acetic acid remaining within the particles is replaced with water in the washing step, so that the structure of a particle is affected somewhat by the conditions of the washing step. It is preferable that the washing is carried out with water of 40 to 90on. Particles of a larger pore volume can be obtained if the above treatment is carried out at a higher temperature.

The spherical particles of the present invention are extremely tough and have a large pore volume, so that they are highly suited for use for example as packings, carriers or adsorbents. Further, because of the toughness of their shells, the particles can be used also in the production of sintered bodies.

When the particles must have surfaces which are more hydrophilic than those of the cellulose acetate, or when the particles are used in contact with a medium which dissolves, swells, or plasticizes the cellulose acetate, they are used in the form of regenerated cellulose particles which can be obtained by saponifying the cellulose acetate particles with an alkali. This saponification may be effected to such an extent that only the surface is saponified or that the particles are completely saponified. It is also possible to obtain hollow particles of regenerated cellulose by saponifying only the surface and treating the particles with a solvent which dissolves cellulose acetate.

The surface-saponified particles of the invention are prepared by soaking the porous, spherical particles of cellulose acetate as disclosed above with an aqueous solution of sodium hydroxide having a concentration of 0.2 to 2 wt. % for 1 to 6 minutes at a ratio of liquid to solid in the range from 3 to 10.

The comparison betweeen the particles before the surface saponification of the present invention and those after the surface saponification of the present invention has revealed that the particle diameter and the sphericity are somewhat reduced and the pore volume is also reduced, by the saponification but that the collapsing strength is somewhat increased in some cases, or decreased in other cases. It was also found that a content of combined acetic acid was kept at 95 /O or above, suggesting that only a small portion of each particle was saponified.

There is no doubt the saponification occurs on only the very surfaces of particles in view of the fact that the surfaces of the particles after the saponification treatment are modified and a high content of combined acetic acid is maintained as mentioned above. The reason why the saponification cannot be attaind except on the surfaces although the particles before saponification are porous and have excellent impregnatability, may be that the aqueous alkali solution which is used in the present invention imparts moderate swellability to the surfaces of the particles to be treated, and this prevents the alkali from infiltrating into the inside of the particles. It is presumed that this surface-swollen layer is reconverted into a layer which is porous yet dense, when the treated particles are washed with water and dried.

The surface-saponified porous spherical cellulose acetate particles of the present invention have the same applications as those of the porous spherical cellulose acetate particles before surface saponification, and have a particularly excellent effect of impregnation and release of polar substances.

Although the present invention relates to surface-saponified porous spherical cellulose acetate particles and to a process for producing the same, it is also possible to produce surface-saponified porous spherical particles of lower fatty acid cellulose esters, such as cellulose propionate and cellulose butyrate, as substitutes for cellulose acetate, by a similar process, and to use these in similar applications.

The present invention will be further described with reference to the following Examples, but is should be noted that the present invention is by no means limited thereto.

Example 1 A ripening dope containing a cellulose diacetate concentration of 25 %, a magnesium sulfate concentration of 0.9 % and a viscosity at 40 C of 2,100 poises was added to a coagulation bath of a composition of an acetic acid to water ratio of 40 60 by weight to effect precipitation and granulation. The apparatus was operated by using a nozzle diameter of 3 mm, a revolution speed of a threee-blade agitator of 1,000 rpm, and a coagulation bath temperature of 40"C to obtain spherically precipitated particles. The particles are centrifugally separated, washed with water of 60'C, and dried.

The physical properties of the particles were measured according to the following methods.

Sphericity: 20 particles were taken up at random and the largest and smallest diameters of each particle were measured with a micrometer. The sphericity was determined according to the following equation.

sphericity , ' (smallest diameterilargest diameter) 20 Pore volume: A mercury porosimeter (a product of Carlo Elba) was used. The volume of mercury intruded into the pores at a pressure in the range of 0 to 1,000 (kg cm2 G) corresponded te a volume of pores in the range of 75 to 75,000 (A). The pore volume is represented in terms of cc per one gram of the sample.

Collapsing strength: A Monsanto tablet hardness tester (a product of Oiwa Medical Machine Manufacturing Co., Ltd.) was used.

An average of the measured values of 10 particles was calculated.

The determined values of the produced spherical particles are as follows: sphere diameter 3.5 4.0 mm sphericity 0.82 pore volume 0.81 cc'g collapsing strength 11.1 kg.

Content of combined acetic acid About 5 g of a powdered sample was dried in a dryer at 100 to 1 05"C for 2 hours, and weighed accurately.

50 cc of purified acetone was added to this sample and the mixture was dissolved completely. 50 cc of a 0.2 N aqueous NaOH solution and 50 cc of a 0.2 N aqueous HCI solution were added thereto in sequence. The resulting solution was titrated with a 0.2N aqueous NaOH solution by using phenolphthalein as an indicator.

The degree of acetylation was calculated according to the following equation: (A - B) x F x 1.201 combined acetic acid (%) = IA - B) x F x 100 weight (g) of sample wherein: A: volume (cc) of 0.2N aqueous NaOH solution B: volume (cc) of 0.2N aqueous NaOH solution added in a blank test F: factor of 0.2N aqueous NaOH solution In the invention, a content of combined acetic acid which is determined in the above shown manner is called also an acetylation degree. This may be calculated as an esterification degree.

Example 2 1,000 g of porous spherical particles comprising cellulose acetate of a degree of acetylation of 54.5 % (a product of Daicel Chemical Industries, Ltd.), and having an average particle diameter of 3.6 mm, a sphericity of 0.87, a collapsing strength of 15 kg, and a pore volume of 0.68 ccig were immersed in 500 cc of a 1% aqueous solution of sodium hydroxide at room temperature for 3 minutes. After centrifugally separating the mixture, the particles were washed with warm water of 40OC until the water after washing became neutral, and then dried in a dryer at 100 to 110'C for 3 hours to obtain surface-saponified porous spherical particles.

These particles had an average degree of acetylation of 53.4 %, an average particle diameter of 3.2 mm, a sphericity of 0.82, a pore volume of 0.43 ccig, and a collapsing strength of 17 kg.

Example 3 100 g of porous spherical particles comprising cellulose acetate of a degree of acetylation of 55.2 % (a product of Daicel Chemical Industries, Ltd.), and having an average particle diameter of 5.3 mm, a sphericity of 0.90, a collapsing strength of 14 kg, and a pore volume of 0.75 cc/g were immmersed in 500 cc of a 0.5% aqueous solution of sodium hydroxide and treated in the same manner as that in Example 2 to obtain surface-saponified porous spherical particles. These particles had an average content of combined acetic acid of 54.5%, an average particle diameter of 5.1 mm, a sphericity of 0.85, a pore volume of 0.51 ccig, and a collapsing strength of 15 kg.

Example 4 2 g of bergamot oil (linalyl acetate content of 40 %) was addedto 10 g of the surface-saponified spherical particles obtained in Example 2 and the mixture was agitated. After about 10 minutes, the liquid was completely impregnated, and the surfaces of the particles became dry and non-sticky. Separately, spherical particles before the surface saponification of Example 2 were impregnated with a perfume by a similar treatment. The surfaces of the particles were sticky and tended to stick to each other.

On the contrary, when the surface-saponified spherical particles which were obtained in Example 2 and impregnated with a perfume were stored at 80-C, their surfaces did not become sticky.

The evaporation rate of the perfume in an open air at a room temperature was determined. 10 days were necessary for 50 % evaporation, and 45 days were necessary for 90 % evaporation. This suggested an excellent effect of slow release.

Claims (12)

1. Porous, spherical particles consisting substantially of cellulose acetate, having an acetylation degree of 49 to 60 %, a particle diameter of 0.05 to 10 mm, a sphericity of at least 0.7, a pore volume of at least 0.4 cc/g and a collapsing strength of at least 9 kg or higher.

2. Particles as claimed in Claim 1, having a sphericity of at least 0.8, a pore volume of at least 0.65 cc/g.

3. Particles as claimed in Claims 1 or 2, the surfaces of which have been saponified.

4. Particles as claimed in Claim 3, in which the surface of the particles consists substantially of cellulose and the core of the particles consists substantially of cellulose acetate, having an acetylation of 48 to 59 %, a particle diameter of 0.05 to 10 mm, a sphericity of at least 0.7, a pore volume of at least 0.4 ccig and a collapsing strength of at least 1 Okg.

5. Particles as claimed in any of claims 1 to 4, having an acetylation degree of 50 to 58 % and a particle diameter of 0.5 to 10 mm.

6. Porous, spherical particles consisting substantially of cellulose acetate, substantially as herein described with reference to and as illustrated in any of Examples 1 to 4.

7. A process for producing porous spherical cellulose acetate particles using a dope comprising a solution formed by dissolving a cellulose acetate of a degree of esterification of 2.0 to 2.8 in an acetic acid/water (80/20 to 90/10, by weight) solvent so that the concentration of the cellulose acetate is 25 t 7 wt.

%,feeding said dope through a supply pipe to a coagulation bath comprising an acetic acid/water (30/70 to 42/58, by weight) solvent and having a temperature of 40 + 5"C; operating an agitator having blades passing near a discharge port on the end of said supply pipe; effecting precipitation and granulation while adding water so that the acetic acid to water ratio of the coagulation bath may be maintained at a substantially constant value during said operation; centrifugally separating precipitate particles from the solution; washing these particles with water and drying the particles.

8. A process as claimed in Claim 7 in which the water used for washing the particles is at a temperature of 40 to 90"C.

9. A process for preparing surface-saponified, porous, spherical particles of cellulose acetate, which comprises the step of soaking the porous, spherical particles as defined in Claim 1 or 2 in an aqueous sodium hydroxide solution having a concentration of 0.2 to 2 wt. % for 1 to 6 minutes at a ratio of liquid to solid in the range from 3 to 10.

10. A process as claimed in Claim 7 in which the product is the particles having the physical properties as defined in Claim 1 or 2.

11. A process as claimed in Claim 9 in which the product is the particles having the physical properties as defined in Claims 3 or 4.

12. A process for preparing porous spherical cellulose acetate articles substantially as herein described with reference to and as illustrated in any of Examples 1 to 4.