Process for producing an alkali salt of a carboxymethylcellulose ether

Abstract: A process is disclosed for the preparation of an alkali salt of a carboxymethylcellulose ether by reacting a cellulosic material with an etherifying agent, in the presence of an alkali, in an aqueous organic solvent, wherein the improve­ ment comprises adding the etherifying agent and only part of the entire amount of said alkali in the initial stage of the reaction, thereby initiating the etherification reaction in the presence of an excess amount of the etherifying agent such that the molar ratio of is in the range of 0.10 to 0.99; and subsequently adding the remainder of said alkali in one or more portions in a second stage and carrying out the etherification reaction in such a manner that said molar ratio of alkali etherifying agent in the final stage becomes at least 1.00. An additional embodiment of the invention comprises repeating this procedure using the product of the first reaction as the starting material in the second reaction, whereby an alkali carboxymethylcellulose salt having a high degree of substitution can be obtained.

Description: The present invention relates to processes for producing an alkali metal salt of carboxymethylcellulose ether (hereinafter referred to as CMC) having a uniform substituent distribution, a high degree of substitution (DS 0,5-3,0) and excellent transparency by means of a solvent process. The term "CMC" is commonly used in the art to mean sodium carboxymethyl cellulose in particular, but in the present context the term "CMC" includes not only the sodium salt, but also other alkali metal salts, such as the potassium salt. CMC is generally produced by reacting a cellulosic material with an etherifying agent in the presence of an alkali. It is well known to use sodium hydroxide as the alkali and monochloroacetic acid or its alkali salt as the etherifying agent. Processes for the production of CMC may be classified roughly into two groups, i.e., (1) aqueous medium processes wherein an aqueous reaction medium is used, as described in US-A-2 524 024, and (2) solvent processes wherein an organic solvent, including mixtures of water and one or more organic solvents, is used as disclosed in DE-A-2 557 576 and C.A. Vol. 74, No. 22, page 73. Solvent processes have been employed in practice on an industrial scale in many cases because these processes have the advantages that an alkali cellulose can be obtained using the alkali in an amount smaller than the amount required in an aqueous medium process, the etherification reaction is completed in a relatively short period of time, the availability of the etherifying agent is high, the amount of the etherifying agent needed is small and high quality CMC can be obtained. In the production of CMC according to one solvent process, cellulose is first reacted with sodium hydroxide in an aqueous organic solvent to form an alkali salt of cellulose, and the monochloroacetic acid is added to the reaction mixture to carry out the etherification reaction. In another solvent process, sodium monochloroacetate is added to cellulose in an aqueous organic solvent to impregnate the cellulose with sodium monochloroacetate, and then sodium hydroxide is added thereto to carry out the etherification reaction. In both process, the molar ratio of alkali/etherifying agent in the etherification reaction system is given by the formula: This ratio is at least 1.0 and is generally maintained at about 1.10, the optimum alkali/etherifying agent molar ratio range being 1.0-1.30. This range was selected because, if this molar ratio is above 1.30, a side reaction of sodium monochloroacetate as shown in the following reaction (1) is likely to occur so as to reduce the available content of expensive sodium monochloroacetate, and such a result is economically disadvantageous. On the other hand, if this molar ratio is less than 1.0, glycolic acid is formed by a side reaction according to the following reaction (2) when the alkali in the reaction system has been consumed, thereby making the reaction system acidic. The glycolic acid attacks the carboxyl groups of the CMC, thereby converting part of the CMC into its free acid form and thereby seriously reducing the solubility of the resulting CMC: (1) CICH 2 COONa+NaOH→CH 2 (OH)COONa+NaCI (2) CICH 2 COONa+H 2 O→CH 2 (OH)COOH+NaCl Therefore, in the production of CMC, the alkali/etherifying agent molar ratio is generally regulated to be about 1.10 so that the etherification reaction is carried out in the presence of an excess amount of the alkali and, after completion of the reaction, the excess alkali is neutralized with, for example, acetic acid, whereby to obtain CMC. Upon investigation, the present inventors surprisingly have found that CMC having a uniform substituent distribution and an excellent transparency can be obtained, with a monochloroacetic acid availability far higher than that of conventional processes, by a process comprising reacting a cellulosic material with an etherifying agent, in the presence of an alkali, in an aqueous organic solvent, to form an alkali salt of carboxymethylcellulose ether, wherein the etherification reaction is initiated in the presence of an excess amount of the etherifying agent such that the molar ratio of alkalietherifying agent in the reaction system, namely, is 0.10 to 0.70 during an initial stage after the addition of a portion of the total alkali and the entire amount of the etherifying agent, and the etherification reaction is continued in a second stage wherein the remainder of the alkali is added in one or more subportions so as to prevent the acidification of the reaction system due to the consumption of the alkali as the etherification reaction proceeds, whereby the molar ratio of alkali/etherifying agent, namely, becomes at least 1.0 when the etherification reaction is completed. According to the present invention the molar ratio of alkaliletherifying agent in the initial stage of the etherification reaction is regulated to be within the range of 0.10 to 0.70, preferably 0.30 to 0.70, lower than the usual range of 1.0 to 1.30 employed in the conventional processes, such that the reaction in the initial stage is carried out in the presence of an excess amount of the etherifying agent. Consequently, the above-mentioned side reaction (1) is controlled and the availability of monochloroacetic acid is kept high. In the reaction of preparing CMC, the diffusion (or penetration) into the cellulose of sodium monochloroacetate, which has a lower compatibility with cellulose than that of the alkali, is considered to be a rate-controlling step. Therefore, if the etherification reaction of preparing CMC is carried out, in the presence of an excess amount of an alkali, at a temperature of as high as 60° to 80°C, as in the conventional processes, the etherification is completed by the excess amount of the alkali before the sodium monochloroacetate is uniformly diffused or penetrated into the cellulose fibers, resulting in a non-uniform substituent distribution in the obtained CMC. However, if the etherification is initiated and carried out to some extent in the presence of an excess amount of sodium monochloroacetate, according to the present invention, diffusion or penetration of the sodium monochloroacetate into the cellulose fibers is promoted and reaction with a small amount of the alkali, which has penetrated into the fiber, is effected to obtain CMC having a uniform substituent distribution. It is necessary in the present invention to initiate the reaction in the presence of an excess amount of the etherifying agent, i.e. that the reaction be carried out in the above-mentioned 0.10 to 0.70 molar ratio range for at least 30% of the etherification reaction time period. Subject-matter of the present invention is a process for preparing an alkali metal salt of carboxymethylcellulose ether, which comprises: reacting cellulose, in the presence of an alkali in an aqueous organic solvent, with an etherifying agent effective to etherify said cellulose to form carboxymethylcellulose ether and then recovering said alkali metal salt of carboxymethylcellulose ether from the reaction mixture, which is characterized in that the etherification reaction is carried out in two steps at 60 to 80°C, wherein in the first step the entire amount of said etherifying agent is present in the reaction mixture and the molar ratio of said alkali/said etherifying agent equal to is maintained in the range of from 0.10 to 0.70 for at least 30% of the total etherification reaction period, this being the time period in which the reaction temperature is kept at 30 to 90°C, and then in the second step, additional alkali is added in one or more portions to the reaction mixture obtained from said first step, without adding more of said etherifying agent, until said molar ratio of said alkali/said etherifying agent is at least 1.00, and completing the etherification reaction. As the reaction solvent used in the process of the present invention, there can be mentioned aqueous organic solvents such as ethyl alcohol, n-propyl alcohol, isopropyl alcohol (hereinafter referred to as (PA), n-butyl alcohol, isobutyl alcohol, tert-butyl alcohol or acetone, as well as aqueous organic solvent mixtures such as ethyl alcohol/benzene, ethyl alcohol/toluene or ethyl alcohol/n-hexane. As the alkali, sodium hydroxide or potassium hydroxide is suitably used. As the etherifying agent, there can be used monochloroacetic acid, sodium monochloroacetate, potassium monochloroacetate or an ester of monochloroacetic acid such as ethyl, n-propyl, isopropyl, n-butyl, isobutyl or tertbutyl monochloroacetate. The degree of substitution (hereinafter referred to as DS) of the CMC produced by the process of the present invention is variable within the range of 0.5 to 3.0. The process of the invention is particularly advantageous in the pmduction of CMC having a DS in the range of 0.8 to 2.0 which is substantially equal to that of commercially available CMC prepared using a large amount of the alkali. CMC produced by the process of the present invention contains the substituents uniformly introduced therein. Therefore, as compared with CMC produced by the conventional processes, it contains smaller amounts of (1) insoluble matter and (2) large, partially dissolved, swollen gel, and therefore it has a higher transparency. When CMC obtained according to the present invention is used as an ingredient of printing paste, clogging of the screen is reduced. Further, CMC thus obtained has an excellent resistance to putrefaction. which is very important practical physical property for CMC to be used for drilling engineering works, oil well drilling, production of drinks fermented with lactic acid bacteria, tooth pastes, printing pastes, liquid pastes and fiber wall materials. According to a preferred embodiment of the invention said molar ratio in the first reaction step is in the range of from 0.30 to 0.70, and said molar ratio in the second reaction step is in the range of 1.00 to 1.50, preferably 1.0 to 1.3. The inventors have further found that CMC having an average degree of substitution (DS) of as high as 0.9 to 3.0, preferably 2.0 to 3.0, can be obtained by a process, with a high monochloroacetic acid availability, comprising reacting a cellulosic material with an etherifying agent, in the presence of an alkali, in an aqueous organic solvent, to form an alkali salt of a carboxymethylcellulose ether, which process comprises two sequential reaction steps and the etherification is conducted at 60 to 80°C, which comprises in the first reaction step of the first reaction sequence. reacting cellulose, in the presence of an alkali in an aqueous organic solvent, with an etherifying agent effective to etherify said cellulose to form carboxymethylcellulose ether having an average degree of substitution in the range of from 0.8 to 2.2, wherein the entire amount of said etherifying agent used in the first reaction step is present in the reaction mixture during the first reaction step and the molar ratio of said alkalilsaid etherifying agent equal to is maintained in the range of from 0.10 to 0.70, in particular from 0.30 to 0.70. for at least 30% of the total etherification reaction period; then, in a second reaction step of the first reaction sequence, adding additional alkali to one or more portions to the reaction mixture obtained from said first step, without adding more of said etherifving agent until said molar ratio of said alkali/said etherifying agent is in the range of from 1.00 to 1.50. preferably from 1.0 to 1.3, and completing the etherification reaction to obtain an alkali metal salt of carboxymethylcellulose ether having an average degree of substitution of from 0.8 to 2.2; then in the first reaction step of the second reaction sequence, reacting said alkali metal salt of carboxymethylcellulose obtained from said first reaction sequence, in the presence of an alkali in an aqueous organic solvent, with an additional quantity of said etherifying agent wherein during the first reaction step of said second reaction sequence the molar ratio of said alkali/said etherifying agent is maintained in the range of from 0.10 to 0.70 until the degree of substitution of said alkali metal salt of carboxymethylcellulose is further increased; and then in the second step of said second reaction sequence, adding an additional quantity of said alkali in one or more portions, without adding additional etherifying agent, until said molar ratio of said alkali/said etherifying agent is in the range of from 1.00 to 1.50, preferably from 1.0 to 1.3, to obtain an alkali metal salt of carboxymethylcellulose having a degree of substitution higher than that of the alkali metal salt of carboxymethylcellulose obtained at the end of said first reaction sequence and in the range of from 0.9 to 3.0; and then recovering said latter alkali metal said of carboxymethylce!lulose from the reaction mixture. Accordino to this second embodiment of the present invention, CMC having a DS as high as at least 2.00. preferably 2.0 to 3.0, particularly at least 2.50, can be produced using a two reaction sequence process, with a high availability of monochloroacetic acid, by controlling the side reaction (1) by reducing the amount of the alkali in the reaction system by maintaining the molar ratio of alkali etherifying agent in the initial stages of the first and second reaction sequences in the range of 0.10 to 0.70, preferably 0.30 to 0.70. The reaction conditions, in particular the materials usable as the alkali, cellulosic material, etherifying agent and aqueous organic solvent are the same as in the first embodiment of the invention. It is necessary to initiate the reaction in the presence of an excess amount of the etherifying agent in the initial stages of both of the first and second reaction sequences. It is necessary that the initial stages or both reaction sequences be carried out in the above-mentioned molar ratio range of 0.10 to 0.70, for at least 30% of the total etherification reaction period in each reaction sequence. In the production of CMC by the process of the second embodiment of the invention, the reaction in the second reaction sequence to be carried out after completion of the reaction in the first reaction sequence, can be effected by a method wherein the excess alkali contained in the reaction mixture is neutralized with, for example, acetic acid after completion of the etherification reaction in the first reaction sequence. The mixture is then washed with an aqueous alcohol solution, preferably with a 75% aqueous methanol solution to remove by-products, such as common salt, sodium glycolate and sodium acetate, and the residue is dried and subjected to the reaction in the second reaction sequence. Alternatively, a method wherein the etherification reaction mixture from the first reaction sequence is cooled to a given temperature and subjected directly to the reaction of the second reaction sequence can be employed. The degree of substitution (DS) of CMC produced by the two-reaction sequence process of the present invention varies in the range of 0.9 to 3.0. This two-reaction sequence process is particularly advantageous in the production of CMC having a DS of higher than 2.0, particularly higher than about 2.5, because the production of CMC having such a high DS has been difficult to attain with conventional one-step processes. CMC produced on a commercial scale by the process of the second embodiment of the present invention has a DS of higher than 2.00, particularly higher than 2.5. Therefore, as compared with CMC having a DS of less than 2.00 produced on a commercial scale by the conventional processes, it has higher water-solubility, and aqueous solutions thereof have a higher resistance to chemicals. Therefore, CMC of the invention is preferable for use as an assistant in the production of printing pastes, in drilling engineering works, oil well drilling, as an additive for drinks fermented with lactic acid bacteria or for tooth pastes. In addition, it will be possible to use the CMC of the invention as a reactive, high molecular weight intermediate for other derivatives in other fields. According to the invention, the etherification reaction is conducted at 60 to 80°C, for 5 to 320 minutes, preferably 30 to 90 minutes. A weight ratio of isopropanol to water is 1/1 to 30/1, preferably 4/1 to 20/1. A weight ratio of the solvent mixture to cellulose is 2/1 to 50/1, preferably 3/1 to 30/1. It is preferred that the first stage is ended when 90 to 99 wt.% of NaOH has been used, and the second stage is ended when 100% of the etherifying agent has been used. According to a further preferred embodiment of the invention CMC is prepared using a process which comprises in a first reaction step, dissolving a water-soluble alkali in a solvent mixture of isopropanol and water in which the weight ratio of isopropanol/water is from 1/1 to 30/1, adding cellulose to said solvent mixture in such an amount that the weight ratio of said solvent mixture/said cellulose is from 2/1 to 50/1 to form a slurry, then adding monochloroacetic acid to said slurry so that the molar ratio of said alkali/said monochloroacetic acid equal to is in the range of from 0.30 to 0.70, for at least 30% of the total etherification reaction period, then heating said slurry to a temperature in the range of from 60 to 80°C for 5 to 120 minutes to partially etherify said cellulose to convert same to caraboxymethylcellulose ether; and then, in a second reaction step, adding additional alkali in one or more portions to the reaction mixture obtained from said first step, without adding more of said monochloroacetic acid, until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the reaction mixture to a temperature in the range of from 60 to 80°C for 5 to 120 minutes to complete the etherification reaction; and then recovering from the reaction mixture an alkali metal salt of carboxymethylcellulose having a degree of substitution of from 0.8 to 2.2. A further preferred two reaction sequence process for preparing an alkali metal salt of carboxymethylcellulose wherein each reaction sequence comprises two sequential reaction steps, comprises in the first reaction step of the first reaction sequence, dissolving a watersoluble alkali in a first solvent mixture of isopropanol and water in which the weight ratio of isopropanol/water is from 1/1 to 30/1, adding cellulose to said first solvent mixture containing said alkali in such an amount that the weight ratio of said first solvent mixture/said cellulose is from 2/1 to 50/1 to form a first slurry, then adding monochloroacetic acid to said slurry so that the molar ratio of said alkali/said monochloroacetic acid equal to is in the range of from 0.30 to 0.70, for at least 30% of the total etherification reaction period, then heating said slurry to a temperature in the range of from 60 to 80°C for 5 to 320 minutes to partially etherify said cellulose to convert same to carboxymethylcellulose ether; and then, in a second reaction step of the first reaction sequence, adding additional alkali in one or more portions to the reaction mixture obtained from said first step, without adding more of said monochloroacetic acid, until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the reaction mixture to a temperature in the range of from 60° to 80°C for 5 to 320 minutes to complete the etherification reaction having a degree of substitution of from 0.8 to 2.2; then in the first step of the second reaction sequence, adding said alkali metal salt of carboxymethylcellulose ether having a degree of substitution of from 0.8 to 2.2 obtained in said first reaction sequence to a second solvent mixture containing said alkali having the same range of the same components as said first solvent mixture, then adding monochloroacetic acid thereto to form a second reaction mixture in which said molar ratio of said alkali/said monochloroacetic acid in said second reaction mixture is in the range of from 0.30 to 0.70, then heating said second reaction mixture to a temperature in the range of from 60° to 80°C for 5 to 320 minutes to further increase the degree of substitution of said alkali metal salt of carboxymethylcellulose; then in the second step of said second reaction sequence adding an additional quantity of said alkali in one or more portions to the second reaction mixture, without adding more of said monochloroacetic acid until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the second reaction mixture to a temperature in the range of from 60° to 80°C for 5 to 320 minutes to obtain an alkali metal salt of carboxymethylcellulose having a degree of substitution higher than that of the alkali metal salt of carboxymethylcellulose obtained at the end of said first reaction sequence and in the range of from 2.0 to 3.0; and then recovering said latter salt of carboxymethylcellulose from the second reaction mixture. The following examples and comparative examples will further illustrate the present invention in connection with the drawing which is a graph showing the properties of CMC obtained in the Examples and Comparative Examples. The following properties of the resulting CMC, obtained by the process of the invention, were measured or determined as described below: (1) Degree of substitution (DS): 1 g of CMC was weighed accurately and incinerated in a platinum or porcelain crucible at 600°C. Sodium oxide formed by the incineration was titrated with N/10 sulfuric acid using phenolphthalein as an indicator. From the amount (A ml) of the titrant added, DS was calculated according to the formula: DS= 162×A×f 10000-(80×A×f) wherein f represents a titer of N/10 sulfuric acid. (2) Transparency: The transparency of a 1 wt.% aqueous CMC solution irradiated with a given light source is determined by the height of a liquid column. This is a method conventionally employed in the art. If the reaction is heterogeneous, the transparency is reduced by the unreacted cellulose, undissolved matter, swollen gel, etc. The higher the homogeneity of the reaction is, the higher the transparency will be. (3) Amount of glucose formed by hydrolysis with cellulase (uniformity of substituent distribution): The substituent distribution of CMC includes (1) the distribution of hydroxyl groups in 2-, 3- and 6-positions in the anhydroglucose unit, (2) intramolecular distribution and (3) intermolecular distribution. It is considered that these three types of substituent distributions are closely related to the physical properties of CMC. Further, the intramolecular and intermolecular substituent distributions supposedly exert a great influence on the amount and size of the undissolved matter and the semi-dissolved, swollen gel, and the resistance to putrefaction, both of which are important practical physical properties. The uniformity of the substituent distribution in the present invention was determined by adding 5 mg/g-CMC of a cellulase (cellulase AP; a product of Amano Seiyaku Co., Ltd.) to a 1% aqueous CMC solution to hydrolyze the CMC at room temperature for 140-145 hours, the hydrolysis being substantially complete in about 140 hours. Glucose formed by the hydrolysis was determined according to the glucose oxidase method, as described by M. G. Wirick et al. J. Poly. Sci., Part A-1, vol. 6, 1965 (1968), which discloses that a CMC molecule having a chain of at least 3 unsubstituted anhydroglucose units is hydrolyzed in the presence of a cellulase (a hydrolase for cellulose). The smaller the amount of glucose formed, the higher is the uniformity of the substituent distribution. The subsituent distribution measured herein includes both intramolecular and intermolecular distributions. The amount of glucose formed is represented by the number of glucose molecules per 1000 anhydroglucose units in the CMC (number/1000 AGU). (4) Resistance to putrefaction: It is considered that CMC is putrefied mainly due to the hydrolysis by celulase produced by microorganisms. The resistance to putrefaction was determined from a viscosity ratio before and after the hydrolysis, using a 1% aqueous solution with cellulase as in (3), according to the formula: The higher the viscosity ratio is, the higher is the resistance to putrefaction. *The viscosity was measured by means of a Brookfield L-type viscometer (rotor Nos. 1-4) at 60 rpm at 25°C. (5) Availability of monochloroacetic acid (AM): Availability of monochloroacetic acid (AM) was determined according to the formula: (6) Viscosity: A 1% solution of 2.5 g of CMC was prepared in a cylindrical glass vessel having a diameter of 55 mm and a depth of 125 mm. The temperature was maintained at 25°C. After rotation at a rotor speed of 60 rpm for 1 minute, the viscosity was measured with a Brookfield L-type viscometer. By multiplying the resulting value by a given constant, the viscosity (cP) was determined. The following examples do not limit the present invention. In the Examples and Comparative Examples, parts and percentages are given by weight. Example 1 575 parts of isopropyl alcohol (hereinafter referred to as IPA) were charged in a 5 liter reactor having two-shaft stirring blades, and a solution of 120.6 parts of sodium hydroxide (purity: 98%) in 126.2 parts of pure water was charged therein. After cooling to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%) were added to the mixture, and the mixture was stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 172 parts of monochloroacetic acid (purity: 98%) in 172 parts of IPA was added thereto under cooling and the mixture was stirred at 20° to 30°C for 30 mintues. Thereafter, the temperature was elevated to 60°C over about 10 minutes and the etherification reaction was carried out for 60 minutes. Then a solution of 25.2 parts of sodium hydroxide is 16.8 parts of pure water was added thereto and the mixture was stirred at 60° to 70°C for 15 minutes. After the etherification reaction was carried out at 70°C for 90 minutes, the very small amount of sodium hydroxide remaining was neutralized with acetic acid. After completion of the reaction, the reaction mixture was taken out of the reactor and centrifuged to remove IPA (reaction solvent). The residue was washed with 4000 parts of a 75% aqueous methyl alcohol solution three times to remove by-produced common salts, sodium glycolate and sodium acetate. The residue was centrifuged again to remove the aqueous methyl alcohol solution. The product thus purified was dried with a dryer at 80° to 100°C for about 6 hours to obtain the intended alkali salt of carboxymethylcellulose ether. Comparative Example 1 575 parts of IPA were charged in a 5 liter reactor having two-shaft stirring blades and a solution of 145.8 parts of sodium hydroxide (purity: 98%) in 143 parts of pure water was charged therein. After cooling to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%) were added to the mixture and stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 172 parts of monochloroacetic acid (purity: 98%) in 172 parts of IPA was added thereto under cooling and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 70°C in about 15 minutes and the etherification reaction was carried out for 90 minutes. Then, the remaining very small amount of sodium hydroxide was neutralized with acetic acid. After washing followed by drying, which were carried out in the same manner as in Example 1, purified alkali salt of carboxymethylcellulose ether was obtained by a conventional method as described in Example 1. Examples 2-5 An alkali salt of carboxymethylcellulose ether, according to the present invention, was obtained by the same production, purification and drying methods as described in Example 1, except that the amounts of IPA, water, sodium hydroxide and monochloroacetic acid were altered as shown in Table 1. Comparative Examples 2-5 An alkali salt of carboxymethylcellulose ether was obtained according to the conventional process by the same production, purification and drying methods as in Comparative Example 1 except that the amounts of IPA, water, sodium hydroxide and monochloroacetic acid were altered as shown in Table 1. Example 6 1124 parts of IPA were charged in a 5 liter reactor having two-shaft stirring blades and a solution of 163.2 parts of sodium hydroxide (purity: 98%) in 126.0 parts of pure water was charged therein. After cooling to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%) were added to the mixture and stirred at 29° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 286.2 parts of monochloroacetic acid (purity: 98%) in 286.2 parts of IPA was added thereto under cooling, and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 60°C in about 10 minutes and the etherification reaction was carried out for 60 minutes. A solution of 42.0 parts of sodium hydroxide in 28.0 parts of pure water was added thereto and the etherification reaction was continued at 60°C for 60 minutes. A solution of 42.0 parts of sodium hydroxide in 28.0 parts of pure water was added thereto and the mixture was stirred at 60° to 70°C for 15 minutes. The etherification reaction was carried out at 70°C for 90 minutes. The remaining very small amount of sodium hydroxide was neutralized with acetic acid. After purification followed by drying, both carried out in the same manner as described in Example 1, the intended alkali salt of carboxymethylcellulose ether was obtained. The properties of the CMC obtained in the Examples and Comparative Examples are given in Table 1. Part of the results for the hydrolysis of CMC with cellulase is shown in the drawing with the degree of substitution (DS) of CMC as the abscissa and the amount of glucose formed as the ordinate. In the drawing, an open circle, "○", represents the results obtained for examples of the invention, and a darkened circle, "•", represents the results obtained for the Comparative Examples. It is apparent from Table 1 and the drawing that the alkali salt of carboxymethylcellulose ether obtained by the process of the present invention has (1) higher availability of monochloroacetic acid, (2) higher transparency, (3) a far smaller amount of glucose formed by the hydrolysis with cellulase and, therefore, higher uniformity of the substituent distribution, and (4) more excellent resistance to putrefaction in comparison with the alkali salts of carboxymethylcellulose ether obtained by the conventional process of the comparative examples using the same amounts of the alkali and etherifying agent. Example 7 996 parts of isopropyl alcohol (IPA) were charged in a 5 liter reactor having two-shaft stirring blades and a solution of 136.8 parts of sodium hydroxide (purity: 98%) in 163.6 parts of pure water was charged therein. After cooling to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%, average degree of polymerization: 2300) were added to the mixture, and the mixture was stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 215.5 parts of monochloroacetic acid (purity: 98%) in 215.5 parts of IPA was added thereto under cooling and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 60°C over about 10 minutes and the etherification reaction was carried out for 60 minutes. A solution of 45.6 parts of sodium hydroxide in 30.4 parts of pure water was added thereto and the mixture was stirred at 60° to 70°C for 15 minutes. After the etherification reaction was carried out at 70°C for 90 minutes, the remaining very small amount of sodium hydroxide was neutralized with acetic acid. Thus, the reaction of the first reaction sequence was completed. The reaction mixture was taken out of the reactor and centrifuged to remove IPA (reaction solvent). The residue was washed three times with 4000 parts of a 75% aqueous methyl alcohol solution to remove byproducts, such as common salt, sodium glycolate and sodium acetate, and then dried at 80° to 100°C for about 4 hours to obtain CMC. CMC thus obtained was subjected to the reaction of the second reaction sequence in the same reactor under the same conditions as in the first step. After purification and drying, the intended CMC of the invention was obtained. Comparative Example 6 996 parts of IPA were cahrged in a 5 liter reactor having two-shaft stirring blades and a solution of 182.4 parts of sodium hydroxide (purity: 98%) in 194 parts of pure water was charged therein. After cooling the mixture to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%, average degree of polymerization: 2300) were added to the mixture and stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 215.5 parts of monochloroacetic acid (purity: 98%) in 215.5 parts of IPA was added thereto under cooling and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 70°C in about 15 minutes and the etherification reaction was carried out for 90 minutes. Then, the remaining very small amount of sodium hydroxide was neutralized with acetic acid. Thus, the reaction of the first reaction sequence was completed. The reaction mixture was taken out of the reactor and centrifuged to remove IPA (reaction solvent). The residue was washed with 4000 parts of a 75% aqueous methyl alcohol solution three times to remove by-products and then dried at 80° to 100°C for about 4 hours to obtain CMC. CMC thus obtained was subjected to the reaction of the second reaction sequence in the same reactor under the same conditions as in the first reaction sequence. After the purification and drying procedures, CMC was obtained by a conventional recovery process. Example 8 CMC according to the present invention was obtained by the same production, purification and drying methods as in Example 7 except that the amounts of IPA, water, sodium hydroxide and monochloroacetic acid were altered as shown in Table 2. Comparative Examples 7 and 8 CMC was obtained according to the conventional process by the same production, purification and drying methods as in Comparative Example 6 except that the amounts of IPA, water, sodium hydroxide and monochloroacetic acid were altered as shown in Table 2. Example 9 1687 parts of IPA were charged in a 5 liter reactor having two-shaft stirring blades and a solution of 255.2 parts of sodium hydroxide (purity: 98%) in 166.2 parts of pure water was charged therein. After cooling to 20° to 30°C, 200 parts of powdery cellulose (purity: 95%, average degree of polymerization: 2300) were added to the mixture and the mixture was stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 448.9 parts of monochloroacetic acid (purity: 98%) in 448.9 parts of IPA was added thereto under cooling and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 60°C over about 10 minutes and the etherification reaction was carried out for 30 minutes. A solution of 63.7 parts of sodium hydroxide in 42.5 parts of pure water was added thereto and the etherification reaction was continued at 60°C for 30 minutes. A solution of 82.9 parts of sodium hydroxide in 55.3 parts of pure water was added thereto and the mixture was stirred for 15 minutes. The etherification reaction was carried out at 70°C for 90 minutes. After completion of the etherification reaction, sodium hydroxide remaining in a very small amount was neutralized with acetic acid to complete the reaction in the first reaction sequence. The reaction mixture was then purified and dried in the same manner as described in Example 7. CMC thus obtained was subjected to the reaction of the second reaction sequence in the same reactor and under the same conditions as in the first reaction sequence. After purification and drying, CMC according to the present invention was obtained. Example 10 A solution of 1763 parts of IPA and 82.7 parts of sodium hydroxide (purity: 98%) in 93.0 parts of pure water was charged in a 3 liter separable flask. 75 parts of powdery cellulose (purity: 95%, average degree of polymerization: 2300) were added to the mixture and stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 125.0 parts of monochloroacetic acid in 125.0 parts of IPA was added thereto in portions and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 60°C and the etherification reaction was carried out at 60°C for 60 minutes. A solution of 29.3 parts of sodium hydroxide in 19.5 parts of pure water was added thereto. The temperature was controlled to 70°C and the etherification reaction was carried out at 70°C for 60 minutes. Thus, the reaction in the first reaction sequence was completed. Then, the reaction system was cooled to 15°C and the reaction in the second reaction sequence was initiated. In this reaction sequence, a solution of 82.7 parts of sodium hydroxide in 55.1 parts of pure water was added thereto and stirred at 20° to 30°C for 30 minutes. A solution of 125.0 parts of monochloroacetic acid in 125.0 parts of IPA was added thereto in portions and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 60°C in about 10 minutes and the etherification reaction was carried out for 60 minutes. Then a solution of 29.3 parts of sodium hydroxide in 19.5 g of pure water was added thereto. The temperature was controlled to 70°C and the etherification reaction was carried out at 70°C for 60 minutes. After completion of the etherification reaction, the remaining very small amount of sodium hydroxide was neutralized with acetic acid to complete the reaction of the second reaction sequence. The reaction mixture was centrifuged to remove IPA (reaction solvent). The product was washed three times with 2000 parts of a 75% aqueous methyl alcohol solution to remove by-products. After drying at 80° to 100°C for about 4 hours, CMC of the present invention was obtained. Comparative Example 9 A solution of 1763 parts of IPA and 112.0 parts of sodium hydroxide in 112.5 parts of pure water was charged in a 3 liter separable flask. 75 parts of powdery cellulose (purity: 95%, average degree of polymerization: 2300) were added to the mixture and stirred at 20° to 30°C for 60 minutes to obtain an alkali cellulose. Then, a solution of 125.0 parts of monochloroacetic acid in 125.0 parts of IPA was added thereto in portions and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 70°C over about 15 minutes and the etherification reaction was carried out at 70°C for 60 minutes. Thus, the reaction in the first reaction sequence was completed. Then, the reaction system was cooled to 15°C and the reaction in the second reaction sequence was initiated. In this step, a solution of 112.0 parts of sodium hydroxide in 74.5 parts of pure water was added thereto and the whole was stirred at 20° to 30°C for 30 minutes. A solution of 125.0 parts of monochloroacetic acid in 125.0 parts of IPA was added thereto and the mixture was stirred at 20° to 30°C for 30 minutes. Thereafter, the temperature was elevated to 70°C in about 15 minutes and the etherification reaction was carried out for 60 minutes. After completion of the etherification reaction, the remaining very small amount of sodium hydroxide was neutralized with acetic acid to complete the reaction of the second reaction sequence. After washing and drying in the same manner as described in Example 10, CMC was obtained according to a conventional process. Comparative Examples 10 and 11 The same procedure as in Comparative Example 6 was repeated except that the amounts of IPA, water, sodium hydroxide and monochloroacetic acid were altered as shown in Table 2 to complete the reaction in the first and the second steps. In Comparative Example 10, a third step reaction, the same as the second step reaction, was carried out on the second step reaction product and the product was purified in the same manner as in the second step. In Comparative Example 11, a further fourth step reaction, the same as the third step reaction, was carried out using the third step product as the starting material. Thus, CMC was obtained by conventional processes. It is apparent from Table 2 that, as compared with the conventional processes, the process of the present invention for the production of CMC having a high degree of substitution exhibits a far higher availability of monochloroacetic acid, which is an expensive etherifying agent. According to the process of the present invention, CMC having a degree of substitution of as high as above 2.00, particularly above 2.50, can be produced by the two reaction sequence process, whereas this compound has been produced by three- to five-step processes in the prior art. According to the process of the invention, the production of CMC having such a high degree of substitution on an industrial scale is made possible.

Claims: A process for preparing an alkali metal salt of carboxymethylcellulose ether, which comprises: reacting cellulose, in the presence of an alkali in an aqueous organic solvent, with an etherifying agent effective to etherify said cellulose to form carboxymethylcellulose ether and then recovering said alkali metal salt of carboxymethylcellulose ether from the reaction mixture, characterized in that the etherification reaction is carried out in two steps at 60 to 80°C, wherein in the first step the entire amount of said etherifying agent is present in the reaction mixture and the molar ratio of said alkali/said etherifying agent equal to is maintained in the range of from 0.10 to 0.70 for at least 30% of the total etherification reaction period this being the time period in which the reaction is kept at 30-90°C, and then in the second step, additional alkali is added in one or more pcrtions to the reaction mixture obtained from said first step, without adding more of said etherifying agent, until said molar ratio of said alkali/said etherifying agent is at least 1.00 and completing the etherification reaction. The process of claim 1 wherein said molar ratio in the second reaction step is in the range of from 1.00 to 1.50. The process of claim 2, wherein said molar ratio in the first step is in the range of from 0.30 to 0.70. The process of claim 2, wherein said molar ratio is in the range of from 1.0 to 1.3 at the completion of said second reaction step. A two reaction sequence process for preparing an alkali metal salt of carboxymethylcellulose ether wherein each reaction sequence comprises two sequential reaction steps and the etherification is conducted at 60 to 80°C, which comprises: in the first reaction step of the first reaction sequence, reacting cellulose, in the presence of an alkali in an aqueous organic solvent, with an etherifying agent effective to etherify said cellulose to form carboxymethylcellulose ether having an average degree of substitution in the range of from 0.8 to 2.2, wherein the entire amount of said etherifying agent used in the first reaction step is present in the reaction mixture during the first reaction step and the molar ratio of said alkali/said etherifying agent equal to is maintained in the range of from 0.10 to 0.70 for at least 30% of the total etherification reaction period; then, in a second reaction step of the first reaction sequence, adding additional alkali in one or more portions to the reaction mixture obtained from said first step, without adding more of said etherifying agent, until said molar ratio of said alkali/said etherifying agent is in the range of from 1.00 to 1.50 and completing the etherification reaction to obtain an alkali metal salt of carboxymethylcellulose ether having an average degree of substitution of from 0.8 to 2.2; then in the first reaction step of the second reaction sequence, reacting said alkali metal salt of carboxymethylcellulose obtained from said first reaction sequence, in the presence of an alkali in an aqueous organic solvent, with an additional quantity of said etherifying agent wherein during the first reaction step of said second reaction sequence the molar ratio of said alkali/said etherifying agent is maintained in the range of from 0.10 to 0.70, until the degree of substitution of said alkali metal salt of carboxymethylcellulose is further increased; and then in the second step of said second reaction sequence, adding an additional quantity of said alkali in one or more portions, without adding additional etherifying agent, until said molar ratio of said alkali/said etherifying agent is in the range of from 1.00 to 1.50 to obtain an alkali metal salt of carboxymethylcellulose having a degree of substitution higher than that of the alkali metal salt of carboxymethylcellulose obtained at the end of said first reaction sequence and in the range of from 0.9 to 3.0; and then recovering said latter alkali metal salt of carboxymethylcellulose from the reaction mixture. The process of claim 5, wherein said molar ratio is in the range of from 0.30 to 0.70 in said first step of said first reaction sequence and said first step of said second reaction sequence. The process of any of claims 1 to 6, wherein said etherifying agent is selected from the group consisting of monochloroacetic acid, sodium monochloroacetate, potassium monochloroacetate, and monochloroacetic acid esters, and wherein said alkali is sodium hydroxide or potassium hydroxide. The process of claim 5, wherein said latter alkali salt of carboxymethylcellulose ether recovered from the reaction mixture has a degree of substitution of 2.0 to 3.0. The process of claim 5, including the step of purifying and isolating said alkali metal salt of carboxymethylcellulose ether obtained from the second reaction step of said first reaction sequence and then utilizing same in the first reaction step of said second reaction sequence. The process of claim 5, wherein said alkali metal salt of carboxymethylcellulose ether sait obtained in said second reaction step of the first reaction sequence is subjected directly to said first reaction step of the second reaction sequence without purification and isolation thereof. The process of claim 5, wherein said latter alkali metal salt of carboxymethylcellulose ether recovered from said reaction mixture has a degree of substitution of at least 2.5. The process of claim 9, wherein said purifying and isolating step comprises neutralizing with an acid the excess alkali contained in the reaction mixture from said second reaction step of said first reaction sequence, washing said reaction mixture with an aqueous alcohol solution to remove impurities including salt, sodium glycolate and sodium acetate therefrom, and drying the resulting residue, said residue being said alkali metal salt of carboxymethylcellulose ether having an average degree of substitution of from 0.8 to 2.2. A process for preparing an alkali metal salt of carboxymethylcellulose, which comprises: in a first reaction step, dissolving a water-soluble alkali in a solvent mixture of isopropanol and water in which the weight ratio of isopropanol/water is from 1/1 to 30/1, adding cellulose to said solvent mixture in such an amount that the weight ratio of said solvent mixture/said cellulose is from 2/1 to 50/1 to form a slurry, then adding monochloroacetic acid to said slurry so that the molar ratio of said alkali/said monochloroacetic acid equal to is in the range of from 0.30 to 0.70, for at least 30% of the total etherification reaction period, then heating said slurry to a temperature in the range of from 60 to 80°C for 5 to 120 minutes to partially etherify said cellulose to convert same to carboxymethylcellulose ether; and then, in a second reaction step, adding additional alkali in one or more portions to the reaction mixture obtained from said first step, without adding more of said monochloroacetic acid, until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the reaction mixture to a temperature in the range of from 60 to 80°C for 5 to 120 minutes to complete the etherification reaction; and then recovering from the reaction mixture an alkali metal salt of carboxymethylcellulose having a degree of substitution of from 0.8 to 2.2. A two reaction sequence process for preparing an alkali metal salt of carboxymethylcellulose wherein each reaction sequence comprises two sequential reaction steps, which comprises: in the first reaction step of the first reaction sequence, dissolving a watersoluble alkali in a first solvent mixture of isopropanol and water in which the weight ratio of isopropanol/water is from 1/1 to 30/1, adding cellulose to said first solvent mixture containing said alkali in such an amount that the weight ratio of said first solvent mixture/said cellulose is from 2/1 to 50/1 to form a first slurry, then adding monochloroacetic acid to said slurry so that the molar ratio of said alkali/said monochloroacetic acid equal to is in the range of from 0.30 to 0.70, for at least 30% of the total etherification reaction period, then heating said slurry to a temperature in the range of from 60 to 80°C for 5 to 320 minutes to partially etherify said cellulose to convert same to carboxymethylcellulose ether; and then, in a second reaction step of the first reaction sequence, adding additional alkali in one or more portions to the reaction mixture obtained from said first step, without adding more of said monochloroacetic acid, until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the reaction mixture to a temperature in the range of from 60 to 80°C for 5 to 320 minutes to complete the etherification reaction having a degree of substitution of from 0.8 to 2.2; then in the first step of the second reaction sequence, adding said alkali metal salt of carboxymethylcellulose ether having a degree of substitution of from 0.8 to 2.2 obtained in said first reaction sequence to a second solvent mixture containing said alkali having the same range of the same components as said first solvent mixture, then adding monochloroacetic acid thereto to form a second reaction mixture in which said molar ratio of said alkali/said monochloroacetic acid in said second reaction mixture is in the range of from 0.3 to 0.7, then heating said second raction mixture to a temperature in the range of from 60 to 80°C for 5 to 320 minutes to further increase the degree of substitution of said alkali metal salt of carboxymethylcellulose; then in the second step of said second reaction sequence adding an additional quantity of said alkali in one or more portions to the second reaction mixture, without adding more of said monochloroacetic acid until said molar ratio of said alkali/said monochloroacetic acid is in the range of from 1.00 to 1.50, then heating the second reaction mixture to a temperature in the range of from 60° to 80°C for 5 to 320 minutes to obtain an alkali metal salt of carboxymethylcellulose having a degree of substitution higher than that of the alkali metal salt of carboxymethylcellulose obtained at the end of said first reaction sequence and in the range of from 2.0 to 3.0; and then recovering said latter salt of carboxymethylcellulose from the second reaction mixture.

Inventors: OMIYA TAKEO, OMIYA, TAKEO
Applicants: DAICEL CHEM, DAICEL CHEMICAL INDUSTRIES, LTD.
Application year: 1982
Main classification: C08B11
IPC codes: C08B11