Process for preparing a cellulose derivative

Abstract: A particulate aromatic or araliphatic carbamate of a polysaccharide, having a mean diameter of 1 to 200 µm and a specific surface area of 0.5 to 300 m²/g, is produced by dissolving an aromatic or araliphatic carbamate of a polysaccharide in an organic solvent, adding thereto 0 to 0.5 part by volume of a C₄ to C₂₂ hydrocarbon, adding the resulting solution gradually to a well-stirred aqueous solution of a surfactant, removing the organic solvent, while continuing stirring, isolating the formed solid particles, and washing and drying them. The obtained carbamate has an excellent resolving power and can be used as the stationary phase in preparative liquid chromatography as such without being supported by a carrier.

Description: [Field of Industrial Application] The present invention relates to a polysaccharide derivative, a process for producing the same, and a separating agent. [Prior Art] It is known that a packing material for liquid chromatography wherein use is made of a stationary phase comprising a silica gel and, supported thereon, an ester of a polysaccharide and a carbamate has an excellent capability of optical resolution (see Japanese Patent Publication-A No. 289601/1990). The silica gel used as a support, however, is very expensive. A process for producing a particulate cellulose ester of an aromatic or araliphatic carboxylic acid is well known in the art (see Japanese Patent Publication-A No. 152101/1989). JP-A-63 156 538 relates to a separating agent comprising substituted or non-substituted polysaccharide phenylcarbamate derivatives. Preferred examples of the polysaccharide include cellulose. Grounding the precipitated polysaccharide phenylcarbamate into powder is a preferred method. [Disclosure of the Invention] The present inventors have made extensive studies with a view to solving the above-described problems and, as a result, have found that a particulate aromatic or araliphatic carbamate of cellulose can be easily prepared, has an excellent capability of resolution because it is in the particulate form, particularly has a separation factor larger than that of the carbamate carried on a support, and is suitable for use in preparative liquid chromatography, thus accomplishing the present invention. Accordingly, the present invention provides a process for producing a cellulose derivative comprising a particulate aromatic or araliphatic carbamate of cellulose having a mean particle diameter of 1 to 200 µm and a specific surface area of 0.5 to 300 m 2 /g. In the present invention, the mean particle diameter of the cellulose derivative is 1 to 200 µm although it depends upon the applications, preferably 3 to 20 µm for analytic applications and 10 to 200 µm for preparative applications. It is possible to attain a very narrow mean particle diameter range by fractionation through the use of a conventional method, for example, sedimentation, sifting or centrifugation by means of a cyclone. The specific surface area of the cellulose derivative according to the present invention is 0.5 to 300 m 2 /g, preferably 1 to 80 m 2 /g. The particle is spherical or crushed in its shape, preferably spherical. The surface of the particle may be porous or non-porous, preferably porous for the purpose of increasing the absorption area and improving the performance of separation. The particle diameter distribution is preferably narrow when the particle is used as a separating agent for chromatography. The aromatic or araliphatic carbamate of cellulose according to the process of the present invention is derived from an isocyanate represented by the following formulas (1) or (2): R-N=C=O R-X-N=C=O (wherein R stands for a monovalent aromatic hydrocarbon group which may have a heteroatom and may be unsubstituted or substituted with at least one member selected from the group consisting of a hydrocarbon group having 1 to 12 carbon atoms and optionally a heteroatom, a cyano group, a halogen atom, a hydroxy group, a nitro group, an amino group and a di(C 1 to C 8 alkyl)amino group; and X stands for a divalent hydrocarbon group which has 1 to 4 carbon atoms and which may have a double bond or a triple bond). Examples of the monovalent aromatic hydrocarbon group represented by the R include groups such as phenyl, naphthyl, phenanthryl, anthracyl, indenyl, indanyl, furyl, thionyl, pyrryl, benzofuryl, benzthionyl, indyl, pyridyl, pyrimidyl, quinolinyl and isoquinolinyl. Examples of the substituents of the monovalent aromatic hydrocarbon group represented by the R include an alkyl group having 1 to 12 carbon atoms, an alkoxy group having 1 to 12 carbon atoms, an alkylthio group having 1 to 12 carbon atoms, a cyano group, a halogen atom, an acyl group having 1 to 8 carbon atoms, an acyloxy group having 1 to 8 carbon atoms, a hydroxy group, an alkoxycarbonyl group having 1 to 12 carbon atoms, a nitro group, an amino group and a di(C 1 to C 8 alkyl)amino group. X is a divalent hydrocarbon group having 1 to 4 carbon atoms and may have a double bond or a triple bond. Examples of the X include methylene, ethylene, ethylidene, ethenylene, ethynylene, 1,2- or 1,3-propylene and 1,1- or 2,2-propylidene. The number-average degree of polymerization of the cellulose (the average number of the pyranose rings contained in its molecule) is 5 or more, preferably 10 or more. Although the upper limit of the number-average degree of polymerization is not crucial, the upper limit is preferably 500 or less from the viewpoint of handleability. The aromatic or araliphatic carbamate of cellulose polysaccharide to be used in the process of the present invention can be produced from an isocyanate represented by the formulas (1) or (2) and a polysaccharide by a conventional method. The percentage introduction of the substituent of the cellulose is 10 to 100%, preferably 80 to 100%. The particulate aromatic or araliphatic carbamate of cellulose having a mean particle diameter of 1 to 200 µm and a specific surface area of 0.5 to 300 m 2 /g prepared according to the process of the present invention can be prepared by first dissolving an aromatic or araliphatic carbamate of cellulose in an organic solvent containing 50 to 100% by volume of mesityl oxide adding a hydrocarbon having 4 to 22 carbon atoms in an amount of 0 to 0.5 time by volume that of the organic solvent, gradually adding the resultant solution to a sufficiently agitating aqueous surfactant solution, removing the organic solvent while continuing the agitation, isolating solid particles, and washing and drying the solid particles. In the above-described method, the particle diameter of the resultant cellulose derivative varies depending upon the ratio of the amount of the organic solvent to the amount of the aqueous solution, the concentration of the cellulose derivative, the rate of addition of the organic solvent, and the shapes of the vessel and the stirring blade, when the agitation rate is 10 to 1000 rpm, preferably 100 to 500 rpm. Although the organic solvent is not particularly limited as far as it can dissolve the cellulose carbamate, an organic solvent insoluble in water is particularly preferred. Even if the organic solvent is one which is soluble in water, it can be used after mixing with a solvent insoluble in water. The amount of the hydrocarbon to be added to a solution of a cellulose derivative in an organic solvent is 0 to 0.5 time by volume, preferably 0.1 to 0.3 time by volume that of the organic solvent. The number of carbon atoms of the hydrocarbon is 2 to 22, preferably 4 to 10. Examples of the hydrocarbon include butane, pentane, heptane, hexane, octane, nonane and decane. The ratio of the total volume of the organic solvent, cellulose derivative and hydrocarbon to that of the aqueous surfactant solution is preferably 1 : 10 to 1 : 1. In the present invention, the term "surfactant" refers to an acid, a dibasic acid, a tribasic acid, a tetrabasic acid or a hemiester or salt thereof, preferably an alkyl sulfate having 4 to 18 carbon atoms, particularly preferably a lauryl sulfate. The particulate cellulose derivative thus prepared according to the process of the present invention is useful as a separating agent for separating a racemic mixture, a structural isomer mixture, particularly as a packing material for gas chromatography and liquid chromatography. [Effect of the Invention] The cellulose derivative of the present invention is very useful as a functional material, particularly useful for separating a racemic mixture and a structural isomer mixture. Since the cellulose derivative of the present invention is particulate, it is not necessary to use an expensive supporting material (silica gel) and can be produced in a large quantity at a low cost. Further, when the surface of the particle is made porous, the separation factor can be increased through an increase in the specific surface area of the particle, which enables the separation to be conducted at a high efficiency and a high profitability. [Examples] The present invention will now be described in more detail with reference to the following Examples, though it is not limited to these Examples only. Example 1 8.7 g of cellulose-3,5-dimethylphenylcarbamate was dissolved in 300 ml of mesityl oxide. The resultant solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 400 rpm. The reaction system was heated to 90°C and evacuated while continuing the agitation at the same rate. 250 ml of distilled water was added in the course of the above procedure to distil away mesityl oxide. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 140°C for 16 hr. The yield of the resultant powder was 8.1 g (93%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 3 to 6 µm and a specific surface area of 3.4 m 2 /g (BET method). Example 2 The powder prepared in the Example 1 was packed in a column having an inner diameter of 4.6 mm and a length of 125 mm, and the separation of various racemic compounds listed in Table 1 was conducted by HPLC. The results are given in the Table 1. Example 3 10.0 g of cellulose-3,5-dimethylphenylcarbamate was dissolved in a mixed solvent comprising 250 ml of mesityl oxide and 50 ml of acetone, and 50 ml of n-nonane was added thereto. The resultant solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 400 rpm. The reaction system was heated to 90°C and evacuated while continuing the agitation at the same rate. 200 ml of distilled water was added in the course of the above procedure to distil away mesityl oxide and acetone. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 140°C for 16 hr. The yield of the resultant powder was 7.83 g (78.3%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 3 to 8 µm and a specific surface area of 4.8 m 2 /g (BET method). Example 4 The powder prepared in the Example 3 was packed in a column having an inner diameter of 4.6 mm and a length of 100 mm, and the separation of various racemic compounds listed in the Table 1 was conducted by HPLC. The results are given in the Table 1. Example 5 10.0 g of cellulose-3,5-dimethylphenylcarbamate was dissolved in a mixed solvent comprising 250 ml of mesityl oxide and 50 ml of acetone, and 50 ml of n-nonane was added thereto. The resultant solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 200 rpm. The reaction system was heated to 90°C and evacuated while continuing the agitation at the same rate. 200 ml of distilled water was added in the course of the above procedure to distil away mesityl oxide and acetone. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 140°C for 16 hr. The yield of the resultant powder was 8.46 g (84.6%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 12 to 30 µm and a specific surface area of 1.2 m 2 /g (BET method). Comparative Example 6 10.0 g of amylose-3,5-dimethylphenylcarbamate was dissolved in a mixed solvent comprising 300 ml of chloroform and 6 ml of N,N-dimethylacetamide, and 40 ml of n-heptane was added thereto. The resultant solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 400 rpm. The reaction system was heated to 60°C and evacuated while continuing the agitation at the same rate to distil away the organic solvent. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 90°C for 20 hr. The yield of the resultant powder was 9.41 g (94.1%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 3 to 6 µm and a specific surface area of 4.3 m 2 /g (BET method). Comparative Example 7 The powder prepared in the Example 6 was packed in a column having an inner diameter of 4.6 mm and a length of 125 mm, and the separation of various racemic compounds listed in the Table 1 was conducted by HPLC. The results are given in the Table 1. Ex. 2 Ex. 4 Comparative EX. 7 racemic compd. k 1 ' α k 1 ' α k 1 ' α t-stilbene oxide 5.41 1.76 1.20 2.64 1.76 2.92 Tröger's base 7.15 1.28 1.84 1.21 1.82 1.69 benzoin 15.19 1.58 3.61 1.69 12.95 1.32 phenyl vinyl sulfoxide 12.89 1.25 2.69 1.41 4.93 1.0 trifluoroanthrylethanol 15.76 2.47 2.97 3.52 4.63 1.39 mobile phase: hexane/2-propanol = 9/1 flow rate: 0.5 ml/min temp.: room temp. The HPLC used was one (pump: 880-PU, detector: 875-UV) manufactured by Japan Spectroscopic Co., Ltd. In the table, the volumetric ratio (k 1 ') and the separation factor (a) are defined by the following equations: volumetric ratio (k 1 ') = - retention time of separating compd. - dead time dead time separation factor (α) = volumetric ratio of more strongly adsorbed compd. volumetric ratio of more weakly adsorbed compd. Example 8 10 g of cellulose tris(phenylcarbamate) was dissolved in a mixed solvent comprising 250 ml of mesityl oxide and 50 ml of acetone, and 50 ml of n-nonane was added thereto. The mixture was agitated until the opaque solution turned transparent. The solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 400 rpm. The reaction system was heated to 40°C and evacuated while continuing the agitation at the same rate to distil away the organic solvent. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 140°C for 19 hr. The yield of the resultant powder was 7.2 g (72%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 6 to 15 µm and a specific surface area of 5.4 m 2 /g (BET method). Example 9 The powder prepared in the Example 8 was packed in a column having an inner diameter of 4.6 mm and a length of 125 mm, and the separation of various racemic compounds listed in Table 2 was conducted by HPLC. The results are given in the Table 2. Ex. 9 racemic compd. k 1 ' α t-stilbene oxide 6.13 1.40 phenyl vinyl sulfoxide 58.32 1.15 2,2,2-trifluoro-1-(9-anthryl)-ethanol 9.95 1.36 mobile phase: hexane/2-propanol = 9/1 flow rate: 0.5 ml/min temp.: room temp. The HPLC used was one (pump: 880-PU, detector: 875-UV) manufactured by Japan Spectroscopic Co., Ltd. Example 10 10 g of cellulose tris(phenylcarbamate) was dissolved in a mixed solvent comprising 250 ml of methylene oxide and 10 ml of acetone, and the resultant solution was gradually added in portions to 600 ml of a 0.75% aqueous sodium lauryl sulfate solution with agitating at about 400 rpm. The reaction system was heated to 45°C while continuing the agitation at the same rate to distil away the organic solvent. The residue was isolated by filtration and washed with distilled water and ethanol. The resultant powder was dried in vacuo at 80°C for 20 hr. The yield of the resultant powder was 9.4 g (94%). The powder was classified by sifting and sedimentation to prepare a spherical particle having a diameter of 10 to 30 µm.

Claims: A process for producing a cellulose derivative comprising shperical particles of an aromatic or araliphatic carbamate of cellulose having a mean particle diameter of 1 to 200 µm and a specific surface area of 0.5 to 300 m 2 /g, characterized by first dissolving an aromatic or araliphatic carbamte of cellulose in an organic solvent containing 50 to 100% by volume of mesityl oxide, adding a hydrocarbon having 4 to 22 carbon atoms in an amount of 0 to 0.5 time by volume that of the organic solvent, gradually adding the resultant solution to a sufficiently agitating aqueous surfactant solution, removing the organic solvent while continuing the agitation, isolating solid particles, and washing and drying the solid particles. The process according to claim 1, wherein said aromatic or araliphatic carbamate of cellulose is a compound derived from an isocyanate represented by the following formulae (1) or (2): R-N=C=O R-X-N=C=O wherein R stands for a monovalent aromatic hydrocarbon group which optionally has a heteroatom and may be unsubstituted or substituted with at least one member selected from the group consisting of a hydrocarbon group having 1 to 12 carbon atoms and optionally a heteroatom, a cyano group, a halogen atom, a hydroxy group, a nitro group, an amino group and a di(C 1 to C 8 alkyl) amino group; and X stands for a divalent hydrocarbon group which has 1 to 4 carbon atoms and optionally has have a double bond or a triple bond. The process according to claim 1 or 2, wherein the hydrocarbon is selected from butane, pentane, heptane, hexane, octane, nonane and decane. The process according to any of claims 1 to 3, wherein the hydrocarbon is added in an amount of 0.1 to 0.3 times by volume that of the organic solvent.

Inventors: IKEDA HIROKAZU, IKEDA, HIROKAZU, IKEDA, HIROKAZU, 1132, UNEMURE
Applicants: DAICEL CHEM, DAICEL CHEMICAL INDUSTRIES, LTD.
Application year: 1992
Main classification: C08J3
IPC codes: C08J3, B01J20, B01D15, C08B33, G01N30, C08B15