Method of recovering a lithium chloride

Abstract: The present invention provides a method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metal hydrogen sulfide in a polar solvent under the presence of lithium chloride, separating a solvent insoluble component from the resultant reaction mixture to obtain a solution, and calcinating a residue obtained by removing volatile substances from the resultant solution, as well as a method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metal hydrogen sulfide in a polar solvent under the presence of lithium chloride, separating the granular polymer ingredient from the resultant reaction mixture subjecting the liquid suspension obtained by said separation to solid-liquid separation and calcinating the residue obtained by removing volatile substances from the resultant solution component.

Description: Background of the Invention (1) Field of the Invention The present invention concerns a method of recovering a lithium chloride. More specifically, the present invention concerns a method of recovering a lithium chloride that can economically and efficiently recover, in a simple facility, a lithium chloride used as polymerization agent in the production of polyarylene sulfides. (2) Description of the Related Art Polyarylene sulfides having a structure in which phenylene groups are chained by way of thioether bondings are used generally in various fields as engineering plastics excellent in mechanical properties, chemical resistance, heat resistance, etc. The polyarylene sulfide is usually produced by reacting a dihalogenated aromatic compound and an alkali metal sulfide in a polar solvent. Particularly, if lithium chloride is used for a polymerization agent such as of lithium salt, a white polyarylene sulfide with less salt content can be obtained at high degree of polymerization, and a polyarylene sulfide of optional molecular weight can be obtained. However, since lithium chloride is expensive, it is necessary to recover and reuse the same in view of the production cost of the polyarylene sulfide, and it has been desired a recovery method therefor which is simple and of a reduced cost. As a polymerization agent having the same extent of function as that of lithium chloride, although lithium acetate and lithium benzoate have been known, it is difficult to recover them. Heretofore, as the method of recovering the lithium salt from a reaction mixture of polyarylene sulfide, there has been known, for example, a method of removing the solvent from reaction mixture, washing the solid obtained by said removing with an aqueous solution of an acid such as diluted hydrochloric acid and blowing carbon dioxide to the washing solution or adding a carbonate such as sodium carbonate to deposit lithium carbonate, then conducting filtration to recover as a lithium carbonate or, alternatively, adding hydrochloric acid to lithium carbonate, evaporating to dry the resultant aqueous solution of lithium chloride and recovering as lithium chloride (refer to Japanese Patent Laid-Open No. 202222/1984). However, this method involves problems in that (1) since the recovery procedures are complicate to need a complicate recovery facility and also requires a great amount of carbonate, etc. for depositing lithium carbonate, the cost for the recovery facility is increased to increase the recovery cost, (2) direct and simple recovery of lithium chloride, if it is used as the lithium salt for the polymerization agent, is substantially impossible, and (3) unreacted oligomers or impurities are incorporated into the resultant polyarylene sulfide to reduce the quality thereof. Summary of the Invention The present invention has been made in view of the foregoing situations. That is, the object of the present invention is to provide a method of recovering a lithium chloride that can recover lithium chloride used as the polymerization agent, as well as can recover the lithium chloride at high purity by a simple operation and facility, efficiently and at an high recovery rate. For dissolving the foregoing object, the present inventors have made an earnest study and, as a result, have accomplished the present invention based on the finding that the foregoing object can be attained by conducting specific treatments in a specific combination. That is, the first feature of the invention (defined in claim 1), concerns a method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkaline metal sulfide and/or alkaline metal hydrogen sulfide under the presence of lithium chloride in a polar solvent, separating a solvent-insoluble component from the resultant reaction mixture to obtain a solution, and calcinating a residue obtained by separating volatile substances from the solution. The second feature of the invention (described in claim 6) concerns a method of recovering a lithium chloride, which comprises reacting a dihalogen aromatic compound and an alkali metal sulfide and/or alkali hydrogen sulfide in a polar solvent under the presence of lithium chloride, subjecting a liquid suspension obtained by separating the granular polymer ingredient from the resultant reaction mixture, subjecting the liquid suspension obtained by said separation to solid-liquid separation and calcinating a residue obtained by removing volatile substances from the resultant solution component. Description of the Preferred Embodiment - Reaction Mixture - In the present invention, a reaction mixture obtained by reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metal hydrogen sulfide under the presence of lithium chloride in a polar solvent is the object for the recovery of the lithium chloride. (a) Dihalogenated Aromatic Compound The dihalogenated aromatic compound usable as the starting monomer in the process according to the present invention can include, for example, dihalobenzens such as m-dihalobenzene and p-dihalobenzene; alkyl-substituted dihalobenzenes or cycloalkyl substituted dihalobenzenes such as 2,3-dihalotoluene, 2,5-dihalotoluene, 2,6-dihalotoluene, 3,4-dihalotoluene, 2,5-dihaloxylene, 1-ethyl-2,5-dihalobenzene, 1,2,4,5-tetramethyl-3,6-dihalobenzene, 1-n-hexyl-2,5-dihalobenzene, 1-cyclohexyl-2,5-dihalobenzene, etc.; aryl-substituted dihalobenzenes such as 1-phenyl-2,5-dihalobenzene, 1-benzyl-2,5-dihalobenzene and 1-p-toluyl-2,5-dihalobenzene; dihalobiphenyls such as 4,4-dihalobiphenyl; dihalonaphthalenes such as 1,4-dihalonaphthalene, 1,6-dihalonaphthalene and 2,6-dihalonaphthalene; and 3,5-dihalobenzoate, 4,4′-dihalodiphenylether, 4,4′-dihalodiphenylketone, 4,4′-dihalodiphenylsulfide and 4,4′-dihalodiphenylsulfoxide. Two halogen elements in these dihalogenated aromatic compounds are, respectively, fluorine, chlorine, bromine or iodine, which may be identical or different with each other. Among the dihalogenated aromatic compounds described above, dihalobenzenes are preferred, with dihalobenzenes containing mainly p-dichlorobenzene being preferred particularly. In the present invention, the dihalogenated aromatic compounds may be used alone or two or more of them may be used in combination. In addition, other dihalogenated aromatic compounds, for example, dihalogenated aromatic carboxylic acids or alkali metal salts thereof may be used together. In addition of said dihalogenated aromatic compound, if necessary, branching agent such as trihalobenzen, dihaloaniline and dihalonitrobenzen and molecular weight modifier such as monohalobenzene, thiophenol, phenol and aniline may be used. (b) Alkali Metal Sulfide and Alkali Metal Hydrogen Sulfide In the process according to the present invention, alkali metal sulfide and/or alkali metal hydrogen sulfide (alkali metal sulfide and/or alkali metal hydrogen sulfide may hereinafter referred simply as alkali metal (hydrogen) sulfide) as a sulfur source for the polyarylene sulfide. As the alkali metal sulfide described above, there can be mentioned, for example, lithium sulfide, sodium sulfide, potassium sulfide, rubidium sulfide and lithium sulfide. Among them, sodium sulfide and lithium sulfide are preferred, with sodium sulfide being particularly preferred. As the alkali metal hydrogen sulfide described above, there can be mentioned, for example, lithium hydrogen sulfide (LiHS), sodium hydrogen sulfide (NaHS), potassium hydrogen sulfide (KHS), rubidium hydrogen sulfide (RbHS), calcium hydrogen sulfide (CaHS) and cesium hydrogen sulfide (CeHS). Among them, sodium hydrogen sulfide and lithium hydrogen sulfide are preferred, with sodium hydrogen sulfide being preferred particularly. These various alkali metal (hydrogen) sulfides may be used, respectively, alone or as a combination of one or more of them. In addition, as the alkali metal (hydrogen) sulfide, there can be used compound obtained by a reaction of hydrogene sulfide and alkali metal hydroxide. Further, as the various alkali metal (hydrogen) sulfides, there can be used any of anhydrides, hydrates, aqueous solution, hydrous mixtures, etc. In the case of using a hydrate, aqueous solution or hydrous mixture, dehydration has to be applied before polymerization reaction as described later. (c) Reaction between Dihalogenated Aromatic Compound and Alkali Metal (Hydrogen) Sulfide The reaction between the dihalogenated aromatic compound and the alkali metal (hydrogen) sulfide is conducted in a polar solvent under the presence of lithium chloride at a molar ratio, preferably, of 0.75 : 1 - 2.0 : 1, more preferably, from 0.90 : 1 - 1.2 : 1. (d) Polar Solvent The polar solvent described above can include, for example, organic amides compounds, lactam compounds, urea compounds and organic cyclic phosphor compounds. Specifically, there can be mentioned, for example, N,N-dimethylformamide, N,N-dimethylacetamide, N,N-diethylacetamide, N,N-dipropylacetamide, N,N-dimethyl benzoic acid amide, caprolactam, N-methylcaprolactam, N-ethylcaprolactam, N-isopropylcaprolactam, N-isobutylcaprolactam, N-n-propylcaprolactam, N-n-butylcaprolactam, N-cyclohexylcaprolactam, N-methyl-2-pyrrolidone, N-ethyl-2-pyrrolidone, N-isopropyl-2-pyrrolidone, N-isobutyl-2-pyrrolidone, N-n-propyl-2-pyrrolidone, N-n-butyl-2-pyrrolidone, N-cyclohexyl-2-pyrrolidone, N-methyl-3-methyl-2-pyrrolidone, N-cyclohexyl-2-pyrrolidone, N-ethyl-3-methyl-2-pyrrolidone, N-methyl-3,4,5-trimethyl-2-pyrrolidone, N-methyl-2-piperidone, N-isopropyl-2-piperidone, N-methyl-2-piperidone, N-ethyl-2-piperidone, N-isopropyl-2-piperidone, N-methyl-6-methyl-2-piperidone, N-methyl-3-ethyl-2-piperidone, tetramethyl urea, N,N′-dimethylethylene urea, N,N′-dimethylpropylene urea, 1-methyl-1-oxosulfolan, 1-ethyl-1-oxosulfolan, 1-phenyl-1-oxosulfolane, 1-methyl-1-oxophospholan, 1-n-propyl-1-oxophospholan and 1-phenyl-1-oxophospholan. These polar solvents may be, respectively, used alone or may be used as a mixture of two or more of them. Among the various polar solvents described above, non-protonic organic amides or lactams are preferred. Among them, N-alkylpyrrolidone is preferred, N-methyl-2-pyrrolidone being suitable particularly. (2) Lithium Chloride The lithium chloride is used as the polymerization agent for the polyarylene sulfide. The amount of the lithium chloride used is selected within a range usually from 0.03 to 2.0 mol, preferably, from 0.1 to 1.6 mol based on one mol of the alkali metal (hydrogen) sulfide. If the amount of lithium chloride is less than 0.03 mol, the molecular weight of the resultant polymer is lower or the content of impurity such as sodium chloride present invention in the granular polyarylene sulfide (B) can not be lowered sufficiently. On the other hand, if it exceeds 2.0 mol, no catalytic effect proportional to the amount can be obtained and lithium chloride may rather remain at high concentration in the resultant polymer, which is not preferred. In the case of that no lithium chloride is used as polymerization agent or a small amount of lithium chloride is used, and lithium sulfide as raw material is used, said lithium sulfide react to dihalogene aromatic compound and lithium chloride is obtained and acts as polymerization agent. So, that case is included into this invention. Referring to the amount of the polar solvent used in the process according to the present invention, it may be such an amount sufficient to uniformly proceed the reaction and there is no particular restrictions. Usually it is selected within a range from 0.1 to 10 times by weight based on the total weight of the starting ingredients and the polymerization agent. If the amount is less than 0.1 times by weight, the reaction may possibly be not uniform, whereas if it exceeds 10 times by weight, the volumic efficiency is worsened to undesirably reduce the productivity. (f) Procedure for the Polymerizing Reaction In the present invention, a polyarylene sulfide is formed in the polar solvent by bringing the dihalogenated compound into contact with the alkali metal (hydrogen) sulfide under the presence of a lithium chloride. In a case when one or both of the lithium chloride and the alkali metal (hydrogen) sulfide is in the aqueous solution, hydrous state or a hydrate, it is desirable that the lithium chloride or the alkali metal (hydrogen) sulfide is at first added to the polar solvent, applied with dehydrating procedure such as azeotropic distillation or vacuum destillation to prepare a mixed solution. Then, substantially anhydrous halogenated aromatic compound is added and reacted. Referring then to a preferred example of the reaction between the dihalogenated aromatic compound and the alkali metal (hydrogen) sulfide, the alkali metal (hydrogen) sulfide and the lithium chloride are added each by a required amount in a desired polar solvent, and dehydrating procedure was applied, if required, by means of azeotropic distillation or vacuum destillation etc. (temperature usually within a range from 100 to 220°C). Then, the dihalogenated aromatic compound of a predetermined amount and various kind of additive ingredients used depending on the requirement are added and polymerization reaction is proceeded by heating to a temperature usually within a range from 180 to 330°C and, preferably, 220 to 300°C. If the reaction temeperature is lower than 180°C, the reaction rate is too low for the practical purpose. On the other hand, if it exceed 330°C, it causes side reactions or degradation in the resultant polymer, causing coloration or gelation. The reaction time is usually within 20 hours, preferably, about from 0.1 to 8 hours, although it can not simply be determined since it is dependent on the kind and the ratio of amount of the starting ingredients used, the kind and the amount of the polymerization agent, etc. The polymerizing reaction may be conducted in an inert gas atmosphere such as nitrogen, argon, carbon dioxide or steams. Further, although there is no particular restriction to the reaction pressure, the reaction is usually conducted at an autogenous pressure of the polymerizing reaction system such as of the solvent or a pressure upto about 50 kg/cm² (absolute pressure). In a case where both of the lithium chloride and the alkali metal (hydrogen) sulfide as the starting ingredient are anhydrous, there is no particular restrictions for the order of adding each of the ingredients into the polar solvent. The temperature may either be a one step reaction conducted at an ordinary temperature or a multi-step reaction in which the temperature is elevated stepwise. Furthermore, such a mode of reaction as continuously elevating the temperature gradually may also be employed. - Removal of Solvent-Insoluble Components from the Reaction Mixture - The reaction mixture obtained as described above contains polymer, oligomer, lithium chloride, alkali metal salt, reaction impurity and organic polar solvent. Then, depending on the difference between the solubility of each of the ingredients to the organic polar solvent, it can be said that the reaction mixture comprises an organic polar solvent and solvent-insoluble components. In the case of using lithium (hydrogen) sulfide as the alkali metal (hydrogen) sulfide, the lithium (hydrogen) sulfide forms a solvent-soluble lithium salt after the polymerization reaction. Further, in the case of using sodium (hydrogen) sulfide, etc. as the alkali metal (hydrogen) sulfide, sodium (hydrogen) sulfide forms a solvent-insoluble sodium salt after the polymerization reaction. Accordingly, a recovery method for the lithium chloride may be considered depending on the kind of alkali metal salts derived from alkali metal (hydrogen) sulfides. (1) First Method (defined in claim 1) In a case where the alkali metal chloride derived from the alkali metal (hydrogen) sulfide is soluble to the polar solvent such as a lithium salt, there can be mentioned a method of recovering a lithium chloride as defined in claim 1, which comprises separating a solvent-insoluble component from the reaction mixture to obtain a solution and calcinating the residue obtained by removing volatile substances from the resultant solution. In this case, the solvent-insoluble component usually contains polyarylene sulfide, impurities insoluble to the polar solvent or lithium chloride and/or polar solvent etc. The solution usually contains polar solvent, lithium chloride, arylene sulfide oligomer, unreacted monomer and impurities of by-product etc. As the method of separating the solvent-insoluble component, there can be mentioned, for example, a centrifugal separation method using a centrifugator, a filtration method using a filter, etc. The centrifugal separation method is preferred since clogging due to solid component does not occur. In this way, since the solution obtained by separating solid content from the reaction mixture forms a mixture of an inorganic substance such as lithium chloride and an organic substance such as arylene sulfide oligomer, unreacted monomer and solvent, when the residue obtained by removing the volatile ingredients from the solution is calcinated, a lithium chloride is separated as the calcination residue. Then, the volatile substances usually contain the polar solvent, the unreacted monomer, etc. Accordingly, as the method of removing the volatile ingredients, there can be used, for example, flashing method, an evaporization method using a thin layer evaporator, an evaporation method using a kneading evaporator, etc. Removal of the volatile ingredient is usually conducted by heating under a normal pressure or a reduced pressure, preferrably, under a reduced pressure. In the above mention, lithium sulfide is used as alkali metal sulfide. The similar procedure of the above mention may be used when reaction mixture obtained by polymerization reaction using sodium sulfide contains lithium chloride (soluble in a solvent) and sodium chloride (insoluble in a solvent). In this case, solvent-insoluble components containing sodium chloride is provided to after treatment such as washing with water to obtain a purified polymer. Calcination is conducted by charging the residue into a calcination furnace, and then calcinating at a temperature higher than the decomposing temperature of the arylene sulfide oligomer, etc. (about 350°C), preferably, higher than 400°C and below the melting point of the lithium chloride. If the calcination temperature is lower than the decomposing temperature of the arylene sulfide oligomer, the oligomer can not sufficiently be gasified, failing to remove the oligomer. On the other hand, at a temperature higher than the melting point of the lithium chloride, the lithium chloride may be melted to cause evaporation loss or to promote the formation of lithium oxide, etc. (side reaction), which is not preferable. A preferred calcination temperature is usually within a range from 350 to 800°C and, preferably, from 500 to 700°C. Further, as the calcination method, there can be used a method of calcinating in air while elevating temperature from the start (one step calcination method), a method of calcinating in an inert gas atmosphere such as nitrogen gas while elevating up to the calcination temperature and then calcinating in air (two step calcination method), etc. Since oxidation may occur in the temperature elevating step to impossibly increase the by-products in the one step calcination method, the two step calcination method is preferred. Furthermore, as the calcination furnace, while rotary furnace bed type, belt type, kiln type, etc. may be used, a rotary furnace bed type calcination furnace is preferred in view of the compact structure for the device and the easy operation. The lithium chloride obtained in this way is in a high purity. (2) Second Method (described in claim 6) The method described in claim 6 is a recovery method for a lithium chloride particularly suitable in a case where the alkali metal salt derived from the alkali metal (hydrogen) sulfide is insoluble to the solvent. The method as described in claim 6 concerns a method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metal hydrogen sulfide in a polar solvent under the presence of lithium chloride, separating the granular polymer ingredient from the resultant reaction mixture, subjecting the liquid suspension obtained by said separation to solid-liquid separation and calcinating the residue obtained by removing the volatile substances from the resultant solution component. For the separation of the polymer ingredient, it is preferred to use such a filter that can filtrate only the granular polyarylene sulfide but can not filtrate those solid components such as precipitates of alkali metal halide suspended in the reaction mixture, because the grain size of the deposited polyarylene sulfide is usually more than 0.05 mm, particularly within a range from 0.05 to 0.5 mm whereas the grain size of the alkali metal salt is much smaller than that of the polyarylene sulfide. In view of the above, the filter used for the separation is usually from 200 to 5 mesh, preferably, from 100 to 16 mesh. By such filtration, the content of the alkali metal salt residue in the filtrated polyarylene sulfide is extremely small and, if the alkali metal salt is contained, a polyarylene sulfide of high whiteness can be obtained by merely washing the filtrated polyarylene sulfide with water. In this way, the liquid filtrate comprises solid component such as solvent-insoluble alkali metal halide (for example, sodium chloride) in a suspended state and granular polymer, and the solution component containing polar solvent, lithium chloride, low molecular weight arylene sulfide oligomer and unreacted monomer. Then, the liquid filtrate is subjected to solid-liquid separation. The solid-liquid separation can be conducted by using, for example, centrifugal separation method by using a centrifugator, filtration method, etc. Centrifugation capable of continuous operation with no occurrence of clogging due to the solid component is preferred. The solution component obtained by the solid-liquid separation is removed with the volatile substances in the same manner as the first method (defined in claim 1) and then the residue is calcinated. In view of effective recovering lithium chloride, it is desired that a granular polymer (include large grain size polymer) obtained by the above mentioned separation process and containing small amount of lithium chloride is washed with polar solvent and obtained washing solution is added to the above solution component. - Advantage of Invention - According to the present invention, there can be provide a method of recovering a lithium chloride having the following advantages: (1) lithium chloride used as the polymerization agent can be recovered efficiently, (2) lithium chloride can be recovered by simple procedure and facility and (3) at high recovery rate and high purity, and (4) the content of salts in the resultant polyarylene sulfide can be lowered further and the content of impurities soluble in a solvent in the resultant polyarylene sulfide can be reduced to substantially 0. Example The present invention is to be described more specifically referring to examples of the invention. (Example 1) 9.13 kg (54.3 mol) of sodium sulfide 5-hydrate, 2.30 kg (54.3 mol) of lithium chloride and 30 liter of N-methyl-2-pyrrolidone (NMP) were charged in an autoclave and water was distilled off at 160°C under a reduced pressure. A content of remaining water after distillation was less than it of sodium sulfide 1-hydrate. Then, 10 liter of N-methyl-2-pyrrolidone and 7.98 kg (54.3 mol) of p-dichlorobenzene were added and reacted at 260°C for three hours to obtain a reaction mixture. The reaction mixture was cooled, and granular polyphenylene sulfide (granular PPS) was filtered on a 140 mesh stainless steel gauze to separate granular PPS and liquid filtrate. Then, the granular PPS was washed with 20 liter of NMP. The granular PPS after washing showed 92.5 % yield, a inherent viscosity of η inh of 0.335 (temperature : 206°C, in α-chloronaphthalene at a concentration of 0.4 g/dl) and 210 ppm of sodium ion content. By centrifugating the liquid filtrate obtained by filtration to apply solid-liquid separation, sodium chloride was separated from the liquid filtrate. Then, volatile ingredients (mainly NMP) were distilled off by means of evapolator from the remaining liquid after separating sodium chloride from the liquid filtrate to obtained a residue. When the residue was determined quantitatively, it consisted of 83.8 % by weight of lithium chloride, 5.2 % by weight of NMP and 11.0 % by weight of oligomers. Then, 15 kg of the residues was calcinated in a rotary furnace bed type calcination furnace (manufactured by Tamagawa Kikai Kabushiki Kaisha) under the conditions of a stacked layer thickness of 30 mm, processing temperature of 550°C, nitrogen and air flow rate of 1 Nm³/hr, while staying them in the furnace at first for 2 hours under a nitrogen gas stream and then for one hour under air stream, to obtain 12.5 kg of the calcination residue. The recovery rate (calcination residue/charged amount to the furnace x 100) was 83.3 % by weight. When the residue was determined quantitatively, it consisted of 99.1 % by weight of LiCl and 0.9 % by weight of Li₂SO₄, from which the organics were removed substantially completely. The results are shown in Table 1. (Example 2) The procedures were quite in the same manner as those in Example 1 except for changing the furnace staying time under air stream to 2 hours. The results are shown in Table 1. (Example 3) The procedures were quite in the same manner as those in Example 1 except for changing the temperature to 750°C. The results are shown in Table 1. (Example 4) The procedures were quite in the same manner as those in Example 1 except for changing a content of sodium sulfide to 4.56 kg (27.2 mol) and a content of lithium chloride to 1.25 kg (27.2 mol). The results are shown in Table 1. Example 1 Example 2 Example 3 Example 4 Recovery rate (wt%) 83.3 83.0 83.7 84.0 LiCl content (wt%) 99.1 98.0 95.1 99.3 Li₂SO₄ content (wt%) 0.9 2.0 4.9 0.7

Claims: A method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metal hydrogen sulfide in a polar solvent under the presence of lithium chloride, separating a solvent insoluble component from the resultant reaction mixture to obtain a solution and calcinating a residue obtained by removing volatile substances from the solution. A method of recovering a lithium chloride as defined in claim 1, wherein the alkali metal sulfide is lithium sulfide. A method of recovering a lithium chloride as defined in claim 1, wherein the polar solvent is lactams. A method of recovering a lithium chloride as defined in claim 1, wherein the polar solvent is N-methylpyrrolidone. A method of recovering a lithium chloride as defined in claim 1, wherein the dihalogenated aromatic compound is dihalobenzene. A method of recovering a lithium chloride, which comprises reacting a dihalogenated aromatic compound and an alkali metal sulfide and/or alkali metel hydrogen sulfide in a polar solvent under the presence of lithium chloride, separating the granular polymer ingredient from the resultant reaction mixture subjecting the liquid suspension obtained by said separation to solid-liquid separation and calcinating the residue obtained by removing volatile substances from the resultant solution component. A method of recovering a lithium chloride as defined in claim 6, wherein the alkali metal sulfide is lithium sulfide. A method of recovering a lithium chloride as defined in claim 6, wherein the polar solvent is lactams. A method of recovering a lithium chloride as defined in claim 6, wherein the polar solvent is N-methylpyrrolidone. A method of recovering a lithium chloride as defined in claim 6, wherein the dihalogenated aromatic compound is a dihalobenzene.

Inventors: OGATA NORIO IDEMITSU PETROCHEM, OMORI MASAO, SHIROTA DAIGO, YAMATO HIROYASU IDEMITSU PETRO, OGATA, NORIO IDEMITSU PETROCHEM. COMP. LTD., OMORI, MASAO, SHIROTA, DAIGO, YAMATO, HIROYASU IDEMITSU PETROCHEM. COMP. LTD.
Applicants: IDEMITSU PETROCHEMICAL CO, IDEMITSU PETROCHEMICAL CO. LTD.
Application year: 1988
Main classification: C08G75
IPC codes: C01D15, C08G75