열가소성 셀룰로오스 유도체 복합섬유 및 그 제조방법
The present invention refers to thermoplastic cellulose derivative composite fiber and process for manufacturing method relates to, melt spinning without the organic solvent capable of thick, high speed and star-shape, number under public affairssensitivity thermoplastic cellulose ultrafine fibers to thermoplastic cellulose derivative composite fiber and process for manufacturing method are disclosed. Polymer synthetic resin is mechanical properties, chemical resistance, is characterized in that a stage to a variety of widely used since, in the case of the synthetic resin is selected from product itself when not incineration processing, harmful substances emitted the disadvantages of wealth. Recent social environmental pollution door number is large door number while decomposing it fully introduced into a natural biodegradable resin studies of aluminum and, interest etc. built identifies. [...] group composed as a biodegradable resin, polyethylene [...], poly [...] but excellent in biodegradability or the like, for our mirror number-or devoid of, low melting point and definitive 1 times except for injecting molten resin molded article, such as article number to number of the bath with width army fiber number, thermal stability and must use deployment difficult width army number in a database are disclosed. One of the recent polylactic acid (PLA) or starch which is natural number is supplied from bio [...] product such as product number but are energy, for the preparation of physical properties and the hydrolysis cannot communicate with the servers and pour there are a high temperature dyeing, in the fiber surface side and which is provided with a PLD [...]tenter work progress is rich and has disadvantages (brittle), spinning the device in existing polyester room inside 4000mpm etc. instead of radiation in the door number point difficult. Number of the second dielectric layer of pulp cellulosic material in cultivated and water is not necessary in the biodegradation of the system is the most mass-produced biomass material resources circulating type are disclosed. The use made of fibers such as cellulose fibers produced in the low as to the FEP is used in this example has to be made from spun to the semiconductor layer. In addition, filament material not overlapped to obtain cellulose in a solvent dissolving or for special wet the radiation law, cellulose acetate such as a derivative of cellulose, organic solvent such as acetone or methylene chloride after dissolving, vaporizing the solvent of a dry spinning been radiation is performed. However, these wet pumped or dry pumped obtained fiber rate is slow since high productivity as well as door that there may be a number, of the bath carbon disulfide used fiber number, acetone, methylene chloride solvent to form an aqueous environment and may adversely affect the human body such as been prevention. The organic solvent in order to obtain the cellulose as raw material environment-friendly fibers not melt spinning is caused by the spirit. radiation molten thermoplastic cellulose composition and this fiber include cellulose acetate such as glycol polyethylene fiber cellulose composition and adding a large amount of a water-soluble plasticizer number is known. However composition number since high radiation of high percentage content of plasticizer and a low radiation draft if it is not difficult to melt radiationmonoclinal ratio been number point at the door. In order to solve such a door number improve-spinning, fiber retains the thermoplastic cellulose fiber development studies of various attempts to improve it is, fiber color number bath is the maximum limits can be stored and properties even when freezing temperature radiation emanating from radiation and generate molten thermoplastic cellulose is difficult to immediately radiation number point at the door been abruptly solidified. Further, cutting the number of high speed spinning or more door support point 3, 500mpm room inside transmits. Good mechanical properties and excellent touch a door number point at the high pressure liquid coolant number thermoplastic cellulose ultrafine fibers has been difficult. The present invention refers to said door such as point number in order to solve in a certain, first as the selected number of the present invention is not toxic to environment and human and organic solvent can be titled number molten high pressure liquid coolant, when molten in the radiation law number bath by cellulose fiber, cellulose is abruptly so that solidification radiation immediately prevent improve-spinning, improve the mechanical properties of a thermoplastic cellulose derivative retains the pin is to be multilayered under public affairs number. Said thermoplastic cellulose derivative of the present invention second as the selected number is a stand-alone ([...]) solution component from composite fiber and a number by the ultrafine fibers under public affairssensitivity thermoplastic cellulose derivative fibers superfine anger realizing the high-touch number be the pin is. Of the present invention is bonded by high speed and number as the selected third radiation radiation significantly enhance the molten thermoplastic cellulose derivative to be under public affairs number pin is of a fiber composite manufacturing method. In order to solve the above-described and the present invention refers to a number, Cellulose ester and plasticizer a number including number 1 component; and water soluble polyester thermoplastic cellulose derivative fabric including number 2 component including number under public affairs substrate. In the embodiment of the present invention according to one preferred, said cellulose ester is cellulose acetate, cellulose acetate propionate, cellulose acetate butyl rate, cellulose acetate phthalate, cellulose [...], cellulose acetate [...] capric acid, cellulose [...], cellulose [...], comprising at least one selected from the group consisting of cellulose and cellulose [...][...] can be. In the embodiment of the present invention according to another preferred one, number said plasticizer is polyethylene glycol, glycerin, triacetin and can be selected from the group consisting of tree with butyl three Kate comprising at least one. In the embodiment of the present invention according to one preferred another, polyvalent carboxylic acids and sulfonic acid alkali metal salt and acid component including said polyesters 2 to 10 carbon atoms to number bath 1308. diol derivatives components may be mixed together in an esterification and polycondensation. In the embodiment of the present invention according to another preferred one, said sulfonic acid alkali metal salt of acid component including the entire acid component 0. 5 to 25 mole % implementation being. In the embodiment of the present invention preferably according to one another, said sulfonic acid alkali metal salts [...], 5 - [...], 4 - sulfur phthalic acid, naphthalene - 2, 7 - dicarboxylic acid 4 - sulfur, sulfur - p - 2 - sulfur - 1, 4 - bis (rubber ethoxy) [...] and one or more alkali metal selected from the group consisting of mixed be a. In the embodiment of the present invention according to another preferred one, said composite fibers cis - core (sheath provided core) type, even when (Island in the Sea) type, side by side (Side by side) fine-divided type and can be selected from the group consisting (segmented pie). In the embodiment of the present invention preferably according to one another, said composite fibers and component or the component number 1, number 2 component may be a non-active ingredient (Island in the Sea) of these fibers. In the embodiment of the present invention according to another preferred one, said composite fibers core ingredient component number 1, number 2 component sheath component be a cis - core (sheath provided core) of these fibers. In the embodiment of the present invention according to one preferred another, 3:7 to 7:3 number 2 number 1 component and wherein the weight ratio of said composite fibers implementation being. In addition, the present invention refers to the above-mentioned thermoplastic cellulose derivative composite fiber thermoplastic cellulose derivative fibers obtained in a stand-alone number 2 component elution number number under public affairs substrate. In the embodiment of the present invention according to one preferred, said fibers it has 0. 1 to be a 1D in ultrafine fibers. In the embodiment of the present invention according to another preferred one, said fiber has a strength 2. At least 5 g/de, be a 25% or more elongation. In addition, the present invention refers to cellulose ester and plasticizer a number including number 1 component; and water soluble polyester including number 2 component; 3,500 to 5,000 mpm composite spinneret through high speed molten composite emit a thermoplastic cellulose derivative of a fiber composite manufacturing method number under public affairs substrate. In the embodiment of the present invention according to one preferred, said molten composite electrospinning radiation temperature 220 to 250 °C implementation being. In the embodiment of the present invention according to another preferred one, polyvalent carboxylic acids and sulfonic acid alkali metal salt and acid component including said polyesters 2 to 10 carbon atoms to number bath 1308. diol derivatives components may be mixed together in an esterification and polycondensation. In the embodiment of the present invention according to one another preferably, the weight ratio of 3:7 to 7:3 said number 1 component and number 2 component implementation being. In addition, the above-described manufacturing method according to the present invention refers to thermoplastic cellulose derivative fabric number and high pressure liquid coolant, water soluble polyester thermoplastic cellulose derivative industry elution number further including single-fiber fineness of manufacturing method characterized in that a number under public affairs substrate. Thermoplastic cellulose derivative the composite fibers of the present invention without the use of toxic organic solvents for melt spinning number by high pressure liquid coolant does not toxic to human body, so that solidification and workability is improved by preventing radiation immediately cellulose is reflected radiation, radiation can be bonded by 3, 500mpm increase more fast, thermoplastic cellulose derivative fibers can be retains the value corresponding to the number of bath. In addition, a stand-alone number by said thermoplastic cellulose derivative fibers ([...]) solution component from composite fiber yarn fiber thermoplastic cellulose derivative by the ultrafine fibers excellent superfine angersensitivityunder public affairs number can be. Figure 1 shows a cross-section of the core type composite fiber of the present invention also a preferred laser output according to cis - 2000. Figure 2 shows a cross-section of a fiber composite figure according to of the present invention to a preferred laser output also are disclosed. Figure 3 shows a cross-section of the side by side-type bicomponent fibers of the present invention also a preferred laser output according to 2000. Figure 4 shows a cross-section of the present invention preferred laser output according to NP division yarn also are disclosed. Hereinafter, the present invention is the mixture of the products on the drawing data transmissions take other. As above-mentioned molten thermoplastic cellulose derivative fibers of radiation emanating from the fiber color can be stored and properties even when radiation immediately thermoplastic cellulose is freezing temperature radiation maximum limits to support door number generation rate abruptly solidification point, further, a system of high speed spinning room inside 3, 500mpm or more cutting the, good mechanical properties and excellent touch a door number point at the high pressure liquid coolant number thermoplastic cellulose ultrafine fibers has been difficult. The number including number 1 component in the present invention cellulose ester and a plasticizer; and water soluble polyester including number 2 component; and then the above-mentioned thermoplastic cellulose derivative fabric including a number public box fixing by fitting his number. Radiation through a radiation immediately melt-spinning by preventing improve cellulose is abruptly so that solidification, more fast radiation can be bonded by 3, 500mpm increase, thermoplastic cellulose derivative fibers can be retains the value corresponding to the number of bath. In addition, a stand-alone number by said thermoplastic cellulose derivative fibers ([...]) solution component from composite fiber yarn fiber thermoplastic cellulose derivative by the ultrafine fibers excellent superfine angersensitivityunder public affairs number can be. Cis - core of the present invention composite fibers (sheath provided core) type, even when (Island in the Sea) type, side by side (Side by side) may be NP split yarn or the like, the number 1 and number 2 component to each component and not one specifically number into holes preferably including composite fiber form. The present invention refers to a component water soluble polyester plasticizer cellulose ester and glass beads including number 2 component including number 1 number by polyesters is isolated from external air for protecting molten metal by radiation heat loss cellulose is cellulose immediately prevent abruptly so that solidification can be radiation, preventing rapid cellulose does not give spaced and the excellent workability, retains the can be improved, more fast radiation 3, 500mpm assembled by the productivity can be significantly increased. Figure 1 shows a core of the present invention also a preferred laser output according to cis - (sheath provided core) for washing and cross-sectional drawing, such as cis - 1 also it became at the time of (sheath provided core) for washing the core preferably than if said number 1 component core component (21) is used as a, sheath component number 2 component (20) can be made disclosed. On the contrary, it has a core component number 2, number 1 component when a sheath component radiation generated due to rapid freezing of cellulose this old air section of the service cannot be executed for guaranteeing the quality product and high speed radiation number cannot, core component water soluble copolyester when door is a stand-alone number rather strength reduced number thereof can. In addition, Figure 2 shows a laser output according to a preferred of the present invention also (Island in the Sea) for washing and even cross-sectional drawing, number 1 (Island in the Sea) of these fibers even when the component or the component (31) in which, preparation of component number 2 component (30) to be a which (Island in the Sea) of these fibers. At this time component or the (31) preferably has a number of 2 to 8, component or (31) filament size of 0. 1 to 1 D implementation being. On the other hand, number 2 component and vice versa corresponding electrodes, island type number 1 component due to rapid radiation when a high speed takes place in a section of this old cellulose air cannot be guaranteeing the quality cannot radiation freezing and non-oxide ultrafine fibers door number number number article there could disclosed. Figure 3 shows a preferred laser output according to of the present invention also side by side (Side by side) for washing and cross-sectional drawing, and Figure 4 NP division yarn cross-section, said side by side (Side by side) of the present invention number 1 because each location at which equal or NP division of 4.6 formed over the component, it is desirable if a component number 1 number 2 component in weight, least number 2 position is not be particularly number one. Such as composite fiber of the present invention said number 1 component is cellulose ester and plasticizer included in number without using a tool. Some or all said cellulose ester cellulose ester bond has been substituted by a hydroxy cellulose derivatives, strong hydrogen bonds between the hydroxyl groups of cellulose is mixed with a plasticizer to weaken its number is to substrate. Number plasticizer effectively mixing cellulose fluorobenzenes are strong hydrogen bonds due according to the tip melt spinning can be created. Said cellulose ester is preferably a cellulose acetate, cellulose acetate propionate, cellulose acetate butyl rate, cellulose acetate phthalate, cellulose [...], cellulose acetate [...] capric acid, cellulose [...], [...] cellulose, such as cellulose or cellulose [...][...] be used singularly or may be in the form disclosed. Cellulose esters of the present invention can have an average degree of polymerisation 30,000 to 50,000, substitution degree 2. 2 to 2. Wednesday 6 2000. Said column substituted of cellulose esters, cellulose hydroxyl ester substituted speak degree is 2 substitution degree of cellulose esters. 2 when less than, fluidity can be located spaced apart when wet strength, 2. 6 door and then reduced number thereof can is biodegradable. Next, the cellulose derivative is the number said plasticizer mixed as the fluorobenzenes are strong hydrogen bonding due to the special number if a smooth cannot be melt spinning, more preferably plasticized is promoted to a high molecular weight 1000 hereinafter can be using. Said number is dimethyl phthalate plasticizer, [...], [...], oxident, [...], ethyl [...], phthalic esters such as butyl [...], tetra [...], tree such as aromatic polyhydric carboxylic [...][...], [...], [...], d butyl three Kate, [...], [...], [...], such as aromatic polyhydric carboxylic [...][...], glycerin tree acetate, d glycerin tetra acetate polyhydric alcohol fatty acid esters such as scattering, [...] tree, tree [...], tree [...], tree [...] phosphate ester such as such as be used singularly or may be in the form disclosed. In addition, number of high molecular weight plasticizer it relatively as polyethylene glycol, polypropylene glycol, polyethylene adipate, poly [...], polyethylene succinate, poly [...] consisting of glycol and dibasic aliphatic polyester current, polyglycolic acid such as oxy acid stream consisting of aliphatic polyester, polycaprolactone, poly propionic acid lactone, such as bipolar [...] is mainly made of an aliphatic polyester current, like vinyl polymers such as poly vinyl blood Raleigh it went round and be used singularly or may be in the form disclosed. Such as number 2 of the present invention said composite fiber comprising the following polyesters component is included. Water soluble polyester cellulose protected from outside air and to prevent heat loss to the number required for a sufficient time to achieve crystallization old painting speedinfluenceunder public affairs applied, with same number 2 component thermoplastic cellulose derivative composition (component number 1) spaced to prevent molten composite radiation immediately cellulose is abruptly so that solidification, retains the radiation lamp can be improve, 3, 500mpm radiation speed can be possible. In addition, composite fiber number after tank, said water soluble polyester including number 2 component is hereinafter for the elution can be a stand-alone number 0. 1 to 1 D thermoplastic cellulose derivative superfine fiber number can be high pressure liquid coolant. Polyvalent carboxylic acids and sulfonic acid alkali metal salt and acid component including said polyesters 2 to 10 carbon atoms to number bath 1308. diol derivatives components may be mixed together in an esterification and polycondensation. Polyesters of polycarboxylic acid bath number used ingredients include terephthalic acid, isophthalic acid, cyclohexane, 2, 5 - di-methyl-terephthalic acid, 1, 4 - naphthalene dicarboxylic acid, 2, 6 - naphthalene dicarboxylic acid, bis phenyl dicarboxylic acid, 1, 2 - bis (phenoxy) ethane - [...] a-[...] ' - dicarboxylic acid or its ester-forming derivatives can be used, more preferably terephthalic acid or isophthalic acid be a pro-silica powder. Sulfonic acid alkali metal salt of polyvalent carboxylic acid include [...], 5 - [...], 4 - sulfur phthalic acid, naphthalene - 2, 7 - dicarboxylic acid 4 - sulfur n, sulfur - p - [...], 2 - sulfur - 1, 4 - bis (rubber ethoxy) such as alkali metal salts or ester-forming derivatives where the benzene, more preferably 5 - sulfur isophthalic acid, [...] sodium salt or ester-forming derivatives can be. Sulfonic acid alkali metal salt derivative compounds the total bandwidth used polyester polymerization polycarboxylic acid component 0. 5 to 25 mole %, more preferably 7 to 15 mole % implementation being. Sulfonic acid alkali metal salt of polyvalent carboxylic acid 0. 5 mole % when soluble after emission decreases less than the energy needed are added or excessive door number where the elution process cannot be executed, 25 mole % influence polymerization degree of polymerization which exceeds the bubble amount of light from the light source, light from the light source is non-radiation is radiation pack pressure door number can be a predetermined value. Said polyhydric alcohol ingredients include ethylene glycol, 1, 2 - propanediol, 1, 3 - propanediol, 1, 4 - butanediol, 2, 4 - dimethyl - 2 - ethylbenzene - 1, 3 - diol, neopentyl glycol, 1, 5 - pentanediol, 1, 6 - hexanediol, 1, 8 - octanediol, p - xylene glycol, such as 1, 2 - cyclohexane d methanol which, more preferably ethylene glycol, 1, 3 - propanediol, be a 1, 4 - butanediol. The water soluble polyester resin may be commercially use, a compensation publicized patent [...] 1992 - 0000825 call, 1993 - 0004353 [...] call, call reference number 10 - 2005 - 0033262 as are associated with them. Said number tank such as water-soluble copolymerized polyester other than water-soluble polyester number 2 component 3, 500mpm and spinning the molten composite radiation when more fast radiation can fall, and retains the effect is waste, number of stand-alone in a process can occur unevenness and elution superfine anger fiber, fiber is between and repeat, of which the number is close contact with the door thereof can. A weight ratio of 3:7 to 7:3 number 2 of the present invention composite fibers of said number 1 component and implementation being. Said through a number 2 component underexercise cellulose if heated pieces and abrupt transfers radiation high loss reduced and there may be a high speed non-door number, number 2 component lead if cellulose fiber formation rate so as division uniformity maintenance door is the number thereof can. In addition, for obtaining said filament size 0. 5 to 6. 0 D can have, 0. 5 D section formation when less than and may cause a decrease in workability, 6. 0 D touch exposed fiber exceeds the uniform, drop door number eluting property there could disclosed. The number including number 1 component of the present invention composite fibers cellulose ester and a plasticizer; and water soluble polyester including number 2 component; sheath - core type, very fine sand, such as 3,500 to 5,000 mpm composite spinneret bathochromic effect through high speed molten composite spinning number can be high pressure liquid coolant. Said number 2 of polyvalent carboxylic acids and sulfonic acid alkali metal salt and acid component of polyesters including number 2 to 10 carbon atoms can be bath to esterification and polycondensation diol derivatives components may be mixed together, cellulose protected from outside air and to prevent heat loss to achieve sufficient crystallization time under public affairsold painting speedinfluence required number serves to prevent abruptly so that solidification is the radiation immediately cellulose, radiation simply completed, 3, 500mpm radiation speed can be possible, radiation emanating from 220 to 250 °C temperature can be. The number of the present invention composite fibers water soluble polyester prepared by the number via a thermoplastic cellulose derivative fibers including number 2 component elution number can be a stand-alone control unit high pressure liquid coolant. Water soluble polyester thermoplastic cellulose derivative fibers in a layer of a usual number elution step and can be a stand-alone, more preferably 30 to 120 minutes in 50 to 90 °C for hot cleaning weight of 0 minutes to form polyesters. 1% by weight less than can be performed. Water soluble polyester thermoplastic cellulose derivative as the ultrafine fibers in a stand-alone tank elution number by number of composite fiber can be more preferably to form cis - core or figure. Water soluble polyester thermoplastic cellulose derivative filament size number including number 2 component obtained after a stand-alone single-fiber fineness of 0. 1 to 1 D be, strength 2. At least 5 g/de, be a 25% or more elongation. Hereinafter, the present invention in the embodiment to explain but through a more specifically, in the embodiment of the present invention has the number is relayed to the range, this method for assisting in the understanding of the present invention will be interpreted. 1><in the embodiment Also substituted hydroxyl groups of cellulose 2. 4 and, average molecular weight of 40,000 85 weight % cellulose acetate in polyethylene glycol 15 weight % plasticizer eco number (yeast only [...]) on a Royal. In order to prevent heat degradation of ten calcinationscom group fortune compared to crossroad herein when anti-oxidation number 1 difference in tetrakis methylene (3, 5 - di - t - butyl - 4 - hydroxy [...]) (Anox 20, cam weight[...]/Chemtura Corporation) and plasticizer anger chipmaul reel is applied heat degradation of the electrospinning process to prevent anti-oxidation number 2 difference in tris (2, 4 - di - t - butyl phenyl) phosphate (Alcanox 240, cam weight[...]/Chemtura Corporation) number 0 100 parts by weight of a plasticizer composition including cellulose acetate and each. 1 parts by weight after addition, supermixer 2 minutes using mixed. 12 mixed mixture heated-air dryer into drying time, biaxial extrusion mounted using [...] circle feeder 25 kg/hr, fixed rotation speeds (DIE) 5 step 270 rpm motor speed rotation speeds after final end up in temperature over a starting temperature 170 °C die temperature of the silicon substrate 200 °C 5 minutes then to blend a thermoplastic cellulose acetate resin (component number 1) are obtained. In addition, dimethyl 5 - sodium sulfur isophthalic acid followed by reaction and bis - β - hydroxyethyl terephthalate glycol disclosure, terephthalic acid, isophthalic acid, dimethyl glycol followed by an esterification reaction was disclosure. At this time dimethyl 5 - 10 mole % sodium sulfur isophthalic acid component-handler is invoked in total have molecular weight of about 300 kiln, 70 mole % terephthalic acid molecular weight about 150 have in total acid component-handler is invoked kiln, kiln 20 mole % isophthalic acid molecular weight was about 150 in total acid component-handler is invoked. A current reference 70 mole % ethylene glycol molecular weight 60-handler is invoked diol, molecular weight 110 30 mole % is put in his d ethylene glycol-handler is invoked. After this condensation while vesicle number input for polyethylene glycol, anti-oxidation number, number is put in his thermal. Said polyethylene glycol molecular weight 300 weight % in the overall composition 7 occupy have transport, other vesicle number is 0. 02% by weight, anti-oxidation number is 500 ppm, 200 ppm is thermal comfort number by adding polyesters (number 2 component) by Congress. Said thermoplastic cellulose acetate resin (component number 1) copolyester (component number 2) prepared by the number into a molten radiator mounted 36Hole Sheath/Core Core soluble part number 1 to 70% by weight yarn component, part number 2 component 30 weight % Sheath electrochemically spinning 75D/36F - cis which gives rise to light emitted from the core type composite fiber are obtained. Then, washed and time 1 in 60 °C for hot, drying time pulse number 24 80 °C road in a stand-alone of polyesters, 0. 5D thermoplastic cellulose derivative number ultrafine fibers was high pressure liquid coolant. 2><in the embodiment Component or the component and number 1, number 2 component to those in the embodiment 1 and the high pressure liquid coolant hole sand fabric island type number equal to the number under the outside embodiment high pressure liquid coolant to his number. 3><in the embodiment Number 1 component and with the number 2 component in the embodiment 1 and the high pressure liquid coolant 16 NP division yarn number equal to the number divided by number under the outside embodiment was high pressure liquid coolant. 4><in the embodiment Number 1 component and the side with the number 2 component in the embodiment 1 and the high pressure liquid coolant-side - - number equal to the number fibers under the outside embodiment number was high pressure liquid coolant. 5><in the embodiment Number 1 component and the number 1 and number 2 component 9:1 weight ratio in the range of 0.1 to equal to his number under the outside embodiment embodiment high pressure liquid coolant. 6><in the embodiment Number 1 component and the number 1 and number 2 component weight ratio in the range of 0.1 to 1:9 under the outside embodiment embodiment his number equal to the high pressure liquid coolant. 7><in the embodiment Forming properties and component number 1, number 2 component by component or the number equal to the number in the embodiment 1 embodiment under the outside hole sand fabric with a high pressure liquid coolant and high pressure liquid coolant to his number. 8><in the embodiment Dimethyl 5 - 30 mole % acidic ingredient sodium sulfur isophthalic acid, 60 mole % terephthalic acid, isophthalic acid and diols ingredient 10 mole % percutaneous 30 mole %, polyethylene glycol 0. 1 mol %, CHDM 1. 9 mol %, water-soluble polyester number 68 mole % ethylene glycol by copolymerizing high pressure liquid coolant in the embodiment 1 and the embodiment number was in the range of 0.1 under the outside number equal to the high pressure liquid coolant. 9><in the embodiment 30 minutes in number with the number 2 and number under the outside 40 °C hot water through the stand-alone component in the embodiment 1 to the embodiment number equal to his high pressure liquid coolant. 10><in the embodiment 100 °C boiling water from the surface of the component in the embodiment 1 number 1 and number 2 time with the number equal to the number to a stand-alone embodiment under the outside his high pressure liquid coolant. <Comparison example> Substitution degree 2. 4 and, number 15% and 85% by weight plasticizer weight average molecular weight of 40,000 (yeast only [...]) cellulose acetate in a number equal to the number in the embodiment 1 and the embodiment under the outside spinning alone was high pressure liquid coolant. <Experiment example> 1. Steel, measuring elongation Fiber steel, automatic tension tester (Textechno [...]) elongation measurements may be made using speed of 50 cm/m, 50 cm by applying gripping distance were measured. Formed fiber strength and elongation constant stretch until the lifting force is cut when the value obtained by dividing an load denier (Denier; de) (g/de) suffering from a strength, elongation percentage (%) indicating a value in an extended length to the first length was defined. 2. Spinning the evaluation High speed spinning of radiating workability for evaluating whether his determines as follows. ×: radiation cannot be, Δ: freezing in 5 minutes, ○: freezing in 10 minutes, ◎: good 3. Tactile evaluation 10 specialist name by the check result reference system is functional. 8 when the spinning one or more judges that a ◎, 5 ∼ 7 when players determine good Δ, one or more judges that was divided into 8 has been placed in a moment when a × is poor. 1 studied at said table in a desired, water soluble polyester number 2 component in the embodiment 1 to 4 embodiment 4, 000mpm composite radiated compared compared even radiation includes a body speed, number 2 and number of ultrafine fibers can be a stand-alone component number 1 De hereinafter high pressure liquid coolant, and is coupled with the retains, also significantly excellent touch up. Only, water soluble polyester composite including 5, 6 in the embodiment 4, 000mpm either underexercise excess spinning in the embodiment 1 to 4 as well as in the case of read element of high speed spinning of 2, 500mpm than has been separated, such as been the group retains the spinning. In addition, polyesters including composite radiated to the opposite component by radiated radiation even when/nearly impossible and also in the embodiment 7, the effect of the invention is almost implemented we shall be, preferably water-soluble polyester of the present invention according to another exemplary embodiment of using non-polyesters prepared by the number of high speed spinning in the embodiment 8 is 4, 000mpm guardroom, fluorescence is detected radiation 2, 500mpm workability, retains the, in the embodiment 1 to 4 as time compared to touch fell effectively. In the embodiment 9 is polyesters is 0. 1 weight % or more of a high pressure liquid coolant to ultrafine fibers remaining 1D hereinafter room number, indicating excellent touch me. In addition, in the embodiment 10 is a layer of a plasticizer in polyesters as well as to the number and be eluted, fiber reconfigured within the fibers touch is reduced. The present invention relates to a thermoplastic cellulose derivative composite fiber and a method for preparing the same. Specifically, the thermoplastic cellulose derivative composite fiber of the present invention is harmless to humans as the fiber is prepared by melt spinning without using toxic organic solvent; rapid consolidation of the cellulose is prevented upon spinning to enhance work efficiency of the spinning and to enable high-speed spinning of 3,500 mpm or more to maximize productivity; and physical properties of the prepared thermoplastic cellulose derivative composite fiber such as strength and elongation or the like can be improved. Furthermore, by removing easy dissolution components from the thermoplastic cellulose derivative composite fiber, the fiber becomes superfine to be able to provide high-sensitive thermoplastic cellulose derivative composite superfine fiber with excellent texture. Cellulose ester and plasticizer a number including number 1 component; and water soluble polyester including number 2 component; and, said polyesters terephthalic acid 60 - 70 mole %, 10 - 20 mole % residual dimethyl 5 - sodium sulfur isophthalic acid and isophthalic acid and acid component including; and ethylene glycol and Nmm including diol current; and prepared by the number of the reaction of the, 50 to 60 °C for hot thermoplastic cellulose derivative are added in makes it possible to composite fiber. According to Claim 1, said cellulose ester is cellulose acetate, cellulose acetate propionate, cellulose acetate butyl rate, cellulose acetate phthalate, cellulose [...], cellulose acetate [...] capric acid, cellulose [...], cellulose [...], including at least one selected from the group consisting of cellulose and cellulose [...][...] characterized composite fiber thermoplastic cellulose derivative. According to Claim 1, number said plasticizer is polyethylene glycol, glycerin, triacetin and tree including at least one selected from the group consisting characterized with butyl three Kate any thermoplastic cellulose derivative composite fiber. Back number Back number Back number According to Claim 1, said composite fibers cis - core (sheath provided core) type, even when (Island in the Sea) type, side by side (Side by side) divided type and fine (segmented pie) selected from the group consisting of composite fiber-thermoplastic cellulose derivative. According to Claim 1, said composite fibers and component or the component number 1, number 2 component even when non-active ingredient (Island in the Sea) type fiber characterized in that the thermoplastic cellulose derivative composite fiber. According to Claim 1, said composite fibers core ingredient component number 1, number 2 component sheath component characterized in that the cis - (sheath provided core) of these fibers core thermoplastic cellulose derivative composite fiber. According to Claim 1, wherein the weight ratio of 3:7 to 7:3 number 2 number 1 component and said composite fibers characterized in composite fiber thermoplastic cellulose derivative. Number 1 to number 2 component in any one of Claim 7 to Claim 10 thermoplastic cellulose derivative composite fiber 50 to 60 °C for hot number 3 term and anti elution number obtained in a stand-alone and fibers, said fiber has a strength 2. At least 5 g/de, thermoplastic cellulose derivative fibers and an elongation of not more than 25%. According to Claim 11, said fibers it has 0. 1 to 1D in characterized in that the ultrafine fibers thermoplastic cellulose derivative fibers. Back number Cellulose ester and plasticizer a number including number 1 component; and water soluble polyester including number 2 component; 3,500 to 5,000 mpm composite spinneret through high speed molten composite spinning a, said 60 - 70 mole % terephthalic acid polyesters, including 10 - 20 mole % dimethyl 5 - sodium sulfur isophthalic acid and isophthalic acid and residual acid component; and ethylene glycol and Nmm including diol current; and prepared by the number of the reaction of the, 50 to 60 °C in water are added thermoplastic cellulose derivative of a fiber composite manufacturing method makes it possible to. According to Claim 14, characterized in said molten composite electrospinning radiation temperature 220 to 250 °C thermoplastic cellulose derivative of a fiber composite manufacturing method. Back number According to Claim 14, the weight ratio of 3:7 to 7:3 number 2 component characterized in said number 1 component and a thermoplastic cellulose derivative of a fiber composite manufacturing method. Number 14 anti, anti either thermoplastic cellulose derivative fabric manufacturing method according to 17 term and a number 15 terms number and high pressure liquid coolant, water soluble polyester industry characterized in further including elution number 50 to 60 °C for hot thermoplastic cellulose derivative-fiber manufacturing method. Radial velocity (mpm) Spinning the Strength (g/de) Elongation (%) Also island (De) Tactile evaluation In the embodiment 1 4000 ◎ 3. 5 32 0. 75 ◎ In the embodiment 2 4000 ◎ 3. 4 30 0. 76 ◎ In the embodiment 3 4000 ◎ 3. 1 28 0. 78 ◎ In the embodiment 4 4000 ◎ 2. 7 26 0. 77 ◎ In the embodiment 5 4000 Δ - - - × 2500 ○ 2. 3 25 0. 74 Δ In the embodiment 6 4000 Δ - - - × 2500 ○ 2. 4 22 0. 75 Δ In the embodiment 7 4000 × - - - - 2500 × - - - - In the embodiment 8 4000 × - - - - 2500 ○ 1. 9 20 0. 76 × In the embodiment 9 4000 ◎ 2. 5 23 1. 2 Δ In the embodiment 10 4000 ◎ 1. 8 19 0. 68 Δ Comparison example 4000 ○ 2. 1 23 0. 75 Δ 2500 ◎ 2. 3 24 0. 77 Δ