CN100543060C - The preparation technology of poly lactic acid in use for spinning - Google Patents
The preparation technology of poly lactic acid in use for spinning Download PDFInfo
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Abstract
The invention belongs to technical field of polymer materials, be specifically related to a kind of preparation technology who is applied to poly lactic acid in use for spinning, its concrete steps are as follows: (1). and lactic acid concentrates: controlled temperature, vacuum tightness, the dehydration concentrated lactic acid liquid that concentrates, obtains dewatering; (2). precondensation: add catalyst compoundedly, controlled temperature, vacuum ranges in the reaction times, obtain the precondensation powder; (3). solid state polymerization: add thermo-stabilizer, antioxidant, controlled temperature, vacuum ranges, constant temperature obtains the poly(lactic acid) particle; (4). red shortness's modification: add heat modification agent and mineral acid, controlled temperature in the reaction times, obtains poly(lactic acid).It is directly to carry out mass polymerization by lactic acid monomer, do not add solvent, do not need inert gas environment atmosphere, technology is easy to control, the polycondensating process flow process is short, the yield height, and environmental pollution is little, molecular weight by solid phase polycondensation and red shortness's modification, poly(lactic acid) has significantly and improves, and percent thermal shrinkage significantly reduces.
Description
Technical field
The invention belongs to technical field of polymer materials, be specifically related to a kind of preparation technology who is applied to poly lactic acid in use for spinning.
Background technology
Poly(lactic acid) (english abbreviation: PLA) be novel completely biodegradable material, can be used as multiple uses such as spinning, injection moulding, manufacturing wrapping material, medical material.The big leap ahead of the demand of non-woven applies in weaving, clothes, industry and the agroforestry poly-lactic acid material more widely in recent years.The synthetic method of poly(lactic acid) has two step ring-opening polymerization method and direct polycondensation methods, and wherein direct polycondensation method is divided into solution polycondensation and fusion-process for solid state polycondensation.
Adopt the ring-opening polymerization method can obtain the higher poly-lactic acid products of molecular weight, United States Patent (USP) the 5th, 357, disclosed the method that a kind of open loop prepares polyphosphazene polymer lactic acid No. 035: prepare few polymeric poly(lactic acid) by lactic acid, by making the third glue ester behind the few polymeric poly(lactic acid) distillation purifying, utilize the third glue polyisocyanate polyaddition poly(lactic acid) more again.But this method operational path is long, and complex procedures need expend and reclaim a large amount of organic solvents, and the intermediate product rac-Lactide stores difficulty, and significant loss is big in the reaction process, productive rate is low, the price height of product.Adopt present method preparation cost too high, restricted being extensive use of poly(lactic acid).
Adopt the technology of direct polycondensation method simple, chemical feedstocks, reagent usage quantity are less, and the product yield is higher, but polymerization solvent for use environmental pollution is bigger, residue in simultaneously that difficulty cleans up in the product.
Adopting melt phase polycondensation is that lactic acid monomer is directly carried out mass polymerization, do not need to add solvent, technology is easy to control, have significantly by the solid phase polycondensation molecular weight and to improve, main fusion polycondensation and two steps of solid phase polycondensation of dividing in the operation, it is compared the reaction times and shortens greatly with two step open loop methods, technology is simple, changing the solid phase polycondensation stage over to by melt phase polycondensation only needs crude product is pulverized, and the solid phase polycondensation of subordinate phase is easy to operate, the operation that need not consume a large amount of solvents and purify through recrystallization repeatedly.
Direct method prepares the technical study of poly(lactic acid) starts late, and prepared polylactic acid molecule amount is not high, and atmosphere requires high, and crystallization rate is low, percent thermal shrinkage is high, can not satisfy the non-woven requirement of filature fleece formation.Therefore develop the low poly(lactic acid) technology of preparing of high molecular percent thermal shrinkage,, all have great importance making full use of the development that Natural Resources in China improves additional value of farm products and promotes domestic lactic acid industry.
Summary of the invention
The preparation technology's method that the purpose of this invention is to provide a kind of poly lactic acid in use for spinning, it is directly to carry out mass polymerization by lactic acid monomer, do not add solvent, do not need inert gas environment atmosphere, technology is easy to control, and the polycondensating process flow process is short, the yield height, environmental pollution is little, and the molecular weight by solid phase polycondensation and red shortness's modification, poly(lactic acid) has significantly and improves, and percent thermal shrinkage significantly reduces.
Technical scheme of the present invention is, a kind of preparation technology of poly lactic acid in use for spinning, and its concrete steps are as follows:
(1). lactic acid concentrates:
Lactic acid is packed on the evaporimeter, and controlled temperature is at 45 ℃-95 ℃, and vacuum tightness is 9,000Pa-80, and 000Pa, dehydration concentrates 1-3 hour, and the concentrated lactic acid liquid that obtains dewatering is standby;
(2). precondensation:
With the spissated lactic acid that dewaters is raw material, adds catalyst compoundedly, and controlled temperature is at 170-190 ℃, vacuum ranges 0-1, and 600Pa reacted after 8-12 hour, and with white performed polymer fragmentation, separating liquiding catalyst is pulverized the precondensation powder into 0.1-0.3mm, and is standby;
(3). solid state polymerization:
Add thermo-stabilizer, antioxidant in the precondensation powder, in air, be warming up to 140-165 ℃ by room temperature, vacuum ranges 0-100Pa is incubated 10-33 hour, and obtaining weight-average molecular weight is 120,000-210,000 poly(lactic acid) particle;
(4). red shortness's modification:
In the poly(lactic acid) particle of solid state polymerization, add heat modification agent and mineral acid, vacuum ranges 3,000-8,000Pa, the intensification degree reacted 10-60 minute under the atmospheric pressure in air atmosphere under 170-230 ℃, obtained weight-average molecular weight 120,000-210, the poly(lactic acid) of 000 saturation steam percent thermal shrinkage 1-5%.
Described controlled temperature is the sequencing controlled temperature, and described vacuum tightness is sequencing control vacuum tightness, and its temperature programization and vacuum tightness programmed process are:
(1) lactic acid concentrates: concrete technology is starting temperature with 45 ℃-55 ℃, every half an hour temperature is raise 6-12 ℃ then, with 50,000Pa-80,000Pa is initial vacuum tightness, every half an hour vacuum tightness is reduced by 10 then, 000-15,000Pa, 1-2.5 vaporization temperature reaches 85-95 ℃, vacuum tightness and reaches 9 after hour, 000-12, during 000Pa, constant temperature concentrated half an hour of concentration technology finishes;
(2) precondensation: with the spissated lactic acid that dewaters is raw material, add catalyst compounded, be warmed up to 170-190 ℃, vacuum tightness with 1 ℃ of-3 ℃ of temperature rise rate of per minute and transfer to 600-1,600Pa, react after 6-9 hour, temperature is reduced to 100-120 ℃, and vacuum tightness transfers to 0-100Pa, after constant temperature 2-3 hour, obtain white poly(lactic acid) performed polymer;
(3) solid state polymerization: in air, in the precondensation powder, add thermo-stabilizer, oxidation inhibitor, be warming up to 140-165 ℃ by room temperature, vacuum ranges 0-100Pa, insulation 33h is two sections temperature controls, wherein preceding 10-11h temperature is 140-155 ℃, vacuum ranges 90-100Pa, back 10-22h temperature is 145-165 ℃, vacuum ranges 0-90Pa;
(4) red shortness's modification: in the poly(lactic acid) particle of solid state polymerization, add heat modification agent and mineral acid, vacuum ranges 3,000-8,000Pa, reach 170-230 ℃ with a per minute 1-3 ℃ intensification, after 3-5 minute, in air atmosphere, reacted 10-60 minute under the normal atmosphere (An) condition.
Described solid state polymerization: other is incubated 20-33h is three sections temperature controls, and wherein 0-10h is 140-150 ℃, and vacuum ranges 90-100Pa, 10-20h are 145-155 ℃, and vacuum ranges 80-90Pa, 12-30h are 150-165 ℃, vacuum ranges 0-80Pa.
Described catalyst compounded be the combination catalyst of the compound preparation of 200 order glass puttys of commercially available 37%, the analytical pure HCl of 0.04-0.06 and 0-0.95 nano level glass putty and 0-0.95.
Described thermo-stabilizer is any in methyl tin, barium stearate, Zinic stearas, Magnesium Stearate, the calcium stearate, and consumption is 0-0.3%.
Described oxidation inhibitor is four [β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, β (3,5-di-t-butyl-4-hydroxybenzene) propionic acid octadecanol ester, Tyox B, triphenyl phosphite, three (nonylated phenyl) phosphorous acid ester 2,5-ditert-butylhydro quinone, 4, in 4 '-butyl-two (3-methyl-6-tertiary butyl) phenol any, consumption is 0-0.3%.
Described properties-correcting agent is isocyanuric acid three-glycidyl ester, trihydroxyethyl isocyanuric ester, Tetra hydro Phthalic anhydride, glyoxal ethyline, phosphorous acid dihydroxyphenyl propane ester, vinyl triethoxyl osmanthus alkane, divinyl triammonium base propyl triethoxy osmanthus alkane, 3, in 3 '-diaminodiphenylsulfone(DDS), sec.-propyl three (dioctylphyrophosphoric acid ester) titanic acid ester any, consumption is 0-15%.
The preparation method of described nano level glass putty is dissolved SnCl with commercially available 37%, analytical pure HCl
4, dilute SnCl for 5-20%
4Hydrochloric acid soln adds 1-5%NaBH in solution
4NaOH solution, until pH=11, left standstill 1-3 hour, isolate nanometer tin, obtain the nanometer glass putty after the drying.
Described mineral acid is any in sulfuric acid, phosphoric acid, the hydrochloric acid.
Characteristics of the present invention are:
Adopted sequencing temperature control and sequencing control reaction vacuum tightness in responding.Avoid temperature to cross condition of high vacuum degree and cross low and lactic acid bumping that cause, improve the yield of concentrated lactic acid.
2. in the precondensation process, use catalyzer as mineral acid and the ultra-fine and composite composition of nano metal powder, can after the precondensation process is finished, isolate solid-phase catalyst like this, reduce the impurity of final poly(lactic acid).
3. do not use chainextender in the just usually said chain extension process in the solid state polymerization, but add oxidation inhibitor and thermo-stabilizer, atmosphere of inert gases is not provided simultaneously.Reduce production unit, reduced production energy consumption.
4. carried out heat resistance modifiedly, made poly lactic acid in use for spinning percent thermal shrinkage 1-5%, reached existing nonwoven process requirement.Domestic do not appear in the newspapers and patent known.
Embodiment
The present invention will be further described below in conjunction with the embodiment technical process.
The technical process of fusion-solid state polymerization is as follows:
1, lactic acid concentration technology: adopt programed temperature and vacuum tightness, when lactic acid begins to concentrate, contain large quantity of moisture in the lactic acid, viscosity is lower, if it is low excessively that temperature is crossed condition of high vacuum degree, can cause the lactic acid bumping, reduce the yield of lactic acid, carry out along with spissated, have part lactic acid to assemble the poly(lactic acid) of synthesized micromolecule, the moisture of generation is also extracted out concentrate system by vacuum pump, and lactic acid viscosity increases gradually, just elevated temperature progressively reduces vacuum tightness.Concrete technology is starting temperature with 45 ℃-55 ℃, every half an hour temperature is raise 6-12 ℃ then, with 50,000-80,000Pa is initial vacuum tightness, every half an hour vacuum tightness is reduced by 10 then, 000-15,000Pa, 1-2.5 vaporization temperature reaches 85-95 ℃, vacuum tightness and reaches 9,000-12,000Pa after hour, constant temperature concentrates and finishes half an hour, and the lactic acid that obtains dewatering concentrates.Acid by dehydrating lactic finishes, the concentrated lactic acid yield reaches 83～92%.
2, precondensation technology: after the spissated lactic acid adding of dewatering is catalyst compounded, when being warmed up to 170-190 ℃ with 1 ℃ of-3 ℃ of temperature rise rate of per minute, vacuum tightness is transferred to 600-1, and 600Pa reacts after 6-9 hour, temperature drops to 100-120 ℃, vacuum tightness transfers to 0-100Pa, after constant temperature 2-3 hour, and the white performed polymer fragmentation that reaction is obtained, separating liquiding catalyst is pulverized the precondensation powder into 0.1-0.3mm.
3, solid state polymerization technique: in air, in the precondensation powder, add thermo-stabilizer, antioxidant, be warming up to 140-165 ℃ by 20 ℃ of room temperatures, vacuum ranges 0-100Pa, insulation 20-33h is two sections temperature controls, wherein preceding 10-11h temperature is 140-155 ℃, vacuum ranges 90-100Pa, back 10-22h temperature is 145-165 ℃, vacuum ranges 0-90Pa, and obtaining weight-average molecular weight is 120,000-210,000 poly(lactic acid) particle;
Other is incubated 20-33h can also be three sections temperature controls, wherein 0-10h is 140-150 ℃, vacuum ranges 90-100Pa, 10-20h is 145-155 ℃, and vacuum ranges 80-90Pa, 20-30h are 150-165 ℃, vacuum ranges 0-80Pa, obtaining weight-average molecular weight is 120,000-210,000 poly(lactic acid) particle.
4, red shortness's modified technique: in the poly(lactic acid) particle of solid state polymerization, add heat modification agent and mineral acid, vacuum ranges 3,000-8,000Pa reaches 170-230 ℃ with a per minute 1-3 ℃ intensification, after 3-5 minute, in air atmosphere, reacted 10-60 minute under the normal atmosphere (An) condition, obtain weight-average molecular weight 120,000-210, the poly(lactic acid) of 000 saturation steam percent thermal shrinkage 1-5%.
Among the above-mentioned preparation technology, wherein:
Catalyzer: employed catalyzer is commercially available (37%, the analytical pure) HCl of 0.04-0.06 and the combination catalyst of 0-0.95 nanometer glass putty and the compound preparation of 0-0.95 glass putty (less than 200 orders), wherein nanometer glass putty self-control.
Nano level glass putty self-control method: HCl dissolves SnCl with commercially available (37%, analytical pure)
4, dilute SnCl for 5-20%
4Hydrochloric acid soln adds 1-5%NaBH in solution
4NaOH solution, until pH=11, left standstill 1-3 hour, isolate nanometer tin, obtain the nanometer glass putty after the drying.
Oxidation inhibitor: be four [β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, β (3,5-di-t-butyl-4-hydroxybenzene) propionic acid octadecanol ester, Tyox B, triphenyl phosphite, three (nonylated phenyl) phosphorous acid ester 2,5-ditert-butylhydro quinone, 4, in 4 '-butyl-two (3-methyl-6-tertiary butyl) phenol any, consumption is 0-0.3%.
Thermo-stabilizer: be in methyl tin, barium stearate, Zinic stearas, Magnesium Stearate, the calcium stearate any, consumption is 0-0.3%.
Red shortness's properties-correcting agent: be isocyanuric acid three-glycidyl ester, trihydroxyethyl isocyanuric ester, Tetra hydro Phthalic anhydride, glyoxal ethyline, phosphorous acid dihydroxyphenyl propane ester, vinyl triethoxyl osmanthus alkane, divinyl triammonium base propyl triethoxy osmanthus alkane, 3, in 3 '-diaminodiphenylsulfone(DDS), sec.-propyl three (dioctylphyrophosphoric acid ester) titanic acid ester any, consumption is 1%-15%.
Mineral acid: be in sulfuric acid, phosphoric acid, the hydrochloric acid any.
Below by specific embodiment the present invention is further elaborated.
Embodiment 1:
1. lactic acid concentrates
The lactic acid of 300mL is packed in the 1000mL round-bottomed flask, on Rotary Evaporators, fix, make round-bottomed flask submerge in the water-bath, controlled temperature is at 50 ℃, and pressure is 50,000Pa, every half an hour temperature is raise 10 ℃ later on, vacuum tightness reduces by 10,000Pa, vaporization temperature reaches 90 ℃ after 1 hour, vacuum tightness reduces by 9, and during 000Pa, constant temperature finishes after concentrating half an hour, obtain the concentrated lactic acid that dewaters, the concentrated lactic acid yield reaches 85～91%.
2. precondensation
The lactic acid that 220g concentrated is put into the revolving bottle that rotates film evaporator, add composite catalyst 0.015%HCl, 0.1% glass putty, 0.2% self-control nanometer glass putty, be warmed up to 180 ℃ with 1 ℃ of temperature rise rate of per minute in the oil bath, start vacuum pump, slowly vacuum tightness is transferred to 750Pa, polymerization 8h cools to 110 ℃ with this understanding, vacuum tightness obtains oyster white lactic acid performed polymer 80Pa constant temperature 2.5 hours.With its fragmentation, isolating catalyzer builds up behind the body (in the revolving bottle of rotation film evaporator, by the precondensation process, catalyzer has been assembled agglomerating because of the density difference, wrapped up by the lactic acid of precondensation, when broken oyster white lactic acid performed polymer, the catalyzer natural separation), pulverize precondensation powder into 0.2mm.
Below can divide following three kinds for catalyst proportion:
(1) catalyst proportion: 0.3% glass putty (200 order), 0.015% (37% analytical pure) HCl can obtain the lactic acid performed polymer of weight-average molecular weight 29,000 as 2 precondensation;
(2) catalyst proportion: 0.3% nanometer glass putty (self-control), 0.015% (37% analytical pure) HCl can obtain the lactic acid performed polymer of weight-average molecular weight 30,000 as 2 precondensation;
(3) catalyst proportion: 0.1% nanometer glass putty (self-control), 0.2% glass putty (200 order), 0.015% (37% analytical pure) HCl can obtain the lactic acid performed polymer of weight-average molecular weight 40,000 as 2 precondensation.
3. solid state polymerization:
Add 0.3% 4 [β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, be warming up to 140 ℃ by room temperature, insulation 20h is two sections temperature controls, and wherein preceding 10h temperature is 140 ℃, and vacuum tightness is 100Pa, back 10h temperature is 145 ℃, vacuum tightness is 90Pa, obtains weight-average molecular weight and be 135,000 poly(lactic acid) particle.
4. red shortness's modification:
In the poly(lactic acid) particle of solid state polymerization, add 10% heat modification agent isocyanuric acid three-glycidyl ester and 0.02% (37% analytical pure) HCl, vacuum tightness is 8,000Pa, be warmed up to 190 ℃ of temperature with 3 ℃ of temperature rise rates of per minute, after 3 minutes, reaction is 20 minutes under air atmosphere normal atmosphere (An) condition, and obtaining weight-average molecular weight is the poly(lactic acid) of 145,000 saturation steam percent thermal shrinkage 1-4%.
Embodiment 2
Its concrete preparation method is with embodiment 1, and different is:
1. lactic acid concentrates
The lactic acid of 300mL is packed in the 1000mL round-bottomed flask, on Rotary Evaporators, fix, make round-bottomed flask submerge in the water-bath, controlled temperature is at 45 ℃, pressure is 70, and 000Pa raises temperature 12 ℃ every half an hour later on, vacuum tightness reduces by 15,000Pa, vaporization temperature reaches 85 ℃, vacuum tightness reduction by 10 after 2 hours, during 000Pa, constant temperature concentrates after half an hour and finishes, and obtains the concentrated lactic acid that dewaters.The concentrated lactic acid yield reaches 83～90%.
2. precondensation
The lactic acid that 220g concentrated is put into revolving bottle, add composite catalyst 0.015%HCl, 0.2% glass putty, 0.1% self-control nanometer glass putty, be warmed up to 170 ℃ with 2 ℃ of temperature rise rates of per minute in the oil bath, start vacuum pump, slowly vacuum tightness is transferred to 600Pa, with this understanding polymerization 6h, cool to 100 ℃, vacuum tightness is at 100Pa, and constant temperature 2h obtains oyster white lactic acid performed polymer.With its fragmentation, after isolating catalyzer and building up body, pulverize precondensation powder into 0.1mm.
Catalyst proportion is with embodiment 1.
3. solid state polymerization:
Add 0.3% barium stearate, be warming up to 140 ℃ by room temperature, insulation 30h is three sections temperature controls, and wherein 0-10h is 140 ℃, and vacuum tightness is 90Pa; 10-20h is 145 ℃, and vacuum tightness is 80Pa; 20-30h is 150 ℃, and vacuum tightness is 70Pa, obtains weight-average molecular weight and be 145,000 poly(lactic acid) particle.
4. red shortness's modification:
In the poly(lactic acid) particle of solid state polymerization, add 10% heat modification agent trihydroxyethyl isocyanuric ester and 0.02% (37% analytical pure) HCl, vacuum tightness is 6,000Pa, be warmed up to 230 ℃ of temperature with 1 ℃ of temperature rise rate of per minute, after 5 minutes, depress reaction 10 minutes at the air atmosphere normal atmospheric, obtain the poly(lactic acid) of weight-average molecular weight 150,000 saturation steam percent thermal shrinkage 1-4%.
Embodiment 3
Its concrete preparation method is with embodiment 1, and different is:
1. lactic acid concentrates
The lactic acid of 300mL is packed in the 1000mL round-bottomed flask, on Rotary Evaporators, fix, make round-bottomed flask submerge in the water-bath, controlled temperature is at 55 ℃, and pressure is 80,000Pa, every half an hour temperature is raise 6 ℃ later on, vacuum tightness reduces by 14,000Pa, and vaporization temperature reaches 95 ℃, vacuum tightness and is reduced to 12 after 2.5 hours, during 000Pa, constant temperature concentrates after half an hour and finishes, and obtains the concentrated lactic acid that dewaters, and the concentrated lactic acid yield reaches 83～92%.
2. precondensation
The lactic acid that 220g concentrated is put into revolving bottle, add composite catalyst 0.015%HCl, 0.1% glass putty, 0.2% self-control nanometer glass putty, be warmed up to 190 ℃ with 3 ℃ of temperature rise rates of per minute in the oil bath, start vacuum pump, slowly vacuum tightness is transferred to 1,600Pa, polymerization 9h with this understanding, cool to 120 ℃, vacuum tightness obtains oyster white lactic acid performed polymer 70Pa constant temperature 3 hours.With its fragmentation, after isolating catalyzer and building up body, pulverize precondensation powder into 0.3mm.
Catalyst proportion is with embodiment 1.
3. solid state polymerization:
Add 0.3% thermo-stabilizer barium stearate, insulation 33h is two sections temperature controls, and wherein preceding 11h temperature is 155 ℃, and vacuum tightness is 95Pa; Back 22h temperature is 165 ℃, and vacuum tightness is 75Pa, obtains weight-average molecular weight and be 167,000 poly(lactic acid) particle.
4. red shortness's modification:
3 of adding 0.3%, 3 '-diaminodiphenylsulfone(DDS), vacuum tightness is 3,000Pa is warmed up to 170 ℃ with 2 ℃ of temperature rise rates of per minute, after 4 minutes, depressed constant temperature 60 minutes at normal atmospheric, obtaining weight-average molecular weight is the poly(lactic acid) of 170,000 saturation steam percent thermal shrinkage 1-3%.
Need to prove that the present invention is not limited only to the foregoing description, the present invention uses catalyzer can also be mineral acid (H in specific implementation process
2SO
4, H
3PO
4, HCl) and the composite composition of other metal-powder of nano level (any one or more different gradation mixture in magnesium, zinc, the aluminium), can after the precondensation process is finished, isolate solid-phase catalyst like this, reduce the impurity of final poly(lactic acid).
Do not use chainextender in the just usually said chain extension process in the solid state polymerization, but add oxidation inhibitor and thermo-stabilizer, add antioxidant and thermo-stabilizer and be not limited only to the cited item number of the foregoing description, can also be: β (3,5-di-t-butyl-4-hydroxybenzene) propionic acid octadecanol ester, Tyox B, triphenyl phosphite, three (nonylated phenyl) phosphorous acid ester 2,5-ditert-butylhydro quinone, 4, any in 4 '-butyl-two (3-methyl-6-tertiary butyl) phenol, methyl tin, Zinic stearas, Magnesium Stearate, the calcium stearate.Atmosphere of inert gases is not provided simultaneously.Reduce production unit, reduced production energy consumption.
Carried out heat resistance modified, the properties-correcting agent that adds is not limited only to the cited item number of the foregoing description, can also be: Tetra hydro Phthalic anhydride, phosphorous acid dihydroxyphenyl propane ester, vinyl triethoxyl osmanthus alkane, divinyl triammonium base propyl triethoxy osmanthus alkane, 3, in 3 '-diaminodiphenylsulfone(DDS), the sec.-propyl three (dioctylphyrophosphoric acid ester) any, make poly lactic acid in use for spinning saturation steam percent thermal shrinkage 1-5%, reached existing nonwoven process requirement.
Claims (5)
1, the preparation technology of poly lactic acid in use for spinning is directly to carry out mass polymerization by lactic acid monomer, and its concrete steps are as follows:
1), lactic acid concentrates: lactic acid is packed into when beginning to concentrate on the evaporimeter, with 45 ℃～55 ℃ is that starting temperature, 50000～80000Pa are initial vacuum tightness, every 0.5h 6～12 ℃ of temperature risings, vacuum tightness are reduced 10000-15000Pa, behind 1～2.5h, temperature reaches 85～95 ℃, vacuum tightness and reaches 9000～12000Pa, constant temperature 0.5h can obtain the lactic acid that dewaters again, and the acid by dehydrating lactic enrichment factor reaches 83～92%;
2), system precondensation powder: commercially available 37% of will dewater spissated lactic acid and 0.04-0.06, the catalyst compounded mixing of analytical pure HCl and the compound preparation of 200 order glass puttys of 0-0.95 nano level glass putty and 0-0.95, when being warmed up to 170～190 ℃ with 1 ℃～3 ℃ temperature rise rates of per minute, vacuum tightness is transferred to 600～1600Pa, behind reaction 6～9h, temperature drops to 100～120 ℃, vacuum tightness transfers to 0～100Pa, constant temperature 2～3h again, obtain the preshrunk aggressiveness of white, separating liquiding catalyst, must pulverize is the precondensation powder of 0.1～0.3mm;
3), solid state polymerization: in air, the precondensation powder is mixed with 0-0.3% thermo-stabilizer, 0-0.3% antioxidant, rise to 140～165 ℃ for 20 ℃ by vacuum tightness 0～100Pa, temperature, insulation 33h obtains weight-average molecular weight and is 120000～210000 poly(lactic acid) particle; Insulation 33h is two sections temperature controls, and wherein preceding 11h temperature is 140-155 ℃, vacuum ranges 90-100Pa, and back 22h temperature is 145-165 ℃, vacuum ranges 0-90Pa;
4), red shortness's modification: the poly(lactic acid) particle of solid state polymerization is mixed with heat modification agent and the mineral acid of 0-15% again, vacuum tightness 3000-8000Pa, reach 170～230 ℃ with 1～3 ℃ of intensification of per minute, after 3～5 minutes, under the air atmosphere atmospheric pressure, reacted 10～60 minutes, and obtained the poly(lactic acid) of weight-average molecular weight 120000～210000 saturation steam percent thermal shrinkages 1～5%.
2, the preparation technology of poly lactic acid in use for spinning according to claim 1 is characterized in that: described thermo-stabilizer is wherein a kind of in methyl tin, barium stearate, Zinic stearas, Magnesium Stearate, the calcium stearate.
3, the preparation technology of poly lactic acid in use for spinning according to claim 1, it is characterized in that: described antioxidant is four [β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, β (3,5-di-t-butyl-4-hydroxybenzene) propionic acid octadecanol ester, Tyox B, triphenyl phosphite, three (nonylated phenyl) phosphorous acid ester, 2,5-di-tert-butyl hydroquinone, 4, wherein a kind of in 4 '-butyl-two (3-methyl-6-tertiary butyl) phenol.
4, the preparation technology of poly lactic acid in use for spinning according to claim 1, it is characterized in that: described heat modification agent is isocyanuric acid three-glycidyl ester, trihydroxyethyl isocyanuric ester, Tetra hydro Phthalic anhydride, glyoxal ethyline, phosphorous acid dihydroxyphenyl propane ester, vinyltriethoxysilane, divinyl triamino propyl-triethoxysilicane, 3, wherein a kind of in 3 '-diaminodiphenylsulfone(DDS), sec.-propyl three (dioctylphyrophosphoric acid ester) titanic acid ester.
5, the preparation technology of poly lactic acid in use for spinning according to claim 1 is characterized in that: described mineral acid is wherein a kind of in sulfuric acid, phosphoric acid, the hydrochloric acid.
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| CN102643418B (en) * | 2012-04-20 | 2014-05-14 | 北京化工大学 | Method for preparing polylactic acid from lactic acid under catalysis of titanium composite catalyst |
| CN106633017B (en) * | 2016-10-17 | 2019-03-29 | 杭州铭众生物科技有限公司 | A kind of preparation method of polydactyl acid |
| CN109679074B (en) * | 2018-11-30 | 2020-07-28 | 中粮集团有限公司 | Composite stabilizer for polylactic acid polymerization, and application and use method thereof |
| CN111909525A (en) * | 2020-08-07 | 2020-11-10 | 东莞市固泰有机硅有限公司 | High-temperature-resistant silicon rubber containing phenyl and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1557853A (en) * | 2004-02-05 | 2004-12-29 | 哈尔滨工业大学 | Process for direct preparation of poly-lactic acid from lactic acid by melt/solid phase polycondensation |
| CN1594393A (en) * | 2004-07-15 | 2005-03-16 | 合肥工业大学 | Method for preparing high molecular weight poly-L-lactic acid by melt polycondensation-solid phase polymerization |
| CN1616515A (en) * | 2004-10-18 | 2005-05-18 | 上海氯碱化工股份有限公司 | Process for preparing high molecular weight poly lactic acid by fusion polycondensation-solid phase polymerization |
| CN1718607A (en) * | 2004-07-07 | 2006-01-11 | 同济大学 | Solid state polymerization prepares the method for poly-lactic acid in high molecular weight |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1557853A (en) * | 2004-02-05 | 2004-12-29 | 哈尔滨工业大学 | Process for direct preparation of poly-lactic acid from lactic acid by melt/solid phase polycondensation |
| CN1718607A (en) * | 2004-07-07 | 2006-01-11 | 同济大学 | Solid state polymerization prepares the method for poly-lactic acid in high molecular weight |
| CN1594393A (en) * | 2004-07-15 | 2005-03-16 | 合肥工业大学 | Method for preparing high molecular weight poly-L-lactic acid by melt polycondensation-solid phase polymerization |
| CN1616515A (en) * | 2004-10-18 | 2005-05-18 | 上海氯碱化工股份有限公司 | Process for preparing high molecular weight poly lactic acid by fusion polycondensation-solid phase polymerization |
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