CN108689833A - A kind of high-pure lactic acid preparation method of stabilization - Google Patents

A kind of high-pure lactic acid preparation method of stabilization Download PDF

Info

Publication number
CN108689833A
CN108689833A CN201810555080.5A CN201810555080A CN108689833A CN 108689833 A CN108689833 A CN 108689833A CN 201810555080 A CN201810555080 A CN 201810555080A CN 108689833 A CN108689833 A CN 108689833A
Authority
CN
China
Prior art keywords
lactic acid
purity
added
diluent
acid preparation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201810555080.5A
Other languages
Chinese (zh)
Other versions
CN108689833B (en
Inventor
丁玉娟
曾飞
邵世勇
夏源
牛春霞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANHUI HEAL STAR PHARMACEUTICAL CO LTD
Original Assignee
ANHUI HEAL STAR PHARMACEUTICAL CO LTD
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ANHUI HEAL STAR PHARMACEUTICAL CO LTD filed Critical ANHUI HEAL STAR PHARMACEUTICAL CO LTD
Priority to CN201810555080.5A priority Critical patent/CN108689833B/en
Publication of CN108689833A publication Critical patent/CN108689833A/en
Application granted granted Critical
Publication of CN108689833B publication Critical patent/CN108689833B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/50Use of additives, e.g. for stabilisation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of high-pure lactic acid preparation methods of stabilization, specifically include following steps:(1)It feeds intake:Lactic acid is added in reaction kettle, is stirred evenly, diluent and depolymerizing agent, heating stirring are then added;(2)Vacuum distillation:Collect the step(1)In fraction;(3)It preserves:By the step(2)The fraction of collection imports in the collecting tank for filling purified water, is then discharged in hermetically sealed can, seals room temperature preservation.The technical problem to be solved by the present invention is to lactic acid can occur self-polymerization in purification process, the problem for causing its purity and stability not high, the present invention adds diluent and depolymerizing agent in commercially available lactic acid, carry out vacuum distillation purifying, the high-pure lactic acid distilled out is diluted storage immediately, the high-pure lactic acid stablized.

Description

A kind of high-pure lactic acid preparation method of stabilization
Technical field
The present invention relates to a kind of lactic acid preparation method more particularly to a kind of high-pure lactic acid preparation methods of stabilization.
Background technology
Lactic acid is widely used in the important organic acid of chemical industry, light industry, food and medicine.In recent years, lactic acid is in medicine and doctor Application constantly expands in terms of medicine intermediate.It has also been found that the autopolymer of lactic acid and its there is life with the copolymers of other compounds Object degradability, application value are increasingly that people pay attention to;For chemical industry, the lactic acid of field of light industry, purity also need not be too high;And it uses In the lactic acid of food and medicine, just there are very high requirement, therefore input great effort research both at home and abroad to its purity and stability The separation and purification of lactic acid, but so far, the refined purification of lactic acid does not all solve very well, is primarily due to lactic acid and is purifying Self-polymerization can occur for process, and this polymer can be good at coexisting with lactic acid, and which results in commercially available lactic acid, no Pipe is that food-grade or pharmaceutical grade all contain 10%-15% lactic acid polymers.
Invention content
The object of the present invention is to provide a kind of high-pure lactic acid preparation methods of stabilization, in order to solve lactic acid in purification process Self-polymerization can occur, the problem for causing its purity and stability not high.
To achieve the goals above, present invention employs following technical solutions:
The present invention provides a kind of high-pure lactic acid preparation method of stabilization, specifically includes following steps:
(1) it feeds intake:Lactic acid is added in reaction kettle, is stirred evenly, diluent and depolymerizing agent are then added, heating is stirred It mixes;
(2) it is evaporated under reduced pressure:Collect the fraction in the step (1);
(3) it preserves:The fraction that the step (2) is collected is imported in the collecting tank for filling purified water, is then discharged to close In sealed cans, room temperature preservation is sealed;
The lactic acid of pharmaceutical grade preserves:The fraction that the step (2) is collected is imported in the collecting tank for filling water for injection, so After be discharged in hermetically sealed can, seal room temperature preservation, pharmaceutical grade lactic acid requires purity and stability high, and water for injection is selected to replace Purified water can improve the purity and stability of lactic acid, ensure that drug effect.
Preferably, diluent is high boiling solvent in step (1), and the high boiling solvent is preferably glycerine, poly- second two Alcohol, one kind in two polyglycerols or mutual mixture.
Preferably, depolymerizing agent is organic amine compound or quaternary ammonium salt in step (1), and the organic amine compound is preferred For tetrabutylammonium bromide, diisopropylethylamine, N, one kind in N- dimethyl butylamines or mutual mixture.
Preferably, lactic acid is added in reaction kettle by step (1), is stirred evenly, is then added diluent and depolymerizing agent, It is warming up to 140~150 DEG C.
Preferably, the condition that fraction is collected in step (2) is 110~120 DEG C of temperature, and pressure is -0.2~-0.15Mpa.
Preferably, in step (3) when lactic acid concn reaches 10%~15% in collecting tank, stop collecting.
Preferably, the addition quality of diluent is 2~3 times of lactic acid inventory in step (1).
Preferably, the addition quality of depolymerizing agent is 0.02~0.05 times of lactic acid inventory in step (1).
Advantageous effect of the present invention:The technical problem to be solved by the present invention is to lactic acid can occur self-polymerization in purification process, The problem for causing its purity and stability not high, the present invention add diluent and depolymerizing agent in commercially available lactic acid, carry out decompression steaming Purifying is evaporated, the high-pure lactic acid distilled out is diluted storage immediately.Realize following purpose:1, it distills in substrate and increases boiling point Solvent dilutes and depolymerizing agent is added, and avoids lactic acid in distillation process from polymerizeing rapidly at high temperature, lactic acid is under a high concentration condition Easily polymerization, it is therefore desirable to add dilution dilution agent, additionally incorporate depolymerizing agent and prevent its polymerization;2, by the lactic acid distilled out immediately with pure Change water, which is diluted under the concentration of 10%-15%, to be stored, and lactic acid is stablized at this concentration, substantially will not during storage It polymerize.
Description of the drawings
Fig. 1 is commercially available lactic acid purity chromatogram.
Fig. 2 is the purity chromatogram after commercially available lactic acid purification.
Fig. 3 is the purity chromatogram that diluent is added in commercially available lactic acid.
Fig. 4 is the purity chromatogram that depolymerizing agent is added in commercially available lactic acid.
Fig. 5 is the purity chromatogram that diluent and depolymerizing agent is added in commercially available lactic acid.
Fig. 6 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 5% concentration immediately 1 month Figure.
Fig. 7 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 5% concentration immediately 2 months Figure.
Fig. 8 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 5% concentration immediately 3 months Figure.
Fig. 9 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 10% concentration immediately 1 month Figure.
Figure 10 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 10% concentration immediately 2 months Figure.
Figure 11 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 10% concentration immediately 3 months Figure.
Figure 12 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 15% concentration immediately 1 month Figure.
Figure 13 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 15% concentration immediately 2 months Figure.
Figure 14 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 15% concentration immediately 3 months Figure.
Figure 15 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 20% concentration immediately 1 month Figure.
Figure 16 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 20% concentration immediately 2 months Figure.
Figure 17 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 20% concentration immediately 3 months Figure.
Figure 18 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 25% concentration immediately 1 month Figure.
Figure 19 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 25% concentration immediately 2 months Figure.
Figure 20 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 25% concentration immediately 3 months Figure.
Figure 21 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 30% concentration immediately 1 month Figure.
Figure 22 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 30% concentration immediately 2 months Figure.
Figure 23 is the purity chromatography stored under the lactic acid distilled out is diluted with purified water to 30% concentration immediately 3 months Figure.
Figure 24 is commercially available lactic acid, without dilution agent and depolymerizing agent, only adds diluent, only adds depolymerizing agent and diluent reconciliation The Contrast on effect purity chromatogram that poly- agent two adds simultaneously.
Specific implementation mode
In order to deepen the understanding of the present invention, present invention work is further retouched in detail below in conjunction with drawings and examples It states, the present embodiment is only used for explaining the present invention, does not constitute and limits to protection scope of the present invention.
Embodiment 1
(at pharmaceutcal corporation, Ltd, lot number 161204, purity 63.5%, commercially available lactic acid is or not Henan day for the commercially available lactic acid of 50Kg Pipe is that food-grade or pharmaceutical grade all contain 10%-15% lactic acid polymers, and after storing a period of time, polymer can increase More, the commercially available lactic acid purity bought in the present embodiment and following embodiment is 63.5%), to do purity chromatogram, obtain chromatography Fig. 1, table 1 corresponding with chromatogram 1 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.260 2009274 270110 63.517 6865 1.309 0.206 --
2 9.804 937772 70515 29.645 12126 1.195 0.356 19.738
3 12.003 216303 4883 6.838 1664 1.128 1.177 2.869
It amounts to 3163348 345508 100.000
Embodiment 2
The commercially available lactic acid of 50Kg (Henan day is at pharmaceutcal corporation, Ltd, lot number 161204, purity 63.5%), to 50Kg market milks Acid is refined, and the 2 corresponding table 2 of purity chromatogram of lactic acid is as follows after refining:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.250 2302995 308394 71.222 6735 1.318 0.207 --
2 4.703 1800 239 0.056 9125 1.500 0.197 2.238
3 9.809 928758 69894 28.723 12151 1.194 0.356 18.472
It amounts to 3233552 378526 100.000
Embodiment 3
The commercially available lactic acid of 50Kg (Henan day is at pharmaceutcal corporation, Ltd, lot number 161204, purity 63.5%), it is anti-to be added to 300L It answers in kettle, stirs evenly, 100Kg glycerine is added, be warming up to 140 DEG C, stir, vacuum distillation collects 110 DEG C, -0.2Mpa's Fraction imports the fraction of collection in the collecting tank for filling 300Kg purified waters, when lactic acid concn reaches 12% in collecting tank, Stop collecting, blowing seals room temperature preservation.
The 3 corresponding table 3 of purity chromatogram that diluent is added in lactic acid is as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.211 2644396 359904 79.115 6834 1.319 0.204 --
2 9.441 698089 55637 20.885 12585 1.157 0.337 19.357
It amounts to 3342485 415541 100.000
Embodiment 4
The commercially available lactic acid of 50Kg (Henan day is at pharmaceutcal corporation, Ltd, lot number 161204, purity 63.5%), it is anti-to be added to 300L It answers in kettle, stirs evenly, 1.32Kg tetrabutylammonium bromide is added, be warming up to 140 DEG C, stir, vacuum distillation collects 110 DEG C ,- The fraction of collection is imported in the collecting tank for filling 300Kg purified waters, waits for that lactic acid concn reaches in collecting tank by the fraction of 0.2Mpa When 12%, stop collecting, blowing seals room temperature preservation.
The 4 corresponding table 4 of purity chromatogram that depolymerizing agent is added in lactic acid is as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.210 2798827 379728 86.686 6786 1.327 0.204 --
2 4.693 1322 205 0.041 9418 1.478 0.193 2.425
3 9.446 428529 26614 13.273 10438 0.966 0.370 16.876
It amounts to 3228679 406546 100.000
Embodiment 5
The commercially available lactic acid of 50Kg (Henan day is at pharmaceutcal corporation, Ltd, lot number 161204, purity 63.5%), it is anti-to be added to 300L It answers in kettle, stirs evenly, 100Kg glycerine and 1.32Kg tetrabutylammonium bromide is added, be warming up to 140 DEG C, stirring, decompression is steamed It evaporates, collects 110 DEG C, the fraction of collection is imported in the collecting tank for filling 300Kg purified waters, waits for collecting tank by the fraction of -0.2Mpa When middle lactic acid concn reaches 12%, stop collecting, blowing seals room temperature preservation.
Diluent is added in lactic acid and the 5 corresponding table 5 of purity chromatogram of depolymerizing agent is as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.246 3769165 477651 98.606 6081 1.378 0.218 --
2 4.767 35149 6102 0.920 13722 1.001 0.163 2.741
3 9.803 18151 1395 0.475 12523 1.186 0.350 19.625
It amounts to 3822466 485149 100.000
Commercially available lactic acid, without dilution agent and the depolymerizing agent bought, only plus diluent, only plus depolymerizing agent and diluent reconciliation Contrast on effect spectrogram such as Figure 24, Figure 24 that poly- agent two adds simultaneously are followed successively by commercially available lactic acid, without dilution agent reconciliation from top to bottom Poly- agent, the spectrum curve for adding diluent, depolymerizing agent and diluent and depolymerizing agent two only being added to add simultaneously, bind profile Figure 24, It is as follows that spectrogram 1-5 and table 1-5 can obtain table 6:
Table 6 plus diluent and depolymerizing agent and the Contrast on effect being not added with
Note:"+", which represents, to be added, and "-" representative is not added with
As can be seen from Table 6, when diluent only adds one of which substance with depolymerizing agent, purity ratio is not added with any type object Purity is high when matter, and when the two is added simultaneously, purity can reach 98.60%, it will thus be seen that adding diluent in commercially available lactic acid And depolymerizing agent, vacuum distillation purifying is carried out, the high-pure lactic acid distilled out is diluted to the lactic acid purity that storage obtains immediately It is very high, it disclosure satisfy that application of the lactic acid in food and medicine.
The lactic acid distilled out is diluted immediately with purified water under the concentration of 5%-30% below and stores different time The corresponding peak table of purity chromatogram it is as follows:
1, the lactic acid distilled out stores 1 month purity chromatogram 6 under being diluted immediately to 5% concentration with purified water is right The peak table 7 answered is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.193 2953422 434805 98.076 7340 1.363 0.196 --
2 9.461 57947 4790 1.924 13199 1.122 0.329 20.061
It amounts to 3011369 439595 100.000
2, the lactic acid distilled out stores 2 months purity chromatogram 7 under being diluted immediately to 5% concentration with purified water is right The peak table 8 answered is as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.113 2785448 344051 97.301 5632 1.515 0.219 --
2 4.647 10971 2019 0.383 13554 1.078 0.160 2.818
3 9.122 66304 5176 2.316 11395 1.187 0.342 17.850
It amounts to 2862723 351246 100.000
3, the lactic acid distilled out stores 3 months purity chromatogram 8 under being diluted immediately to 5% concentration with purified water is right The peak table 9 answered is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.134 2994108 458764 96.939 7685 1.379 0.189 --
2 8.875 94534 8421 3.061 13215 1.136 0.309 19.059
It amounts to 3088642 467186 100.000
4, the lactic acid distilled out stores 1 month purity chromatogram 9 under being diluted immediately to 10% concentration with purified water Corresponding peak table 10 is as follows:
PDA Ch1 20gnm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.131 1631444 238707 99.053 6909 1.312 0.199 --
2 8.922 15599 1325 0.947 12125 1.075 0.324 18.324
It amounts to 1647042 240032 100.000
5, the lactic acid distilled out stores 2 months purity chromatograms 10 under being diluted immediately to 10% concentration with purified water Corresponding peak table 11 is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.192 3298328 482038 98.870 7248 1.382 0.197 --
2 9.465 37685 3124 1.130 13251 1.135 0.329 20.057
It amounts to 3336014 485162 100.000
6, the lactic acid distilled out stores 3 months purity chromatograms 11 under being diluted immediately to 10% concentration with purified water Corresponding peak table 12 is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.132 1567441 229407 98.300 6952 1.310 0.198 --
2 8.905 27105 2300 1.700 12120 1.142 0.324 18.296
It amounts to 1594547 231707 100.000
7, the lactic acid distilled out stores 1 month purity chromatogram 12 under being diluted immediately to 15% concentration with purified water Corresponding peak table 13 is as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.115 2881438 350514 98.336 5493 1.531 0.222 --
2 4.643 7423 980 0.253 10700 2.307 0.180 2.628
3 9.152 41332 3204 1.411 11279 1.192 0.345 17.202
It amounts to 2930192 354697 100.000
8, the lactic acid distilled out stores 2 months purity chromatograms 13 under being diluted immediately to 15% concentration with purified water Corresponding peak table 14 is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.131 3175954 485439 98.769 7524 1.391 0.191 --
2 8.828 39587 3572 1.231 13442 1.123 0.305 18.974
It amounts to 3215542 489011 100.000
9, the lactic acid distilled out stores 3 months purity chromatograms 14 under being diluted immediately to 15% concentration with purified water Corresponding peak table 15 is as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.141 3108911 474479 97.938 7500 1.382 0.191 --
2 8.869 65455 5827 2.062 13281 1.133 0.308 18.946
It amounts to 3174366 480306 100.000
10, the lactic acid distilled out stores 1 month purity chromatogram under being diluted immediately to 20% concentration with purified water 15 corresponding peak tables 16 are as follows:
PDA Ch1 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.140 1537255 225899 97.371 7110 1.310 0.196 --
2 8.905 41498 3509 2.629 11997 1.121 0.325 18.272
It amounts to 1578752 229408 100.000
11, the lactic acid distilled out stores 2 months purity chromatograms under being diluted immediately to 20% concentration with purified water 16 corresponding peak tables 17 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.123 3272913 451017 97.102 6684 1.392 0.202 --
2 4.639 15072 2503 0.447 11418 1.064 0.174 2.748
3 9.236 83609 6706 2.451 12520 1.192 0.330 18.249
It amounts to 3370594 460227 100.000
12, the lactic acid distilled out stores 3 months purity chromatograms under being diluted immediately to 20% concentration with purified water 17 corresponding peak tables 18 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.126 3051056 422826 95.687 6748 1.383 0.201 --
2 4.639 7712 1252 0.242 10824 1.091 0.178 2.706
3 9.250 129815 10580 4.071 12583 1.192 0.330 18.145
It amounts to 3188583 434657 100.000
13, the lactic acid distilled out stores 1 month purity chromatogram under being diluted immediately to 25% concentration with purified water 18 corresponding peak tables 19 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.125 2947321 408629 96.279 6755 1.379 0.201 --
2 4.640 11817 1903 0.386 10728 1.065 0.179 2.711
3 9.254 102094 8266 3.335 12583 1.192 0.330 18.123
It amounts to 3061232 418799 100.000
14, the lactic acid distilled out stores 2 months purity chromatograms under being diluted immediately to 25% concentration with purified water 19 corresponding peak tables 20 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.125 2708822 375997 94.862 6771 1.370 0.201 --
2 4.635 6580 1074 0.230 10759 1.084 0.179 2.686
3 9.234 140137 11381 4.908 12514 1.196 0.330 18.075
It amounts to 2855539 388452 100.000
15, the lactic acid distilled out stores 3 months purity chromatograms under being diluted immediately to 25% concentration with purified water 20 corresponding peak tables 21 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.122 3059748 422184 94.274 6705 1.387 0.201 --
2 4.639 9146 1485 0.282 10856 1.062 0.178 2.727
3 9.289 176696 14222 5.444 12462 1.199 0.333 18.199
It amounts to 3245589 437891 100.000
16, the lactic acid distilled out stores 1 month purity chromatogram under being diluted immediately to 30% concentration with purified water 21 corresponding peak tables 22 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.124 3052086 421254 96.215 6699 1.383 0.202 --
2 4.637 8969 1459 0.283 10941 1.087 0.177 2.705
3 9.236 111084 9031 3.502 12528 1.192 0.330 18.128
It amounts to 3172138 431744 100.000
17, the lactic acid distilled out stores 2 months purity chromatograms under being diluted immediately to 30% concentration with purified water 22 corresponding peak tables 23 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.130 2696144 374192 94.199 6806 1.373 0.200 --
2 4.641 5810 948 0.203 10836 1.101 0.178 2.695
3 9.246 160214 13031 5.598 12584 1.196 0.330 18.133
It amounts to 2862168 388171 100.000
18, the lactic acid distilled out stores 3 months purity chromatograms under being diluted immediately to 30% concentration with purified water 23 corresponding peak tables 24 are as follows:
Detector A 209nm
Peak number Retention time Area Highly Area % Theoretical cam curve Tailing factor USP peak width Separating degree (USP)
1 4.122 2991473 414077 93.995 6745 1.384 0.201 --
2 4.638 6590 1068 0.207 10743 1.083 0.179 2.718
3 9.274 184520 14896 5.798 12492 1.200 0.332 18.151
It amounts to 3182583 430041 100.000
It can be obtained such as the following table 25 by peak table 7-24 and spectrogram 6-23:
The stability contrast of the lactic acid of 25 various concentration of table
As seen from the above table, the lactic acid storage of a concentration of 10%-15% is stablized, and will not be gathered substantially during storage It closes.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto, Any one skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.

Claims (8)

1. a kind of high-pure lactic acid preparation method of stabilization, which is characterized in that specifically include following steps:
(1)It feeds intake:Lactic acid is added in reaction kettle, is stirred evenly, diluent and depolymerizing agent, heating stirring are then added;
(2)Vacuum distillation:Collect the step(1)In fraction;
(3)It preserves:By the step(2)The fraction of collection imports in the collecting tank for filling purified water, is then discharged to hermetically sealed can In, seal room temperature preservation.
2. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(1) Middle diluent be high boiling solvent, the high boiling solvent be preferably glycerine, polyethylene glycol, one kind in two polyglycerols or Mutual mixture.
3. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(1) Middle depolymerizing agent is organic amine compound or quaternary ammonium salt, and the organic amine compound is preferably tetrabutylammonium bromide, diisopropyl Base ethamine, N, one kind in N- dimethyl butylamines or mutual mixture.
4. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(1) Lactic acid is added in reaction kettle, is stirred evenly, diluent and depolymerizing agent are then added, is warming up to 140~150 DEG C.
5. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(2) The middle condition for collecting fraction is 110~120 DEG C of temperature, and pressure is -0.2~-0.15Mpa.
6. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(3) In when lactic acid concn reaches 10%~15% in collecting tank, stop collect.
7. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(1) The addition quality of middle diluent is 2~3 times of lactic acid inventory.
8. a kind of high-pure lactic acid preparation method of stabilization according to claim 1, it is characterised in that:The step(1) The addition quality of middle depolymerizing agent is 0.02~0.05 times of lactic acid inventory.
CN201810555080.5A 2018-06-01 2018-06-01 Stable high-purity lactic acid preparation method Active CN108689833B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810555080.5A CN108689833B (en) 2018-06-01 2018-06-01 Stable high-purity lactic acid preparation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810555080.5A CN108689833B (en) 2018-06-01 2018-06-01 Stable high-purity lactic acid preparation method

Publications (2)

Publication Number Publication Date
CN108689833A true CN108689833A (en) 2018-10-23
CN108689833B CN108689833B (en) 2021-03-16

Family

ID=63848519

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810555080.5A Active CN108689833B (en) 2018-06-01 2018-06-01 Stable high-purity lactic acid preparation method

Country Status (1)

Country Link
CN (1) CN108689833B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0986532A1 (en) * 1997-06-06 2000-03-22 Brussels Biotech Method for purifying lactic acid
CN1287113A (en) * 1999-06-28 2001-03-14 罗姆和哈斯公司 Process for producing (methyl) propenoic acid
CN101495440A (en) * 2006-08-02 2009-07-29 株式会社吴羽 Method for purifying hydroxycarboxylic acid, method for producing cyclic ester, and method for producing polyhydroxycarboxylic acid
CN107098808A (en) * 2017-05-05 2017-08-29 湖北壮美生物科技有限公司 The preparation method and process units of a kind of high-purity, high content normal temperature not crystalline lactic acid product

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0986532A1 (en) * 1997-06-06 2000-03-22 Brussels Biotech Method for purifying lactic acid
CN1287113A (en) * 1999-06-28 2001-03-14 罗姆和哈斯公司 Process for producing (methyl) propenoic acid
CN101495440A (en) * 2006-08-02 2009-07-29 株式会社吴羽 Method for purifying hydroxycarboxylic acid, method for producing cyclic ester, and method for producing polyhydroxycarboxylic acid
CN107098808A (en) * 2017-05-05 2017-08-29 湖北壮美生物科技有限公司 The preparation method and process units of a kind of high-purity, high content normal temperature not crystalline lactic acid product

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李晓: "《药品生产企业国际通用管理标准 GMP/ISO14001认证与文件编制标准》", 31 July 2002, 光明日报出版社 *

Also Published As

Publication number Publication date
CN108689833B (en) 2021-03-16

Similar Documents

Publication Publication Date Title
CN100422178C (en) Process for producing imide compound
Absalan et al. Extraction and high performance liquid chromatographic determination of 3-indole butyric acid in pea plants by using imidazolium-based ionic liquids as extractant
CN103012252B (en) Method for recovering pyridine from pyridine hydrochloride water solution
CN108251462B (en) Method for recovering and treating caproic acid in anaerobic fermentation liquid
CN112514898A (en) Method for preparing 2- (4-chlorophenoxy) -1-propanol
CN106674244A (en) Preparation method of cineole
CN108689833A (en) A kind of high-pure lactic acid preparation method of stabilization
CN102988285A (en) Docetaxel injection composition and preparation method thereof
CN106831358A (en) A kind of preparation method of dipropylene glycol
CN100334056C (en) Production of unsaturated ketone
CN111454129B (en) Preparation method of high-purity phenoxyethanol
CN103025692A (en) Method for preparing chlorohydrins composition and method for preparing epichlorohydrin using chlorohydrins composition prepared thereby
CN106187678B (en) The preparation method of one kind chloro- 1,2- propylene glycol of (R) -3-
CN108383695A (en) The preparation method and applications of eugenol and the eugenol being prepared
WO2019034149A1 (en) Catalyst for preparing propylene glycol phenyl ether and method for synthesizing propylene glycol phenyl ether
CN110656008B (en) Method for reducing content of urea and ethyl carbamate in yellow wine brewing process
CN107827876A (en) A kind of preparation method of voriconazole raceme
CN107125432A (en) A kind of process of Yupingfeng dregs of a decoction fermentation
CN104725336A (en) Method for preparing 1,2-limonene epoxide at room temperature
CN105385536A (en) Method for preparing blending liquor containing various flavor components through liquid fermentation
CN107164413A (en) The purposes of Yupingfeng dregs of a decoction tunning
CN108440284A (en) A kind of synthetic method of organic synthesis intermediate ethyl pyruvate
CN104894169B (en) A kind of preparation method of (S) -1,1,1- Trifluoroisoproanol
CN104490766B (en) Allicin solution and its production method
CN110975901B (en) Catalyst and method for preparing geraniol by hydrogenating citral by using same

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant