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CN106977509B - The multiple water law method for crystallising of thiamine hydrochloride - Google Patents

The multiple water law method for crystallising of thiamine hydrochloride Download PDF

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Publication number
CN106977509B
CN106977509B CN201710195515.5A CN201710195515A CN106977509B CN 106977509 B CN106977509 B CN 106977509B CN 201710195515 A CN201710195515 A CN 201710195515A CN 106977509 B CN106977509 B CN 106977509B
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filtrate
thiamine hydrochloride
filter residue
temperature
water
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CN106977509A (en
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李来成
陈英明
崔胜凯
严建斌
沈燕
王龙海
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JIANGSU BROTHER VITAMINS CO Ltd
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JIANGSU BROTHER VITAMINS CO Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D417/00Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00
    • C07D417/02Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00 containing two hetero rings
    • C07D417/04Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and sulfur atoms as the only ring hetero atoms, not provided for by group C07D415/00 containing two hetero rings directly linked by a ring-member-to-ring-member bond

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Plural Heterocyclic Compounds (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention discloses a kind of multiple water crystallization technique of thiamine hydrochloride, include the following steps: Temperature fall after thiamine hydrochloride crude product and purified water heating stirring to thiamine hydrochloride dissolution, cooled down again with ice water and keeps the temperature crystallization and filtration, filtrate I and filter residue I are obtained, filter residue I obtains thiamine hydrochloride with ethanol washing;Filtrate I is concentrated, stirs I Temperature fall of filtrate, then cooled down with ice water and keep the temperature crystallization and filtration, filter to get filtrate II and filter residue II, and filter residue II obtains thiamine hydrochloride with ethanol washing;Filtrate II is concentrated, stirs Temperature fall after filtrate I, then cooled down with ice water and keep the temperature crystallization and filtration, filter to get filtrate III and filter residue III, and filter residue III obtains thiamine hydrochloride with ethanol washing.The present invention replaces alcohol method to crystallize using the crystallization of multiple water law, improves the yield of thiamine hydrochloride;The natural deposited dry density of thiamine hydrochloride can also be promoted simultaneously from 0.20 to 0.56g/mL, dramatically improve the natural deposited dry density of thiamine hydrochloride.

Description

The multiple water law method for crystallising of thiamine hydrochloride
Technical field
The invention belongs to the method for crystallising of thiamine hydrochloride, are more particularly to a kind of side of the multiple water law crystallization of thiamine hydrochloride Method.
Background technique
Existing thiamine hydrochloride alcohol crystal need to consume a large amount of ethyl alcohol, higher cost;And the hydrochloric acid for passing through alcohol crystal Thiamines, natural deposited dry density is smaller, influences the quality of thiamine hydrochloride.
Summary of the invention
The object of the present invention is to provide one kind, cost is relatively low and the multiple water law of the higher thiamine hydrochloride of bulk density crystallizes Method.
According to an aspect of the invention, there is provided a kind of multiple water crystallization technique of thiamine hydrochloride, which is characterized in that packet Include following steps:
Temperature fall after thiamine hydrochloride crude product and purified water being stirred at a temperature of 60 DEG C~70 DEG C to thiamine hydrochloride dissolution 8 DEG C~12 DEG C are cooled to 25 DEG C~27 DEG C, then with ice water, 15min~25min crystallization and filtration is kept the temperature, obtains filtrate I and filter residue I, filter residue I obtains thiamine hydrochloride with ethanol washing;
Filtrate I is concentrated, is naturally cooling to 20 DEG C~30 after stirring I 15min of filtrate~25min at a temperature of 45 DEG C~55 DEG C DEG C, then be cooled to 8 DEG C~12 DEG C with ice water and keep the temperature 15min~25min crystallization and filtration, filter to get filtrate II and filter residue II, Filter residue II obtains thiamine hydrochloride with ethanol washing;
Be concentrated filtrate II, at a temperature of 45 DEG C~55 DEG C stir I 15min of filtrate~25min after be naturally cooling to 20 DEG C~ 30 DEG C, then be cooled to 8 DEG C~12 DEG C with ice water and keep the temperature 15min~25min crystallization and filtration, filter to get filtrate III and filter residue III, filter residue III obtains thiamine hydrochloride with ethanol washing.
A kind of multiple water crystallization technique of thiamine hydrochloride, includes the following steps:
Temperature fall after thiamine hydrochloride crude product and purified water being stirred at a temperature of 60 DEG C~70 DEG C to thiamine hydrochloride dissolution 10 DEG C are cooled to 25 DEG C, then with ice water, is filtered after keeping the temperature 20min, obtains filtrate I and filter residue I, filter residue I obtains salt with ethanol washing Allithiamine;
Filtrate I is concentrated, is naturally cooling to 25 DEG C after stirring I 20min of filtrate at 50 °C, then be cooled to 10 with ice water DEG C and keep the temperature 20min, filter to get filtrate II and filter residue II, and filter residue II obtains thiamine hydrochloride with ethanol washing;
Filtrate II is concentrated, is naturally cooling to 25 DEG C after stirring I 20min of filtrate at 50 °C, then be cooled to ice water 10 DEG C and 20min is kept the temperature, filter to get filtrate III and filter residue III, and filter residue III obtains thiamine hydrochloride with ethanol washing.
In some embodiments, the filtrate III is for producing as subcrystalline raw material again, comprising:
Filtrate III is reacted with ammonium nitrate, ammonium hydroxide, is cooled to 8 DEG C after reaction, resulting filter residue first is filtered in filtering Dry product I is dried to obtain after alcohol washing;
The dry product I is reacted with methanol, sour methanol, after reaction, slow cooling is cooled to 25 DEG C, then with ice water 15 DEG C, the raw material that resulting filter residue methanol washing and drying must be used to crystallize again is filtered in filtering.
In some embodiments, concentration filtrate I to solid-liquid mass ratio is 100:74~76.
In some embodiments, concentration filtrate II to solid-liquid mass ratio is 100:74~76.
It has the advantage that: the present invention replaces alcohol method to crystallize using the crystallization of multiple water law, the yield of thiamine hydrochloride is improved; Filter residue is made to the raw material recrystallized, 20% cost is reduced on raw material;It is crystallized by multiple water law, it can also be by salt The natural deposited dry density of allithiamine is promoted from 0.20 to 0.56g/mL, and the natural packing for dramatically improving thiamine hydrochloride is close Degree.
Specific embodiment
Embodiment 1
200g thiamine hydrochloride is added in three-necked flask, three-necked flask is put into 60 DEG C~70 DEG C of water by 152g purified water In bath, stirring is completely dissolved thiamine hydrochloride, closes the heater switch of water-bath, makes three-necked flask whole system with water-bath Cool down slowly together.When temperature drops to 25 DEG C or so, 10 DEG C are down to ice water, and keep the temperature 20min.Filter to get filtrate I and filter Slag I, filtrate I are stand-by, dried after the 30g ethanol washing of filter residue I weight be 72.43g thiamine hydrochloride, yield 36.22%, Quality analysis is qualified, and the bulk density of finished product is promoted to 0.5g/mL by the 0.2g/mL of raw material.
It is 100:76 that filtrate I, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, then is transferred to three mouthfuls In flask, in the water-bath of 50 DEG C of merging, 20min is stirred, the heater switch of water-bath is closed, makes it with water-bath Temperature fall. When temperature is reduced to 25 DEG C or so, 10 DEG C are cooled to ice water, keeps the temperature 20min.Filter to get filtrate II and filter residue II, filter residue II With dried after 20g ethanol washing weight be 42.5g thiamine hydrochloride, yield 21.25%, quality analysis is qualified, finished product Bulk density is promoted to 0.54g/mL by the 0.5g/mL of raw material.
It is 100:76 that filtrate II, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, is being transferred to three mouthfuls It in flask, is placed in 50 DEG C of water-bath, stirs 20min, close the heater switch of water-bath, make it with water-bath Temperature fall. When temperature drops to 25 DEG C or so, 10 DEG C are down to ice water, and keep the temperature 20min.Filter to get filtrate III and filter residue III, and filter residue III is used Thiamine hydrochloride of the weight for 20.84g is dried to obtain after 10g ethanol washing, yield 10.42%, quality analysis is qualified, the heap of finished product Product density is promoted to 0.56g/mL by the 0.54g/mL of raw material.
The joint yield of three step water crystallizations is 67.89%.
By filtrate III and ammonium nitrate, ammonium hydroxide reaction, after reaction, 8 DEG C is cooled to, filters resulting filter residue IV and use 30g It is dried after methanol washing, obtains 55.23g dry product I.
55.23g dry product and methanol, sour methanol are reacted, after reaction, when slow cooling is to 25 DEG C or so, then use ice Water is cooled to 15 DEG C.The dry product II for the 55.78g that resulting filter residue is washed and dried with 30g methanol is filtered, quality analysis is qualified.
Raw material of the dry product II as water crystallization, repeating the above steps carries out three step water crystallization methods again and crystallizes to it, The comprehensive utilization ratio of raw material is 95.8%.
Embodiment 2
200g thiamine hydrochloride is added in three-necked flask, three-necked flask is put into 60 DEG C~70 DEG C of water by 152g purified water In bath, stirring is completely dissolved thiamine hydrochloride, closes the heater switch of water-bath, makes three-necked flask whole system with water-bath Cool down slowly together.When temperature drops to 27 DEG C or so, 12 DEG C are down to ice water, and keep the temperature 25min.Filter to get filtrate I and filter Slag I, filtrate I are stand-by, dried after the 30g ethanol washing of filter residue I weight be 73.56g thiamine hydrochloride, yield 36.78%, Quality analysis is qualified, and the bulk density of finished product is promoted to 0.5g/mL by the 0.2g/mL of raw material.
It is 100:74 that filtrate I, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, then is transferred to three mouthfuls In flask, in the water-bath of 50 DEG C of merging, 15min is stirred, the heater switch of water-bath is closed, makes it with water-bath Temperature fall. When temperature is reduced to 25 DEG C or so, 8 DEG C are cooled to ice water, keeps the temperature 15min.Filter to get filtrate II and filter residue II, filter residue II With dried after 20g ethanol washing weight be 42.8g thiamine hydrochloride, yield 21.4%, quality analysis is qualified, the heap of finished product Product density is promoted to 0.52g/mL by the 0.5g/mL of raw material.
It is 100:78 that filtrate II, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, is being transferred to three mouthfuls It in flask, is placed in 50 DEG C of water-bath, stirs 25min, close the heater switch of water-bath, make it with water-bath Temperature fall. When temperature drops to 30 DEG C or so, 12 DEG C are down to ice water, and keep the temperature 25min.Filter to get filtrate III and filter residue III, and filter residue III is used Thiamine hydrochloride of the weight for 22.04g is dried to obtain after 10g ethanol washing, yield 11.02%, quality analysis is qualified, the heap of finished product Product density is promoted to 0.56g/mL by the 0.52g/mL of raw material.
The joint yield of three step water crystallizations is 69.2%.
By filtrate III and ammonium nitrate, ammonium hydroxide reaction, after reaction, 8 DEG C is cooled to, filters resulting filter residue IV and use 30g It is dried after methanol washing, obtains 56.04g dry product I.
56.04g dry product and methanol, sour methanol are reacted, after reaction, when slow cooling is to 25 DEG C or so, then use ice Water is cooled to 15 DEG C.The dry product II for the 55.18g that resulting filter residue is washed and dried with 30g methanol is filtered, quality analysis is qualified.
Raw material of the dry product II as water crystallization, repeating the above steps carries out three step water crystallization methods again and crystallizes to it, The comprehensive utilization ratio of raw material is 96.5%.
Embodiment 1
200g thiamine hydrochloride is added in three-necked flask, three-necked flask is put into 60 DEG C~70 DEG C of water by 152g purified water In bath, stirring is completely dissolved thiamine hydrochloride, closes the heater switch of water-bath, makes three-necked flask whole system with water-bath Cool down slowly together.When temperature drops to 27 DEG C or so, 12 DEG C are down to ice water, and keep the temperature 25min.Filter to get filtrate I and filter Slag I, filtrate I are stand-by, dried after the 30g ethanol washing of filter residue I weight be 72.02g thiamine hydrochloride, yield 36.01%, Quality analysis is qualified, and the bulk density of finished product is promoted to 0.5g/mL by the 0.2g/mL of raw material.
It is 100:74 that filtrate I, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, then is transferred to three mouthfuls In flask, in the water-bath of 45 DEG C of merging, 15min is stirred, the heater switch of water-bath is closed, makes it with water-bath Temperature fall. When temperature is reduced to 20 DEG C or so, 8 DEG C are cooled to ice water, keeps the temperature 15min.Filter to get filtrate II and filter residue II, filter residue II With dried after 20g ethanol washing weight be 43.6g thiamine hydrochloride, yield 21.8%, quality analysis is qualified, the heap of finished product Product density is promoted to 0.53g/mL by the 0.5g/mL of raw material.
It is 100:78 that filtrate II, which is concentrated into solid-liquid mass ratio by Rotary Evaporators at 50 DEG C, is being transferred to three mouthfuls It in flask, is placed in 45 DEG C of water-bath, stirs 15min, close the heater switch of water-bath, make it with water-bath Temperature fall. When temperature drops to 25 DEG C or so, 11 DEG C are down to ice water, and keep the temperature 20min.Filter to get filtrate III and filter residue III, and filter residue III is used Thiamine hydrochloride of the weight for 21.24g is dried to obtain after 10g ethanol washing, yield 10.62%, quality analysis is qualified, the heap of finished product Product density is promoted to 0.56g/mL by the 0.53g/mL of raw material.
The joint yield of three step water crystallizations is 68.43%.
By filtrate III and ammonium nitrate, ammonium hydroxide reaction, after reaction, 8 DEG C is cooled to, filters resulting filter residue IV and use 30g It is dried after methanol washing, obtains 55.43g dry product I.
55.43g dry product and methanol, sour methanol are reacted, after reaction, when slow cooling is to 25 DEG C or so, then use ice Water is cooled to 15 DEG C.The dry product II for the 56.87g that resulting filter residue is washed and dried with 30g methanol is filtered, quality analysis is qualified.
Raw material of the dry product II as water crystallization, repeating the above steps carries out three step water crystallization methods again and crystallizes to it, The comprehensive utilization ratio of raw material is 96.7%.
Above-described is only some embodiments of the present invention.For those of ordinary skill in the art, it is not taking off Under the premise of from the invention design, various modifications and improvements can be made, and these are all within the scope of protection of the present invention.

Claims (5)

1. the multiple water crystallization technique of thiamine hydrochloride, which comprises the steps of:
25 are naturally cooling to after thiamine hydrochloride crude product and purified water being stirred at a temperature of 60 DEG C~70 DEG C to thiamine hydrochloride dissolution DEG C~27 DEG C, then 8 DEG C~12 DEG C are cooled to ice water, 15mi n~25mi n crystallization and filtration is kept the temperature, filtrate I and filter residue I are obtained, Filter residue I obtains thiamine hydrochloride with ethanol washing;
Filtrate I is concentrated, is naturally cooling to 20 DEG C~30 after stirring I 15mi n~25mi n of filtrate at a temperature of 45 DEG C~55 DEG C DEG C, then be cooled to 8 DEG C~12 DEG C with ice water and keep the temperature 15mi n~25mi n crystallization and filtration, filter to get filtrate II and filter residue II, filter residue II obtains thiamine hydrochloride with ethanol washing;
Filtrate II is concentrated, is naturally cooling to 20 DEG C~30 after stirring I 15mi n~25mi n of filtrate at a temperature of 45 DEG C~55 DEG C DEG C, then be cooled to 8 DEG C~12 DEG C with ice water and keep the temperature 15mi n~25mi n crystallization and filtration, filter to get filtrate III and filter residue III, filter residue III obtains thiamine hydrochloride with ethanol washing.
2. the multiple water crystallization technique of thiamine hydrochloride according to claim 1, which comprises the steps of:
25 are naturally cooling to after thiamine hydrochloride crude product and purified water being stirred at a temperature of 60 DEG C~70 DEG C to thiamine hydrochloride dissolution DEG C, then 10 DEG C are cooled to ice water, it is filtered after keeping the temperature 20mi n, obtains filtrate I and filter residue I, filter residue I obtains hydrochloric acid sulphur with ethanol washing Amine;
Filtrate I is concentrated, is naturally cooling to 25 DEG C after stirring I 20mi n of filtrate at 50 °C, then be cooled to 10 DEG C with ice water And 20mi n is kept the temperature, filter to get filtrate II and filter residue II, and filter residue II obtains thiamine hydrochloride with ethanol washing;
Filtrate II is concentrated, is naturally cooling to 25 DEG C after stirring I 20mi n of filtrate at 50 °C, then be cooled to 10 DEG C with ice water And 20mi n is kept the temperature, filter to get filtrate III and filter residue III, and filter residue III obtains thiamine hydrochloride with ethanol washing.
3. the multiple water crystallization technique of thiamine hydrochloride according to claim 1, which is characterized in that the filtrate III is for making It is taken as subcrystalline raw material again, comprising:
Filtrate III is reacted with ammonium nitrate, ammonium hydroxide, is cooled to 8 DEG C after reaction, filtering is filtered resulting filter residue and washed with methanol Dry product I is dried to obtain after washing;
The dry product I is reacted with methanol, sour methanol, after reaction, slow cooling is cooled to 15 to 25 DEG C, then with ice water DEG C, the raw material that resulting filter residue methanol washing and drying must be used to crystallize again is filtered in filtering.
4. the multiple water crystallization technique of thiamine hydrochloride according to claim 1, which is characterized in that concentration filtrate I to solid-liquid Mass ratio is 100:74~78.
5. the multiple water crystallization technique of thiamine hydrochloride according to claim 1, which is characterized in that concentration filtrate II to solid-liquid Mass ratio is 100:74~78.
CN201710195515.5A 2017-03-29 2017-03-29 The multiple water law method for crystallising of thiamine hydrochloride Active CN106977509B (en)

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Publication number Priority date Publication date Assignee Title
CN111087393B (en) * 2019-12-30 2021-11-23 江苏兄弟维生素有限公司 Thiamine hydrochloride, drying method and application thereof, and vitamin B1

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102952126A (en) * 2012-12-03 2013-03-06 华中药业股份有限公司 Novel method for synthesizing vitamin B1 hydrochloride
CN104817551A (en) * 2015-05-07 2015-08-05 常州大学 New method of preparing vitamin B1 hydrochloride
CN105315272A (en) * 2015-10-19 2016-02-10 天津大学 Method for preparing thiamine hydrochloride crystal product

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102952126A (en) * 2012-12-03 2013-03-06 华中药业股份有限公司 Novel method for synthesizing vitamin B1 hydrochloride
CN104817551A (en) * 2015-05-07 2015-08-05 常州大学 New method of preparing vitamin B1 hydrochloride
CN105315272A (en) * 2015-10-19 2016-02-10 天津大学 Method for preparing thiamine hydrochloride crystal product

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