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CN201823337U - Concentrating and crystallizing equipment for 5-hydroxyl tryptophan - Google Patents

Concentrating and crystallizing equipment for 5-hydroxyl tryptophan Download PDF

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Publication number
CN201823337U
CN201823337U CN2010205282942U CN201020528294U CN201823337U CN 201823337 U CN201823337 U CN 201823337U CN 2010205282942 U CN2010205282942 U CN 2010205282942U CN 201020528294 U CN201020528294 U CN 201020528294U CN 201823337 U CN201823337 U CN 201823337U
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concentration
tank
membrane
hydroxytryptophan
pipeline
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Expired - Fee Related
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CN2010205282942U
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郑志忠
蒋荔馨
陈义
甘全明
林志华
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Xiamen Top Health Biological Engineering Co., Ltd.
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Yingjie Warner (xiamen) Biological Engineering Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract

本实用新型公开了一种5-羟基色氨酸的浓缩结晶设备,包括通过管道依次相连的原料罐、输料泵、离子交换树脂罐、蒸发器、结晶罐,其特征还在于离子交换树脂罐后和蒸发器前的管道上还依次安装有中间料罐、保安过滤器、高压泵、膜浓缩装置和透析罐,本实用新型主要优点在于,相比于传统直接进行蒸发浓缩结晶方法,5-羟基色氨酸提取液先经过膜浓缩,而膜浓缩具有节能、高效能优点,降低了生产成本。

The utility model discloses a concentration and crystallization device for 5-hydroxytryptophan, which comprises a raw material tank, a feeding pump, an ion exchange resin tank, an evaporator and a crystallization tank which are successively connected through pipelines, and is characterized in that the ion exchange resin tank The pipelines in the rear and in front of the evaporator are also successively installed with an intermediate material tank, a security filter, a high-pressure pump, a membrane concentration device and a dialysis tank. The hydroxytryptophan extract is first concentrated by membrane, and the membrane concentration has the advantages of energy saving and high efficiency, which reduces the production cost.

Description

一种5-羟基色氨酸的浓缩结晶设备A kind of concentration and crystallization equipment of 5-hydroxytryptophan

技术领域technical field

本实用新型涉及一种浓缩结晶设备,特别是涉及一种5-羟基色氨酸的浓缩结晶设备。The utility model relates to a concentration and crystallization device, in particular to a concentration and crystallization device for 5-hydroxytryptophan.

背景技术Background technique

5-羟基色氨酸(又名五羟基色氨酸、5-HTP)是一种天然的氨基酸,其化学名为5-羟基-3-吲哚基-α-氨基丙酸,分子量为220.23。五羟基色氨酸主要是从加纳籽中提取,加纳籽是热带豆科灌木植物加纳谷物Griffonia simplicifolia的干燥种子,野生于加纳、象牙海岸和多哥等西非国家。五羟基色氨酸具有多种生物学作用,是重要的神经类药物和保健药原料,临床上应用非常广泛,有重要的利用价值和广阔的市场前景。5-Hydroxytryptophan (also known as five-hydroxytryptophan, 5-HTP) is a natural amino acid, its chemical name is 5-hydroxy-3-indolyl-α-alanine, and its molecular weight is 220.23. Penta-hydroxytryptophan is mainly extracted from Ghana seed, which is the dry seed of Griffonia simplicifolia , a tropical leguminous shrub plant, which grows wild in West African countries such as Ghana, Ivory Coast and Togo. Five-hydroxytryptophan has a variety of biological effects, and is an important raw material for neurological drugs and health care drugs. It is widely used in clinical practice, has important utilization value and broad market prospects.

目前5-羟基色氨酸的提取制备方法大多采用:压榨或石油醚脱油→水/溶剂萃取→脱色→过滤→浓缩→结晶→重结晶,且5-羟基色氨酸的提取液的浓缩主要是通过蒸发浓缩过程来实现,其中蒸发浓缩使用的设备主要是蒸发器。蒸发浓缩具有浓缩倍数高等优点,但是蒸发浓缩液具有能耗大、成本高等缺点。5-羟基色氨酸的提取液脱色过滤后溶液中的5-羟基色氨酸含量较低,如果直接进行蒸发浓缩,将大大增加蒸发成本和蒸发时间。At present, most of the extraction and preparation methods of 5-hydroxytryptophan are: pressing or petroleum ether deoiling→water/solvent extraction→decolorization→filtration→concentration→crystallization→recrystallization, and the concentration of the extract of 5-hydroxytryptophan is mainly It is realized through the process of evaporative concentration, in which the equipment used for evaporative concentration is mainly an evaporator. Evaporation and concentration has the advantages of high concentration multiples, but the evaporative concentrate has the disadvantages of high energy consumption and high cost. The content of 5-hydroxytryptophan in the solution after decolorization and filtration of the extract of 5-hydroxytryptophan is relatively low. If it is directly evaporated and concentrated, the evaporation cost and evaporation time will be greatly increased.

膜分离是在20世纪初出现,20世纪60年代后迅速崛起的一门分离新技术。膜分离技术由于兼有分离、浓缩、纯化和精制的功能,又有高效、节能、环保、分子级过滤及过滤过程简单、易于控制等特征,因此,目前已广泛应用于食品、医药、生物、环保、化工、冶金、能源、石油、水处理、电子等领域,产生了巨大的经济效益和社会效益,已成为当今分离科学中最重要的手段之一。Membrane separation is a new separation technology that appeared in the early 20th century and rose rapidly after the 1960s. Membrane separation technology has been widely used in food, medicine, biology, Environmental protection, chemical industry, metallurgy, energy, petroleum, water treatment, electronics and other fields have produced huge economic and social benefits, and have become one of the most important means in today's separation science.

发明内容Contents of the invention

本实用新型针对传统5-羟基色氨酸蒸发浓缩设备能耗高等缺点,设计一种改良的5-羟基色氨酸的蒸发浓缩设备,达到降低生产成本的目的。The utility model aims at the shortcomings of traditional 5-hydroxytryptophan evaporation and concentration equipment such as high energy consumption, and designs an improved 5-hydroxytryptophan evaporation and concentration equipment to achieve the purpose of reducing production costs.

为达到上述目的,本实用新型提出的技术方案是:一种5-羟基色氨酸的浓缩结晶设备,包括通过管道依次相连的原料罐、输料泵、离子交换树脂罐、蒸发器、结晶罐,其特征还在于离子交换树脂罐后、蒸发器前的管道上还依次安装有中间料罐、保安过滤器、高压泵、阀门、膜浓缩装置和透析罐,且膜浓缩装置浓缩液出口通过回流管道与中间料罐相连,通过浓缩管道与蒸发器相连,其特征还在于所述的回流管道和浓缩管道上还安装有阀门。In order to achieve the above object, the technical solution proposed by the utility model is: a kind of concentration and crystallization equipment of 5-hydroxytryptophan, including a raw material tank, a feeding pump, an ion exchange resin tank, an evaporator, and a crystallization tank connected in sequence through pipelines , it is also characterized in that an intermediate material tank, a security filter, a high-pressure pump, a valve, a membrane concentration device and a dialysis tank are successively installed on the pipeline behind the ion exchange resin tank and in front of the evaporator, and the outlet of the concentrated solution of the membrane concentration device passes through the backflow The pipeline is connected with the intermediate material tank, and connected with the evaporator through the concentration pipeline, and the feature is that valves are also installed on the return pipeline and the concentration pipeline.

所述的高压泵为隔膜泵或卧式离心泵,保安过滤器过滤精度为50-200μm,膜浓缩装置所用的膜组件为卷式纳滤膜或卷式反渗透膜。The high-pressure pump is a diaphragm pump or a horizontal centrifugal pump, the filtration precision of the safety filter is 50-200 μm, and the membrane assembly used in the membrane concentration device is a roll-type nanofiltration membrane or a roll-type reverse osmosis membrane.

所述的回流管道上还安装有换热器。A heat exchanger is also installed on the return pipeline.

通过上述技术方案,本实用新型设备用于5-羟基色氨酸浓缩结晶主要优点在于,相比于传统直接进行蒸发浓缩结晶方法,5-羟基色氨酸提取液先经过膜浓缩,而膜浓缩具有节能、高效能优点,能够大大减少生产成本。Through the above technical scheme, the main advantage of the utility model equipment for 5-hydroxytryptophan concentration and crystallization is that, compared with the traditional direct evaporation concentration and crystallization method, the 5-hydroxytryptophan extract is first concentrated through the membrane, and the membrane concentration It has the advantages of energy saving and high efficiency, and can greatly reduce production costs.

附图说明Description of drawings

图1 为本实用新型的设备结构图;Fig. 1 is the equipment structural diagram of the present utility model;

其中:1.原料罐、2.进料管道、3.输料泵、4.离子交换树脂罐、5.中间料罐、6.保安过滤器、7.高压泵、8.膜浓缩装置、9.透析罐、10.回流管道、11.换热器、12.阀门、13.浓缩管道、14.蒸发器、15.结晶罐。Among them: 1. Raw material tank, 2. Feed pipeline, 3. Feed pump, 4. Ion exchange resin tank, 5. Intermediate material tank, 6. Security filter, 7. High pressure pump, 8. Membrane concentration device, 9 . Dialysis tank, 10. Return pipeline, 11. Heat exchanger, 12. Valve, 13. Concentrator pipeline, 14. Evaporator, 15. Crystallization tank.

具体实施方式Detailed ways

下面结合具体实施方式和附图对本实用新型做进一步说明。Below in conjunction with specific embodiment and accompanying drawing, the utility model is further described.

如附图1本实用新型的设备结构图所示,一种5-羟基色氨酸的浓缩结晶设备:原料罐1通过进料管道2依次与输料泵3、离子交换树脂罐4、中间料罐5、保安过滤器6、高压泵7、阀门12相连后,再与膜浓缩装置8相连,膜浓缩装置8的透析液出口通过管道与透析罐9相连,膜浓缩装置8浓缩液出口通回流管道10与中间料罐5相连,通过浓缩管道13与蒸发器14相连,蒸发器14再与结晶罐15相连。回流管道10和浓缩管道13上还安装有阀门12,回流管道上还安装有换热器11。As shown in the equipment structure diagram of the present utility model in accompanying drawing 1, a kind of concentrated crystallization equipment of 5-hydroxytryptophan: raw material tank 1 is successively connected with feeding pump 3, ion exchange resin tank 4, intermediate material through feed pipeline 2 Tank 5, security filter 6, high-pressure pump 7, and valve 12 are connected, and then connected to membrane concentration device 8, the dialysate outlet of membrane concentration device 8 is connected to dialysis tank 9 through pipelines, and the concentrated solution outlet of membrane concentration device 8 is connected to backflow The pipeline 10 is connected with the intermediate material tank 5, and is connected with the evaporator 14 through the concentration pipeline 13, and the evaporator 14 is connected with the crystallization tank 15 again. A valve 12 is also installed on the return pipeline 10 and the concentration pipeline 13, and a heat exchanger 11 is also installed on the return pipeline.

所用到的高压泵6可以为隔膜泵或卧式离心泵,保安过滤器7为滤袋,过滤精度为50-200μm,膜分离装置8中所用的膜组件为卷式纳滤膜或卷式反渗透膜。The high-pressure pump 6 used can be a diaphragm pump or a horizontal centrifugal pump. The security filter 7 is a filter bag with a filtration accuracy of 50-200 μm. The membrane module used in the membrane separation device 8 is a roll-type nanofiltration membrane or roll-type reverse filter. permeable membrane.

设备运行时,5-羟基色氨酸提取液从原料罐1中通过输料泵3经进料管道2泵入离子交换树脂罐4,经离子交换吸附后,由高压泵6 泵入膜浓缩装置中,由于是采用卷式纳滤膜或卷式反渗透膜,不含5-羟基色氨酸的透析液透过膜,进入透析罐中,5-羟基色氨酸浓缩液则经过回流管道10回流到中间料罐5中进一步循环浓缩,或者通过浓缩管道13进入蒸发器中进一步蒸发浓缩,蒸发浓缩到一定浓缩倍数后,则进入结晶罐15中进行冷却结晶。When the equipment is running, the 5-hydroxytryptophan extract is pumped from the raw material tank 1 into the ion exchange resin tank 4 through the feed pump 3 through the feed pipe 2, and after ion exchange adsorption, it is pumped into the membrane concentration device by the high pressure pump 6 In the process, due to the roll-type nanofiltration membrane or roll-type reverse osmosis membrane, the dialysate without 5-hydroxytryptophan passes through the membrane and enters the dialysis tank, and the 5-hydroxytryptophan concentrate passes through the return pipeline 10 Return to the intermediate tank 5 for further circulation and concentration, or enter the evaporator through the concentration pipeline 13 for further evaporation and concentration, and after evaporation and concentration to a certain concentration multiple, enter the crystallization tank 15 for cooling and crystallization.

综上所述,通过将本实用新型设备用于5-羟基色氨酸浓缩结晶主要优点在于,相比于传统直接进行蒸发浓缩结晶方法,5-羟基色氨酸提取液先经过纳滤膜或反渗透膜浓缩,而膜浓缩具有节能、高效能优点,能够大大减少生产成本。In summary, the main advantage of using the device of the present invention for the concentration and crystallization of 5-hydroxytryptophan is that, compared with the traditional method of direct evaporation, concentration and crystallization, the 5-hydroxytryptophan extract is first passed through a nanofiltration membrane or Reverse osmosis membrane concentration, and membrane concentration has the advantages of energy saving and high efficiency, which can greatly reduce production costs.

Claims (4)

1.一种5-羟基色氨酸的浓缩结晶设备,包括通过管道依次相连的原料罐、输料泵、离子交换树脂罐、蒸发器、结晶罐,其特征还在于离子交换树脂罐后、蒸发器前的管道上还依次安装有中间料罐、保安过滤器、高压泵、阀门、膜浓缩装置和透析罐,且膜浓缩装置浓缩液出口通过回流管道与中间料罐相连,通过浓缩管道与蒸发器相连,其特征还在于所述的回流管道和浓缩管道上还安装有阀门。1. a kind of concentrated crystallization equipment of 5-hydroxytryptophan, comprise the raw material tank that is connected successively by pipeline, feeding pump, ion exchange resin tank, evaporator, crystallization tank, it is characterized in that after ion exchange resin tank, evaporation The pipeline in front of the device is also successively installed with an intermediate material tank, a safety filter, a high-pressure pump, a valve, a membrane concentration device and a dialysis tank, and the outlet of the concentrated solution of the membrane concentration device is connected to the intermediate material tank through a return pipeline, and is connected to the evaporation tank through a concentration pipeline. The device is connected, and it is also characterized in that valves are also installed on the return pipeline and the concentration pipeline. 2.如权利要求1所述的一种5-羟基色氨酸的浓缩结晶设备,其特征在于所述的保安过滤器过滤精度为50-100μm。2. A kind of 5-hydroxytryptophan concentration and crystallization equipment as claimed in claim 1, characterized in that the filtration precision of the security filter is 50-100 μm. 3.如权利要求1所述的一种5-羟基色氨酸的浓缩结晶设备,其特征在于所述的膜浓缩装置所用的膜组件为卷式纳滤膜或卷式反渗透膜。3. The concentration crystallization equipment of a kind of 5-hydroxytryptophan as claimed in claim 1, it is characterized in that the membrane assembly used in the membrane concentration device is a roll-type nanofiltration membrane or a roll-type reverse osmosis membrane. 4.如权利要求1所述的一种5-羟基色氨酸的浓缩结晶设备,其特征在于所述的回流管道上还安装有换热器。4. The concentrated crystallization equipment of a kind of 5-hydroxytryptophan as claimed in claim 1, it is characterized in that a heat exchanger is also installed on the described return pipeline.
CN2010205282942U 2010-09-14 2010-09-14 Concentrating and crystallizing equipment for 5-hydroxyl tryptophan Expired - Fee Related CN201823337U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102600722A (en) * 2012-03-28 2012-07-25 于水利 Membrane separation device for high-concentration feed liquid and separation method
CN102807521A (en) * 2011-05-30 2012-12-05 江苏乐科热力科技有限公司 Concentrating crystallization process for tryptophan or glyphosate by using mechanical vapor recompression technology
CN105592901A (en) * 2013-06-24 2016-05-18 沃尔夫冈·赫恩佐 Crystallization systems and methods

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102807521A (en) * 2011-05-30 2012-12-05 江苏乐科热力科技有限公司 Concentrating crystallization process for tryptophan or glyphosate by using mechanical vapor recompression technology
CN102807521B (en) * 2011-05-30 2015-01-28 江苏乐科热力科技有限公司 Concentrating crystallization process for tryptophan or glyphosate by using mechanical vapor recompression technology
CN102600722A (en) * 2012-03-28 2012-07-25 于水利 Membrane separation device for high-concentration feed liquid and separation method
CN105592901A (en) * 2013-06-24 2016-05-18 沃尔夫冈·赫恩佐 Crystallization systems and methods
US10238988B2 (en) 2013-06-24 2019-03-26 Major Bravo Limited Crystallization system and process

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