CN203877923U - Active carbon recycling system used in crude drug production process - Google Patents

Active carbon recycling system used in crude drug production process Download PDF

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Publication number
CN203877923U
CN203877923U CN201420222691.5U CN201420222691U CN203877923U CN 203877923 U CN203877923 U CN 203877923U CN 201420222691 U CN201420222691 U CN 201420222691U CN 203877923 U CN203877923 U CN 203877923U
Authority
CN
China
Prior art keywords
active carbon
receiving tank
filter
pipelines
utility
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.)
Expired - Fee Related
Application number
CN201420222691.5U
Other languages
Chinese (zh)
Inventor
陈政权
夏卫平
欧阳杰
王水才
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.)
HUBEI TEYER PHARMACEUTICAL CO Ltd
Original Assignee
HUBEI TEYER 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
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Priority to CN201420222691.5U priority Critical patent/CN203877923U/en
Application granted granted Critical
Publication of CN203877923U publication Critical patent/CN203877923U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model provides an active carbon recycling system used in a crude drug production process. The active carbon recycling system comprises a reaction kettle, wherein a filter is arranged at one side of the reaction kettle; a receiving tank is arranged at one end of the filter; the reaction kettle, the filter and the receiving tank are connected by pipelines; valves are arranged on the pipelines; a sand core filter stick is arranged in the filter; the reaction kettle and the receiving tank are connected with a vacuum system by pipelines; valves are arranged on the pipelines. The system disclosed by the utility model can improve product yield and can lower production cost; the treated active carbon can be reutilized by deep processing, so that resources are saved, and environmental pollution is also reduced.

Description

A kind of for production of raw medicine process gac recovery system
Technical field
The utility model belongs to chemical machinery field, refers to particularly a kind of system that reclaims adsorb medicine from gac.
Background technology
Bulk drug ganciclovir, valaciclovir hydrochlordide are in process of production time, need purify with gac, decolour, after being finished, gac is carried out to burning disposal, because gac has also adsorbed a certain amount of medicine simultaneously, when processing, can cause environmental pollution, in sum if recycle, can improve product yield, reduce production costs, the gac after processing also can recycle after deep processing, economizes on resources.
Utility model content
The purpose of this utility model is to overcome deficiency of the prior art, and provides a kind of for production of raw medicine process gac recovery system.
The technical solution of the utility model is achieved in that
Provide a kind of for production of raw medicine process gac recovery system, comprise a reactor, it is characterized in that: a side of described reactor is provided with strainer, one end of strainer is provided with receiving tank, between described reactor, strainer, receiving tank three, by pipeline, be connected, on pipeline, be equipped with valve, in described strainer, be provided with core filter stick, described reactor is respectively connected with vacuum system by pipeline with receiving tank, and pipeline is provided with valve.
Working process of the present utility model and advantage are: open the vacuum valve on reactor, open vacuum by purified water suction reactor, drop into pending gac, be warming up to medicine and dissolve, after medicine dissolves completely, vacuum valve on off-response still, other valve in system is all opened, feed liquid in reactor is filtered to rear suction receiving tank, gac is trapped in strainer, collection is recycling by deep processing, and feed liquid cooling crystallization can obtain product through again refining.This system can improve product yield, reduces production costs, and the gac after processing is recycling through deep processing, economizes on resources, and has also reduced environmental pollution.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the utility model.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described, but and be limited to following examples:
It in Fig. 1, is gac recovery system, one side of reactor 1 is provided with strainer 2, one end of strainer 2 is provided with receiving tank 3, between reactor 1, strainer 2, receiving tank 3 threes, by pipeline 4, be connected, on pipeline 4, be equipped with valve 5, in described strainer 2, be provided with core filter stick, reactor 1 is respectively connected with vacuum system by pipeline 4 with receiving tank 3, and pipeline 4 is provided with valve 5.
Although shown detailed embodiment of the present utility model above, apparent, those skilled in the art is under prerequisite of the present utility model, can carry out part modifications and changes; The content of mentioning in description above and accompanying drawing, only as illustrative case, not, as to restriction of the present utility model, has a kind of for production of raw medicine process gac recovery system of above-mentioned technical characterictic, all falls into the utility model protection domain.

Claims (1)

1. one kind for production of raw medicine process gac recovery system, comprise a reactor, it is characterized in that: a side of described reactor is provided with strainer, one end of strainer is provided with receiving tank, between described reactor, strainer, receiving tank three, by pipeline, be connected, on pipeline, be equipped with valve, in described strainer, be provided with core filter stick, described reactor is respectively connected with vacuum system by pipeline with receiving tank, and pipeline is provided with valve.
CN201420222691.5U 2014-05-04 2014-05-04 Active carbon recycling system used in crude drug production process Expired - Fee Related CN203877923U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420222691.5U CN203877923U (en) 2014-05-04 2014-05-04 Active carbon recycling system used in crude drug production process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420222691.5U CN203877923U (en) 2014-05-04 2014-05-04 Active carbon recycling system used in crude drug production process

Publications (1)

Publication Number Publication Date
CN203877923U true CN203877923U (en) 2014-10-15

Family

ID=51678447

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420222691.5U Expired - Fee Related CN203877923U (en) 2014-05-04 2014-05-04 Active carbon recycling system used in crude drug production process

Country Status (1)

Country Link
CN (1) CN203877923U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109808934A (en) * 2019-03-20 2019-05-28 中国恩菲工程技术有限公司 Gas-phase silica packs the recyclable device and recovery method of quick-fried bag product

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109808934A (en) * 2019-03-20 2019-05-28 中国恩菲工程技术有限公司 Gas-phase silica packs the recyclable device and recovery method of quick-fried bag product

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20141015

Termination date: 20180504