CN2726696Y - Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device - Google Patents
Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device Download PDFInfo
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- CN2726696Y CN2726696Y CN 200420079030 CN200420079030U CN2726696Y CN 2726696 Y CN2726696 Y CN 2726696Y CN 200420079030 CN200420079030 CN 200420079030 CN 200420079030 U CN200420079030 U CN 200420079030U CN 2726696 Y CN2726696 Y CN 2726696Y
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Abstract
The utility model provides a composite type Chinese medicinal liquid concentrating and alcohol reclaiming device for the Chinese drugs pharmaceutics, comprising an outer circulation type vacuum concentrating device made up by a heater, an evaporator, a condenser and a liquid receiver tank. The utility model is characterized in that a secondary steam outlet is arranged on the upper part of the evaporator, and as well as a rectifying tower connected with a valve is arranged on the upper part of the evaporator, and the secondary steam outlet and the rectifying tower are evenly communicated through the valve and pipelines with the components of the same condenser, etc. therefore the exchange of the valve and the transformation assembly can be controlled. When the concentrating (containing cream collecting) and the reclaiming are provided, the partial components are shared respectively. Compared with the prior art, the utility model avoids the repetition arrangement of the components with the same functions. The utility model satisfies the requirement of the production process, and as well as the utility model improves equipment utilization ratio, and the utility model reduces investment and operating cost. The structure with double effects saves energy still.
Description
The utility model relates to Chinese medicine preparation equipment, and particularly a kind of combined type herb liquid concentrates, alcohol recovering device.
General herb liquid concentrates, ethanol reclaims needs three covering devices, and the one, the outer circulation type vacuum concentrator is with lixiviate thin liquid simmer down to liquid extract; The 2nd, the jacket type vacuum concentration pot changes molten liquid extract and then the simmer down to medicinal extract of handling that waits with alcohol precipitation; The 3rd, alcohol recovering device is proposed dense recovery with the Diluted Alcohol rectifying of preparation process generation and is used.Chinese medicine preparation production mostly is intermittently operated, heater in this three covering device, evaporimeter, condenser, be provided with because of repeating by the identical parts of function such as liquid bath, often cause part idle in different production time sections, this had both increased equipment investment cost, increase factory building and floor space again, reduce capacity utilization, caused the wasting of resources.At present, not only do concentrated but also make the device that ethanol reclaims in the prior art, a boil-off outlet is only established on its evaporimeter top, when this outlet is only established condenser, doing simple distillation can not make ethanol separate fully with water, the concentration of alcohol that reclaims is still lower, does to concentrate also can produce condensing reflux and reduced evaporation rate on the contrary; When in this outlet is only established, loading the rectifying column of material, do to concentrate the eliminating that has then hindered boil-off.
The purpose of this utility model provides a kind of identical parts of function of avoiding and repeats to be provided with, can satisfy equally with the less parts combination concentrate, ethanol reclaims technological requirement, a tractor serves several purposes, joint are supported energy-conservation simplification device.
The technical scheme that realizes the purpose of this utility model is: comprise have steam inlet, the liquid bath that is subjected to of the heater of condensation-water drain, evaporimeter, condenser, connection vacuum port forms the outer circulation type vacuum concentrating apparatus, the characteristics that had are that evaporimeter top both had been provided with the indirect steam outlet, be communicated with condenser by valve and pipeline, be provided with the rectifying column that is connected with valve again, also be communicated with condenser by valve and pipeline, formation combined type herb liquid concentrates, the ethanol recovery structure.
Also the steam inlet of heater can be linked to each other with another evaporimeter top indirect steam outlet of imitating the outer circulation type vacuum concentrator by valve and pipeline, the condensation-water drain of this heater is communicated with being subjected to liquid bath by valve and pipe bundle condenser, constitutes concentrated, the ethanol recovery structure of economic benefits and social benefits combined type herb liquid.
The utility model exported because both be provided with indirect steam on evaporimeter top, be provided with the rectifying column that is connected with valve again, and all by members such as valve and the same condensers of Guan Luoyu, thereby the switching of energy control valve, the conversion combination, difference common sparing parts are compared with prior art when concentrating with the ethanol recovery, have avoided the identical parts of function to repeat to be provided with, both satisfied manufacturing technique requirent, improve utilization rate of equipment and installations, save equipment investment and operating cost again, reduce factory building and floor space.
Concrete structure of the present utility model is provided by following embodiment and accompanying drawing thereof.
Fig. 1 is that the combined type herb liquid that basis the utility model proposes concentrates, the schematic diagram of a kind of single-action structure of alcohol recovering device.
Fig. 2 is that the combined type herb liquid that basis the utility model proposes concentrates, the schematic diagram of a kind of economic benefits and social benefits structure of alcohol recovering device.
As shown in Figure 1, comprise that heater (8), evaporimeter (5), the condenser (19) of have steam inlet (7), condensation-water drain (9), the liquid bath (13) that is subjected to that is communicated with vacuum port (14) form the outer circulation type vacuum concentrating apparatus, unlike the prior art be, evaporimeter (5) top both had been provided with indirect steam outlet (2), be communicated with condenser (19) by valve (20) and pipeline, be provided with the rectifying column (1) that is connected with valve (4) again, also be communicated with condenser (19) by valve (21) and pipeline, formation combined type herb liquid concentrates, the ethanol recovery structure.In preparation is produced, only by the switching of control valve, can constitute different parts combinations, thereby satisfy different manufacturing technique requirents, certainly, the still pump that need be correlated with, receiver etc.
As the single-action structure, be with the boiler primary steam that enters heater (8) from steam inlet (7) as thermal source, heat herb liquid or Diluted Alcohol carburation by evaporation.When concentrating, close valve (4), (21), open valve (3), (20), (6), (10), under vacuum action, boil-off enters multiple the coagulating of condenser (19) by the road from indirect steam outlet (2) and is liquid, can enter to be collected in after cooler (15) cooling again and be subjected to liquid bath (13), the herb liquids many for foam can be provided with valve (3) and vapour liquid separator (18), in order to the foam that disappears.When receiving cream, close valve (4), (21), (6), (10), utilize negative pressure of vacuum that the herb liquid liquid extract is sucked in the evaporimeter (5), steam port (12) the valve heating feed liquid of opening heating jacket (11) is to medicinal extract.When ethanol reclaims, close valve (3), (20), open valve (4), (21), (6), (10), the Diluted Alcohol steam that is heated vaporization is because of only feeding the rectifying column (1) with filler, so the steam that rises can fully contact mixing with the condensate liquid that flows down, and carry out heat exchange, thereby steam more upwards, low boiling component is high more, regulates the reflux ratio discharging and can obtain high concentration finished product ethanol.According to conditions such as preheater, head tank are set, both can adopt continuously, the semi-continuous distillation mode, also can adopt the batch distillation mode, but both atmospheric operations, but also low vacuum operation, to improve distilling rate, method of operating and prior art are roughly the same.During intermittently operated, the end that condenser (19) can be set all communicates with two Room of the voltage stabilizing buffer (27) of two cell structures, to guarantee liquid in-out two end air pressure balances, the adjusting reflux ratio is carried out smoothly.
As shown in Figure 2, for improving energy-saving effect and evaporation rate, the steam inlet (7) of heater (8) can be linked to each other with another evaporimeter (23) top indirect steam outlet (22) of imitating the outer circulation type vacuum concentrator by valve (24) and pipeline, the condensation-water drain (9) of this heater (8) is communicated with being subjected to liquid bath (13-1) by valve (25) and pipe bundle condenser (26), constitutes concentrated, the ethanol recovery structure of economic benefits and social benefits combined type herb liquid.It is basic identical with single-action that each production operation is imitated in back one, different is, when concentrating, close heater (8) steam inlet (7) valve, open valve (24), at this moment, the boiler primary steam is to enter last effect heater heating, so, becoming the heater (8) of imitating back one can utilize last effect indirect steam as thermal source, also become simultaneously the condenser of last effect, uncooled indirect steam can enter the pipe bundle condenser (26) with cooling water then and obtain being subjected to liquid bath (13-1) than entering after the abundant condensation.This is subjected to liquid bath (13-1) can be set to three cell structures, ethanol is respectively finished product ethanol storeroom, vacuum chamber and condensate liquid from top to bottom and collects drain chamber when reclaiming, other operations can be determined in addition, that control principle is set is similar to prior art for valve on it, so just can be under break vacuum mode of operation not, finish the storage and the discharging of condensation cooling fluid, can realize separately handling of finished product ethanol and other condensate liquids.Receiving the cream operation can operate with reference to single-action.Ethanol can the boiler primary steam be thermal source both when reclaiming, and the indirect steam in the time of also can utilizing last effect to evaporate is thermal source.
Vacuum port (14) also can be set, be subjected to liquid bath (13) or (13-1) connect cyclone separator (17), can prevent that ethanol tail gas from running material, with abundant recovery with cooling water jecket (16).
Claims (6)
1. a combined type herb liquid concentrates, alcohol recovering device, comprise and have steam inlet (7), the heater (8) of condensation-water drain (9), evaporimeter (5), condenser (19), the liquid bath (13) that is subjected to that is communicated with vacuum port (14) is formed the outer circulation type vacuum concentrating apparatus, it is characterized in that evaporimeter (5) top both had been provided with indirect steam outlet (2), be communicated with condenser (19) by valve (20) and pipeline, be provided with the rectifying column (1) that is connected with valve (4) again, also be communicated with by valve (21) and pipeline, constitute combined type and concentrate with condenser (19), the ethanol recovery structure.
2. according to the described device of claim 1, the steam inlet (7) that it is characterized in that heater (8) links to each other with another evaporimeter (23) top indirect steam outlet (22) of imitating the outer circulation type vacuum concentrator by valve (24) and pipeline, the condensation-water drain (9) of this heater (8) is communicated with being subjected to liquid bath (13-1) by valve (25) and pipe bundle condenser (26), constitutes concentrated, the ethanol recovery structure of economic benefits and social benefits combined type herb liquid.
3. according to the described device of claim 2, it is characterized in that being subjected to liquid bath (13-1) is three cell structures.
4. according to claim 1 or 2 described devices, it is characterized in that evaporimeter (5) bottom is provided with heating jacket (11).
5. according to claim 1 or 2 described devices, it is characterized in that vacuum port (14), be subjected to liquid bath (13) or (13-1) connect cyclone separator (17) with cooling water jecket (16).
6. according to claim 1 or 2 described devices, an end of condenser when it is characterized in that batch distillation (19) all communicates with two Room of the voltage stabilizing buffer (27) of two cell structures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420079030 CN2726696Y (en) | 2004-08-27 | 2004-08-27 | Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420079030 CN2726696Y (en) | 2004-08-27 | 2004-08-27 | Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2726696Y true CN2726696Y (en) | 2005-09-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420079030 Expired - Fee Related CN2726696Y (en) | 2004-08-27 | 2004-08-27 | Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device |
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| CN (1) | CN2726696Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007555A (en) * | 2012-12-19 | 2013-04-03 | 温州市天龙轻工设备有限公司 | Vacuum concentrator |
| CN103387480A (en) * | 2013-06-28 | 2013-11-13 | 赛普（无锡）膜科技发展有限公司 | Device of vaporized ethanol recovery and method thereof |
| CN104165350A (en) * | 2014-07-30 | 2014-11-26 | 湖州荣胜生物科技股份有限公司 | Cooling water recycling device of concentrating boiler |
| CN104524789A (en) * | 2014-11-28 | 2015-04-22 | 悦康药业集团安徽天然制药有限公司 | Single-effect concentrated alcohol recovering apparatus |
| CN109529403A (en) * | 2019-01-03 | 2019-03-29 | 沈奇光 | Energy-saving dual-use traditional Chinese medicine extraction, concentrator |
| CN111330306A (en) * | 2019-11-01 | 2020-06-26 | 广东金宗机械有限公司 | Percolation leaching system and processing technology thereof |
-
2004
- 2004-08-27 CN CN 200420079030 patent/CN2726696Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103007555A (en) * | 2012-12-19 | 2013-04-03 | 温州市天龙轻工设备有限公司 | Vacuum concentrator |
| CN103007555B (en) * | 2012-12-19 | 2015-07-01 | 王良源 | Vacuum concentrator |
| CN103387480A (en) * | 2013-06-28 | 2013-11-13 | 赛普（无锡）膜科技发展有限公司 | Device of vaporized ethanol recovery and method thereof |
| CN104165350A (en) * | 2014-07-30 | 2014-11-26 | 湖州荣胜生物科技股份有限公司 | Cooling water recycling device of concentrating boiler |
| CN104165350B (en) * | 2014-07-30 | 2016-01-13 | 湖州荣胜生物科技股份有限公司 | Concentration pan cooling water recycling device |
| CN104524789A (en) * | 2014-11-28 | 2015-04-22 | 悦康药业集团安徽天然制药有限公司 | Single-effect concentrated alcohol recovering apparatus |
| CN109529403A (en) * | 2019-01-03 | 2019-03-29 | 沈奇光 | Energy-saving dual-use traditional Chinese medicine extraction, concentrator |
| CN111330306A (en) * | 2019-11-01 | 2020-06-26 | 广东金宗机械有限公司 | Percolation leaching system and processing technology thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |