CN209005247U - A kind of Chinese patent drug production alcohol high efficiente callback tower - Google Patents
A kind of Chinese patent drug production alcohol high efficiente callback tower Download PDFInfo
- Publication number
- CN209005247U CN209005247U CN201821570219.5U CN201821570219U CN209005247U CN 209005247 U CN209005247 U CN 209005247U CN 201821570219 U CN201821570219 U CN 201821570219U CN 209005247 U CN209005247 U CN 209005247U
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- tower
- destilling
- destilling tower
- chinese patent
- patent drug
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Abstract
The utility model discloses a kind of Chinese patent drug production alcohol high efficiente callback towers, including distillation still, destilling tower and condenser, measuring tank is installed above distillation still, the left and right ends of distillation still are respectively arranged with steam inlet and outlet pipe, the quantity of destilling tower is two, the top and bottom end of two destilling towers are separately installed with triple valve, in the packing layer for being internally provided with layer-stepping of destilling tower, it is separate type between adjacent packing layer, the flowmeter of monitoring air-flow is provided between destilling tower and condenser, circulating water outlet and liquid outlet are respectively arranged with above and below condenser, cooler and finished pot are installed below liquid outlet, Chinese patent drug production alcohol high efficiente callback tower, by being separately installed with triple valve on the top of destilling tower and bottom end, realize the series connection of two destilling towers and used in parallel, effectively improve distillation Purity facilitates being replaced for destilling tower, guarantees being carried out continuously for distillation process.
Description
Technical field
The utility model relates to recovery tower technical field, specially a kind of Chinese patent drug production alcohol high efficiente callback tower.
Background technique
Chinese patent drug be using Chinese medicine as raw material, under the guidance of traditional Chinese medical theory, in order to prevent and treat the needs of disease,
It is processed into the Chinese herbal product of a customization agent according to the prescription and preparation process of regulation, is through national drug supervision department batch
A kind of Chinese materia medica preparation of quasi- commercialization.
It generally can be by programs such as immersion, washing, dissolution, mixing, in the process of processing in the process of Chinese patent drug
In can generally be carried out in alcolhol burner solvent, in order to increase economic efficiency, economize on resources, generally can by alcohol by recovery tower into
Row recycling carries out use next time, and alcohol distillation column is the principle for being lower than other solution boiling points using alcohol boiling point, and use is slightly higher
In the temperature of alcohol boiling point, after needing the alcoholic solution recycled to carry out heating distillation, absolute alcohol gas is precipitated, it is molten to improve alcohol
The concentration of liquid achievees the purpose that recovered alcohol, existing alcohol distillation column are tasted to need replacing during recovered alcohol and be filled out
Material, and the distillation tower structure of integral type tastes needs in replacement process and stops operation, and seriously reduces actual production efficiency.
Utility model content
The purpose of this utility model is to provide a kind of Chinese patent drug production alcohol high efficiente callback towers, by destilling tower
Top and bottom end are separately installed with triple valve, realize the series connection of two destilling towers and used in parallel, effectively improve the purity of distillation,
Facilitate being replaced for destilling tower, guarantees being carried out continuously for distillation process.
To achieve the above object, the utility model provides the following technical solutions: a kind of Chinese patent drug production is efficiently returned with alcohol
Tower, including distillation still, destilling tower and condenser are received, measuring tank is installed above the distillation still, filtrate passes through measuring tank
Distillation still is flowed into after metering, the left and right ends of the distillation still are respectively arranged with steam inlet and outlet pipe, destilling tower and steaming
It evaporates and is connected between kettle by outlet pipe, the quantity of the destilling tower is two, and the top and bottom end of two destilling towers are pacified respectively
It is separate type, the steaming between the packing layer for being internally provided with layer-stepping of destilling tower, adjacent packing layer equipped with triple valve
The flowmeter for being provided with monitoring air-flow between tower and condenser is evaporated, is respectively arranged with recirculated water above and below the condenser
Outlet and liquid outlet are equipped with cooler and finished pot below the liquid outlet.
Preferably, be provided with sliding rail between adjacent packing layer, packing layer can under the drive of sliding rail with steaming
It evaporates tower and relative displacement occurs, be convenient for changing filler.
Preferably, the quantity of described filler layer is 3-5 layers.
Preferably, the valve of control triple valve single circulation and three-dimensional circulation is installed above the triple valve.
Preferably, cooling pipe is provided between the liquid outlet and cooler and between cooler and finished pot.
Compared with prior art, the beneficial effects of the utility model are as follows:
The utility model is provided with triple valve, triple valve setting by two destilling towers of setting between two destilling towers
On the top and bottom end of destilling tower, realizes the series connection of two destilling towers and be connected in parallel, through distillation still treated alcohol gas,
Destilling tower is flowed by outlet pipe, destilling tower can carry out single-pass process and binary channels is steamed according to actual distillation needs
It evaporates, effectively increases distillation efficiency, the packing layer for being internally provided with layer-stepping of destilling tower is separation between adjacent packing layer
Formula, sliding rail is provided between adjacent packing layer, and packing layer can occur under the drive of sliding rail with destilling tower opposite
Displacement, is convenient for changing filler, and the design of double destilling towers, so that filler in replacement process, does not need to stop distillation process yet,
The progress for guaranteeing distillation process, improves actual production efficiency.
Detailed description of the invention
Fig. 1 is the utility model overall structure diagram；
Fig. 2 is the utility model destilling tower structural schematic diagram.
In figure: 1 distillation still；2 destilling towers；3 condensers；4 measuring tanks；5 steam inlets；6 outlet pipes；7 triple valves；8 fill out
The bed of material；9 flowmeters；10 circulating water outlets；11 liquid outlets；12 coolers；13 finished pots；14 sliding rails；15 valves；16 is cooling
Pipeline.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
A kind of Chinese patent drug production alcohol high efficiente callback tower referring to FIG. 1-2, including distillation still 1, destilling tower 2 and condensation
Device 3, the top of distillation still 1 are equipped with measuring tank 4, flow into distillation still 1, a left side for distillation still 1 after the metering that filtrate passes through measuring tank 4
Right both ends are respectively arranged with steam inlet 5 and outlet pipe 6, are connected between destilling tower 2 and distillation still 1 by outlet pipe 6, steam
The quantity for evaporating tower 2 is two, and the top and bottom end of two destilling towers 2 are separately installed with triple valve 7, the top installation of triple valve 7
There is the valve 15 of control triple valve 7 single circulation and three-dimensional circulation, in the packing layer 8 for being internally provided with layer-stepping of destilling tower 2,
It is separate type between adjacent packing layer 8, sliding rail 14 is provided between adjacent packing layer 8, packing layer 8 can be in sliding rail
Relative displacement occurs with destilling tower 2 under the drive in road 14, is convenient for changing filler, the quantity of packing layer 8 is 3-5 layer, destilling tower 2 and
It is provided with the flowmeter 9 of monitoring air-flow between condenser 3, is respectively arranged with circulating water outlet 10 above and below condenser 3
With liquid outlet 11, the lower section of liquid outlet 11 is equipped with cooler 12 and finished pot 13, between liquid outlet 11 and cooler 12 and
Cooling pipe 16 is provided between cooler 12 and finished pot 13.
In use, being provided with triple valve 7 between two destilling towers 2 by two destilling towers 2 of setting, triple valve 7 is arranged
It on the top and bottom end of destilling tower 2, realizes the series connection of two destilling towers 2 and is connected in parallel, through treated the alcohol gas of distillation still 1
Body flows into destilling tower 2 by outlet pipe 6, and destilling tower 2 can carry out single-pass process and double according to actual distillation needs
Channel distillation, effectively increases distillation efficiency, the packing layer 8 for being internally provided with layer-stepping of destilling tower 2, adjacent packing layer 8
Between be separate type, be provided with sliding rail 14 between adjacent packing layer 8, packing layer 8 can be under the drive of sliding rail 14
Relative displacement occurs with destilling tower 2, is convenient for changing filler, and the design of double destilling towers 2, so that filler is in replacement process,
It does not need to stop distillation process, guarantees the progress of distillation process, improve actual production efficiency.
In summary: Chinese patent drug production alcohol high efficiente callback tower, by pacifying respectively on the top of destilling tower 2 and bottom end
Equipped with triple valve 7, realizes the series connection of two destilling towers 2 and used in parallel, effectively improve the purity of distillation, facilitate replacing for destilling tower
Use is changed, guarantees being carried out continuously for distillation process.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of Chinese patent drug production alcohol high efficiente callback tower, including distillation still (1), destilling tower (2) and condenser (3), described
It is equipped with above distillation still (1) measuring tank (4), flows into distillation still (1) after the metering that filtrate passes through measuring tank (4), feature
Be: the left and right ends of the distillation still (1) are respectively arranged with steam inlet (5) and outlet pipe (6), destilling tower (2) and steaming
It evaporates and is connected between kettle (1) by outlet pipe (6), the quantity of the destilling tower (2) is two, the top of two destilling towers (2)
Triple valve (7) are separately installed with bottom end, in the packing layer (8) for being internally provided with layer-stepping of destilling tower (2), adjacent filler
It is separate type between layer (8), the flowmeter (9) of monitoring air-flow is provided between the destilling tower (2) and condenser (3), it is described
Circulating water outlet (10) and liquid outlet (11) are respectively arranged with above and below condenser (3), under the liquid outlet (11)
Side is equipped with cooler (12) and finished pot (13).
2. a kind of Chinese patent drug production alcohol high efficiente callback tower according to claim 1, it is characterised in that: adjacent filler
It is provided with sliding rail (14) between layer (8), packing layer (8) can occur under the drive of sliding rail (14) with destilling tower (2)
Relative displacement is convenient for changing filler.
3. a kind of Chinese patent drug production alcohol high efficiente callback tower according to claim 2, it is characterised in that: described filler layer
(8) quantity is 3-5 layers.
4. a kind of Chinese patent drug production alcohol high efficiente callback tower according to claim 1, it is characterised in that: the triple valve
(7) valve (15) of control triple valve (7) single circulation and three-dimensional circulation is installed above.
5. a kind of Chinese patent drug production alcohol high efficiente callback tower according to claim 1 to 4, it is characterised in that: described
It is provided with cooling pipe (16) between liquid outlet (11) and cooler (12) and between cooler (12) and finished pot (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821570219.5U CN209005247U (en) | 2018-09-26 | 2018-09-26 | A kind of Chinese patent drug production alcohol high efficiente callback tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821570219.5U CN209005247U (en) | 2018-09-26 | 2018-09-26 | A kind of Chinese patent drug production alcohol high efficiente callback tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209005247U true CN209005247U (en) | 2019-06-21 |
Family
ID=66834315
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821570219.5U Expired - Fee Related CN209005247U (en) | 2018-09-26 | 2018-09-26 | A kind of Chinese patent drug production alcohol high efficiente callback tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209005247U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114984604A (en) * | 2022-06-30 | 2022-09-02 | 张闻龙 | Continuous double-tower distillation system |
-
2018
- 2018-09-26 CN CN201821570219.5U patent/CN209005247U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114984604A (en) * | 2022-06-30 | 2022-09-02 | 张闻龙 | Continuous double-tower distillation system |
| CN114984604B (en) * | 2022-06-30 | 2024-01-09 | 河南金大地化工有限责任公司 | Continuous double-tower distillation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190621 Termination date: 20200926 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |