CN207445611U - A kind of Salvia root P.E enrichment facility - Google Patents
A kind of Salvia root P.E enrichment facility Download PDFInfo
- Publication number
- CN207445611U CN207445611U CN201721529503.3U CN201721529503U CN207445611U CN 207445611 U CN207445611 U CN 207445611U CN 201721529503 U CN201721529503 U CN 201721529503U CN 207445611 U CN207445611 U CN 207445611U
- Authority
- CN
- China
- Prior art keywords
- concentration tank
- tank
- pipe
- discharge nozzle
- feed pipe
- 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
Links
- 241001072909 Salvia Species 0.000 title claims abstract description 16
- 235000017276 Salvia Nutrition 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- 238000007599 discharging Methods 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 3
- 239000000565 sealant Substances 0.000 claims description 3
- 238000001704 evaporation Methods 0.000 abstract description 10
- 230000008020 evaporation Effects 0.000 abstract description 10
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000004480 active ingredient Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000013475 authorization Methods 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of Salvia root P.E enrichment facilities, including concentration tank, the concentration tank top left hand is equipped with vacuum pump, motor is equipped on the right side of the vacuum pump, the motor output end is equipped with rotation axis, the rotation axis is through concentration tank upper wall and extends to inside concentration tank, the rotation axis bottom is equipped with agitating vane on two side, the concentration tank left upper part is equipped with feed pipe, the feed pipe is equipped with feed pipe valve, the concentration tank bottom is equipped with heating tube, the concentration tank right end lower part is equipped with discharge nozzle, the discharge nozzle is equipped with discharging tube valve, rewinding tank is equipped with below the discharge nozzle；Return duct is equipped in the middle part of the concentration tank right end, the return duct top is equipped with gas-liquid separator, and the gas-liquid separator right end is equipped with exhaust pipe, and the gas-liquid separator left end is equipped with condenser pipe.The utility model is simple in structure, of low cost, easy to use, and evaporation rate is fast, and cocnentration factor is high and energy consumption is low.
Description
Technical field
The utility model is related to Radix Salviae Miltiorrhizae extractive technique field more particularly to a kind of Salvia root P.E enrichment facilities.
Background technology
Salvia root P.E is process by the drying root and rhizome extraction of labiate Radix Salviae Miltiorrhizae, general by crushing, carrying
The techniques such as take, extract, concentrating, drying obtain, it is general to obtain after Radix Salviae Miltiorrhizae extract liquor that improve solution dense, it is necessary to carry out concentration and evaporation
Degree, and present enrichment facility is of high cost, energy consumption is greatly and the economic benefit of creation is not directly proportional.
Through retrieval, Chinese patent Authorization Notice No. discloses a kind of enrichment facility for CN205516534U, including concentration tank
Body, the first condenser, vapour liquid separator, the second condenser, cooler and submerged soil, concentration tank body top connect with the first condenser
It connects, the first condenser is connected with vapour liquid separator one end, and the vapour liquid separator other end is connected with the second upper end of condenser, and second is cold
Condenser lower end is connected with cooler upper end, and cooler lower end is connected again with submerged soil, and concentration tank base is equipped with heat preservation sandwich layer, protects
Heating tube in warm interlayer is installed, heating interlayer is equipped in the middle part of concentration tank body, heating interlayer is connected with external hot water pipeline.
Existing enrichment facility has the following disadvantages：The apparatus structure is complicated, and cost of manufacture is high, and evaporation rate is slow,
It is big to complete concentration technology energy consumption, easily causes the waste of the energy.
Utility model content
The purpose of this utility model is to provide a kind of Salvia root P.E enrichment facility, possess it is simple in structure, it is of low cost,
The advantages of easy to use, evaporation rate is fast, and cocnentration factor is high and energy consumption is low, solves that evaporation rate is slow, energy consumption is high, waste of energy
Problem.
According to a kind of Salvia root P.E enrichment facility of the utility model embodiment, including concentration tank, the concentration tank deck
End left side is equipped with vacuum pump, and motor is equipped on the right side of the vacuum pump, and the motor output end is equipped with rotation axis, the rotation
Axis is through concentration tank upper wall and extends to inside concentration tank, and the rotation axis bottom is equipped with agitating vane on two side, described
Concentration tank left upper part is equipped with feed pipe, and the feed pipe is equipped with feed pipe valve, and the concentration tank bottom is equipped with heating tube,
The concentration tank right end lower part is equipped with discharge nozzle, and the discharge nozzle is equipped with discharging tube valve, is equipped with and receives below the discharge nozzle
Batch can；Return duct is equipped in the middle part of the concentration tank right end, the return duct top is equipped with gas-liquid separator, the gas-liquid separator
Right end is equipped with exhaust pipe, and the gas-liquid separator left end is equipped with condenser pipe, and the condenser pipe top left hand is equipped with water outlet, described
Water inlet is equipped on the right side of condenser pipe bottom, the condenser pipe left end is equipped with steam lead, the steam lead bottom and concentration tank
Top communicates.
Further, the discharge nozzle right end is equipped with strainer, and the feed pipe left end is equipped with dustproof cover.
Further, the exhaust pipe right end is equipped with exhaust collection tank.
Further, temperature measuring set is equipped on the right side of the concentration upper end, the temperature measuring set bottom is through concentration
Tank upper wall is simultaneously extended to inside concentration tank 1.
Further, the heating tube is in " M " shape.
Further, the feed pipe, discharge nozzle are connected by bolt with concentration tank and junction scribbles fluid sealant.
The utility model has an advantageous effect in that compared with prior art：
1st, material can be entered by feed pipe in concentration tank, and heating tube is passed through heating steam and concentration tank can be carried out
Heating, heating tube can ensure that concentration tank bottom is heated evenly in " m " shape, accelerate evaporation rate；Motor drives rotation axis to make
Agitating vane rotates, and concentrate is stirred, equally accelerates evaporation rate；Vacuum pump can be by gas extraction in concentration tank
Vacuum low-pressure state is formed, the boiling point of liquid generally reduces under vacuum low-pressure state, greatly reduces energy requirements, saves energy
Consumption；
2nd, after heating a period of time, liquid starts to evaporate, and is discharged by steam lead, and the condensed pipe cooling of steam is laggard
Enter gas-liquid separator, gas is separated with liquid, be back to containing a small amount of active ingredient liquid of extract in concentration tank, make concentration
Later extracting solution can remain the part active ingredient of extract, keep its flavour；Exhaust collection tank can
The on-condensible gas of gas-liquid separator separates is collected, prevents it from polluting air, dustproof cover can prevent dust from entering in feed pipe, filter
Net being capable of large volume impurity in filtering solution；The apparatus structure is simple, of low cost, easy to use, and evaporation rate is fast, cocnentration factor
Height, energy consumption is low, economizes on resources.
Description of the drawings
Attached drawing is used to provide a further understanding of the present invention, and a part for constitution instruction, with this practicality
New embodiment for explaining the utility model, does not form the limitation to the utility model together.In the accompanying drawings：
Fig. 1 be the utility model proposes a kind of Salvia root P.E enrichment facility structure diagram；
Fig. 2 be the utility model proposes a kind of Salvia root P.E enrichment facility heating-pipe structure schematic diagram.
In figure：1- concentration tanks, 2- heating tubes, 3- dischargings tube valve, 4- rewindings tank, 5- strainers, 6- discharge nozzles, 7- reflux
Pipe, 8- exhaust collections tank, 9- exhaust pipes, 10- gas-liquid separators, 11- water inlets, 12- condenser pipes, 13- water outlets, 14- temperature
Measuring instrument, 15- steam leads, 16- vacuum pumps, 17- dustproof covers, 18- feed pipes, 19- feed pipes valve, 20- motor, 21-
Rotation axis, 22- agitating vanes.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, 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 embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
With reference to Fig. 1-2, a kind of Salvia root P.E enrichment facility including concentration tank 1, can contain liquid, 1 top of concentration tank
Left side is equipped with vacuum pump 16, and the model 2BV-2060 of vacuum pump can evacuate gas in tank body and form low-voltage vacuum state, drop
Low boiling point of liquid, the vacuum pump right side are equipped with motor 20, motor model Y315M-10,20 output terminal of motor
Equipped with rotation axis 21, the rotation axis 21 is through 1 upper wall of concentration tank and extends to inside concentration tank 1,21 bottom of rotation axis
Agitating vane 22 is equipped on two side, can rotate and liquid is stirred, accelerates evaporation, 1 left upper part of concentration tank is equipped with
Feed pipe 18, feed pipe 18 are equipped with feed pipe valve 19, and control solution disengaging, 1 bottom of concentration tank is equipped with heating tube 2, heating
The model MTL2016 of pipe, can heat tank body, and 1 right end lower part of concentration tank is equipped with discharge nozzle 6, and discharge nozzle 6 is equipped with
Discharge tube valve 3, solution can be controlled to pass in and out, and 6 lower section of discharge nozzle is equipped with rewinding tank 4, can collect concentrate；Concentration tank 1 is right
End middle part is equipped with return duct 7, and liquid can be made to be back in concentration tank 1, and 7 top of return duct is equipped with gas-liquid separator 10, can
Gas and liquid are separated, 10 right end of gas-liquid separator is equipped with exhaust pipe 9, can discharge void gas, and gas-liquid separator 10 is left
End is equipped with condenser pipe 12, and steam can be cooled down, and 12 top left hand of condenser pipe is equipped with water outlet 13, and 12 bottom of condenser pipe is right
Side is equipped with water inlet 11, and 12 left end of condenser pipe is equipped with steam lead 15, makes steam from this discharge, 15 bottom of steam lead and concentration
1 top of tank connects.
6 right end of discharge nozzle is equipped with strainer 5, can prevent the large volume impurity in solution from entering rewinding tank 4, and feed pipe 18 is left
End is equipped with dustproof cover 17, can prevent dust from entering 18 foul solution of feed pipe, and 9 right end of exhaust pipe is equipped with exhaust collection tank 8, energy
Enough collecting tail gas prevents it from polluting air, is equipped with temperature measuring set 14 on the right side of 1 top of concentration tank, 14 bottom of temperature measuring set is run through
1 upper wall of concentration tank is simultaneously extended to inside concentration tank 1, can real-time monitoring temperature, heating tube 2 be in " M " shape, concentration tank 1 can be made
Homogeneous heating, the feed pipe 18, discharge nozzle 6 are connected by bolt with concentration tank 1 and junction scribbles fluid sealant, makes charging
Pipe 18,6 replacement easy to disassemble of discharge nozzle and cleaning.
In use, vacuum pump 16, heating tube 2, motor 20 are powered, dustproof cover 17 and feed inlet valve 19 are opened, it will
Solution is poured into from feed pipe 18 in concentration tank 1, is started vacuum pump 16 and is evacuated, and starting motor 20 rotates agitating vane 22
Liquid is stirred, then starts heating tube 2 and is heated；By 14 real-time monitored tank body temperature of temperature measuring set, reach
Liquid evaporation is discharged from steam lead 15 after to partially liq boiling point, and steam enters condenser pipe 12, by tap water from water inlet 11
Be passed through, water outlet 13 is discharged, to steam carry out cooling treatment, it is cooled after gas-liquid mixture enter gas-liquid separator 10, contain
The return duct 7 for having extract a small amount of active ingredient liquid from 10 bottom of gas-liquid separator is flow back into concentration tank 1, and on-condensible gas leads to
Exhaust pipe 9 is crossed into exhaust collection tank 8, until concentration process terminates, vacuum pump 16 and motor 20 is closed and stops heating, beat
Outputing expects pipe valve 3 makes concentrate be flowed into from discharge nozzle 6 in rewinding tank 4, completes concentration technology.
Part is not described in detail for the utility model, is the known technology of those skilled in the art.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that in the case where not departing from the principle of the utility model and spirit can these embodiments be carried out with a variety of variations, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of Salvia root P.E enrichment facility, it is characterised in that：Including concentration tank (1), concentration tank (1) top left hand is set
There is vacuum pump (16), motor (20) is equipped on the right side of the vacuum pump, motor (20) output terminal is equipped with rotation axis (21),
The rotation axis (21) is through concentration tank (1) upper wall and extends to concentration tank (1) inside, rotation axis (21) the bottom two side
On be equipped with agitating vane (22), concentration tank (1) left upper part is equipped with feed pipe (18), and the feed pipe (18) is equipped with
Feed pipe valve (19), concentration tank (1) bottom are equipped with heating tube (2), and concentration tank (1) the right end lower part is equipped with discharge nozzle
(6), the discharge nozzle (6) is equipped with discharging tube valve (3), and rewinding tank (4) is equipped with below the discharge nozzle (6)；The concentration
Return duct (7) is equipped in the middle part of tank (1) right end, return duct (7) top is equipped with gas-liquid separator (10), the gas-liquid separator
(10) right end is equipped with exhaust pipe (9), and gas-liquid separator (10) left end is equipped with condenser pipe (12), condenser pipe (12) top
Left side is equipped with water outlet (13), is equipped with water inlet (11) on the right side of condenser pipe (12) bottom, condenser pipe (12) left end is set
There is steam lead (15), steam lead (15) bottom is communicated with concentration tank (1) top.
2. a kind of Salvia root P.E enrichment facility according to claim 1, it is characterised in that：Discharge nozzle (6) right end
Equipped with strainer (5), feed pipe (18) left end is equipped with dustproof cover (17).
3. a kind of Salvia root P.E enrichment facility according to claim 1, it is characterised in that：Exhaust pipe (9) right end
Equipped with exhaust collection tank (8).
4. a kind of Salvia root P.E enrichment facility according to claim 1, it is characterised in that：Concentration tank (1) top
Right side is equipped with temperature measuring set (14), and temperature measuring set (14) bottom is through concentration tank (1) upper wall and extends to concentration tank
(1) it is internal.
5. a kind of Salvia root P.E enrichment facility according to claim 1, it is characterised in that：The heating tube (2) is in " M "
Shape.
6. a kind of Salvia root P.E enrichment facility according to claim 1, it is characterised in that：The feed pipe (18) goes out
Expects pipe (6) is connected by bolt with concentration tank (1) and junction scribbles fluid sealant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721529503.3U CN207445611U (en) | 2017-11-15 | 2017-11-15 | A kind of Salvia root P.E enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721529503.3U CN207445611U (en) | 2017-11-15 | 2017-11-15 | A kind of Salvia root P.E enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207445611U true CN207445611U (en) | 2018-06-05 |
Family
ID=62279924
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721529503.3U Expired - Fee Related CN207445611U (en) | 2017-11-15 | 2017-11-15 | A kind of Salvia root P.E enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207445611U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044102A (en) * | 2020-08-31 | 2020-12-08 | 江苏康祥实业集团有限公司 | A multistage evaporation plant for evaporation of sodium hypophosphite aqueous solution |
| CN113398608A (en) * | 2021-07-02 | 2021-09-17 | 江苏辰羽堂生物科技有限公司 | Poria cocos extraction and concentration device |
-
2017
- 2017-11-15 CN CN201721529503.3U patent/CN207445611U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112044102A (en) * | 2020-08-31 | 2020-12-08 | 江苏康祥实业集团有限公司 | A multistage evaporation plant for evaporation of sodium hypophosphite aqueous solution |
| CN112044102B (en) * | 2020-08-31 | 2022-02-08 | 江苏康祥实业集团有限公司 | A multistage evaporation plant for evaporation of sodium hypophosphite aqueous solution |
| CN113398608A (en) * | 2021-07-02 | 2021-09-17 | 江苏辰羽堂生物科技有限公司 | Poria cocos extraction and concentration device |
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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: 20180605 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |