CN206853145U - Continous way medicinal extract enrichment machine - Google Patents
Continous way medicinal extract enrichment machine Download PDFInfo
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- CN206853145U CN206853145U CN201720327778.2U CN201720327778U CN206853145U CN 206853145 U CN206853145 U CN 206853145U CN 201720327778 U CN201720327778 U CN 201720327778U CN 206853145 U CN206853145 U CN 206853145U
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- medicinal extract
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- vaporization chamber
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Abstract
The utility model provides a kind of continous way medicinal extract enrichment machine, including double pipe heater, and feed pump connection sleeve pipe calorifier inlets, double pipe heater outlet connection heating chamber, heating chamber connection vaporization chamber, vaporization chamber is above product receiving tank；Surge tank is provided with upper opening, intermediate openings and bottom opening；The upper opening connection vacuum pump inlet of surge tank, vacuum pump outlet connection vacuum buffer tank；The lower openings of the intermediate openings connection condenser of surge tank, the upper opening connection vapour liquid separator of condenser, vapour liquid separator connection vaporization chamber upper opening；The bottom opening connection turbulence pump of surge tank.The utility model improves product concentration densities, and concentration time is short, while energy consumption is small, and cost is low；And this equipment can be concentrated uninterruptedly, substantially increase operating efficiency；Can also full-automatic on-line cleaning, device interior is pollution-free to producing alternately product entirely without dead angle.
Description
Technical field
A kind of concentrator is the utility model is related to, more particularly to it is a kind of for plant extraction liquid, food and drink concentration life
The continous way medicinal extract enrichment machine of production.
Background technology
In current plant extraction liquid, food and drink concentration production, there is portioned product requirement to be concentrated to 1: 1.4~1: 1.8
(paste), and because of product effective ingredient characteristic issues, be heated at high temperature for a long time, effective ingredient can be caused to lose or lose completely
Effect.
Traditional concentrator, following defect be present：
1st, product can only be concentrated into 1: 1.2~1: 1.4 or so；
2nd, concentration process spends time length, and product is heated at high temperature for a long time, and product contacts easy gelatinization with equipment wall surface
And coking, material easy to foaming can not often concentrate completely, or serious run is expected in concentration process, causes product to lose.
3rd, concentration process energy consumption is very big, and cost is higher.
Utility model content
The technical problems to be solved in the utility model is how to improve the concentrated solution density of concentrator, shorten concentration process
Time, reduce concentration process energy consumption.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is to provide a kind of continous way medicinal extract enrichment machine,
It is characterized in that：Including double pipe heater, feed pump connection sleeve pipe calorifier inlets, double pipe heater outlet connects heating chamber,
Heating chamber connects vaporization chamber, and vaporization chamber is above product receiving tank；
Surge tank is provided with upper opening, intermediate openings and bottom opening；The upper opening connection vacuum pump inlet of surge tank,
Vacuum pump outlet connects vacuum buffer tank；The lower openings of the intermediate openings connection condenser of surge tank, the top of condenser is opened
Mouth connection vapour liquid separator, vapour liquid separator connection vaporization chamber upper opening；The bottom opening connection turbulence pump of surge tank.
Preferably, in addition to switch board, the heating chamber, vaporization chamber, double pipe heater, feed pump, turbulence pump, vavuum pump
It is connected with switch board.
Preferably, the vaporization chamber bottom is provided with cooling section, and density tester and liquid level gauge, cooling section are provided with cooling section
Bottom is provided with valve；Valve is above the product receiving tank.
It is highly preferred that the density tester, liquid level gauge and valve are all connected with the switch board.
Preferably, the vacuum buffer tank top is provided with steam drain.
It is highly preferred that also including automatic cleaning system, automatic cleaning system connects the switch board.
Further, the automatic cleaning system includes centrifugal pump, and centrifugal pump inlet connects the product receiving tank, centrifugation
Pump discharge connects the pipeline between the feed pump and double pipe heater；Centrifugal pump connects the switch board.
The method of work of above-mentioned continous way medicinal extract enrichment machine, step are：
Step 1：Start vavuum pump, vaporization chamber is vacuumized；
Step 2：Material liquid is delivered to double pipe heater by feed pump, double pipe heater is preliminary by the material liquid in it
Heating chamber is sent into after preheating；
Step 3：Steam in heating chamber heats material liquid, and the temperature material after heating enters vaporization chamber, and material liquid is true
Moisture flash evapn under dummy status, water vapour are evacuated to vapour liquid separator by vavuum pump and carry out vapor-liquid separation, the completion liquid after evaporation
Product drops to vaporization chamber bottom with gravity, and is emitted into product receiving tank；
Step 4：In vapour liquid separator, the liquid deposition after separation enters in vapour liquid separator bottom, the gas after separation
Enter condenser, the water entrainment portions gas being condensed into enters surge tank and carries out secondary gas-liquid separation；
Step 5：In surge tank, liquid is discharged outside unit by the bottom opening of surge tank by turbulence pump；Gas is by delaying
The upper opening for rushing tank enters vacuum buffer tank progress gas-liquid separation three times by vavuum pump；
Step 6：In vacuum buffer tank, liquid deposition is in vacuum buffer pot bottom, and gas is through vacuum buffer tank top
Steam drain is discharged.
Preferably, in the step 3, the completion liquid product after evaporation drops to vaporization chamber bottom with gravity, completes liquid quilt
Cooling, no longer explosive evaporation；The density for completing liquid is detected by density tester, and whether analytic density data are qualified, according to
Testing result adjusts systematic parameter, until the density for completing liquid is qualified；When liquid is completed in vaporization chamber bottom reaches setting liquid level, steam
Hair room bottom valve automatically opens up, and will complete liquid and is emitted into product receiving tank, concentration process is completed.
The cleaning method of above-mentioned continous way medicinal extract enrichment machine, step are：Water enters from product receiving tank through centrifugal pump to be fed
Pump and double pipe heater, the water in double pipe heater enter heating chamber, enter back into vaporization chamber, finally discharge, complete to material system
The automatic on-line cleaning of system.
Device provided by the utility model overcomes the deficiencies in the prior art, product density can be concentrated into 1: 1.4~1:
1.8, concentration time is short, avoids product caused loss heated for a long time, while energy consumption is small, and cost is low；And this equipment can connect
It is continuous to concentrate incessantly, substantially increase operating efficiency；Can also full-automatic on-line cleaning, device interior is entirely without dead angle, to handing over
Fork production product is pollution-free.
Brief description of the drawings
Fig. 1 is the continous way medicinal extract enrichment machine structural representation that the present embodiment provides.
Embodiment
With reference to specific embodiment, the utility model is expanded on further.It should be understood that these embodiments are merely to illustrate this
Utility model rather than limitation the scope of the utility model.In addition, it is to be understood that reading the content of the utility model instruction
Afterwards, those skilled in the art can make various changes or modifications to the utility model, and these equivalent form of values equally fall within this Shen
Please appended claims limited range.
The continous way medicinal extract enrichment machine structural representation that Fig. 1 provides for the present embodiment, described continous way medicinal extract enrichment machine
Delayed by heating chamber 1, vaporization chamber 2, product receiving tank 3, condenser 4, vapour liquid separator 5, double pipe heater 6, surge tank 7, vacuum
Rush the composition such as tank 8, feed pump 9, switch board 10, turbulence pump 11, vavuum pump 12, centrifugal pump 13.
Feed pump 9 passes through the entrance of pipeline connection sleeve pipe heater 6, the outlet of double pipe heater 6 connection heating chamber 1, heating chamber 1
Vaporization chamber 2 is connected, vaporization chamber 2 is located at the top of product receiving tank 3.The bottom of vaporization chamber 2 is provided with cooling section, and product receiving tank 3 is located at
Below cooling section.Density tester and liquid level gauge are provided with cooling section, cooling section bottom is provided with valve.Density tester, liquid level
Meter and valve are all connected with switch board 10.
Surge tank 7 is provided with upper opening, intermediate openings and bottom opening.The upper opening connection vavuum pump 12 of surge tank 7
Entrance, vavuum pump 12 outlet connection vacuum buffer tank 8, the top of vacuum buffer tank 8 is provided with steam drain.The middle part of surge tank 7
The lower openings of opening connection condenser 4, the upper opening connection vapour liquid separator 5 of condenser 4, the connection of vapour liquid separator 5 are steamed
Send out the upper opening of room 2.The bottom opening connection turbulence pump 11 of surge tank 7.
Heating chamber 1, vaporization chamber 2, double pipe heater 6, feed pump 9, turbulence pump 11, vavuum pump 12, centrifugal pump 13 etc. with
Switch board 10 connects.
Automatic cleaning system includes centrifugal pump 13, the entrance of centrifugal pump 13 connection product receiving tank 3, the outlet of centrifugal pump 13 connection
Pipeline between feed pump 9 and double pipe heater 6.
The continous way medicinal extract enrichment machine that the present embodiment provides is taken out in use, by the pressure in vaporization chamber 2 by vavuum pump 12
To -0.08Mpa, after the vacustat of room 2 to be evaporated, material liquid is delivered to double pipe heater 6 by feed pump 9, sleeve pipe adds
Material liquid in it is tentatively preheated to 40 DEG C or so by hot device 6, and material liquid then is sent into heating chamber 1 by pipeline.
High steam in heating chamber 1, material liquid was heated to 70 DEG C within several seconds, the temperature material after heating enters
Vaporization chamber 2, moisture flash evapn, water vapour are evacuated to vapour liquid separator 5 by vavuum pump 12 and carry out vapour material liquid under vacuum conditions
Liquid separates.In vapour liquid separator 5, liquid deposition enters condenser 4 in the bottom of vapour liquid separator 5, gas, the water folder being condensed into
Band part gas carries out secondary gas-liquid separation into surge tank 7.In surge tank 7, liquid is passed through by the bottom opening of surge tank 7
Turbulence pump 11 is discharged outside unit；Gas enters vacuum buffer tank 8 by the upper opening of surge tank 7 by vavuum pump 12.Gas exists
Further condensed in vacuum buffer tank 8, liquid deposition is in the bottom of vacuum buffer tank 8, steam discharge of the gas through the top of vacuum buffer tank 8
Mouth discharge.
In vaporization chamber 2, the completion liquid product after evaporation drops to the cooling section of the bottom of vaporization chamber 2 with gravity, will complete liquid
Whether quick cooling, makes the no longer explosive evaporation of completion liquid product, qualified by density tester detection completion liquid, and automatically analyzes
Whether qualified detect data, make vapor (steam) temperature and steaming in amendment adjustment, including the adjustment of charging pump frequency and heating chamber 1 automatically
The adjustment of hair amount.When liquid is completed in the bottom of vaporization chamber 2 reaches setting liquid level, bottom valve automatically opens up, and will complete liquid and is emitted into
In product receiving tank 3, i.e., concentration process is completed.This equipment continuously can be concentrated uninterruptedly.
During cleaning, water enters feed pump 9 and double pipe heater 6, double pipe heater 6 from product receiving tank 3 through centrifugal pump 13
Interior water enters heating chamber 1, enters back into vaporization chamber 2, finally discharges, and completes the automatic on-line cleaning to material system.
Experiment shows that product density can be concentrated to 1: 1.4~1 by the continous way medicinal extract enrichment unit that the present embodiment provides:
1.8, and concentration time is short, efficiency high.Acceptable full-automatic on-line cleaning, device interior are right entirely without dead angle, noresidue simultaneously
Producing alternately product is pollution-free, complies fully with GMP requirements.
Claims (7)
- A kind of 1. continous way medicinal extract enrichment machine, it is characterised in that：Including double pipe heater (6), the heating of feed pump (9) connection sleeve pipe Device (6) entrance, double pipe heater (6) outlet connection heating chamber (1), heating chamber (1) connection vaporization chamber (2), vaporization chamber (2) are located at Above product receiving tank (3)；Surge tank (7) is provided with upper opening, intermediate openings and bottom opening；The upper opening connection vavuum pump of surge tank (7) (12) entrance, vavuum pump (12) outlet connection vacuum buffer tank (8)；Under the intermediate openings connection condenser (4) of surge tank (7) Portion's opening, the upper opening connection vapour liquid separator (5) of condenser (4), vapour liquid separator (5) connection vaporization chamber (2) top are opened Mouthful；The bottom opening connection turbulence pump (11) of surge tank (7).
- A kind of 2. continous way medicinal extract enrichment machine as claimed in claim 1, it is characterised in that：Also include switch board (10), it is described Heating chamber (1), vaporization chamber (2), double pipe heater (6), feed pump (9), turbulence pump (11), vavuum pump (12) are and switch board (10) connect.
- A kind of 3. continous way medicinal extract enrichment machine as claimed in claim 2, it is characterised in that：Vaporization chamber (2) bottom is provided with Cooling section, cooling section is interior to be provided with density tester and liquid level gauge, and cooling section bottom is provided with valve；Valve receives located at the product Above tank (3).
- A kind of 4. continous way medicinal extract enrichment machine as claimed in claim 3, it is characterised in that：The density tester, liquid level gauge The switch board (10) is all connected with valve.
- A kind of 5. continous way medicinal extract enrichment machine as claimed in claim 1, it is characterised in that：Vacuum buffer tank (8) top Provided with steam drain.
- A kind of 6. continous way medicinal extract enrichment machine as claimed in claim 2, it is characterised in that：Also include automatic cleaning system, from Dynamic purging system connects the switch board (10).
- A kind of 7. continous way medicinal extract enrichment machine as claimed in claim 6, it is characterised in that：The automatic cleaning system include from Heart pump (13), centrifugal pump (13) entrance connect the product receiving tank (3), and centrifugal pump (13) outlet connects the feed pump (9) Pipeline between double pipe heater (6)；Centrifugal pump (13) connects the switch board (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720327778.2U CN206853145U (en) | 2017-03-30 | 2017-03-30 | Continous way medicinal extract enrichment machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720327778.2U CN206853145U (en) | 2017-03-30 | 2017-03-30 | Continous way medicinal extract enrichment machine |
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| Publication Number | Publication Date |
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| CN206853145U true CN206853145U (en) | 2018-01-09 |
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| CN201720327778.2U Active CN206853145U (en) | 2017-03-30 | 2017-03-30 | Continous way medicinal extract enrichment machine |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106943757A (en) * | 2017-03-30 | 2017-07-14 | 上海东富龙科技股份有限公司 | A kind of continous way medicinal extract enrichment machine and its work, cleaning method |
-
2017
- 2017-03-30 CN CN201720327778.2U patent/CN206853145U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106943757A (en) * | 2017-03-30 | 2017-07-14 | 上海东富龙科技股份有限公司 | A kind of continous way medicinal extract enrichment machine and its work, cleaning method |
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