CN207507037U - One Plant Extracts material enrichment facility - Google Patents
One Plant Extracts material enrichment facility Download PDFInfo
- Publication number
- CN207507037U CN207507037U CN201721485169.6U CN201721485169U CN207507037U CN 207507037 U CN207507037 U CN 207507037U CN 201721485169 U CN201721485169 U CN 201721485169U CN 207507037 U CN207507037 U CN 207507037U
- Authority
- CN
- China
- Prior art keywords
- steam
- outlet
- condensate
- tank
- inner canister
- 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
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a Plant Extracts material enrichment facilities, including evaporator and cooling tank, the evaporator is made of inner and outer tank, the top of the inner canister is provided with steam (vapor) outlet, the steam (vapor) outlet is connected with steam pipe, the steam pipe is connected with steam inlet A, the steam inlet A is set to the top of outer tank, steam inlet B is provided with below the steam inlet A, the top of the inner canister is provided with feed inlet, the lower part of the inner canister is provided with concentrated solution outlet, the lower part of the outer tank is provided with condensate outlet, the condensate outlet is connected with condensate line, the condensate line is connected with condensate liquid import, the condensate liquid import is set to the top of cooling tank, the lower part of the cooling tank is provided with cooling water outlet；Total, the utility model has the advantages that at low cost, low energy consumption, evaporation efficiency is high and highly practical.
Description
Technical field
The utility model is related to concentrator technical field more particularly to a Plant Extracts material enrichment facilities.
Background technology
Containing natural activity component in the root of plant, stem, leaf, extraction element is used to carry out the root, stem, leaf of natural plants
Extraction so that the active constituent in herbaceous plant root, stem, leaf is dissolved in extractant, is extracted active component, is obtained plant extract
Liquid, plant extraction liquid the techniques such as are separated by filtration, compress and obtaining pure plant extraction liquid；Existing concentration extraction setting is mostly
It is using heating evaporation concentrator, this kind equipment includes vaporization chamber, vaporation-type, condensing and cooling chamber, vaporization chamber, evaporation
Formula, condensing and cooling chamber are independently arranged, of high cost, from the evaporation liquid that vaporization chamber evaporates without recycle be condensed,
Cooling obtains cooling water, and energy consumption is higher, and evaporation efficiency is low；Therefore, it is necessary to one kind, low energy consumption, the high concentrator of evaporation efficiency.
Invention content
The purpose of this utility model is to overcome the deficiencies in the prior art, and offer one kind is at low cost, low energy consumption, evaporation
Efficient and highly practical plant extract material enrichment facility.
What the purpose of this utility model was realized in：One Plant Extracts material enrichment facility, including evaporator and cold
But tank, the evaporator are made of inner and outer tank, and the top of the inner canister is provided with steam (vapor) outlet, and the steam goes out
Mouth is connected with steam pipe, and the steam pipe is connected with steam inlet A, the steam inlet A and is set to the top of outer tank, institute
Steam inlet B is provided with below the steam inlet A stated, the top of the inner canister is provided with feed inlet, the inner canister
Lower part be provided with concentrated solution outlet, the lower part of the outer tank is provided with condensate outlet, condensate outlet connection
There is condensate line, the condensate line is connected with condensate liquid import, and the condensate liquid import is set to the top of cooling tank,
The lower part of the cooling tank is provided with cooling water outlet.
Valve is both provided on the feed inlet, concentrated solution outlet and cooling water outlet.
The advantageous effect that the utility model generates：The utility model discloses a Plant Extracts material enrichment facility, packets
Evaporator and cooling tank are included, evaporator is made of inner and outer tank, hot steam is passed through into outer tank from steam inlet B, by outer
Hot steam in tank heats inner canister, the material concentration and evaporation in inner canister, and steam enters from the steam (vapor) outlet of interior upper end
It to steam pipe, enters in outer tank, inner canister is heated using the steam that inner canister evaporates, the energy through steam pipe and steam inlet A
Utilization rate is high, and low energy consumption；Steam is condensed into liquid during being heated to inner canister, and condensate liquid is gone out by the condensate liquid of outer tank lower part
Mouthful flow into condensate line, condensed liquid pipe and condensate liquid import to cooling tank, cooling water is from the cooling water outlet of cooling tank lower part
The lower part of outflow evaporator is provided with concentrated solution outlet, and valve, the concentrated liquid outlet stream of concentrate are provided on concentrated solution outlet
Go out；Evaporator and cooling tank are only set, it is at low cost, and evaporator inner canister is heated through row using the steam in evaporator, energy consumption
Low, thickening efficiency is high；Total, the utility model has the advantages that at low cost, low energy consumption, evaporation efficiency is high and highly practical.
Description of the drawings
Fig. 1 is the structure diagram of one Plant Extracts material enrichment facility of the utility model.
In figure：1st, inner canister 2, steam inlet A 3, steam inlet B 4, outer tank 5, valve 6, concentrated solution outlet
7th, condensate outlet 8, cooling water outlet 9, cooling tank 10, condensate liquid import 11, condensate line 12, feed inlet
13rd, steam (vapor) outlet 14, steam pipe.
Specific embodiment
Embodiment 1
As shown in Figure 1, a Plant Extracts material enrichment facility, including evaporator and cooling tank 9, the evaporator by
Inner canister 1 and outer tank 4 form, and the top of the inner canister 1 is provided with steam (vapor) outlet 13, and the steam (vapor) outlet 13 is connected with steam
Pipe 14, the steam pipe 14 are connected with steam inlet A2, and the steam inlet A2 is set to the top of outer tank 4, described
Steam inlet A2 below be provided with steam inlet B3, the top of the inner canister 1 is provided with feed inlet 12, the inner canister
1 lower part is provided with concentrated solution outlet 6, and the lower part of the outer tank 4 is provided with condensate outlet 10, the condensate outlet
Even 10 condensate line 11 is connected to, the condensate line 11 is connected with condensate liquid import 7, and the condensate liquid import 7 is set to
The top of cooling tank 9, the lower part of the cooling tank 9 are provided with cooling water outlet 8.
Valve is both provided on the feed inlet 12, concentrated solution outlet 6 and cooling water outlet 8.
The utility model discloses a Plant Extracts material enrichment facility, including evaporator and cooling tank, evaporator by
Inner and outer tank form, and hot steam is passed through into outer tank from steam inlet B, inner canister is added by the hot steam in outer tank
Heat, the material concentration and evaporation in inner canister, the steam (vapor) outlet of steam from interior upper end enter steam pipe, through steam pipe and steam into
Mouth A is entered in outer tank, inner canister is heated using the steam that inner canister evaporates, energy utilization rate is high, and low energy consumption；Steam is to inner canister
Liquid is condensed into during heating, condensate liquid flows into condensate line, condensed liquid pipe by the condensate outlet of outer tank lower part
With condensate liquid import to cooling tank, cooling water is provided with concentration from the lower part of the cooling water outlet outflow evaporator of cooling tank lower part
Liquid exports, the concentrated liquid outlet outflow of concentrate.
Embodiment 2
As shown in Figure 1, a Plant Extracts material enrichment facility, including evaporator and cooling tank 9, the evaporator by
Inner canister 1 and outer tank 4 form, and the top of the inner canister 1 is provided with steam (vapor) outlet 13, and the steam (vapor) outlet 13 is connected with steam
Pipe 14, the steam pipe 14 are connected with steam inlet A2, and the steam inlet A2 is set to the top of outer tank 4, described
Steam inlet A2 below be provided with steam inlet B3, the top of the inner canister 1 is provided with feed inlet 12, the inner canister
1 lower part is provided with concentrated solution outlet 6, and the lower part of the outer tank 4 is provided with condensate outlet 10, the condensate outlet
Even 10 condensate line 11 is connected to, the condensate line 11 is connected with condensate liquid import 7, and the condensate liquid import 7 is set to
The top of cooling tank 9, the lower part of the cooling tank 9 are provided with cooling water outlet 8, the feed inlet 12, concentrated solution outlet 6
Valve is both provided with on cooling water outlet 8.
The utility model discloses a Plant Extracts material enrichment facility, including evaporator and cooling tank, evaporator by
Inner and outer tank form, and hot steam is passed through into outer tank from steam inlet B, inner canister is added by the hot steam in outer tank
Heat, the material concentration and evaporation in inner canister, the steam (vapor) outlet of steam from interior upper end enter steam pipe, through steam pipe and steam into
Mouth A is entered in outer tank, inner canister is heated using the steam that inner canister evaporates, energy utilization rate is high, and low energy consumption；Steam is to inner canister
Liquid is condensed into during heating, condensate liquid flows into condensate line, condensed liquid pipe by the condensate outlet of outer tank lower part
With condensate liquid import to cooling tank, cooling water is provided with concentration from the lower part of the cooling water outlet outflow evaporator of cooling tank lower part
Liquid exports, and valve, the concentrated liquid outlet outflow of concentrate are provided on concentrated solution outlet；Evaporator and cooling tank are only set, into
This is low, and evaporator inner canister is heated through row using the steam in evaporator, and low energy consumption, and thickening efficiency is high；Total, this practicality is new
Type has the advantages that at low cost, low energy consumption, evaporation efficiency is high and highly practical.
Claims (2)
- A 1. Plant Extracts material enrichment facility, including evaporator and cooling tank, it is characterised in that：The evaporator is by interior Tank and outer tank composition, the top of the inner canister are provided with steam (vapor) outlet, and the steam (vapor) outlet is connected with steam pipe, described Steam pipe is connected with steam inlet A, and the steam inlet A is set to the top of outer tank, is set below the steam inlet A Steam inlet B is equipped with, the top of the inner canister is provided with feed inlet, and the lower part of the inner canister is provided with concentrated solution outlet, The lower part of the outer tank is provided with condensate outlet, and the condensate outlet is connected with condensate line, the condensate liquid Pipe is connected with condensate liquid import, and the condensate liquid import is set to the top of cooling tank, the lower part setting of the cooling tank There is cooling water outlet.
- 2. Plant Extracts material enrichment facility as described in claim 1, it is characterised in that：The feed inlet, concentration Liquid exports and is both provided with valve on cooling water outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721485169.6U CN207507037U (en) | 2017-11-09 | 2017-11-09 | One Plant Extracts material enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721485169.6U CN207507037U (en) | 2017-11-09 | 2017-11-09 | One Plant Extracts material enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207507037U true CN207507037U (en) | 2018-06-19 |
Family
ID=62537598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721485169.6U Expired - Fee Related CN207507037U (en) | 2017-11-09 | 2017-11-09 | One Plant Extracts material enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207507037U (en) |
-
2017
- 2017-11-09 CN CN201721485169.6U patent/CN207507037U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103893991B (en) | A kind of Chinese medicine thermal circulation extracting concentrating method | |
| CN203469533U (en) | Continuous reflux extraction device of traditional Chinese medicine | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN203763899U (en) | Chinese medicinal herb thermal circulating extracting and concentrating system | |
| CN103638690A (en) | Boiling and extracting device and method for honeysuckle | |
| CN102363085A (en) | Method and special device for extracting and concentrating water extraction liquid medicine of Chinese medicine | |
| CN102031200A (en) | Method for extracting wide fragrant (basil) plant essential oil | |
| CN207507037U (en) | One Plant Extracts material enrichment facility | |
| CN103908799B (en) | A kind of extraction concentrates all-in-one | |
| CN205115421U (en) | High -efficient extraction device that retrieves of plant extract fragrance | |
| CN2754696Y (en) | Thermal reflux energy-saving extracting concentrator with double direction and effective | |
| CN209500817U (en) | A kind of vaporising device suitable for sticky thick paste | |
| CN201415068Y (en) | Device for extracting and concentrating effective ingredient of traditional Chinese medicine | |
| CN204434587U (en) | Fruit wine vacuum distillation device | |
| CN207445611U (en) | A kind of Salvia root P.E enrichment facility | |
| CN207468568U (en) | A kind of forced-ventilated plants essential oil extraction equipment | |
| CN101612487A (en) | The extraction of effective components of Chinese medicinal and concentrator and extraction and method for concentration | |
| CN203281053U (en) | Quadruple-effect downstream falling-film evaporator for preparation of inositol | |
| CN103598980B (en) | A kind of Chinese medicine extraction enrichment facility | |
| CN204910802U (en) | Self -circulation MVR heat pump evaporation system | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN205381978U (en) | Solar energy sea water desalting device | |
| CN204134243U (en) | Novel evaporation atomization Despumation device | |
| CN204319832U (en) | A kind of low temperature extracts concentrated equipment integrating | |
| CN202315398U (en) | Device specially for extracting and concentrating water extraction medicinal liquid of traditional Chinese medicine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180619 Termination date: 20211109 |