CN203060870U - Multi-effective energy-saving concentration device - Google Patents
Multi-effective energy-saving concentration device Download PDFInfo
- Publication number
- CN203060870U CN203060870U CN2012206701232U CN201220670123U CN203060870U CN 203060870 U CN203060870 U CN 203060870U CN 2012206701232 U CN2012206701232 U CN 2012206701232U CN 201220670123 U CN201220670123 U CN 201220670123U CN 203060870 U CN203060870 U CN 203060870U
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- CN
- China
- Prior art keywords
- heater
- effect
- effective
- enrichment facility
- evaporator
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a multi-effective energy-saving concentration device and relates to a chemical plant. The multi-effective energy-saving concentration device comprises an extraction solution feed pump, a first effective concentration device, a second effective concentration device, a third effective concentration device, a fourth effective concentration device, a fifth effective concentration device and a concentrated solution discharge pump, wherein the first effective concentration device comprises a first effective heater and a first effective evaporator; the first effective concentration device comprises a first effective heater and a first effective evaporator; the second effective concentration device comprises a second effective heater and a second effective evaporator; the third effective concentration device comprises a third effective heater and a third effective evaporator; the fourth effective concentration device comprises a fourth effective heater and a fourth effective evaporator; and the fifth effective concentration device comprises a fifth effective heater and a fifth effective evaporator. Compared with the prior art, the multi-effective energy-saving concentration device protected by the utility model can save energy resources on one hand and can discharge liquid medicine with strong medicine flavor and high content of effective constituents on the other hand; and an energy-saving effect is good.
Description
Technical field
The utility model relates to a kind of chemical industry concentrator, particularly a kind of efficient energy-saving enrichment facility.
Background technology
Existing Chinese medicine extracts the general concentration extraction method that adopts, repeatedly soak raw material with extractor, and then extract is transported to enrichment facility concentrates, and enrichment facility generally adopts the single-action enrichment facility, it is bigger that the disadvantage of this kind method is to concentrate the steam requirement on the one hand, and energy waste is serious, and foam is arranged when being on the other hand to concentrate, and the soup flavour of a drug that come out after concentrating are lighter, and active constituent content is not high.
Summary of the invention
The purpose of this utility model just is to provide a kind of efficient energy-saving enrichment facility, and this efficient energy-saving enrichment facility can be saved the energy on the one hand, and the soup flavour of a drug that come out on the other hand are dense, and active constituent content is higher.
The technical solution of the utility model is: a kind of efficient energy-saving enrichment facility, described efficient energy-saving enrichment facility comprises the extract feed pump, first imitates enrichment facility, second imitates enrichment facility triple effect enrichment facility, the quadruple effect enrichment facility, the 5th imitates enrichment facility, the concentrate discharging pump, described first imitates enrichment facility comprises that first imitates heater and first single-effect evaporator, described second imitates enrichment facility comprises that second imitates heater and second single-effect evaporator, the triple effect enrichment facility comprises triple effect heater and third effect evaporator, the quadruple effect enrichment facility comprises quadruple effect heater and fourth evaporator, and the 5th imitates enrichment facility comprises that the 5th imitates heater and quintuple effect evaporator.
As preferably, described efficient energy-saving enrichment facility also comprises vaccum drainage means, and this vaccum drainage means comprises condenser, liquid seal can, draining pump and vavuum pump.
As preferably, described extract feed pump, concentrate discharging pump, first imitate that heater, the first single-effect evaporator inwall, second are imitated heater, the second single-effect evaporator inwall, triple effect heater, third effect evaporator inwall, quadruple effect heater, fourth evaporator inwall, the 5th imitates heater and the quintuple effect evaporator inwall all adopts the Ocr18Ni9 stainless steel.
As preferably, the described first effect heater, first single-effect evaporator, second are imitated on heater, second single-effect evaporator, third effect evaporator, quadruple effect heater, fourth evaporator, the 5th effect heater and the quintuple effect evaporator outer surface and are provided with heat-insulation layer respectively, the outer corrosion resistant plate that adopts of described heat-insulation layer.
Compared with prior art, the beneficial effects of the utility model are: because adopted the multiple-effect inspissator, therefore extract is after first effect concentrates, entering second effect, triple effect, quadruple effect and the 5th effect again further concentrates, therefore the flavour of a drug that come out are dense, the active constituent content height, and, non-foam produces in the whole concentration process, has further improved the quality of concentrate.And the heat-insulation layer that arranges respectively on the first effect heater, first single-effect evaporator, the second effect heater, second single-effect evaporator, triple effect heater, third effect evaporator, quadruple effect heater, fourth evaporator, the 5th effect heater and the quintuple effect evaporator outer surface has prevented energy loss effectively.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Efficient energy-saving enrichment facility as shown in Figure 1, this efficient energy-saving enrichment facility comprises extract feed pump 9, first imitates enrichment facility, second imitates enrichment facility, the triple effect enrichment facility, the quadruple effect enrichment facility, the 5th imitates enrichment facility, the concentrate discharging pump, first imitates enrichment facility comprises that first imitates heater 1 and first single-effect evaporator 2, second imitates enrichment facility comprises that second imitates heater 3 and second single-effect evaporator 4, the triple effect enrichment facility comprises triple effect heater 5 and third effect evaporator 6, the quadruple effect enrichment facility comprises that quadruple effect heater 7 and fourth evaporator 8, the five effect enrichment facilities comprise that the 5th imitates heater 9 and quintuple effect evaporator 10.
The efficient energy-saving enrichment facility also comprises vaccum drainage means, and this vaccum drainage means comprises condenser 11, liquid seal can 12, draining pump 17 and vavuum pump 18.
Extract feed pump 15, concentrate discharging pump 16, first are imitated heater 1, first single-effect evaporator, 2 inwalls, second are imitated heater 3, second single-effect evaporator, 4 inwalls, triple effect heater 5, third effect evaporator 6 inwalls, quadruple effect heater 7, fourth evaporator 8 inwalls, the 5th effect heater 9 and quintuple effect evaporator 10 and all adopted the Ocr18Ni9 stainless steel to make.
The first effect heater 1, first single-effect evaporator 2, second are imitated on heater 3, second single-effect evaporator 4, triple effect heater 5, third effect evaporator 6, quadruple effect heater 7, fourth evaporator 8, the 5th effect heater 9 and quintuple effect evaporator 10 outer surfaces and are provided with heat-insulation layer respectively, and the outer corrosion resistant plate that adopts of heat-insulation layer is made.
First imitates heater 1, second imitates heater 3 employing strake formula heaters.
During production, extract enters first through extract feed pump 15 backs earlier and imitates heater 1 heating under the control of feed rate meter 13, feed liquid after the heating enters first single-effect evaporator 2, moisture evaporates from top, first feed liquid of imitating after concentrating enters 3 heating of the second effect heater, and the heating back enters second and imitates inspissator 4 from the top.Second feed liquid of imitating after concentrating enters 5 heating of triple effect heater, and the heating back enters triple effect inspissator 6 from the top.Feed liquid after triple effect concentrates enters 7 heating of quadruple effect heater, and the heating back enters quadruple effect inspissator 8 from the top.Feed liquid after quadruple effect concentrates enters the 5th and imitates heater 9 heating, and the heating back enters the 5th and imitates inspissator 10 from the top.The steam that quintuple effect evaporator 8 produces enters condenser 11 and carries out condensation, and the 5th concentrate of imitating after concentrating enters the concentrate storage facility through discharging flow meter 14 from the bottom by concentrate discharging pump 16.
Extract can carry out preheating earlier in pre-hot heater 19 before entering 1 heating of the first effect heater, with the required heat of saving subsequent technique, thereby can save the energy.
Above-mentioned embodiment is only as explanation of the present utility model and unrestricted; the utility model protection domain also should comprise those apparent conversions to those skilled in the art, conversion, variation or substitute; and in the ken that those of ordinary skills possess, can also under the prerequisite that does not break away from this utility model aim, make various variations.
Claims (4)
1. efficient energy-saving enrichment facility, it is characterized in that: described efficient energy-saving enrichment facility comprises the extract feed pump, first imitates enrichment facility, second imitates enrichment facility, the triple effect enrichment facility, the quadruple effect enrichment facility, the 5th imitates enrichment facility, the concentrate discharging pump, described first imitates enrichment facility comprises that first imitates heater and first single-effect evaporator, described second imitates enrichment facility comprises that second imitates heater and second single-effect evaporator, the triple effect enrichment facility comprises triple effect heater and third effect evaporator, the quadruple effect enrichment facility comprises quadruple effect heater and fourth evaporator, and the 5th imitates enrichment facility comprises that the 5th imitates heater and quintuple effect evaporator.
2. efficient energy-saving enrichment facility according to claim 1, it is characterized in that: described efficient energy-saving enrichment facility also comprises vaccum drainage means, and this vaccum drainage means comprises condenser, liquid seal can, draining pump and vavuum pump.
3. efficient energy-saving enrichment facility according to claim 1 is characterized in that: described extract feed pump, concentrate discharging pump, first imitate that heater, the first single-effect evaporator inwall, second are imitated heater, the second single-effect evaporator inwall, triple effect heater, third effect evaporator inwall, quadruple effect heater, fourth evaporator inwall, the 5th imitates heater and the quintuple effect evaporator inwall all adopts the Ocr18Ni9 stainless steel.
4. efficient energy-saving enrichment facility according to claim 1, it is characterized in that: the described first effect heater, first single-effect evaporator, second are imitated on heater, second single-effect evaporator, third effect evaporator, quadruple effect heater, fourth evaporator, the 5th effect heater and the quintuple effect evaporator outer surface and are provided with heat-insulation layer respectively, the outer corrosion resistant plate that adopts of described heat-insulation layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206701232U CN203060870U (en) | 2012-12-07 | 2012-12-07 | Multi-effective energy-saving concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012206701232U CN203060870U (en) | 2012-12-07 | 2012-12-07 | Multi-effective energy-saving concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203060870U true CN203060870U (en) | 2013-07-17 |
Family
ID=48759700
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012206701232U Expired - Fee Related CN203060870U (en) | 2012-12-07 | 2012-12-07 | Multi-effective energy-saving concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203060870U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467247A (en) * | 2018-12-14 | 2019-03-15 | 南通三圣石墨设备科技股份有限公司 | A kind of titanium dioxide acid waste water recycling system and technique |
-
2012
- 2012-12-07 CN CN2012206701232U patent/CN203060870U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467247A (en) * | 2018-12-14 | 2019-03-15 | 南通三圣石墨设备科技股份有限公司 | A kind of titanium dioxide acid waste water recycling system and technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20131207 |