CN203540347U - Reverse-osmosis oleuropein concentration device - Google Patents
Reverse-osmosis oleuropein concentration device Download PDFInfo
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- CN203540347U CN203540347U CN201320698725.3U CN201320698725U CN203540347U CN 203540347 U CN203540347 U CN 203540347U CN 201320698725 U CN201320698725 U CN 201320698725U CN 203540347 U CN203540347 U CN 203540347U
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- pipeline
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- osmosis membrane
- reverse osmosis
- heat exchanger
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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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Abstract
The utility model relates to a reverse-osmosis oleuropein concentration device which comprises a material supply pump, a stoste box with a finished product discharging opening, a stainless steel high-pressure pump and a reverse-osmosis membrane component, wherein the tail end of the material supply pump is connected with a precision filter through a pipeline I; the precision filter is connected with the top of the stoste box through a pipeline II; the bottom of the stoste box is connected with the reverse-osmosis membrane component through a pipeline III by the stainless steel high-pressure pump; a concentrated liquid outlet of the reverse-osmosis membrane component is connected with a heat exchanger through a pressure gauge, a pressure adjustment valve and a concentrated liquid flowmeter in sequence; one end of the heat exchanger is connected with the top of the stoste box through a pipeline IV; a permeated liquid outlet of the reverse-osmosis membrane component is connected with a residual liquid discharging opening through a permeated liquid flowmeter. The reverse-osmosis oleuropein concentration device is low in energy consumption, simple in flow and energy-saving during working under normal temperature and can prevent deterioration of the quality of a raw material and loss of nutritious components; meanwhile, the color change of the raw material is small.
Description
Technical field
The utility model relates to food, health products manufacture field, relates in particular to the reverse osmosis concentrated compression apparatus of oleuropein.
Background technology
Oleuropein (Oleuropein) is a kind of active material in olive growing leaves, there is stronger oxidation resistance, can alleviate the degree of oxidation of low-density lipoprotein, prevention coronary heart disease, atherosclerotic generation, also can releive vascular smooth muscle and reducing blood pressure, is widely used in medicine and healthcare industry.The bitter glucoside extract of high-purity olive only has a handful of countries to develop product in the world.Conventional method organic solvent extraction destroys composition, increases production cost, also causes environmental pollution simultaneously, and extraction step is loaded down with trivial details, and the production cycle is long.
Form to reduced pressure concentration after the concentrated lixiviate of employing conventionally of oleuropein in current China industrial production, energy consumption is large, the high-temperature heating of long period can destroy again part nutritional labeling wherein, its major defect is: energy consumption is high, thickening temperature is high, in concentration process, quality easily worsens, nutrition and fragrance matter can lose, at high temperature concentrated pigment composition changes greatly, destroyed nature, after concentrated, lmpurities is more, the one-time investment of equipment is large, floor space is large, auxiliary equipment is many, operate more complicated, the shortcomings such as operating cost height.
Utility model content
It is low that technical problem to be solved in the utility model is to provide a kind of energy consumption of carrying out at normal temperatures, can prevent that the deterioration of material quality and loss, the color and luster of nutritional labeling and fragrance matter from changing the reverse osmosis concentrated compression apparatus of little oleuropein.
For addressing the above problem, the reverse osmosis concentrated compression apparatus of oleuropein described in the utility model, is characterized in that: this device comprises charging pump, is provided with the stoste case of finished product floss hole, stainless steel high-pressure pump and reverse osmosis membrane assembly; The end of described charging pump is connected with accurate filter by pipeline I, and this accurate filter is connected with described stoste box top by pipeline II; The bottom of described stoste case is connected with described reverse osmosis membrane assembly by described stainless steel high-pressure pump through pipeline III; Concentrated solution outlet in described reverse osmosis membrane assembly is connected with heat exchanger by Pressure gauge, pressure regulator valve, concentrated solution discharge meter successively, and one end of this heat exchanger is connected with described stoste box top by pipeline IV; The liquid outlet that sees through in described reverse osmosis membrane assembly is connected with residual liquid discharge mouth by seeing through flow quantity meter.
In described pipeline I, pipeline II, pipeline III, be equipped with control valve.
Described heat exchanger is provided with electron temperature probe.
The utility model compared with prior art has the following advantages:
1, owing to being provided with reverse osmosis membrane assembly in the utility model, this reverse osmosis membrane assembly has the selective feature that sees through other macromolecular substances, isolated lixiviate chemical substance, therefore, the utility model not only carries out that energy consumption is low at normal temperatures, flow process is simple, save the energy, and can prevent the deterioration of material quality and the loss of nutritional labeling, the color and luster of raw material variation is simultaneously little, is specially adapted to the processing of heat-sensitive substance.After adopting the utility model, resulting feed purity is high.
2, owing to being provided with Pressure gauge, pressure regulator valve in the utility model, therefore, effective controlled circulation feed liquid operating pressure.
3, owing to being provided with heat exchanger in the utility model, therefore, effective controlled circulation feed liquid running temperature; Meanwhile, heat exchanger is provided with electron temperature probe, therefore, and can be according to design temperature auto-controll operation temperature.
4, the little and simple structure of the utility model equipment volume, expense is lower, efficiency is higher, is applicable to the technique such as separated, concentrated, purifying, clarification of organic matter and inorganic matter.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the specific embodiment of the present utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
In figure: 1-charging pump, 2-accurate filter, 3-stoste case, 4-stainless steel high-pressure pump, 5-reverse osmosis membrane assembly, 6-Pressure gauge, 7-pressure regulator valve, 8-heat exchanger 9-through flow quantity meter 10-concentrated solution discharge meter.
The specific embodiment
As shown in Figure 1, the reverse osmosis concentrated compression apparatus of oleuropein, this device comprises charging pump 1, is provided with the stoste case 3 of finished product floss hole, stainless steel high-pressure pump 4 and reverse osmosis membrane assembly 5.
The end of charging pump 1 is connected with accurate filter 2 by pipeline I, and this accurate filter 2 is connected with stoste case 3 tops by pipeline II; The bottom of stoste case 3 is connected with reverse osmosis membrane assembly 5 by stainless steel high-pressure pump 4 through pipeline III; Concentrated solution outlet in reverse osmosis membrane assembly 5 is connected with heat exchanger 8 by Pressure gauge 6, pressure regulator valve 7, concentrated solution discharge meter 10 successively, and one end of this heat exchanger 8 is connected with stoste case 3 tops by pipeline IV; The liquid outlet that sees through in reverse osmosis membrane assembly 5 is connected with residual liquid discharge mouth by seeing through flow quantity meter 9.
Wherein: in pipeline I, pipeline II, pipeline III, be equipped with control valve.Heat exchanger 8 is provided with electron temperature probe.
During use, pending oleuropein leaching liquor passes through the rear inflow stoste of accurate filter 2 case 3 by charging pump 1, by stainless steel high-pressure pump 4, be input in reverse osmosis membrane assembly 5, after reverse osmosis membrane assembly 5 concentrating and separating, the concentrated solution outlet of concentrate by reverse osmosis membrane assembly 5 enters 3 circulations of stoste case and is concentrated into finished product after Pressure gauge 6, pressure regulator valve 7, concentrated solution discharge meter 10, heat exchanger 8, and discharges from finished product floss hole; Seeing through liquid discharges from residual liquid discharge mouth after seeing through flow quantity meter 9 by the liquid outlet that sees through of reverse osmosis membrane assembly 5.
Claims (3)
1. the reverse osmosis concentrated compression apparatus of oleuropein, is characterized in that: this device comprises charging pump (1), is provided with the stoste case (3) of finished product floss hole, stainless steel high-pressure pump (4) and reverse osmosis membrane assembly (5); The end of described charging pump (1) is connected with accurate filter (2) by pipeline I, and this accurate filter (2) is connected with described stoste case (3) top by pipeline II; The bottom of described stoste case (3) is connected with described reverse osmosis membrane assembly (5) by described stainless steel high-pressure pump (4) through pipeline III; Concentrated solution outlet in described reverse osmosis membrane assembly (5) is connected with heat exchanger (8) by Pressure gauge (6), pressure regulator valve (7), concentrated solution discharge meter (10) successively, and one end of this heat exchanger (8) is connected with described stoste case (3) top by pipeline IV; The liquid outlet that sees through in described reverse osmosis membrane assembly (5) is connected with residual liquid discharge mouth by seeing through flow quantity meter (9).
2. the reverse osmosis concentrated compression apparatus of oleuropein as claimed in claim 1, is characterized in that: in described pipeline I, pipeline II, pipeline III, be equipped with control valve.
3. the reverse osmosis concentrated compression apparatus of oleuropein as claimed in claim 1, is characterized in that: described heat exchanger (8) is provided with electron temperature probe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320698725.3U CN203540347U (en) | 2013-11-07 | 2013-11-07 | Reverse-osmosis oleuropein concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320698725.3U CN203540347U (en) | 2013-11-07 | 2013-11-07 | Reverse-osmosis oleuropein concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203540347U true CN203540347U (en) | 2014-04-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320698725.3U Expired - Fee Related CN203540347U (en) | 2013-11-07 | 2013-11-07 | Reverse-osmosis oleuropein concentration device |
Country Status (1)
| Country | Link |
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| CN (1) | CN203540347U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030473A (en) * | 2014-06-23 | 2014-09-10 | 深圳市凯尔迪光电科技有限公司 | COD separation device and method for organic wastewater |
-
2013
- 2013-11-07 CN CN201320698725.3U patent/CN203540347U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030473A (en) * | 2014-06-23 | 2014-09-10 | 深圳市凯尔迪光电科技有限公司 | COD separation device and method for organic wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140416 Termination date: 20141107 |
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| EXPY | Termination of patent right or utility model |