CN202478616U - Dual-jet concentration device - Google Patents
Dual-jet concentration device Download PDFInfo
- Publication number
- CN202478616U CN202478616U CN2012200808772U CN201220080877U CN202478616U CN 202478616 U CN202478616 U CN 202478616U CN 2012200808772 U CN2012200808772 U CN 2012200808772U CN 201220080877 U CN201220080877 U CN 201220080877U CN 202478616 U CN202478616 U CN 202478616U
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- China
- Prior art keywords
- collection chamber
- nozzle
- tank
- pressure
- pressure jet
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- 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 - Lifetime
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Abstract
The utility model relates to a dual-jet concentration device which comprises a gas collection chamber concentration tank and a nozzle arranged in the gas collection chamber concentration tank, and is characterized in that an inlet of the nozzle is connected onto a jet water tank through a jet water pump; an outlet of the nozzle is communicated with a neck of a high-pressure jet device; an inlet end of the high-pressure jet device is connected onto a cold water tank through a high-pressure jet water pump; an outlet of the high-pressure jet device is communicated with the cold water tank; and the top of the gas collection chamber concentration tank is further connected with a hot material pipe. When the dual-jet concentration device disclosed by the utility model runs, water discharged by the high-pressure jet water pump passes through the high-pressure jet device to produce negative pressure at the neck of the high-pressure jet device, and water vapor produced from intake concentrated materials in vacuum is condensed; and the water vapor produced by the concentrated materials in the gas collection chamber concentration tank in vacuum is induced into the neck of the high-pressure jet device by water mist sprayed by the nozzle so as to accelerate condensation. In such a way, materials are circulated to obtain a concentrated product..
Description
Technical field
The utility model belongs to the enrichment facility technical field, is specifically related to a kind of pair of injection enrichment facility.
Background technology
In recent years, scientific and technical personnel do a lot of work the Steam Heating that released one after another enrichment facility for the energy utilization rate that improves enrichment facility both at home and abroad; The heat pump enrichment facility, the heating using microwave enrichment facility all has an evaporation and concentration jar in these devices; Heating is by concentrated liquid in jar, obtains concentrated product after making its boiling vaporization, and the shortcoming of these devices is that equipment investment is many; Energy consumption is big, and energy utilization rate is low.
Summary of the invention
The purpose of this invention is to provide a kind of pair of injection enrichment facility, can remedy the above-mentioned deficiency of prior art.
Two injection enrichment facilities of the utility model have a collection chamber concentration tank and the nozzle that is installed in the collection chamber concentration tank, it is characterized in that the inlet of nozzle is connected on the injection water tank through jet pump; The outlet of nozzle is communicated with the throat of high-pressure injector; The arrival end of above-mentioned high-pressure injector is connected on the cold water storage cistern through the high-pressure injection water pump; The outlet of high-pressure injector is communicated with cold water storage cistern; The top of described collection chamber concentration tank also is connected with heat material pipe.
Above-mentioned collection chamber concentration tank below is equipped with tapping valve.
The below of above-mentioned injection water tank is equipped with blowoff valve.
Overflow pipe is equipped with in the upper end of above-mentioned cold water storage cistern, and cold water storage cistern in cooling tube is housed.
The device of the utility model is when operation, and when high-pressure injector was passed through in the draining of high-pressure injection water pump, in throat's generation negative pressure of high-pressure injector, the steam that the concentrated material of suction produces under vacuum got into condensation; And the water smoke of nozzle ejection produces concentrated material in the collection chamber concentration tank under vacuum steam is induced into the throat of high-pressure injector, to quicken condensation.So recycle stock obtains concentrated product.The device of the utility model has the efficient height, saves the energy, advantages such as equipment investment is few, operating maintenance is simple, safety, health, integrated protection environment.Adaptable across food, pharmacy, chemical industry, produce industries such as fresh water, cold water.
Description of drawings
Fig. 1: the general structure sketch map of the utility model.
The specific embodiment
As shown in Figure 1; Two injection enrichment facilities of the utility model include a collection chamber concentration tank 5; Nozzle 4 is arranged in the collection chamber concentration tank 5, and the inlet of nozzle 4 links to each other with the outlet of jet pump 7 through pipeline 6, and the inlet of jet pump 7 is connected with injection water tank 9 through pipeline 8.The outlet of collection chamber concentration tank 5 is connected with high-pressure injector 3.The inlet of high-pressure injector 3 is linked to each other by the outlet of pipeline 2 with high-pressure injection water pump 1, and the inlet of high-pressure injection water pump 1 is communicated with cold water storage cistern 14 through pipeline 17; The outlet of high-pressure injection water pump 1 links to each other with the inlet of high-pressure injector 3 through pipeline 2, and the outlet of high-pressure injector 3 links to each other with cold water storage cistern 14.Cooling tube 16 is housed in the cold water storage cistern 14; Blowoff valve 15,10 is equipped with in the bottom of cold water storage cistern 14, injection water tank 9, and overflow pipe 13 is equipped with on the top of cold water storage cistern 14.Concentrate is got in the top of collection chamber concentration tank 5 by heat material pipe 12, and concentrated product is discharged by the tapping valve 11 of collection chamber concentration tank 5 bottoms.
The device of the utility model is in operation; When high-pressure injector 3 is passed through in the draining of high-pressure injection water pump 1; Throat at high-pressure injector 3 produces negative pressure; Suck the steam that concentrate produces and carry out condensation under vacuum, the water smoke of nozzle 4 ejections is induced into high-pressure injector 3 and quickens condensation concentrates steam that material produces in the collection chamber concentration tank 5 under vacuum again, and so recycle stock obtains concentrated product.
Claims (5)
1. a two injection enrichment facility has a collection chamber concentration tank (5) and is installed in the nozzle (4) in the collection chamber concentration tank (5), it is characterized in that the inlet of described nozzle (4) is connected on the injection water tank (9) through jet pump (7); The outlet of nozzle (4) is communicated with the throat of high-pressure injector (3); The arrival end of above-mentioned high-pressure injector (3) is connected on the cold water storage cistern (14) through high-pressure injection water pump (1); The outlet of high-pressure injector (3) is communicated with cold water storage cistern (14); And the top of collection chamber concentration tank (5) also is connected with heat material pipe (12).
2. device as claimed in claim 1 is characterized in that the below of described collection chamber concentration tank (5) is equipped with tapping valve (11).
3. device as claimed in claim 1 is characterized in that the below of described injection water tank (9) is equipped with blowoff valve (10).
4. device as claimed in claim 1 is characterized in that overflow pipe (13) is equipped with in the upper end of described cold water storage cistern (14).
5. device as claimed in claim 1 is characterized in that cooling tube (16) is equipped with in the inside of described cold water storage cistern (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200808772U CN202478616U (en) | 2012-03-06 | 2012-03-06 | Dual-jet concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200808772U CN202478616U (en) | 2012-03-06 | 2012-03-06 | Dual-jet concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202478616U true CN202478616U (en) | 2012-10-10 |
Family
ID=46953080
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200808772U Expired - Lifetime CN202478616U (en) | 2012-03-06 | 2012-03-06 | Dual-jet concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202478616U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103785185A (en) * | 2014-02-11 | 2014-05-14 | 莱州市新力复合材料有限公司 | Evaporation and concentration system and method |
-
2012
- 2012-03-06 CN CN2012200808772U patent/CN202478616U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103785185A (en) * | 2014-02-11 | 2014-05-14 | 莱州市新力复合材料有限公司 | Evaporation and concentration system and method |
| CN103785185B (en) * | 2014-02-11 | 2016-03-23 | 莱州市新力复合材料有限公司 | A kind of evaporation concentration system and method for concentration |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160817 Address after: 200000 Shanghai city Xuhui District Xi Road No. 242 building 4 Room 305 Patentee after: Shanghai Ting Feng computer room Engineering Co., Ltd Address before: 266003 Shandong province Qingdao City Dengzhou Road No. 39 Building 2 unit 11 Room 202 Patentee before: Li Liangsong |
|
| CX01 | Expiry of patent term |
Granted publication date: 20121010 |
|
| CX01 | Expiry of patent term |