CN204952315U - Tertiary foam formula separator that removes - Google Patents
Tertiary foam formula separator that removes Download PDFInfo
- Publication number
- CN204952315U CN204952315U CN201520655126.2U CN201520655126U CN204952315U CN 204952315 U CN204952315 U CN 204952315U CN 201520655126 U CN201520655126 U CN 201520655126U CN 204952315 U CN204952315 U CN 204952315U
- Authority
- CN
- China
- Prior art keywords
- foam removal
- formula
- separator cylinder
- removal assembly
- type foam
- 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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Abstract
The utility model discloses a tertiary foam formula separator that removes, including separator cylinder (41), rotating wash bowl (42), be equipped with the silk screen formula and remove foam subassembly (43) in this separator cylinder (41) still be equipped with plate dislocation formula in separator cylinder (41) and remove foam subassembly (45) the flash steam export (46) of separator cylinder (41) is located to be equipped with baffle baffling formula and is removed foam subassembly (48). The utility model discloses loop through this plate dislocation formula, silk screen formula, baffle baffling formula and remove the three level of foam subassembly and else remove the foam process, reached good defoaming effect, effectively avoid damaging the compressor of MVR evaporimeter, reached evaporation effect and the quality of stablizing whole vaporization system.
Description
Technical field
The present invention relates to mechanized equipment field, specifically relate to a kind of separator being applied to the evaporimeter of the conglomeraties such as pharmacy, food, chemical industry, environmental protection.
Background technology
At present, mechanical steam recompression (being called for short MVR) evaporimeter is that recycling Secondary-steam heating principle makes the feed liquid in evaporator system maintain fluidized state, improve the concentration of feed liquid to reach technical requirement, it comprises feed pump, condensate pump, discharging pump, vavuum pump, heater, separator, compressor.Separator in MVR evaporimeter generally adopts single-stage foam removal (for screen type foam removal assembly) mode, fine foam and fine drop is caused not to remove completely, along with the indirect steam in separator enters compressor, and compressor is running up (compressor rotary speed is generally at 20000r/m), these fine foam and fine drop indirect steam pipeline pool together can become large and high-speed impact on the impeller of compressor, thus major injury is caused to it.
Summary of the invention
The object of the invention is to overcome above-mentioned deficiency, and a kind of multilevel defoaming, foam removal three grades of foam removal formula separators of good performance are provided.
Object of the present invention realizes by following technical solution: three grades of foam removal formula separators, comprise Membrane Separator Cylinder for CFB Boiler, rotating wash bowl, at this Membrane Separator Cylinder for CFB Boiler built with screen type foam removal assembly, plate dislocation type foam removal assembly is also housed in described Membrane Separator Cylinder for CFB Boiler, baffle plate deflector type foam removal assembly is housed in the indirect steam exit of described Membrane Separator Cylinder for CFB Boiler.
After adopting the present invention, successively by the foam removal process of three ranks of this plate dislocation type, screen type, baffle plate deflector type foam removal assembly, reach excellent foam removal effect, effectively avoid the compressor damaging MVR evaporimeter, reach the evaporation effect and quality of stablizing whole vapo(u)rization system.
Accompanying drawing explanation
Below in conjunction with accompanying drawing and embodiment, the present invention is described in further detail.
Fig. 1 is the mounting structure schematic diagram of the present invention's three grades of foam removal formula separators.
Detailed description of the invention
Known with reference to Fig. 1, the present invention's three grades of foam removal formula separators, comprise Membrane Separator Cylinder for CFB Boiler 41, rotating wash bowl 42, at this Membrane Separator Cylinder for CFB Boiler 41 built with screen type foam removal assembly 43 (for known technology), plate dislocation type foam removal assembly 45 is also housed in described Membrane Separator Cylinder for CFB Boiler 41, exports 46 places (by indirect steam pipeline 49) at the indirect steam of described Membrane Separator Cylinder for CFB Boiler 41 and baffle plate deflector type foam removal assembly 48 is housed.
Wherein, described Membrane Separator Cylinder for CFB Boiler 41 is also equipped with looks lamp 44, visor 47.Airflow hole 50 on the multilayer plate 52 of described plate dislocation type foam removal assembly 45 (plate at least two-layer above and present lower placement) mutually staggers; The baffle plate 51 of described baffle plate deflector type foam removal assembly 48 intersects with vapor flow approach axis or vertical and leave gap, to make the motion in deflector type in this baffle plate deflector type foam removal assembly of the isolated gas of separator, the bottom of described baffle plate deflector type foam removal assembly 48 is connected with Membrane Separator Cylinder for CFB Boiler 41.
For gas isolated in separator, the first order adopts plate dislocation type foam removal assembly, adopts multilayer stainless steel plate, the airflow hole mutual dislocation on it, make steam helically formula to rise and the macrofoam of large drop is eliminated.The second level adopts traditional screen type foam removal assembly, again can be separated gas-liquid, and fine drop foam is eliminated further.The third level adopts baffle plate deflector type foam removal assembly, changes the moving line of steam, and make can not completely except the fine drop foam in devaporation can be gathered on baffle plate, gets back in Membrane Separator Cylinder for CFB Boiler bottom the cone being finally left to this baffle plate deflector type foam removal assembly again.For this reason, realize foam removal rate at 99% the above object, reach the effect of high-efficient defoaming.
The evaporimeter energy consumption of the present invention's application is low, operate steadily, security performance is high, and it is widely used in multiple industries such as pharmacy, food, chemical industry, environmental protection, alcoholic, milk processed, beverage, sugaring.
Claims (2)
1. three grades of foam removal formula separators, comprise Membrane Separator Cylinder for CFB Boiler (41), rotating wash bowl (42), at this Membrane Separator Cylinder for CFB Boiler (41) built with screen type foam removal assembly (43), it is characterized in that: plate dislocation type foam removal assembly (45) is also housed in described Membrane Separator Cylinder for CFB Boiler (41), at indirect steam outlet (46) place of described Membrane Separator Cylinder for CFB Boiler (41), baffle plate deflector type foam removal assembly (48) is housed.
2. three grades of foam removal formula separators as claimed in claim 1, is characterized in that: the airflow hole (50) on the multilayer plate (52) of described plate dislocation type foam removal assembly (45) mutually staggers; The baffle plate (51) of described baffle plate deflector type foam removal assembly (48) intersects with vapor flow approach axis or vertical and leave gap, to make the motion in deflector type in this baffle plate deflector type foam removal assembly of the isolated steam of separator, the bottom of described baffle plate deflector type foam removal assembly (48) is connected with Membrane Separator Cylinder for CFB Boiler (41).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520655126.2U CN204952315U (en) | 2015-08-17 | 2015-08-17 | Tertiary foam formula separator that removes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520655126.2U CN204952315U (en) | 2015-08-17 | 2015-08-17 | Tertiary foam formula separator that removes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204952315U true CN204952315U (en) | 2016-01-13 |
Family
ID=55047414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520655126.2U Expired - Fee Related CN204952315U (en) | 2015-08-17 | 2015-08-17 | Tertiary foam formula separator that removes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204952315U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108579114A (en) * | 2018-05-24 | 2018-09-28 | 周封 | Evaporation concentration system material trapping recycling and separator |
-
2015
- 2015-08-17 CN CN201520655126.2U patent/CN204952315U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108579114A (en) * | 2018-05-24 | 2018-09-28 | 周封 | Evaporation concentration system material trapping recycling and separator |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160113 Termination date: 20180817 |