CN217092113U - Rapid cooling negative pressure flash system - Google Patents
Rapid cooling negative pressure flash system Download PDFInfo
- Publication number
- CN217092113U CN217092113U CN202122282448.5U CN202122282448U CN217092113U CN 217092113 U CN217092113 U CN 217092113U CN 202122282448 U CN202122282448 U CN 202122282448U CN 217092113 U CN217092113 U CN 217092113U
- Authority
- CN
- China
- Prior art keywords
- steam
- pump
- negative pressure
- rapid cooling
- hot press
- 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.)
- Active
Links
Images
Abstract
The utility model provides a rapid cooling negative pressure flash distillation system belongs to the milk production mechanical equipment field. The problems of long cooling time and large ice water consumption of the existing heat exchanger are solved. It includes flash tank, hot press pump, condenser and material pump, be equipped with lateral wall feed inlet, bottom discharge mouth and top steam outlet on the flash tank, the lateral wall feed inlet sets up along a jar body tangential direction, the bottom discharge mouth links to each other with the material pump, the hot press pump is provided with steam inlet, induction port and gas outlet, the top steam outlet of flash tank links to each other with the induction port of hot press pump, the steam inlet of hot press pump links to each other with the live steam pipeline, the gas outlet of hot press pump links to each other with the condenser. It is mainly used for dairy production.
Description
Technical Field
The utility model belongs to dairy production mechanical equipment field especially relates to a rapid cooling negative pressure flash distillation system.
Background
Need use the heat sink to carry out cooling treatment to the material in whey production process so that follow-up crystallization, the heat sink of now generally using is plate-type or tubular heat exchanger, adopts the indirect cooling's mode, and the cooling time is longer, influences production efficiency, and the frozen water consumption is great, is unfavorable for energy saving and consumption reduction.
SUMMERY OF THE UTILITY MODEL
The utility model discloses a solve the problem among the prior art, provide a rapid cooling negative pressure flash distillation system.
In order to achieve the above purpose, the utility model adopts the following technical scheme: the utility model provides a rapid cooling negative pressure flash distillation system, it includes flash tank, hot press pump, condenser and material pump, be equipped with lateral wall feed inlet, bottom discharge mouth and top steam outlet on the flash tank, the lateral wall feed inlet sets up along a jar body tangential direction, the bottom discharge mouth links to each other with the material pump, the hot press pump is provided with steam inlet, induction port and gas outlet, the top steam outlet of flash tank links to each other with the induction port of hot press pump, the steam inlet of hot press pump links to each other with the live steam pipeline, the gas outlet of hot press pump links to each other with the condenser.
Furthermore, a top steam outlet of the flash tank is connected with a suction port of the hot-pressing pump through a first steam communicating pipe.
Furthermore, the flash tank is connected with a first steam communicating pipe in a welding mode, and the first steam communicating pipe is connected with an air suction port of the hot-pressure pump through a flange.
Furthermore, a steam inlet is formed in the condenser, and an air outlet of the hot-pressure pump is connected with the steam inlet through a second steam communicating pipe.
Furthermore, the air outlet of the hot-pressure pump is connected with a second steam communicating pipe through a flange, and the second steam communicating pipe is connected with a steam inlet of the condenser in a welding mode.
Furthermore, a cooling water inlet, a cooling water outlet, a condensed water outlet and a vacuum pump interface are arranged on the condenser, the cooling water inlet enters cooling water, the cooling water outlet discharges cooling water, the condensed water outlet discharges condensed water, and the vacuum pump interface is connected with a vacuum pump.
Further, the vacuum pump discharges noncondensable gas.
Furthermore, the bottom discharge hole is in a conical seal head form.
Furthermore, a cleaning ball is arranged inside the flash tank.
Further, the flash system uses 304 stainless steel.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model provides a current heat exchanger cooling time long, the big problem of frozen water consumption. The utility model discloses can shorten the cooling time greatly, improve production efficiency, can reduce frozen water consumption, the energy saving. Meets the food sanitation requirement and can be cleaned in situ without disassembly.
Drawings
Fig. 1 is a schematic view of a working flow of a rapid cooling negative pressure flash evaporation system according to the present invention;
fig. 2 is a schematic view of a section structure of a side wall feed inlet of the flash tank.
1-flash evaporation tank, 2-first steam communicating pipe, 3-hot pressure pump, 4-second steam communicating pipe, 5-condenser, 6-vacuum pump, 7-material pump.
Detailed Description
The technical solution in the embodiment of the present invention will be clearly and completely explained below with reference to the drawings in the embodiment of the present invention.
The embodiment is described with reference to fig. 1-2, and a rapid cooling negative pressure flash evaporation system comprises a flash evaporation tank 1, a hot press pump 3, a condenser 5 and a material pump 7, wherein the flash evaporation tank 1 is provided with a side wall feed inlet, a bottom discharge port and a top steam outlet, the side wall feed inlet is arranged along the tangential direction of a tank body, the bottom discharge port is connected with the material pump 7, the hot press pump 3 is provided with a steam inlet, an air suction port and a gas outlet, the top steam outlet of the flash evaporation tank 1 is connected with the air suction port of the hot press pump 3, the steam inlet of the hot press pump 3 is connected with a raw steam pipeline, and the gas outlet of the hot press pump 3 is connected with the condenser 5.
In the embodiment, a top steam outlet of a flash tank 1 is connected with an air suction port of a hot-pressing pump 3 through a first steam communicating pipe 2, the flash tank 1 is connected with the first steam communicating pipe 2 in a welding manner, the first steam communicating pipe 2 is connected with the air suction port of the hot-pressing pump 3 through a flange, a condenser 5 is provided with a steam inlet, an air outlet of the hot-pressing pump 3 is connected with the steam inlet through a second steam communicating pipe 4, the air outlet of the hot-pressing pump 3 is connected with the second steam communicating pipe 4 through a flange, the second steam communicating pipe 4 is connected with the steam inlet of the condenser 5 in a welding manner, the condenser 5 is provided with a cooling water inlet, a cooling water outlet, a condensed water outlet and a vacuum pump interface, the cooling water inlet is filled with cooling water, the cooling water outlet is used for discharging cooling water, the condensed water outlet is used for discharging condensed water, the vacuum pump interface is connected with a vacuum pump 6, the vacuum pump 6 is used for discharging non-condensable gas, a bottom discharge port is in a conical seal head form, avoiding the residue of the feed liquid. The inside cleaning ball that is provided with of flash tank ensures the cleaning performance. The flash distillation system adopts 304 stainless steel material, and the surface all satisfies food level health requirement, and the seal ring that uses all adopts food level material.
This embodiment material is tangent line flow mode entering flash tank 1's inside through flash tank 1's lateral wall feed inlet, the material can be followed a jar wall rotatory flow, flow is dispersed downwards along a jar wall to the spiral mode, the great so flash evaporation velocity of heat-transfer surface is extremely fast, the hot press pump 3 with flash tank 1 UNICOM can use raw steam to extract the inside gas of flash tank 1 as power and make the inside vacuum environment that forms of flash tank 1 simultaneously, consequently, high temperature material gets into flash tank 1 inside back moisture can flash evaporation rapidly, material temperature can reduce then flow from flash tank 1 bottom discharge gate rapidly simultaneously. The condenser 5 communicated with the air outlet of the hot-pressing pump 3 condenses and recovers the steam discharged by the hot-pressing pump 3. The time of the whole material cooling process is extremely short, the requirement can be met only within 1 second, the cooling water of the condenser 5 can be recycled, and the steam condensate can be recycled, so that the energy is saved.
The above detailed description is given to the rapid cooling negative pressure flash evaporation system provided by the present invention, and the specific examples are applied herein to explain the principle and the implementation of the present invention, and the description of the above examples is only used to help understanding the method and the core idea of the present invention; meanwhile, for the general technical personnel in the field, according to the idea of the present invention, there are changes in the specific implementation and application scope, to sum up, the content of the present specification should not be understood as the limitation of the present invention.
Claims (10)
1. The utility model provides a rapid cooling negative pressure flash distillation system which characterized in that: it includes flash tank (1), hot press pump (3), condenser (5) and material pump (7), be equipped with lateral wall feed inlet, bottom discharge mouth and top steam outlet on flash tank (1), the lateral wall feed inlet sets up along jar body tangential direction, the bottom discharge mouth links to each other with material pump (7), hot press pump (3) are provided with steam inlet, induction port and gas outlet, the top steam outlet of flash tank (1) links to each other with the induction port of hot press pump (3), the steam inlet of hot press pump (3) links to each other with raw steam pipeline, the gas outlet of hot press pump (3) links to each other with condenser (5).
2. The rapid cooling negative pressure flash system of claim 1, wherein: and a top steam outlet of the flash tank (1) is connected with a suction port of the hot-pressing pump (3) through a first steam communicating pipe (2).
3. The rapid cooling negative pressure flash system of claim 2, wherein: flash tank (1) and first steam communicating pipe (2) welding link to each other, first steam communicating pipe (2) pass through the flange with the induction port of heat pump (3) and link to each other.
4. The rapid cooling negative pressure flash system according to claim 1, wherein: the condenser (5) is provided with a steam inlet, and the air outlet of the hot-pressure pump (3) is connected with the steam inlet through a second steam communicating pipe (4).
5. The rapid cooling negative pressure flash system of claim 4, wherein: the gas outlet of the hot-pressing pump (3) is connected with the second steam communicating pipe (4) through a flange, and the second steam communicating pipe (4) is connected with the steam inlet of the condenser (5) in a welding mode.
6. The rapid cooling negative pressure flash system of claim 1, wherein: the condenser (5) is provided with a cooling water inlet, a cooling water outlet, a condensed water outlet and a vacuum pump interface, the cooling water inlet enters cooling water, the cooling water outlet discharges cooling water, the condensed water outlet discharges condensed water, and the vacuum pump interface is connected with a vacuum pump (6).
7. The rapid cooling negative pressure flash system of claim 6, wherein: the vacuum pump (6) discharges non-condensable gas.
8. The rapid cooling negative pressure flash system of claim 1, wherein: the bottom discharge hole is in a conical end socket form.
9. The rapid cooling negative pressure flash system of claim 1, wherein: a plurality of cleaning balls are arranged inside the flash tank (1).
10. The rapid cooling negative pressure flash system of claim 1, wherein: the flash system uses 304 stainless steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122282448.5U CN217092113U (en) | 2021-09-18 | 2021-09-18 | Rapid cooling negative pressure flash system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122282448.5U CN217092113U (en) | 2021-09-18 | 2021-09-18 | Rapid cooling negative pressure flash system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217092113U true CN217092113U (en) | 2022-08-02 |
Family
ID=82576355
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122282448.5U Active CN217092113U (en) | 2021-09-18 | 2021-09-18 | Rapid cooling negative pressure flash system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217092113U (en) |
-
2021
- 2021-09-18 CN CN202122282448.5U patent/CN217092113U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204034294U (en) | The board-like forced-circulation evaporator of novel triple effect | |
| CN201181170Y (en) | Evaporating air cooler | |
| CN203355311U (en) | Improved MVR evaporator | |
| CN204034287U (en) | Board-like thermodynamic steam Compression Evaporation device | |
| CN217092113U (en) | Rapid cooling negative pressure flash system | |
| CN208155095U (en) | A kind of mating condenser for steam turbine | |
| CN102778136A (en) | Easily cleaned condenser | |
| CN217297904U (en) | System for recovering waste heat of blast furnace slag flushing water | |
| CN211394332U (en) | Ethanol distillation condenser | |
| CN211346401U (en) | Vacuum low-temperature dehydration equipment | |
| CN204313671U (en) | A kind of water-cooling type ASuitable Air Coolerwith Efficiency | |
| CN203447784U (en) | Anti-scaling circulating type tobacco extracting solution concentration device | |
| CN207379322U (en) | A kind of cooling tower liquid matchmaker forced condensation fog dispersal collecting system | |
| CN1188654C (en) | Constant flow velocity steam-water heat exchanger | |
| CN112811492A (en) | Device for treating production line wastewater through combination of heat pump concentration and drying device | |
| CN215464433U (en) | Traditional chinese medicine reation kettle of rapid condensation | |
| CN201434606Y (en) | Air-cooled condenser for making wine | |
| CN204963609U (en) | Multiple -effect graphite heat exchanger | |
| CN206121196U (en) | Pneumatic forced circulation triple -effect evaporator | |
| CN108917418B (en) | Concurrent tube bundle vacuumizing device for air cooling island | |
| CN205803440U (en) | A kind of wine brewing condensing plant | |
| CN209027320U (en) | A kind of Air-Cooling Island fair current tube bank vacuum evacuation device | |
| CN103691137B (en) | Fish pressed liquor concentrator | |
| CN220038855U (en) | Water trap is used in production of modified calcium hydrate | |
| CN210473469U (en) | Multistage condensing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221028 Address after: Room A201, No. 60 Shimao Avenue, Building 11, Innovation and Entrepreneurship Plaza, Science and Technology Innovation City, Harbin Hi tech Industrial Development Zone, 150,028, Heilongjiang Province Patentee after: HEILONGJIANG REALGOAL TECHNOLOGY CO.,LTD. Patentee after: HEILONGJIANG FEIHE DAIRY Co.,Ltd. Address before: 150028 2nd floor, 62 Shimao Avenue, Songbei District, Harbin City, Heilongjiang Province Patentee before: HEILONGJIANG REALGOAL TECHNOLOGY CO.,LTD. |
|
| TR01 | Transfer of patent right |