CN201415101Y - Gas water separator of freeze dryer - Google Patents
Gas water separator of freeze dryer Download PDFInfo
- Publication number
- CN201415101Y CN201415101Y CN2009203032564U CN200920303256U CN201415101Y CN 201415101 Y CN201415101 Y CN 201415101Y CN 2009203032564 U CN2009203032564 U CN 2009203032564U CN 200920303256 U CN200920303256 U CN 200920303256U CN 201415101 Y CN201415101 Y CN 201415101Y
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- water
- type drier
- freezing type
- water separator
- sewage
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Abstract
The utility model relates to a gas water separator of freeze dryer, and particularly to a gas water separator of a freeze dryer. The gas water separator comprises a sealing barrel body and water obstructing baffles. The utility model is characterized in that an air inlet pipe is provided at the lower side wall of the sealing barrel body. The upper part of the sealing barrel body is provided with an air discharge pipe. Two sides of the sealing barrel body at the upper side of the air inlet pipe are provided with a plurality of water obstructing baffles which are staggered from one another. A silk screen layer is provided at the sealing barrel body between the water obstructing baffles and the air discharge pipe. A water outlet is provided at the connection between the water obstructing baffles and the sealing barrel body. The bottom of the sealing barrel body is provided with a sewage opening. The gas water separator of freeze dryer provided by the utility model has the characteristicsof excellent gas water separation effect, low cost and long service life.
Description
Technical field
The utility model relates to a kind of water separator, especially a kind of freeze drier water separator.
Background technology
Freezing type drier mainly is made up of refrigeration system, heat-exchange system, carbonated drink piece-rate system and corresponding electric control system four parts.Saturated compressed air is in cooling procedure, can in heat exchanger, gather a large amount of condensation waters, also there are a large amount of more tiny water droplet water smokes to be suspended in and enter the precool heat exchanger device in the compressed air, after these water droplet water smokes enter the precooling regenerator, along with the part " double evaporation-cooling " of carrying out of heat exchange is returned gas phase, make in the finished product gas moisture increase cause dew point to rise, the aqueous water that another part has little time to evaporate then enters user pipe with air-flow, make in the gas equipment of downstream aqueous water to occur, certainly will influence the quality of product like this.For the aqueous water that condenses in the heat transfer process can well be separated from finished product gas, thereby guarantee the quality of finished product gas, it is essential that water separator is set, and is obligato vitals in the freezing type drier.
Existing freezing type drier gas-liquid separator generally adopts baffle separator, whirlwind separator, or the steam-water separator of micron filter precision filter core is housed.For baffle separator, compressed air enters separator along air inlet pipe, and air-flow is subjected to stopping of baffle plate, is mixed in just can the adhere surface that is trapped in baffle plate and be accumulated into the bigger drop of particle diameter at baffle edge and fall into separator bottom of airborne water droplet.For whirlwind separator, compressed air portion's pipeline from container tangentially enters separator, utilizes the centrifugal force drop that severe is bigger that produces when rotatablely moving to separate with air-flow.The drawback that both exist all is to separate the drop of the above greater particle size of 10 μ m, and the drop that can't separate than small particle diameter causes finished product gas dew point to rise.For the steam-water separator that micron filter precision filter core is housed,, cost of manufacture height, service life lack, need regularly to change (generally being about 8000 hours), operating cost height though separating effect is preferably arranged.
Summary of the invention
The utility model mainly is the technical problem that solves that existing in prior technology carbonated drink is separated thoroughly, production cost is high, service life is short etc., and a kind of simple in structure, steam-water separation effect good, cost is low, the life-span is grown freeze drier water separator is provided.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals: a kind of freezing type drier water separator, it comprises sealing staving and water retaining separater, the lower sides that it is characterized in that described sealing staving is provided with air inlet pipe, the top of sealing staving is provided with blast pipe, the sealing staving both sides of air inlet pipe upside are provided with some interlaced water retaining separaters, be provided with silk screen layer in the sealing staving between water retaining separater and the blast pipe, junction between water retaining separater and the sealing staving is provided with discharge outlet, and the bottom of sealing staving is provided with the sewage mouth.The compressed air that has a large amount of drop liquid mists enters gas-liquid separator by the freezing type drier evaporimeter, evenly on the bump water retaining separater, the lower surface of the sticking water retaining separater of a large amount of water droplets builds up into the bigger drop of particle diameter and falls into sealing staving bottom along cylinder inner surface, prevents to be taken away by air-flow.The water droplet of small particle diameter then can't capture along with compressed air enters silk screen layer because of baffle plate, under the descending centrifugation layer by layer of the silk screen of different meshes, enter the discharge outlet of water retaining separater bottom along cylinder inner surface, fall into sealing staving bottom along cylinder inner surface more at last, prevent to be taken away by air-flow.The compressed air that separates the drying that finishes rises to sealing staving top and enters blast pipe again, enters at last and carries out heat exchange in the precooling regenerator.Big water gaging of separating and impurity are discharged by the sewage mouth.
As preferably, described water retaining separater and horizontal line have the 15-45 degree elevation angle, and the downside of water retaining separater is provided with some dash hooks.The dash hook has strengthened the surface area of water fender, makes it can adhere to drop greatly.
As preferably, described blast pipe is vertical with the sealed cylinder axis, inserts inner barrel, and is provided with from the horizontal by the angular cut at 30-45 degree angle, and otch up.Make compressed air after filtering not be with unsegregated liquid mist to enter the precooling regenerator.
As preferably, described air inlet pipe is vertical with the cylindrical shell axis, inserts inner barrel, and is provided with from the horizontal by 30-45 degree angle angular cut, and otch down.Make a large amount of drop liquid mists that have that come out from evaporimeter strike on the water retaining separater again to even distribution after the turning down.
As preferably, the bottom of described sealing staving is provided with a truncated cone-shaped polywater ring, and described sewage mouth is located at the inboard of polywater ring.The water that is separated accumulates in the truncated cone-shaped polywater ring, prevents to be taken away by air-flow.
As preferably, described sewage mouth links to each other with sewage pipe, and the sewage pipe end is provided with a blowoff valve, electronics water trap of sewage pipe bypass.Big water gaging of separating and impurity are entered by sewage outlet in the blow-off pipe, and water discharges via electronics water trap self-timing.And be deposited on impurity such as welding slag in the blow-off pipe, iron filings, discharge by the regular Blowoff ball valve of opening.
As preferably, the described sewage pipe bypass that is provided with the electronics water trap is provided with an electricity row service valve.When blow-off pipe takes place to stop up, can arrange service valve by electricity and handle.
The beneficial effect that brings of the present utility model is, the beneficial effects of the utility model are: effectively separate a large amount of drop liquid mists that come out with air-flow in the freezing type drier evaporimeter 1., finished product gas dew point can not risen because of gas-liquid separator separates efficient is low, guarantee the freezing type drier stable performance.2. simple in structure, cheap, no operating cost.3. owing to added Blowoff ball valve, blow-off line is difficult for stopping up, and has prolonged the service life of electronics water trap greatly.4. equipment is convenient for installation and maintenance, simple.
Description of drawings
Accompanying drawing 1 is a kind of structural representation of the present utility model.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: accompanying drawing 1 is a kind of structural representation of the present utility model.The utility model is a kind of freezing type drier water separator, it comprises a sealing staving 1 and some water retaining separaters 3, the lower sides of sealing staving is provided with horizontally disposed air inlet pipe 11, this air inlet pipe stretches into sealing staving middle part, the top of sealing staving is provided with and is horizontally disposed with blast pipe 12, and this blast pipe stretches into sealing staving middle part.Air inlet pipe and blast pipe are respectively equipped with down and 45 degree angular cuts up.The sealing staving both sides of air inlet pipe upside are provided with some interlaced water retaining separaters, and the downside of water retaining separater is provided with some dash hooks 4.Be provided with silk screen layer 2 in the sealing staving between water retaining separater and the blast pipe, junction between water retaining separater and the sealing staving is provided with discharge outlet, the bottom of sealing staving is provided with a truncated cone-shaped polywater ring 5, and the sealing staving bottom of polywater ring inboard is provided with sewage mouth 6, and the sewage mouth links to each other with blow-off pipe 10.The blow-off pipe end is provided with a blowoff valve 9, electronics water trap 8 of blow-off pipe bypass.The sewage pipe bypass of electronics water trap is provided with an electricity row service valve 7.
The compressed air that has a large amount of drop liquid mists enters gas-liquid separator by the freezing type drier evaporimeter, because of the admission line of cutting sth. askew circulates down, upwards return on the water retaining separater that evenly impinges upon cross arrangement after striking sealing staving bottom, a large amount of water droplets sticks on the lower surface and dash crotch of water retaining separater, build up into the bigger drop of particle diameter and fall in the truncated cone-shaped polywater ring of separator bottom, prevent to be taken away by air-flow along cylinder inner surface.The water droplet of small particle diameter then can't capture along with compressed air enters silk screen layer because of baffle plate, under the descending centrifugation layer by layer of the silk screen of different meshes, enter the discharge outlet of water retaining separater bottom along cylinder inner surface, fall in the trapezoidal round platform in separator bottom along cylinder inner surface more at last, prevent to be taken away by air-flow.The compressed air that separates the drying that finishes rises to sealing staving top and enters discharge duct again, enters at last and carries out heat exchange in the precooling regenerator.
Big water gaging of separating and impurity are entered by sewage outlet in the sewage pipe, and water is via the discharging of electronics water trap self-timing, and are deposited on impurity such as welding slag in the sewage pipe, iron filings, discharge by the regular Blowoff ball valve of opening.
Claims (10)
1. freezing type drier water separator, it comprises sealing staving (1) and water retaining separater (3), the lower sides that it is characterized in that described sealing staving is provided with air inlet pipe (11), the top of sealing staving is provided with blast pipe (12), the sealing staving both sides of air inlet pipe upside are provided with some interlaced water retaining separaters, be provided with silk screen layer (2) in the sealing staving between water retaining separater and the blast pipe, junction between water retaining separater and the sealing staving is provided with discharge outlet, and the bottom of sealing staving is provided with sewage mouth (6).
2. a kind of freezing type drier water separator according to claim 1 is characterized in that described water retaining separater and horizontal line have the 15-45 degree elevation angle, and the downside of water retaining separater is provided with some dash hooks (4).
3. a kind of freezing type drier water separator according to claim 1 is characterized in that described blast pipe is vertical with the sealed cylinder axis, inserts inner barrel, and is provided with from the horizontal by the angular cut at 30-45 degree angle, and otch up.
4. according to claim 1 or 2 or 3 described a kind of freezing type drier water separators, it is characterized in that described air inlet pipe is vertical with the cylindrical shell axis, insert inner barrel, and be provided with that otch down from the horizontal by 30-45 degree angle angular cut.
5. according to claim 1 or 2 or 3 described a kind of freezing type drier water separators, it is characterized in that the bottom of described sealing staving is provided with a truncated cone-shaped polywater ring, described sewage mouth is located at the inboard of polywater ring.
6. a kind of freezing type drier water separator according to claim 4 is characterized in that the bottom of described sealing staving is provided with a truncated cone-shaped polywater ring, and described sewage mouth is located at the inboard of polywater ring.
7. according to claim 1 or 2 or 3 described a kind of freezing type drier water separators, it is characterized in that described sewage mouth links to each other with sewage pipe, the sewage pipe end is provided with a blowoff valve, electronics water trap of sewage pipe bypass.
8. a kind of freezing type drier water separator according to claim 4 is characterized in that described sewage mouth links to each other with sewage pipe, and the sewage pipe end is provided with a blowoff valve, electronics water trap of sewage pipe bypass.
9. a kind of freezing type drier water separator according to claim 7 is characterized in that the described sewage pipe bypass that is provided with the electronics water trap is provided with an electricity row service valve.
10. a kind of freezing type drier water separator according to claim 8 is characterized in that the described sewage pipe bypass that is provided with the electronics water trap is provided with an electricity row service valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203032564U CN201415101Y (en) | 2009-05-18 | 2009-05-18 | Gas water separator of freeze dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203032564U CN201415101Y (en) | 2009-05-18 | 2009-05-18 | Gas water separator of freeze dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201415101Y true CN201415101Y (en) | 2010-03-03 |
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ID=41791511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009203032564U Expired - Lifetime CN201415101Y (en) | 2009-05-18 | 2009-05-18 | Gas water separator of freeze dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201415101Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691236A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Dual-layer baffle-type natural gas washing tank |
| CN105879511A (en) * | 2016-06-15 | 2016-08-24 | 超滤动力（安徽）有限公司 | Efficient water removal separator assembly |
| CN106823670A (en) * | 2017-02-21 | 2017-06-13 | 安徽海纳森环境科技有限公司 | A kind of device of the hot and humid organic exhaust gas of condensation separation |
| CN110180305A (en) * | 2019-05-30 | 2019-08-30 | 天津科技大学 | Rotate alternating expression ultrasonic wave Despumation device |
| CN110668627A (en) * | 2019-09-20 | 2020-01-10 | 天津科技大学 | High-efficiency ultrasonic rotary film deoxidization head |
| CN112944860A (en) * | 2021-02-09 | 2021-06-11 | 嘉兴知途信息咨询有限公司 | Fabric drying method |
-
2009
- 2009-05-18 CN CN2009203032564U patent/CN201415101Y/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103691236A (en) * | 2013-12-17 | 2014-04-02 | 成都展望能源机械有限公司 | Dual-layer baffle-type natural gas washing tank |
| CN105879511A (en) * | 2016-06-15 | 2016-08-24 | 超滤动力（安徽）有限公司 | Efficient water removal separator assembly |
| CN106823670A (en) * | 2017-02-21 | 2017-06-13 | 安徽海纳森环境科技有限公司 | A kind of device of the hot and humid organic exhaust gas of condensation separation |
| CN110180305A (en) * | 2019-05-30 | 2019-08-30 | 天津科技大学 | Rotate alternating expression ultrasonic wave Despumation device |
| CN110668627A (en) * | 2019-09-20 | 2020-01-10 | 天津科技大学 | High-efficiency ultrasonic rotary film deoxidization head |
| CN112944860A (en) * | 2021-02-09 | 2021-06-11 | 嘉兴知途信息咨询有限公司 | Fabric drying method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: HANGZHOU SHANLI PURIFY EQUIPMENT CORPORATION Free format text: FORMER NAME: HANGZHOU SHANLI PURIFY EQUIPMENT CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang province 311107 Renhe Town of Yuhang District Zhang Road No. 220 Patentee after: HANGZHOU SHANLI PURIFY EQUIPMENT CORPORATION Address before: Hangzhou City, Zhejiang province 311107 Renhe Town of Yuhang District Zhang Road No. 220 Patentee before: Hangzhou Shanli Purify Equipment Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20100303 |
|
| CX01 | Expiry of patent term |