CN203389507U - Cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator - Google Patents
Cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator Download PDFInfo
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- CN203389507U CN203389507U CN201320024129.7U CN201320024129U CN203389507U CN 203389507 U CN203389507 U CN 203389507U CN 201320024129 U CN201320024129 U CN 201320024129U CN 203389507 U CN203389507 U CN 203389507U
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- drier
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Abstract
The utility model discloses a cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator which is widely applied to the drying industry. The steam-water separator comprises a barrel body (1); an air inlet (2) is arranged at one side of the upper part of the barrel body, and an air outlet (14) is arranged at the other side of the upper part of the barrel body; the air inlet (2) is connected with an inner barrel (7); a temperature and humidity sensor (8) is arranged in the top of the barrel body (1); a sterilizer (11) is arranged at the side of the temperature and humidity sensor (8); the inner barrel (7) is internally provided with an internal spiral type flow deflector (6); a screen filter (5) is arranged at the lower side in the barrel body (1) and at the outer side of the lower part of the inner barrel (7). The cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator is simple and efficient as well as energy-saving and environment-friendly, has the functions of sterilization and disinfection, enables the heat energy to be completely used in a circulating way, and is excellent in effect especially for the products such as marine products, fish, tea, tobacco and medicinal materials which need to keep the original flavor in the drying process.
Description
Technical field
The utility model relates to a kind of dedusting dehumidifying carbonated drink separation equipment, the definite full recuperation of heat dedusting dehumidifying of a kind of cyclone type hot-air carbonated drink seperator that says.
Background technology
Grain, fruits and vegetables, flesh of fish water content are high; can not deposit and transport; deposit and transport and will dry; oven dry will produce hot and humid gas; hot and humid gas directly discharges the energy and will waste; newly enter air-borne bacteria seriously polluted; affect product quality; some hot and humid gas suspension is many; can not meet production, life is too high to air moisture content and suspension is too many requirement; for product quality improves to greatest extent, in order to save the needs of the energy and environmental protection, after all will processing the heat energy gas of needs utilization, recycle.
Existing airdryer generally adopts condensing dehumidifier, and its shortcoming is that investment is many, and production cost is high, and treatment effeciency is low, and can not process suspension and contain oils foreign material, and the gas that contains these materials needs to filter in addition rear labor cleaning, and production efficiency is low.
Summary of the invention
The purpose of this utility model is to provide the full recuperation of heat dedusting dehumidifying of the cyclone type hot-air carbonated drink seperator of a kind of simple and efficient, energy-conservation environmental protection again, sterilization and sterilization.
The utility model adopts following technology to implement its goal of the invention, the full recuperation of heat dedusting dehumidifying of a kind of cyclone type hot-air carbonated drink seperator, it comprises cylindrical shell, support, cylindrical shell one side is provided with air inlet, opposite side is provided with gas outlet, air inlet connects inner core, anion source and check valve are housed between the two, Temperature Humidity Sensor is equipped with in cylinder top inside, sterilizer is equipped with in Temperature Humidity Sensor side, rotary type shuttle valve is housed in gas outlet, inner-spiral type flow deflector is housed in inner core, well strainer is housed below inner barrel, drier is housed above well strainer, heater is equipped with in drier outside, cylindrical shell bottom is connected with cone bucket, in cone bucket, flow plug is housed, cone bucket bottom is connected with filter, filter is connected with ball-cock assembly by tube connector, cone bucket one side is provided with sewage draining exit.Above structure belongs to internal cyclone formula, be applicable to process composition very complicated and process after gas require Gao place.
Choked flow net is equipped with in cylindrical shell inner side, and separate mesh is equipped with in filter cylinder outside, in the middle of choked flow net and separate mesh, external spiral formula flow deflector is housed, and above structure belongs to external cyclone formula, is applicable to processing the simple less demanding place of gas.
Owing to having adopted above technical scheme, manufacturing structure is simple, use cost is cheap, divided gas flow is respond well, drying and hot and humid heat energy utilization field, energy-saving and environmental protection effect is remarkable, meets the needs of especially and keeps original local flavor, needs the product of drying as meat fish, tealeaves, tobacco and so on.
Accompanying drawing explanation
Fig. 1 is the dedusting dehumidifying carbonated drink separator structure schematic diagram that the utility model separated component is complicated, degree of drying requirement is high.
Fig. 2 is A-A cutaway view.
Fig. 3 is that the utility model divided gas flow composition is simple, the less demanding dedusting dehumidifying of degree of drying carbonated drink separator structure schematic diagram.
The specific embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
The gas turnover humiture that comprises the utility model detects disinfecting mechanism, internal cyclone mechanism, separating mechanism, drier, regeneration sector, external cyclone mechanism, gets rid of mechanism's composition.
As shown in Figure 1, it comprises the full recuperation of heat dedusting dehumidifying of cyclone type hot-air carbonated drink seperator, cylindrical shell 1 top one side is provided with air inlet 2, opposite side is provided with gas outlet 14, air inlet 2 connects inner core 7, inner core 7 is provided with anion source 3 and check valve 4 in the middle of connecting air inlet 2, Temperature Humidity Sensor 8 is equipped with in cylindrical shell 1 inside, top, sterilizer 11 is equipped with in Temperature Humidity Sensor 8 sides, in inner core 7, be provided with inner-spiral type flow deflector 6, at inner core 7 lower outsides, cylindrical shell 1 inner lower is provided with well strainer 5, well strainer 5 tops are provided with drier 9, heater 10 is equipped with in drier 9 outsides, heater 10 bottoms, well strainer 5 tops are provided with regeneration air inlet 15, cylindrical shell 1 top is provided with regeneration moisture exhausting port 12, 14 tops, gas outlet are provided with rotary type shuttle valve 13.Cylindrical shell 1 bottom connects cone bucket 21, and cone Dou21 bottom is provided with filter 18, and filter 18 has tube connector 19 to be connected with ball-cock assembly 20, and a side of cone bucket 21 is provided with sewage draining exit 17, and flow plug 22 is equipped with in cone bucket 21 inner sides, and cone bucket 21 is supported by bracing frame 16.
As shown in Figure 2, drier 9 structures adopt plication, and drier is contained in flabellum inside.
As shown in Figure 3, choked flow net 23 is equipped with in cylindrical shell 1 inner side, and external spiral formula flow deflector 24 is located in the middle of separate mesh 25 and choked flow net 23, and filter screen 27 is equipped with in filter cylinder 26 the insides.
Gas turnover humiture described in the utility model detects disinfecting mechanism, comprise that cylindrical shell 1 one sides are provided with air inlet 2, cylindrical shell 1 opposite side is provided with gas outlet 14, the outer middle side part of cylindrical shell 1 is provided with regeneration air inlet 15, air inlet 2 is provided with anion source 3 and check valve 4 in the middle of connecting inner core 7, cylindrical shell 1 inside, top is provided with Temperature Humidity Sensor 8, and sterilizer 11 is equipped with in Temperature Humidity Sensor side, and cylindrical shell 1 top is provided with moisture exhausting port 12, rotary type shuttle valve 13.
Internal cyclone described in the utility model mechanism, is provided with inner-spiral type flow deflector 6 in the middle of comprising inner core 7, and air inlet 2 is provided with anion source 3 and check valve 4 in the middle of connecting inner cores 7.
Separating mechanism described in the utility model, comprises that cylindrical shell 1 inside, the outer basifacial of inner core 7 are provided with well strainer 5, and well strainer 5 above middle part is provided with drier 9, and drier 9 lower ends are supported on inner core 7 outsides, support and are provided with the elevation angle.
Drier described in the utility model, comprises that drier 9 adopts plication structure, and drier is contained in flabellum inside.
Regeneration sector described in the utility model, comprises that drier 9 outsides are equipped with heater 10, and heater 10 is provided with regeneration air inlet 15 below, and cylindrical shell 1 top is provided with regeneration moisture exhausting port 12.
External cyclone described in the utility model mechanism, comprises that external spiral flow deflector 24 1 sides are equipped with choked flow net 23, and opposite side is equipped with separate mesh 25, and filter screen 27 is equipped with in filter cylinder 26 the insides.
Eliminating described in the utility model mechanism, comprises that cone bucket 21 inside are equipped with flow plug 22, and cone bucket outside is provided with sewage draining exit 17, and cone bucket bottom is provided with filter 18, and pipeline 19 is connected filter 18 with ball-cock assembly 20.
Operation principle:
When hot-air enters internal cyclone formula inner core by one-way valve opens, in inside spin flow deflector enters cone bucket, moisture content is discharged by ball-cock assembly after well strainer separation, and gas is separated through filter screen, drier absorption remains after moisture content, and rotary type shuttle valve lower disc is opened through gas outlet and discharged and recycle.After drier is saturated, heater heats drier, and moisture content is firmly discharged by moisture exhausting port by check valve and rotary type shuttle valve lower disc shelves.External cyclone formula just according to process gaseous species on internal cyclone formula basis by spiral flow deflector and filter screen reversing of position, increase work efficiency.
Claims (8)
1. the full recuperation of heat dedusting dehumidifying of cyclone type hot-air carbonated drink seperator, it comprises that cylindrical shell (1) top one side is provided with air inlet (2), opposite side is provided with gas outlet (14), air inlet (2) connects inner core (7), inner core (7) is provided with anion source (3) and check valve (4) in the middle of connecting air inlet (2), Temperature Humidity Sensor (8) is equipped with in cylindrical shell (1) inside, top, sterilizer (11) is equipped with in Temperature Humidity Sensor (8) side, in inner core (7), be provided with inner-spiral type flow deflector (6), at inner core (7) lower outside, cylindrical shell (1) inner lower is provided with well strainer (5), well strainer (5) top is provided with drier (9), heater (10) is equipped with in drier (9) outside, heater (10) bottom, well strainer (5) top is provided with regeneration air inlet (15), cylindrical shell (1) top is provided with regeneration moisture exhausting port (12), top, gas outlet (14) is provided with rotary type shuttle valve (13), cylindrical shell (1) bottom connects cone bucket (21), cone bucket (21) bottom is provided with filter (18), filter (18) has tube connector (19) that ball-cock assembly (20) is connected, one side of cone bucket (21) is provided with sewage draining exit (17), flow plug (22) is equipped with in cone bucket (21) inner side, cone bucket (21) is supported by bracing frame (16), choked flow net (23) is equipped with in cylindrical shell (1) inner side, external spiral formula flow deflector (24) is housed in the middle of choked flow net (23) and separate mesh (25), filter screen (27) is equipped with in filter cylinder (26) the inside.
2. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises gas turnover, humiture detects, disinfecting mechanism, cylindrical shell (1) one side is provided with air inlet (2), cylindrical shell (1) opposite side is provided with gas outlet (14), the outer middle side part of cylindrical shell (1) is provided with regeneration air inlet (15), air inlet (2) the inside is provided with anion source (3) and check valve (4), cylindrical shell (1) inside, top is provided with Temperature Humidity Sensor (8), sterilizer (11) is equipped with in Temperature Humidity Sensor (8) side, cylinder top is provided with moisture exhausting port (12), rotary type shuttle valve (13).
3. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises internal cyclone mechanism, in the middle of inner core (7), be provided with inner-spiral type flow deflector (6), air inlet (2) is provided with anion source (3) and check valve (4) in the middle of connecting inner core (7).
4. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises separating mechanism, cylindrical shell (1) is inner, inner core (7) outer lower portion is provided with well strainer (5), well strainer (5) above middle part is provided with drier (9), drier (9) lower end is supported on inner core (7) outside, supports and is provided with the elevation angle.
5. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises drier, and drier (9) adopts plication structure, and drier is contained in flabellum inside.
6. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises regeneration sector, heater (10) is equipped with in drier (9) outside, heater (10) is provided with regeneration air inlet (15) below, and cylindrical shell (1) top is provided with regeneration moisture exhausting port (12).
7. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises external cyclone mechanism, external spiral formula flow deflector (24) one sides are equipped with choked flow net (23), opposite side is equipped with separate mesh (25), and filter screen (27) is equipped with in filter cylinder (26) the inside.
8. according to the full recuperation of heat dedusting dehumidifying of cyclone type hot-air described in claims 1 carbonated drink seperator, it comprises gets rid of mechanism, flow plug (22) is equipped with in cone bucket (21) inside, cone bucket (21) outside is provided with sewage draining exit (17), cone bucket (21) bottom is provided with filter (18), and pipeline (19) is connected filter (18) with ball-cock assembly (20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320024129.7U CN203389507U (en) | 2013-01-17 | 2013-01-17 | Cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320024129.7U CN203389507U (en) | 2013-01-17 | 2013-01-17 | Cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator |
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| CN203389507U true CN203389507U (en) | 2014-01-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201320024129.7U Expired - Lifetime CN203389507U (en) | 2013-01-17 | 2013-01-17 | Cyclone type hot air total heat recovery dust-removing and dehumidifying steam-water separator |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103933834A (en) * | 2013-01-17 | 2014-07-23 | 陈永真 | Whirlwind hot-air total heat recovery dedusting dehumidifying gas-water separator |
| CN104012636A (en) * | 2014-05-20 | 2014-09-03 | 浙江海洋学院 | Circulating marine product drying equipment |
| CN104083993A (en) * | 2014-07-22 | 2014-10-08 | 何国豪 | Pressure-impacting centrifugal dehumidifier with guiding and adsorbing device |
| CN107321115A (en) * | 2017-08-18 | 2017-11-07 | 马鞍山市顺达环保设备有限公司 | One kind dehumidifying bag-type dust collector |
| CN108097033A (en) * | 2017-09-01 | 2018-06-01 | 阿丽贝（鞍山）塑料防腐设备有限公司 | Plastics waste gas purification apparatus and its bypass processing system |
| CN108993103A (en) * | 2018-09-30 | 2018-12-14 | 天津华电北宸分布式能源有限公司 | A kind of dehumidifying filter device |
| CN109603363A (en) * | 2019-01-25 | 2019-04-12 | 江苏师范大学 | Aqueous vapor seperating vale, environment-friendly type air dust pelletizing system |
-
2013
- 2013-01-17 CN CN201320024129.7U patent/CN203389507U/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103933834A (en) * | 2013-01-17 | 2014-07-23 | 陈永真 | Whirlwind hot-air total heat recovery dedusting dehumidifying gas-water separator |
| CN103933834B (en) * | 2013-01-17 | 2016-05-25 | 陈永真 | The full recuperation of heat dedusting dehumidifying of cyclone type hot-air carbonated drink seperator |
| CN104012636A (en) * | 2014-05-20 | 2014-09-03 | 浙江海洋学院 | Circulating marine product drying equipment |
| CN104012636B (en) * | 2014-05-20 | 2017-07-28 | 浙江海洋学院 | Circulating marine product drying equipment |
| CN104083993A (en) * | 2014-07-22 | 2014-10-08 | 何国豪 | Pressure-impacting centrifugal dehumidifier with guiding and adsorbing device |
| CN107321115A (en) * | 2017-08-18 | 2017-11-07 | 马鞍山市顺达环保设备有限公司 | One kind dehumidifying bag-type dust collector |
| CN107321115B (en) * | 2017-08-18 | 2020-05-19 | 安徽顺达环保科技股份有限公司 | Dehumidification sack dust collector |
| CN108097033A (en) * | 2017-09-01 | 2018-06-01 | 阿丽贝（鞍山）塑料防腐设备有限公司 | Plastics waste gas purification apparatus and its bypass processing system |
| CN108993103A (en) * | 2018-09-30 | 2018-12-14 | 天津华电北宸分布式能源有限公司 | A kind of dehumidifying filter device |
| CN108993103B (en) * | 2018-09-30 | 2023-11-10 | 天津华电北宸分布式能源有限公司 | Dehumidification filter equipment |
| CN109603363A (en) * | 2019-01-25 | 2019-04-12 | 江苏师范大学 | Aqueous vapor seperating vale, environment-friendly type air dust pelletizing system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140115 Effective date of abandoning: 20160525 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |