CN103721429B - Liquid material concentration equipment - Google Patents
Liquid material concentration equipment Download PDFInfo
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- CN103721429B CN103721429B CN201310748209.1A CN201310748209A CN103721429B CN 103721429 B CN103721429 B CN 103721429B CN 201310748209 A CN201310748209 A CN 201310748209A CN 103721429 B CN103721429 B CN 103721429B
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- housing
- pipe
- filter material
- liquid material
- air inlet
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Abstract
The invention discloses liquid material concentration equipment. According to the equipment, a negative pressure circulation pipe (8), a fan (1), a positive pressure circulation pipe (2), a cyclone dust remover (3), a connecting pipe (4), a bag-type dust remover (5), a bag-type dust remover (6) and an adjustment valve (7) form a circulation channel; a liquid material is added through an atomizer mounted in the negative pressure circulation pipe (8); the atomized liquid material microparticles form a fluidization state and flow at a high speed by virtue of high-speed air stream generated by the fan; water of the liquid microparticles is quickly taken away by air stream and is discharged through the bag-type dust removers; a concentrated material is collected in the cyclone dust remover (3). The liquid material concentration equipment is high in material concentration speed, high in efficiency and low in energy consumption.
Description
Technical field
The present invention relates to a kind of concentrator of liquid material.
Background technology
The concentrated general of existing liquid material adopts heating liquid material, and the method that liquid boiling is vaporized realizes, and energy consumption is high, and efficiency is lower.
Summary of the invention
Technical problem to be solved by this invention is to provide the liquid material concentrator that a kind of energy consumption is low, efficiency is high.
Technical scheme of the present invention is: a kind of concentrator of liquid material, comprises negative-pressure cyclic pipe, blower fan, malleation circulation pipe, cyclone dust collectors, tube connector, sack cleaner, control valve, negative-pressure cyclic pipe is three-way pipe, and three ports of three-way pipe are outlet respectively, import and control valve interface, said modules presses the outlet of negative-pressure cyclic pipe, air inlet, fan outlet, malleation circulation pipe, cyclone dust collectors air inlet, cyclone dust collectors exhaust outlet, tube connector, sack cleaner air inlet pipe, sack cleaner ash releasing tube, control valve, the sequential communication of negative-pressure cyclic pipe control valve interface becomes circulation canal, the ash discharging hole of cyclone dust collectors is provided with blow-off valve, negative-pressure cyclic pipe inside is provided with atomizer, blow-off valve is for discharging the liquid material being collected in and being concentrated in ash bucket, atomizer is used for liquid material being atomized into particulate and adding in equipment, sack cleaner for separating of and discharge moisture, control valve makes it be in barotropic state for regulating the internal pressure of sack cleaner.
Blower fan is power source of the present invention, makes the liquid material being atomized into particulate form fluidized state and flow at high speed for generation of high velocity air, in order to improve the flowing velocity of fluidisation state material, can be concatenated formation blower fan group use with two with fan.
Sack cleaner preferred pulse sack cleaner, pulse bag type dust collector in embodiment comprises housing, filter material, air inlet pipe, ash releasing tube and back-blowing device, housing is tube structure, and shell one end is provided with air inlet pipe, and the other end is provided with ash releasing tube, one end of air inlet pipe is outside housing, the other end stretches in housing, and one end of ash releasing tube is outside housing, and the other end stretches in housing, housing is also provided with exhaust outlet, the air-flow that exhaust outlet is separated for discharging filter material, filter material is tube structure, is arranged in housing, and filter material one end hoop sleeve is contained in air inlet pipe, and other end hoop sleeve is contained on ash releasing tube, back-blowing device is for removing the material being deposited under airflow function and filter material affecting filter material gas permeability, back-blowing device is by impulse electromagnetic valve, deflector and air bleeding valve composition, impulse electromagnetic valve is arranged on housing, its outlet is communicated with enclosure interior, import is connected with compressed air source, deflector is arranged on the place of positive paired pulses electromagnetic valve outlet in housing, make it directly can not blow to filter material for blocking compressed air, in order to avoid high-speed compressed air damages filter material, air bleeding valve is arranged on exhaust outlet, while exhaust valve closure, impulse electromagnetic valve is opened, pass into compressed air in housing and blowback is carried out to filter material.
In order to increase heating load, heater can be installed in negative-pressure cyclic passage or adopt tool negative-pressure cyclic pipe with dissection, in interlayer, passing into heat medium.
In order to accelerate the velocity of discharge of moisture, more than one sack cleaner of can connecting again on sack cleaner.
The present invention forms circulation canal by negative-pressure cyclic pipe, blower fan, malleation circulation pipe, cyclone dust collectors, tube connector, sack cleaner, control valve, the high velocity air utilizing blower fan to produce makes the liquid material being atomized into particulate form fluidisation state and flow at high speed, the moisture of liquid particle is taken away fast by air-flow and discharges through sack cleaner, material concentrates that speed is fast, efficiency is high, because moisture evaporation absorbs amount of heat, the wet gas current temperature of discharging is low, the part kinetic transformation of blower fan is can for the heat energy of moisture vaporization, wasted energy obtains utilization, and energy consumption is low.
Accompanying drawing explanation
Fig. 1 is the structure chart of the concentrator embodiment of a kind of liquid material of the present invention.
Fig. 2 is the sectional view of sack cleaner in Fig. 1.
Fig. 3 is the sectional view along A-A line in Fig. 1.
Detailed description of the invention
Below in conjunction with drawings and Examples, the invention will be further described, but embodiment is not construed as limiting the invention.
See Fig. 1, Fig. 2 and Fig. 3, the concentrator of this liquid material comprises negative-pressure cyclic pipe 8, blower fan 1, malleation circulation pipe 2, cyclone dust collectors 3, tube connector 4, sack cleaner 5, sack cleaner 6, control valve 7, negative-pressure cyclic pipe 8 is three-way pipes, three ports of three-way pipe are outlet respectively, import and control valve interface, said modules exports by negative-pressure cyclic pipe 8, blower fan 1 air inlet, blower fan 1 air outlet, malleation circulation pipe 2, cyclone dust collectors 3 air inlet, cyclone dust collectors 3 exhaust outlet, tube connector 4, sack cleaner 5 air inlet pipe 40, sack cleaner 5 ash releasing tube 49, sack cleaner 6 air inlet pipe 40, sack cleaner 6 ash releasing tube 49, control valve 7, the sequential communication of negative-pressure cyclic pipe 8 control valve interface becomes circulation canal, the ash discharging hole of cyclone dust collectors 3 is provided with blow-off valve 9, negative-pressure cyclic pipe 8 inside is provided with atomizer 10.
Sack cleaner 5, sack cleaner 6 are pulse bag type dust collectors that structure is identical, comprise housing 41, filter material 47, air inlet pipe 40, ash releasing tube 49 and back-blowing device, housing 41 is tube structures, housing 41 one end is provided with air inlet pipe 40, the other end is provided with ash releasing tube 49, one end of air inlet pipe 40 is outside housing 41, the other end stretches in housing 41, one end of ash releasing tube 49 is outside housing 41, the other end stretches in housing 41, housing 41 is also provided with exhaust outlet 46, the air-flow that exhaust outlet 46 is separated for discharging filter material 47, filter material 47 is tube structures, is arranged in housing 41, and filter material 47 one end hoop sleeve is contained in air inlet pipe 40, and other end hoop sleeve is contained on ash releasing tube 49, back-blowing device is for removing the material being deposited under airflow function and filter material affecting filter material gas permeability, back-blowing device is by impulse electromagnetic valve 42, deflector 43 and air bleeding valve 45 form, impulse electromagnetic valve installs 42 on housing 41, its outlet is communicated with housing 41 inside, import is connected with compressed air source, deflector 43 is arranged on the place that in housing, positive paired pulses magnetic valve 42 exports, it is made can not directly to blow to filter material 47 for blocking compressed air, in order to avoid high-speed compressed air damages filter material 47, air bleeding valve 45 is arranged on exhaust outlet 46, while air bleeding valve 45 is closed, impulse electromagnetic valve 42 is opened, pass into compressed air in housing 41 and blowback is carried out to filter material 47.
Claims (4)
1. the concentrator of a liquid material, it is characterized in that: the concentrator of described liquid material comprises negative-pressure cyclic pipe, blower fan, malleation circulation pipe, cyclone dust collectors, tube connector, sack cleaner, control valve, negative-pressure cyclic pipe is three-way pipe, three ports of three-way pipe are outlet respectively, import and control valve interface, said modules presses the outlet of negative-pressure cyclic pipe, air inlet, fan outlet, malleation circulation pipe, cyclone dust collectors air inlet, cyclone dust collectors exhaust outlet, tube connector, sack cleaner air inlet pipe, sack cleaner ash releasing tube, control valve, the sequential communication of negative-pressure cyclic pipe control valve interface becomes circulation canal, the ash discharging hole of cyclone dust collectors is provided with blow-off valve, negative-pressure cyclic pipe inside is provided with atomizer.
2. the concentrator of liquid material according to claim 1, is characterized in that: described sack cleaner is pulse bag type dust collector.
3. the concentrator of liquid material according to claim 2, it is characterized in that: described pulse bag type dust collector comprises housing, filter material, air inlet pipe, ash releasing tube and back-blowing device, housing is tube structure, and shell one end is provided with air inlet pipe, and the other end is provided with ash releasing tube, one end of air inlet pipe is outside housing, the other end stretches in housing, and one end of ash releasing tube is outside housing, and the other end stretches in housing, housing is also provided with exhaust outlet, the air-flow that exhaust outlet is separated for discharging filter material; Filter material is tube structure, is arranged in housing, and filter material one end hoop sleeve is contained in air inlet pipe, and other end hoop sleeve is contained on ash releasing tube; Back-blowing device is for removing the material being deposited under airflow function and filter material affecting filter material gas permeability, back-blowing device is made up of impulse electromagnetic valve, deflector and air bleeding valve, impulse electromagnetic valve is arranged on housing, its outlet is communicated with enclosure interior, import is connected with compressed air source, and deflector is arranged on the place of positive paired pulses electromagnetic valve outlet in housing, makes it directly can not blow to filter material for blocking compressed air, in order to avoid high-speed compressed air damages filter material, air bleeding valve is arranged on exhaust outlet.
4. the concentrator of the liquid material described in claim 1 or 2, is characterized in that: more than one sack cleaner of connecting again on described sack cleaner.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310748209.1A CN103721429B (en) | 2013-12-31 | 2013-12-31 | Liquid material concentration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310748209.1A CN103721429B (en) | 2013-12-31 | 2013-12-31 | Liquid material concentration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103721429A CN103721429A (en) | 2014-04-16 |
| CN103721429B true CN103721429B (en) | 2015-06-17 |
Family
ID=50445876
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310748209.1A Active CN103721429B (en) | 2013-12-31 | 2013-12-31 | Liquid material concentration equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN103721429B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103720725A (en) * | 2013-12-31 | 2014-04-16 | 昆明特康科技有限公司 | Circulating fluidized bed equipment and pine pollen production method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3324567A (en) * | 1965-07-19 | 1967-06-13 | Nat Dairy Prod Corp | Drying method and apparatus |
| CN2089150U (en) * | 1990-06-16 | 1991-11-20 | 陈少华 | Airflow circulating drier |
| CN102019095A (en) * | 2009-09-23 | 2011-04-20 | 石惠良 | Spray drying machinery with cyclone separator |
| CN202070178U (en) * | 2011-04-27 | 2011-12-14 | 金伟均 | Spray cooling drying machine |
-
2013
- 2013-12-31 CN CN201310748209.1A patent/CN103721429B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3324567A (en) * | 1965-07-19 | 1967-06-13 | Nat Dairy Prod Corp | Drying method and apparatus |
| CN2089150U (en) * | 1990-06-16 | 1991-11-20 | 陈少华 | Airflow circulating drier |
| CN102019095A (en) * | 2009-09-23 | 2011-04-20 | 石惠良 | Spray drying machinery with cyclone separator |
| CN202070178U (en) * | 2011-04-27 | 2011-12-14 | 金伟均 | Spray cooling drying machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103721429A (en) | 2014-04-16 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 650236, Kunming District, Yunnan District, Yinhai, Guandu district 15, 1 units, 6 floor, Room 601 Applicant after: KUNMING TEKANG TECHNOLOGY CO., LTD. Address before: 650236 No. 535, No. 5, building 1, Yunnan overseas Chinese Pioneer Park, No. 13-2, Yunnan information base, Kunming economic and Technological Development Zone, Shanghai Applicant before: KUNMING TEKANG TECHNOLOGY CO., LTD. |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yang Yusheng Inventor after: Zeng Yawen Inventor after: Du Juan Inventor before: Jia Ping Inventor before: Zeng Yawen Inventor before: Du Juan |
|
| COR | Change of bibliographic data | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160317 Address after: 675200 old dam area, Longchuan Town Industrial Zone, Nanhua County, Chuxiong Yi Autonomous Prefecture, Yunnan Patentee after: SOUTH CHINA NEW CENTURY BIOLOGICAL ENGINEERING CO., LTD. Address before: 650236, Kunming District, Yunnan District, Yinhai, Guandu district 15, 1 units, 6 floor, Room 601 Patentee before: KUNMING TEKANG TECHNOLOGY CO., LTD. |