CN103657520A - Powder material and liquid material mixing equipment - Google Patents
Powder material and liquid material mixing equipment Download PDFInfo
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- CN103657520A CN103657520A CN201310748132.8A CN201310748132A CN103657520A CN 103657520 A CN103657520 A CN 103657520A CN 201310748132 A CN201310748132 A CN 201310748132A CN 103657520 A CN103657520 A CN 103657520A
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Abstract
The invention discloses powder material and liquid material mixing equipment. According to the equipment, a circulating passage is formed by a fan (1), a circulating pipeline I (2), a dust collector (4), a dust collector (10), an adjusting valve (5), an air inlet tee (6) and a circulating pipeline II (7), a powder material is added through a material charging valve (8), a liquid material is added through an atomizer arranged on the circulating pipeline II (7), the powder material and the liquid material are mixed and dried in the circulating passage under the effect of airflow generated by the fan, and wet gas is exhausted along with the airflow separated out from the dust collector. The equipment is simple in structure, convenient to operate and high in drying speed.
Description
Technical field
The present invention relates to a kind of powder material and liquid material mixing apparatus, belong to the technical fields such as the mixing of powder liquid, pneumatic conveying drying.
Background technology
The principle of fluidized bed granulation equipment is with air-flow, powder to be suspended, with atomizer, spray into binder again, make powder condense into particle, and then with thermal current by particle drying, can in an equipment, complete mixing, granulate and be dried, fluidized bed granulation equipment is also for the mixing of powder material and liquid material, but existing fluidized bed granulation equipment exists the deficiencies such as structure and complicated operation, rate of drying be slow.
Summary of the invention
Technical scheme to be solved by this invention is to provide a kind of simple in structure, more convenient operation, fast powder material and the liquid material mixing apparatus of rate of drying.
For realizing the technical scheme that the present invention takes, be: a kind of powder material and liquid material mixing apparatus, comprise blower fan, circulation line I, deduster, control valve, air inlet threeway, circulation line II, said modules is pressed fan outlet, circulation line I, deduster air inlet pipe, remover ash discharge dust pipe, control valve, air inlet threeway, circulation line II, the order of blower fan import is communicated with into circulation canal, in circulation line I, be provided with discharge gate, blow-off valve is installed on discharge gate, it is air inlet that air inlet threeway also has a port, intake valve is installed on air inlet, in circulation line II, be provided with two charge doors, on a charge door, charging valve is installed, on another charge door, atomizer is installed.Circulation canal is to realize powder to mix with liquid and dry place, deduster is used for from the separated wet gas current of fluidisation state material, control valve is by regulating the internal pressure of deduster to regulate the velocity of discharge of moisture, blow-off valve is for discharge, intake valve is for air inlet, charging valve is for add powder in circulating line, and atomizer is for spraying in circulation canal after liquid material atomization.
Deduster preferred pulse sack cleaner, pulse bag type dust collector in embodiment comprises housing, air inlet pipe, ash releasing tube, cloth bag and back-blowing device, housing is tube structure, housing one end is provided with air inlet pipe, and the other end is provided with ash releasing tube, and one end of air inlet pipe is outside housing, the other end stretches in housing, one end of ash releasing tube is outside housing, and the other end stretches in housing, is also provided with exhaust outlet on housing; Cloth bag is arranged in housing, and cloth bag one end is contained in air inlet pipe with hoop sleeve, and the other end is contained on ash releasing tube with hoop sleeve; Back-blowing device is deposited in for removing the material that affects cloth bag gas permeability on cloth bag under airflow function, back-blowing device is comprised of back-flushing valve, blowback threeway and air bleeding valve, one end and the exhaust outlet of blowback threeway join, the other end and air bleeding valve join, also have one end and back-flushing valve to join, the other end and the high-pressure air source of back-flushing valve are joined.In the time of exhaust valve closure, back-flushing valve is opened, and passes into high pressure draught cloth bag is carried out to blowback in housing.
Deduster can be many, and many duster parallels are used together.
Powder material of the present invention and liquid material mixing apparatus are work like this: close blow-off valve and charging valve, open intake valve, start blower fan, and mobile at effect downstream high-speed circulating in circulation canal of blower fan; Open charging valve and add powder, powder under the effect of high velocity air, form fluidisation state and in circulating line high-speed circulating flow; Start atomizer and add liquid material, be dispersed into the liquid material of particulate and the powder Quick uniform of fluidisation state mixes, between the compound of high degree of dispersion in air-flow and gas, carry out rapidly heat and exchange of moisture, moisture in compound is vaporized, the air-flow of separating with deduster is discharged through deduster exhaust outlet, and compound is dried; After being dried, open blow-off valve, compound is along with air-flow is discharged through blow-off valve.
In order to increase heating load, can in circulation line II, heater be installed.
Powder material of the present invention and liquid material mixing apparatus form circulation canal by blower fan, circulation line I, deduster, control valve, air inlet threeway, circulation line II, by charging valve, add powder material, by atomizer, add liquid material, under the airflow function producing at blower fan, powder material completes and mixes and be dried with liquid material in circulation canal, the air-flow that moisture is separated with deduster is discharged, and device structure is simple, easy to operate, rate of drying is fast.
Accompanying drawing explanation
Fig. 1 is the structure chart of a kind of powder material of the present invention and liquid material mixing apparatus embodiment.
Fig. 2 is along the cutaway view of A-A line in Fig. 1.
Fig. 3 is the cutaway view of deduster in Fig. 1.
In figure, each Reference numeral is: 1, blower fan; 2, circulation line I; 3, blow-off valve; 4, deduster; 5, control valve; 6, air inlet threeway; 7, circulation line II; 8, charging valve; 9, intake valve; 10, deduster; 11, atomizer; 12, outer tube; 13, inner tube; 14, interlayer; 40, air inlet pipe; 41, housing; 45, air bleeding valve; 46, exhaust outlet; 47, cloth bag; 49, ash releasing tube; 50, blowback threeway; 51, back-flushing valve.
The specific embodiment
Below in conjunction with drawings and Examples, the invention will be further described, but embodiment is not construed as limiting the invention.
Referring to Fig. 1 to Fig. 3, this powder material and liquid material mixing apparatus comprise blower fan 1, circulation line I 2, deduster 4, deduster 10, control valve 5, air inlet threeway 6, circulation line II 7, said modules is communicated with into circulation canal by the order of blower fan 1 outlet, circulation line I 2, deduster 4 air inlet pipe, deduster 4 ash releasing tubes, deduster 10 air inlet pipe, deduster 10 ash releasing tubes, control valve 5, air inlet threeway 6, circulation line II 7, blower fan 1 import, in circulation line I 2, be provided with discharge gate, blow-off valve 3 is installed on discharge gate; In air inlet threeway 6, also having a port is air inlet, and intake valve 9 is installed on air inlet; Circulation line II 7 is comprised of outer tube 12 and inner tube 13, and outer tube 12 is sleeved on the outside of inner tube 13, between outer tube 12 and inner tube 13, forms interlayer 14, and interlayer 14 is communicated with steam pipework, and circulation line II 7 is both for the circulation canal of material, again for the heating of material; In circulation line II 7, be provided with two charge doors, on a charge door, charging valve 8 be installed, atomizer 11 is installed on another charge door.Circulation canal is to realize feed liquid to mix and dry place, deduster 4 and deduster 10 are for from the separated wet gas current of fluidisation state material, control valve 5 is by regulating the internal pressure of deduster 4 and deduster 10 to regulate the velocity of discharge of moisture, blow-off valve 3 is for discharge, charging valve 8 is for add powder in circulating line, and atomizer 11 is for spraying in circulation canal after liquid material atomization.
This powder material is identical with deduster 10 structures with the deduster 4 of liquid material mixing apparatus, it is all pulse bag type dust collector, pulse bag type dust collector comprises housing 41, air inlet pipe 40, ash releasing tube 49, cloth bag 47 and back-blowing device, housing 41 is tube structures, housing 41 one end are 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, is also provided with exhaust outlet 46 on housing 41; Cloth bag 47 is arranged in housing 41, and cloth bag 47 one end are contained in air inlet pipe 40 with hoop sleeve, and other end hoop sleeve is contained on ash releasing tube 49; Back-blowing device is comprised of back-flushing valve 51, blowback threeway 50 and air bleeding valve 45, one end of blowback threeway 50 and exhaust outlet 46 join, the other end and air bleeding valve 45 join, also have one end and back-flushing valve 51 to join, the other end and the high-pressure air source of back-flushing valve 51 are joined, when air bleeding valve 45 is closed, back-flushing valve 51 is opened, and passes into high pressure draught cloth bag 47 is carried out to blowback in housing 41.
Claims (5)
1. a powder material and liquid material mixing apparatus, it is characterized in that: described powder material and liquid material mixing apparatus comprise blower fan, circulation line I, deduster, control valve, air inlet threeway, circulation line II, said modules is pressed fan outlet, circulation line I, deduster air inlet pipe, remover ash discharge dust pipe, control valve, air inlet threeway, circulation line II, the order of blower fan import is communicated with into circulation canal, in circulation line I, be provided with discharge gate, blow-off valve is installed on discharge gate, it is air inlet that air inlet threeway also has a port, intake valve is installed on air inlet, in circulation line II, be provided with two charge doors, on a charge door, charging valve is installed, on another charge door, atomizer is installed.
2. powder material claimed in claim 1 and liquid material mixing apparatus, is characterized in that: described deduster is many, and many duster parallels together.
3. the powder material described in claim 1 or 2 and liquid material mixing apparatus, is characterized in that: described deduster is pulse bag type dust collector.
4. powder material claimed in claim 3 and liquid material mixing apparatus, it is characterized in that: described pulse bag type dust collector comprises housing, air inlet pipe, ash releasing tube, cloth bag and back-blowing device, housing is tube structure, housing one end is provided with air inlet pipe, and the other end is provided with ash releasing tube, and one end of air inlet pipe is outside housing, the other end stretches in housing, one end of ash releasing tube is outside housing, and the other end stretches in housing, is also provided with exhaust outlet on housing; Cloth bag is arranged in housing, and cloth bag one end is contained in air inlet pipe with hoop sleeve, and the other end is contained on ash releasing tube with hoop sleeve; Back-blowing device is deposited in for removing the material that affects cloth bag gas permeability on cloth bag under airflow function, back-blowing device is comprised of back-flushing valve, blowback threeway and air bleeding valve, one end and the exhaust outlet of blowback threeway join, the other end and air bleeding valve join, also have one end and back-flushing valve to join, the other end and the high-pressure air source of back-flushing valve are joined.
5. powder material claimed in claim 1 and liquid material mixing apparatus, is characterized in that: described circulation line II is comprised of outer tube and inner tube, and outer tube sleeve is contained in the outside of inner tube, between outer tube and inner tube, forms interlayer, and interlayer is communicated with steam pipework.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310748132.8A CN103657520B (en) | 2013-12-31 | 2013-12-31 | A kind of powder material and liquid material mixing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310748132.8A CN103657520B (en) | 2013-12-31 | 2013-12-31 | A kind of powder material and liquid material mixing apparatus |
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| Publication Number | Publication Date |
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| CN103657520A true CN103657520A (en) | 2014-03-26 |
| CN103657520B CN103657520B (en) | 2015-08-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310748132.8A Active CN103657520B (en) | 2013-12-31 | 2013-12-31 | A kind of powder material and liquid material mixing apparatus |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015101279A1 (en) * | 2013-12-31 | 2015-07-09 | 昆明特康科技有限公司 | Circulating fluidized bed apparatus |
| CN110433922A (en) * | 2018-09-21 | 2019-11-12 | 浙江芸洁科技有限公司 | A kind of processing method of konjaku powder |
| CN113171705A (en) * | 2020-11-22 | 2021-07-27 | 湖南贝爱成食品有限公司 | Workshop is with mixed machine of flavouring of fast food |
| CN113441030A (en) * | 2021-07-09 | 2021-09-28 | 南方科技大学 | Material mixing equipment |
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| CN2089150U (en) * | 1990-06-16 | 1991-11-20 | 陈少华 | Airflow circulating drier |
| DE20000841U1 (en) * | 2000-01-19 | 2000-03-30 | Tuchenhagen Gmbh | Nozzle device in a dissolving apparatus for dissolving a solid in a solvent |
| WO2000076650A1 (en) * | 1999-06-16 | 2000-12-21 | Merck Patent Gmbh | Spray-drying installation and a method for using the same |
| CN102091566A (en) * | 2010-12-17 | 2011-06-15 | 常州市鹏多干燥设备有限公司 | One-step granulating and drying equipment with fluidized bed |
| CN102219346A (en) * | 2011-05-26 | 2011-10-19 | 福州庄讯环保科技有限公司 | System for drying and treating sludge by utilizing afterheat to generate high-temperature circulating air |
| CN102814085A (en) * | 2011-06-06 | 2012-12-12 | 李军 | Blowing method and device thereof for pulsed jet cloth filter |
-
2013
- 2013-12-31 CN CN201310748132.8A patent/CN103657520B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2089150U (en) * | 1990-06-16 | 1991-11-20 | 陈少华 | Airflow circulating drier |
| WO2000076650A1 (en) * | 1999-06-16 | 2000-12-21 | Merck Patent Gmbh | Spray-drying installation and a method for using the same |
| DE20000841U1 (en) * | 2000-01-19 | 2000-03-30 | Tuchenhagen Gmbh | Nozzle device in a dissolving apparatus for dissolving a solid in a solvent |
| CN102091566A (en) * | 2010-12-17 | 2011-06-15 | 常州市鹏多干燥设备有限公司 | One-step granulating and drying equipment with fluidized bed |
| CN102219346A (en) * | 2011-05-26 | 2011-10-19 | 福州庄讯环保科技有限公司 | System for drying and treating sludge by utilizing afterheat to generate high-temperature circulating air |
| CN102814085A (en) * | 2011-06-06 | 2012-12-12 | 李军 | Blowing method and device thereof for pulsed jet cloth filter |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015101279A1 (en) * | 2013-12-31 | 2015-07-09 | 昆明特康科技有限公司 | Circulating fluidized bed apparatus |
| CN110433922A (en) * | 2018-09-21 | 2019-11-12 | 浙江芸洁科技有限公司 | A kind of processing method of konjaku powder |
| CN113171705A (en) * | 2020-11-22 | 2021-07-27 | 湖南贝爱成食品有限公司 | Workshop is with mixed machine of flavouring of fast food |
| CN113441030A (en) * | 2021-07-09 | 2021-09-28 | 南方科技大学 | Material mixing equipment |
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| Publication number | Publication date |
|---|---|
| CN103657520B (en) | 2015-08-26 |
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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. 516, 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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Effective date of registration: 20160324 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. |