CN207515481U - A kind of spray drying tower hot air heating system - Google Patents
A kind of spray drying tower hot air heating system Download PDFInfo
- Publication number
- CN207515481U CN207515481U CN201721607766.1U CN201721607766U CN207515481U CN 207515481 U CN207515481 U CN 207515481U CN 201721607766 U CN201721607766 U CN 201721607766U CN 207515481 U CN207515481 U CN 207515481U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- spray drying
- wind turbine
- drying tower
- air
- 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.)
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- 238000001694 spray drying Methods 0.000 title claims abstract description 33
- 238000010438 heat treatment Methods 0.000 title claims abstract description 18
- 229920002456 HOTAIR Polymers 0.000 title claims abstract description 14
- 229920000742 Cotton Polymers 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003245 coal Substances 0.000 abstract description 2
- 238000001035 drying Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000010981 drying operation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 238000009690 centrifugal atomisation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000005035 ginseng Nutrition 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model discloses a kind of spray drying tower hot air heating systems, including spray drying tower, first-class heat exchanger, secondary heat exchanger, the inlet scoop of wind turbine A is communicated with the Nature, air outlet is connect with the cold air inlet being set at the top of the shell side of the spray drying tower, and wind turbine B is connected at the air port of the shell side bottom；The inlet scoop of wind turbine C is communicated with the Nature, air outlet and be connected to wind turbine B air outlets pipeline connect after, import with the first-class heat exchanger is connect, the outlet of the first-class heat exchanger is connected with the import of the secondary heat exchanger, and the outlet of the secondary heat exchanger is connect with positioned at the hot wind inlet of the spray drying top of tower.The utility model can effectively improve heat utilization ratio, reduce the consumption of air heating energy source, the usage amount for often producing 1 ton of product fire coal is reduced to 3.5 tons by 5 tons original of consumption, and under with equal heat transfer boundary condition, the temperature of obtained hot-air is higher by 3-5 DEG C than the prior art.
Description
Technical field
The utility model is related to drying equipment heat circulating system field, specifically a kind of spray drying tower Hot-blast Heating system
System.
Background technology
Spray drying tower is widely used in biological pesticide due to its excellent drying efficiency, medicine, food microorganisms etc.
Industry.In the spray drying tower, air is filtered and heats, and into drier headspace distributor, hot-air is in the shape of a spiral
Evenly into hothouse, feed liquid sprays into imperceptible mist through high speed centrifugal atomization device or high-pressure atomizer at the top of tower body
Shape liquid pearl can be dried within the extremely short time with air current contacting as finished product, and finished product is continuously by dry tower bottom and whirlwind
It is exported in separator, micronic dust material is collected by pulse bag collector.However, in existing production process, lack and tail gas is returned
It receives and utilizes, cause the lost waste of heat.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of spray drying tower hot air heating systems.
In order to solve the above technical problems, a kind of spray drying tower hot air heating system described in the utility model, including wind
Machine A, spray drying tower, wind turbine B, wind turbine C, first-class heat exchanger and secondary heat exchanger, inlet scoop and the Nature phase of the wind turbine A
Logical, air outlet is connect with the cold air inlet being set at the top of the shell side of the spray drying tower, at the air port of the shell side bottom
It is connected with the wind turbine B；The inlet scoop of the wind turbine C is communicated with the Nature, and air outlet is with being connected to the wind turbine B air outlets
Pipeline connect after, the import with the first-class heat exchanger connect, the first-class heat exchanger outlet and the secondary heat exchanger into
Mouth is connected, and the outlet of the secondary heat exchanger is connect with positioned at the hot wind inlet of the spray drying top of tower；The level-one is changed
Include several heat-exchanging components in hot device, secondary heat exchanger.
Further, the inlet scoop of the wind turbine A, wind turbine C are equipped with dust-proof purifying device.
Further, being included at least in the first-class heat exchanger has heat-exchanging component described in three groups.
Further, being included at least in the first-class heat exchanger has heat-exchanging component described in 12 groups.
Further, the dust-proof purifying device is cotton.
The utility model has the following advantages compared with prior art：
（1）Cold wind in nature is sucked and is sent in the shell side of spray drying tower by the utility model, by hot wind blowing
Mist drying tower top entry be sent into tower in, spray drying tower during the work time, due to the cold wind in hot wind and shell side in tower it
Between heat transfer process cause cold wind preheating become warm wind, the natural cold wind that the warm wind of generation is extracted out by wind turbine B and sucked with wind turbine C
After mixing, first time heating is carried out into first-class heat exchanger, is then re-fed into secondary heat exchanger and carries out second of heating, most
Obtained hot wind is heated eventually again by completing drying operation in spray drying tower top entry feeding tower, has been thusly-formed one completely
Cycle, can effectively improve heat utilization ratio, reduce the consumption of air heating energy source, often produce the usage amount of 1 ton of product fire coal
3.5 tons are reduced to by 5 tons original of consumption, effectively reduces production cost.
（2）The utility model air efficiency of heating surface is high, under with equal heat transfer boundary condition, the temperature ratio of obtained hot-air
The prior art is higher by 3-5 DEG C.
（3）The utility model energy conservation and environmental protection for alleviating energy crisis, improves energy utilization rate and is of great significance.
Description of the drawings
Fig. 1 is the structure diagram of the utility model.
In figure：1st, wind turbine A, 2, spray drying tower, 3, shell side, 4, wind turbine B, 5, wind turbine C, 6, first-class heat exchanger, 7, two level
Heat exchanger, 8, heat-exchanging component.
Specific embodiment
Illustrate to be described further the utility model below in conjunction with the accompanying drawings.
A kind of spray drying tower hot air heating system as shown in Figure 1, including wind turbine A1, spray drying tower 2, wind turbine B4,
Wind turbine C5, first-class heat exchanger 6 and secondary heat exchanger 7, the inlet scoop of wind turbine A1 are communicated with the Nature, and air outlet is with being set to spraying
The cold air inlet at 3 top of shell side of drying tower 2 connects, and wind turbine B4 is connected at the air port of 3 bottom of shell side；The inlet scoop of wind turbine C5
Communicated with the Nature, air outlet and be connected to wind turbine B4 air outlets pipeline connect after, the import with first-class heat exchanger 6 is connect,
The outlet of the first-class heat exchanger 6 is connected with the import of secondary heat exchanger 7, and the outlet of secondary heat exchanger 7 is with being located at spray drying tower 2
The hot wind inlet connection at top；Being included at least in first-class heat exchanger 6 has three groups of heat-exchanging components 8, is included at least in first-class heat exchanger 7
There are 12 groups of heat-exchanging components 8；Wind turbine A1, wind turbine C5 inlet scoop be equipped with dust-proof purifying device；Dust-proof purifying device is cotton.
The specific work process of the utility model is as follows：During work, the cold wind in nature is sucked and is sent to by wind turbine A1
In the shell side 3 of spray drying tower 2,2 top entry of hot wind self-spray drying tower is sent into tower, spray drying tower 2 is worked
Cheng Zhong, since the heat transfer process between the cold wind in hot wind and shell side 3 in tower causes cold wind preheating to become warm wind, the warm wind of generation
After being extracted out by wind turbine B4 and being mixed with the wind turbine C5 natural cold wind sucked, first time heating is carried out into first-class heat exchanger 6, so
After be re-fed into secondary heat exchanger 7 and carry out second and heat, finally heat 170 DEG C obtained of hot wind again by spray drying tower 2
Top entry, which is sent into tower, completes drying operation.
It should be noted that above example is merely intended for describing the technical solutions of the present application, but not for limiting the present application.Although ginseng
This is described in detail with novel according to embodiment, it will be apparent to an ordinarily skilled person in the art that this with novel skill
Art scheme is modified or replaced equivalently, and the spirit and scope of new technique scheme are used without departure from this, should all be covered
This is in novel right.
Claims (5)
1. a kind of spray drying tower hot air heating system, it is characterised in that：Including wind turbine A（1）, spray drying tower（2）, wind turbine B
（4）, wind turbine C（5）, first-class heat exchanger（6）And secondary heat exchanger（7）, the wind turbine A（1）Inlet scoop communicated with the Nature, go out
Air port is with being set to the spray drying tower（2）Shell side（3）The cold air inlet connection at top, the shell side（3）The wind of bottom
The wind turbine B is connected at mouthful（4）；The wind turbine C（5）Inlet scoop communicated with the Nature, air outlet and be connected to the wind
Machine B（4）After the pipeline of air outlet is connected, with the first-class heat exchanger（6）Import connection, the first-class heat exchanger（6）Outlet
With the secondary heat exchanger（7）Import connect, the secondary heat exchanger（7）Outlet with positioned at the spray drying tower（2）
The hot wind inlet connection at top；The first-class heat exchanger（6）, secondary heat exchanger（7）Inside include several heat-exchanging components（8）.
2. a kind of spray drying tower hot air heating system according to claim 1, it is characterised in that：The wind turbine A（1）、
Wind turbine C（5）Inlet scoop be equipped with dust-proof purifying device.
3. a kind of spray drying tower hot air heating system according to claim 1, it is characterised in that：The first-class heat exchanger
（6）In include at least have heat-exchanging component described in three groups（8）.
4. a kind of spray drying tower hot air heating system according to claim 1, it is characterised in that：The first-class heat exchanger
（7）In include at least have heat-exchanging component described in 12 groups（8）.
5. a kind of spray drying tower hot air heating system according to claim 2, it is characterised in that：The dust-proof purifying dress
It is set to cotton.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721607766.1U CN207515481U (en) | 2017-11-27 | 2017-11-27 | A kind of spray drying tower hot air heating system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721607766.1U CN207515481U (en) | 2017-11-27 | 2017-11-27 | A kind of spray drying tower hot air heating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207515481U true CN207515481U (en) | 2018-06-19 |
Family
ID=62541429
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|---|---|---|---|
| CN201721607766.1U Active CN207515481U (en) | 2017-11-27 | 2017-11-27 | A kind of spray drying tower hot air heating system |
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| Country | Link |
|---|---|
| CN (1) | CN207515481U (en) |
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2017
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