CN201688675U - Fiber drying flue gas temperature control device - Google Patents
Fiber drying flue gas temperature control device Download PDFInfo
- Publication number
- CN201688675U CN201688675U CN2010201964798U CN201020196479U CN201688675U CN 201688675 U CN201688675 U CN 201688675U CN 2010201964798 U CN2010201964798 U CN 2010201964798U CN 201020196479 U CN201020196479 U CN 201020196479U CN 201688675 U CN201688675 U CN 201688675U
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- China
- Prior art keywords
- flue gas
- air
- drying
- fan
- mixing chamber
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- 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.)
- Expired - Lifetime
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 83
- 239000003546 flue gas Substances 0.000 title claims abstract description 83
- 238000001035 drying Methods 0.000 title claims abstract description 39
- 239000000835 fiber Substances 0.000 title claims abstract description 22
- 238000002156 mixing Methods 0.000 claims abstract description 35
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 239000000428 dust Substances 0.000 claims description 16
- 238000005453 pelletization Methods 0.000 claims description 15
- 239000000779 smoke Substances 0.000 claims description 8
- 238000005516 engineering process Methods 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000003517 fume Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000010355 oscillation Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Images
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- Drying Of Solid Materials (AREA)
Abstract
An embodiment of the utility model relates to a fiber drying flue gas temperature control device, which comprises a flue gas input pipeline, a cooling air input pipeline, a mixing chamber, a flue gas conveying pipeline, a dustproof system, a draft fan, a flue gas mixing box and a drying fan. The flue gas input pipeline and the cooling air input pipeline are arranged on one side of the mixing chamber in parallel, and the mixing chamber, the dustproof system, the draft fan, the flue gas mixing box and the draying fan are sequentially arranged and connected with one another through the flue gas conveying pipe. The temperature control device is characterized in that an air door with adjusting opening degree is arranged at a position on the side face of the flue gas mixing box opposite to an inlet of the drying flue gas fan. On the one hand, the temperature control device can lead in air quantity with adjusting inletting quantity by the air door, more effectively lowers flue gas temperature than traditional technology, and obtains fibers with water content conforming to standards, and on the other hand, after fresh air is added, the device increases total quantity and pressure of flue gas, is simple and easy to realize, is convenient in operation, and lowers running cost.
Description
Technical field
The utility model relates to density fiber board and produces flue gas drying temperature control technology field, particularly relates to a kind of fiber drying flue gas attemperating unit.
Background technology
----screening----boiling------fiber separation----applying glue----drying--------precompressed----hot pressing----cooling----the sanding----check----that grades-packing warehouse-in of mating formation that the Fibreboard Production technological process is: section.
For reaching satisfactory fiber moisture, when being carried out drying, fiber needs after the applying glue step temperature and pressure of flue gas is rationally controlled, generally adopt the flue gas drying technology.But from the flue-gas temperature of heating center usually up to 500 ℃, and the required baking temperature of fiber is about 250 ℃, for example the index of the hot flue gas that my company's fibreboard production line is suitable at present is: in flue-gas temperature 300-360 ℃, in the flue gas pressures 7-12mbar, dry inlet temperature is controlled in the 150-175 ℃ of scope, if so can not regulate to flue-gas temperature, certainly will the drying process temperature of fiber be impacted, too high flue-gas temperature also produces the condition of a fire easily in drying tube simultaneously, need flue-gas temperature is carried out cooling processing for this reason, usually carry cooling air to mix by a 150KW cooling blower with high-temperature flue gas, guarantee the fiber drying technological temperature, but the blower fan long-play causes energy consumption, improves production cost.
The structural representation of the gas fume conveying system of Fig. 1 prior art, with reference to shown in Figure 1, the gas fume conveying system of prior art comprises following components successively: flue gas input channel, cooling air input channel, mixing chamber, smoke conveying duct, dust pelletizing system, air-introduced machine, flue gas blending bin, drying air fan etc.
The utility model content
Technical problem to be solved in the utility model provides a kind of fiber drying flue gas attemperating unit, can effectively regulate flue-gas temperature, and can reduce the energy consumption in fiber drying in the Fibreboard Production, the course of conveying, and then reduces production costs.
For solving the problems of the technologies described above, the utility model is achieved in that
A kind of fiber drying flue gas attemperating unit, comprise: the flue gas input channel, the cooling air input channel, mixing chamber, smoke conveying duct, dust pelletizing system, air-introduced machine, the flue gas blending bin, drying air fan, flue gas input channel and cooling air input channel are located at a side of mixing chamber side by side, the opposite side of mixing chamber is connected to dust pelletizing system by smoke conveying duct, air-introduced machine is located between dust pelletizing system and the flue gas blending bin, drying air fan is located at flue gas blending bin opposite side, between dust pelletizing system and air-introduced machine, be equipped with flue between air-introduced machine and the flue gas blending bin, it is characterized in that being provided with air door at the position relative, flue gas blending bin side with the dry flue gas fans entrance.
Described air door is made up of grid, rocking bar, adjusting YE, and grid is installed in the framework two side of air door, is connected on the air door YE by rocking bar, between rocking bar and the rocking bar, all be connected by oscillating bearing between rocking bar and the grid.When flue-gas temperature changes, temperature sensor in the flue passes to PLC (programmable controller) with the signal of variations in temperature, PLC feeds back to YE after signal is handled then, the corresponding rotating band of making YE shakes the bar motion, rocking bar drives the grid swing, grid can collective open and close under the effect of rocking bar, and the degree that opens and closes is subjected to the interior temperature program instruction of PLC to make corresponding adjusting, enter the amount of the air of system with control, when flue-gas temperature is very high, the air door grid is opened greatly, and when flue-gas temperature was high slightly, the air door grid was opened a little, when flue-gas temperature is moderate, the air door grid is closed, and the aperture of air door grid size just forms an automatic control system with flue-gas temperature like this, and the information exchange between PLC realization and man-machine interface
The utility model has following positive effect: the utility model is provided with the adjustable air door of aperture at the position relative with the dry flue gas fans entrance, flue gas blending bin side, can be according to the height of flue-gas temperature, the amount of the Cryogenic air that control is introduced, generally speaking can introduce than conventional art more the air of the low temperature of volume mix in the flue gas blending bin with high-temperature flue gas, flue gas blower fan outlet temperature is controlled in 300-360 ℃, flue gas pressures rises to 7-12mbar, the drying air fan inlet temperature is reduced to safe below 175 ℃, the pressure oscillation of flue gas be improved significantly.Therefore can reach accurate control flue-gas temperature on the one hand, reduce the purpose of flue-gas temperature, obtain satisfactory fiber moisture.On the other hand, introduce fresh Cryogenic air after, increased the total amount of flue gas, improved the pressure of dry flue gas behind the drying blower fan.Equipment simply is easy to realize, and operation is convenient, has reduced the cost of operation.
Description of drawings
The structural representation of the gas fume conveying system of Fig. 1 prior art;
Fig. 2 is the structural representation of fiber drying flue gas attemperating unit of the present utility model;
Fig. 3 is the adjustable damper overall structure schematic diagram of fiber drying flue gas attemperating unit of the present utility model;
Fig. 4 is the front view of the adjustable damper present position of fiber drying flue gas attemperating unit of the present utility model;
Fig. 5 is the lateral plan of the adjustable damper of fiber drying flue gas attemperating unit of the present utility model.
The specific embodiment
Below in conjunction with the specific embodiment the utility model is described in further detail.
With reference to shown in Figure 2, a kind of fiber drying flue gas attemperating unit, comprise: flue gas input channel 7, cooling air input channel 6, mixing chamber 1, smoke conveying duct 8, dust pelletizing system 2, air-introduced machine 3, flue gas blending bin 4, drying air fan 5, flue gas input channel 7 and cooling air input channel 6 are located at a side of mixing chamber 1 side by side, the opposite side of mixing chamber 1 is connected to dust pelletizing system 2 by smoke conveying duct 8, air-introduced machine 3 is located between dust pelletizing system 2 and the flue gas blending bin 4, drying air fan 5 is located at flue gas blending bin 4 opposite sides, between dust pelletizing system 2 and air-introduced machine 3, be equipped with flue 8 between air-introduced machine 3 and the flue gas blending bin 4, the position relative with drying air fan 5 inlets in flue gas blending bin 8 sides is provided with air door 11.The dust mouth 9 of dust pelletizing system 2 is located at the bottom of dust pelletizing system, and the outlet 10 of drying air fan is located at the top of drying air fan 5.
With reference to shown in Fig. 3 to 5, described air door 11 is made up of grid 12, rocking bar 13, YE 14, grid is installed in the framework two side of air door, is connected on the YE by rocking bar, between rocking bar and the rocking bar, all be connected by oscillating bearing between rocking bar and the grid.When flue-gas temperature changed, grid can collective under the effect of rocking bar opens and closes, and the degree that opens and closes can regulate, and with the amount that adjusting enters the air of system, the YE of installing on the air door is in order to the automatic control storm door aperture.Throttle opening is controlled in the drying equipment robot control system(RCS) of interlocking, and is controlled by dry control operation man-machine interface, controls according to the ability of dried fibres.
The design of damper: by the amount of calculating flue gas flow and needing to replenish fresh air, air intake surplus with due regard to, at the position relative, flue gas blending bin side with the dry flue gas fans entrance, the entry position of drying air fan, open the square air inlet of a 650mm * 650mm, a flap type damper is installed at the air inlet place, and YE is installed, in order to the control throttle opening, the amount of control air.Throttle opening is controlled in the drying equipment robot control system(RCS) of interlocking, and is controlled by dry control operation man-machine interface, controls according to the ability of dried fibres.By reasonable control, flue gas blower fan outlet temperature can be controlled in 300-360 ℃, and flue gas pressures rises to 7-12mbar, and the drying machine inlet temperature is reduced to safe below 175 ℃, the pressure oscillation of flue gas be improved significantly.
The above-mentioned specific embodiment does not limit the technical solution of the utility model in any form, and the technical scheme that mode obtained that every employing is equal to replacement or equivalent transformation all drops on protection domain of the present utility model.
Claims (2)
1. fiber drying flue gas attemperating unit, comprise: flue gas input channel (7), cooling air input channel (6), mixing chamber (1), smoke conveying duct (8), dust pelletizing system (2), air-introduced machine (3), flue gas blending bin (4), drying air fan (5), flue gas input channel (7) and cooling air input channel (6) are located at a side of mixing chamber (1) side by side, the opposite side of mixing chamber (1) is connected to dust pelletizing system (2) by smoke conveying duct (8), air-introduced machine (3) is located between dust pelletizing system (2) and the flue gas blending bin (4), drying air fan (5) is located at flue gas blending bin (4) opposite side, between dust pelletizing system (2) and air-introduced machine (3), be equipped with smoke conveying duct (8) between air-introduced machine (3) and the flue gas blending bin (4), it is characterized in that the position relative with drying air fan (5) inlet in flue gas blending bin (4) side is provided with air door (11).
2. fiber drying flue gas attemperating unit according to claim 1, it is characterized in that described air door (11) is made up of grid (12), rocking bar (13), YE (14), grid (12) is installed in framework two madial walls of air door (11) and is connected on the YE (14) by rocking bar (13), between rocking bar (13) and the rocking bar (13), all be connected by oscillating bearing between rocking bar (13) and the grid (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201964798U CN201688675U (en) | 2010-05-19 | 2010-05-19 | Fiber drying flue gas temperature control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201964798U CN201688675U (en) | 2010-05-19 | 2010-05-19 | Fiber drying flue gas temperature control device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201688675U true CN201688675U (en) | 2010-12-29 |
Family
ID=43376955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201964798U Expired - Lifetime CN201688675U (en) | 2010-05-19 | 2010-05-19 | Fiber drying flue gas temperature control device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201688675U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110292186A (en) * | 2019-08-12 | 2019-10-01 | 上海馨籽咖啡有限公司 | A kind of baking beans machine |
| CN110940180A (en) * | 2019-11-07 | 2020-03-31 | 广东省乾鸿木业有限公司 | Device and method for drying wood fibers at low temperature |
| CN113606595A (en) * | 2021-08-04 | 2021-11-05 | 河北天龙环保科技有限公司 | Multi-valve-group heat storage high-temperature oxidation system |
-
2010
- 2010-05-19 CN CN2010201964798U patent/CN201688675U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110292186A (en) * | 2019-08-12 | 2019-10-01 | 上海馨籽咖啡有限公司 | A kind of baking beans machine |
| CN110292186B (en) * | 2019-08-12 | 2024-06-11 | 上海馨籽咖啡有限公司 | Bean baking machine |
| CN110940180A (en) * | 2019-11-07 | 2020-03-31 | 广东省乾鸿木业有限公司 | Device and method for drying wood fibers at low temperature |
| CN113606595A (en) * | 2021-08-04 | 2021-11-05 | 河北天龙环保科技有限公司 | Multi-valve-group heat storage high-temperature oxidation system |
| CN113606595B (en) * | 2021-08-04 | 2024-03-29 | 河北天龙环保科技有限公司 | Multi-valve-group heat-storage high-temperature oxidation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Muya wood (Fujian) Co. Ltd. Assignor: Daya Sci & Tech. Co., Ltd. Contract record no.: 2011320000408 Denomination of utility model: Fiber drying flue gas temperature control device Granted publication date: 20101229 License type: Exclusive License Record date: 20110325 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151118 Address after: Danyang city Jiangsu Road on the north side of the 212300 large province of Danyang Development Zone Patentee after: Dare Wood Based Panel Group Co., Ltd. Address before: 212300 No. 95 Jinling West Road, Danyang Economic Development Zone, Jiangsu, China Patentee before: Daya Sci & Tech. Co., Ltd. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20101229 |
|
| CX01 | Expiry of patent term |