CN203657385U - Secondary drying tunnel kiln for cellular SCR denitration catalyst - Google Patents
Secondary drying tunnel kiln for cellular SCR denitration catalyst Download PDFInfo
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- CN203657385U CN203657385U CN201320795264.1U CN201320795264U CN203657385U CN 203657385 U CN203657385 U CN 203657385U CN 201320795264 U CN201320795264 U CN 201320795264U CN 203657385 U CN203657385 U CN 203657385U
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- drying tunnel
- owner body
- secondary drying
- denitrating catalyst
- tunnel cave
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Abstract
A secondary drying tunnel kiln for a cellular SCR denitration catalyst comprises a drying tunnel kiln body, a hot air supplying device and a drying trolley. The drying tunnel kiln body is provided with an inlet and an outlet. The secondary drying tunnel kiln is characterized by further comprising a draught fan used for pumping waste gas; the hot air supplying device comprises a heater, an air feeder and a circulating fan; the heater, the air feeder and the circulating fan are connected together through an air feeding pipeline; the drying trolley can enter the drying tunnel kiln body. According to the secondary drying tunnel kiln, an excellent hot air heating system and an excellent waste gas absorption system are arranged, so that full-automatic continuous production is achieved, hand labor intensity is lowered, an operation environment is improved, product quality can be enhanced, and labor intensity is low.
Description
Technical field
The utility model relates to a kind of drying device, is specifically related to a kind of secondary drying tunnel cave for the production of honeycomb fashion SCR denitrating catalyst.
Background technology
Due to mankind's activity and economic fast development, China's environment is seriously damaged, and extreme climate showed increased causes serious threat to people's life and property, causes heavy losses to country, has hindered the sustainable development of national economy simultaneously.Country has also paid huge cost in order to administer environment.
The current discharged nitrous oxides total amount of China has exceeded 1,800 ten thousand tons, if do not take effective control measure, 5 years Chinese nitrogen oxide emissions of Future Ten will continue to increase, and may reach more than 3,000 ten thousand tons to the year two thousand twenty.China is coal-fired big country, and coal-burning power plant is the primary emission source of nitrogen oxide, accounts for 40% of total amount, will become the first batch of control object of country.
Honeycomb ceramics SCR denitrating catalyst Main Function is by the NO in discharging waste gas
xconvert nitrogen and steam to, to reach environmental emission standard.
SCR device is mainly made up of two large main bodys: remove agent preparation system and reactor body.By spray into reactant NH in reactor
3, NOx is reduced to nitrogen.Because this reduction reaction is comparatively responsive to temperature, therefore need add catalyst with intensified response activity, meet the temperature requirement of reaction.
Honeycomb fashion SCR denitrating catalyst main component generally comprises nano-TiO
2, V
2o
5and WO
3.These three kinds of shared catalyst ratios of composition exceed 95 ﹪, and TiO
2proportion is generally 80%～85%.In order to meet production technology needs, guarantee easy extrusion modling, also needing in addition to increase the mixture additives such as some viscose glues and glass fibre increases pug intensity and mobility, adjusts its physical property.Due to these compositions stir mixing rear mobility and plasticity poor, moulding difficulty is larger.Again because the water holding capacity of product is poor, atmospheric crack very easily after moulding is also higher to the production engineering specifications of dry kiln.In dry run, can produce some NH
3, SO
3deng corrosive gas, the quality of product is had to certain influence, therefore, dry kiln need to possess good heating system and waste gas absorbing system, and wants to realize automatic operation, raises the efficiency.
Summary of the invention
The utility model provides a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave.This secondary drying tunnel cave can be realized automated production, and high insulating effect is energy-saving and cost-reducing, has good hot air heating system and waste gas absorbing system, and product quality is high.
In order to solve the problems of the technologies described above, the utility model is achieved through the following technical solutions: a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave, comprise the drying alley kiln owner body, hot air supplier, the dry dolly that are provided with entrance and outlet, it is characterized in that, also comprise the air-introduced machine for extracting waste gas, described hot air supplier comprises heater, pressure fan, circulating fan, described heater, pressure fan, circulating fan link together by air supply duct, and described dry dolly can enter in described drying alley kiln owner body.Described heater heats with wind for being dried, blower-use is in dry after heating delivered to air supply duct with wind, circulating fan extracts the hot blast in air supply duct product is carried out to heat drying, the waste gas producing is discharged through described air-introduced machine, this air circulation system can well heat product, combustion gas simultaneously, reduces the impact of waste gas on product.Described dry dolly can easily transport product and enter in described drying alley kiln owner body.
As preferably, in described drying alley kiln owner body, be provided with delivery track, described dry dolly is provided with the wheel mating with described delivery track.By described delivery track, dolly can one one be close to and enters in drying alley kiln owner body, convenient and swift, saves time, and has improved efficiency.
As preferably, described circulating fan is crisscross arranged in the both sides of described drying alley kiln owner body.Such setting makes hot blast rationally penetrate the cellular space of product to carry out repeatedly circulating-heating, dry, effective.
As preferably, described pressure fan is connected with frequency-variable controller.Can control overall air output, and then control temperature.
As preferably, described air-introduced machine is connected with frequency-variable controller.Can control overall exhaust air rate.
As preferably, the porch of described drying alley kiln owner body is provided with hydraulic pusher structure.By described hydraulic pusher structure, dry dolly can enter described delivery track easily.
As preferably, the exit of described drying alley kiln owner body is provided with automatic traction device.Described automatic traction device can easily pull out the dry dolly in described drying alley kiln owner body.
As preferably, the body frame of described drying alley kiln owner body is shape, and the kiln body of described drying alley kiln owner body is thermal insulating composite panel, and entrance and the exit of described drying alley kiln owner body are provided with gate.Can improve the heat insulation effect in dry run.
Compared with prior art, the utlity model has following beneficial effect: 1, the utility model is realized continuously full-automatic production, reduces hand labor intensity, improved operating environment.
2, dry wind repeatedly circulates, is evenly dried, energy-saving and cost-reducing.
3, the fire-retardant coefficient of kiln body case of drying alley kiln owner body is high, and high insulating effect is energy-saving and cost-reducing.
4, design temperature curve, makes the heating of product experience, freeze-day with constant temperature, cooling overall process, produces continuously, guarantees the steady quality of product.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Fig. 2 is sectional view of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing and the specific embodiment, the utility model is described in further detail: a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave, comprise the drying alley kiln owner body 7, hot air supplier, the dry dolly 1 that are provided with entrance and outlet, also comprise the air-introduced machine 5 for extracting waste gas, described hot air supplier comprises heater 2, pressure fan 3, circulating fan 4, described heater 2, pressure fan 3, circulating fan 4 link together by air supply duct 9, and described dry dolly 1 can enter in described drying alley kiln owner body 7.In described drying alley kiln owner body 7, be provided with delivery track 6, described dry dolly 1 is provided with the wheel mating with described delivery track 6.Described circulating fan 4 is crisscross arranged in the both sides of described drying alley kiln owner body 7.Described pressure fan 3 is connected with frequency-variable controller.Described air-introduced machine 5 is also connected with frequency-variable controller.The porch of described drying alley kiln owner body 7 is provided with hydraulic pusher structure.The exit of described drying alley kiln owner body 7 is provided with automatic traction device.The body frame of described drying alley kiln owner body 7 is shape, and the kiln body of described drying alley kiln owner body 7 is thermal insulating composite panel, described drying alley kiln owner body) entrance and exit be provided with gate.
When work, described dry dolly 1 honeycomb fashion SCR denitrating catalyst base substrate is transported in secondary drying tunnel cave, and described dry dolly 1 is shape, and disjunctor backboard is set, and backboard is simultaneously as the subregion dividing plate in dry tunnel cave main body 7.Wheel is arranged at dry dolly 1 bottom, slides in orbit, and dolly is close to each other, heads into and movement by the hydraulic top truck system of inlet side.Every two parking stalls are a hot air circulation district, are divided into multiple districts.Heater 2 heats with wind dry, and pressure fan 3 is sent into dry after heating in air supply duct 9 with wind, and circulating fan 4 extracts the hot blast in air supply duct 9, blows to product.Because circulating fan 4 shifts to install in the both sides of described drying alley kiln owner body 7, hot blast can rationally penetrate the cellular space of product and carry out circulating-heating, dry, and drying effect is good.Meanwhile, the waste gas producing in dry run is got rid of by air-introduced machine 5, makes product quality unaffected.
Described pressure fan 3 is connected with frequency-variable controller, and described air-introduced machine 5 is connected with frequency-variable controller.The amount of adjustable air-supply and air draft, the temperature of adjusting drying alley kiln owner body 7, reaches better drying effect.
Claims (8)
1. a honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave, comprise the drying alley kiln owner body (7), hot air supplier, the dry dolly (1) that are provided with entrance and outlet, it is characterized in that, also comprise the air-introduced machine (5) for extracting waste gas, described hot air supplier comprises heater (2), pressure fan (3), circulating fan (4), described heater (2), pressure fan (3), circulating fan (4) link together by air supply duct (9), and described dry dolly (1) can enter in described drying alley kiln owner body (7).
2. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 1, it is characterized in that, in described drying alley kiln owner body (7), be provided with delivery track (6), described dry dolly (1) is provided with the wheel mating with described delivery track (6).
3. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 2, is characterized in that, described circulating fan (4) is crisscross arranged in the both sides of described drying alley kiln owner body (7).
4. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 3, is characterized in that, described pressure fan (3) is connected with frequency-variable controller.
5. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 4, is characterized in that, described air-introduced machine (5) is connected with frequency-variable controller.
6. according to a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave described in claim 1 ~ 5 any one, it is characterized in that, the porch of described drying alley kiln owner body (7) is provided with hydraulic pusher structure.
7. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 6, is characterized in that, the exit of described drying alley kiln owner body (7) is provided with automatic traction device.
8. a kind of honeycomb fashion SCR denitrating catalyst secondary drying tunnel cave according to claim 7, it is characterized in that, the body frame of described drying alley kiln owner body (7) is shape, the kiln body of described drying alley kiln owner body (7) is thermal insulating composite panel, and entrance and the exit of described drying alley kiln owner body (7) are provided with gate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320795264.1U CN203657385U (en) | 2013-12-06 | 2013-12-06 | Secondary drying tunnel kiln for cellular SCR denitration catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320795264.1U CN203657385U (en) | 2013-12-06 | 2013-12-06 | Secondary drying tunnel kiln for cellular SCR denitration catalyst |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203657385U true CN203657385U (en) | 2014-06-18 |
Family
ID=50923764
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320795264.1U Expired - Fee Related CN203657385U (en) | 2013-12-06 | 2013-12-06 | Secondary drying tunnel kiln for cellular SCR denitration catalyst |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203657385U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104075554A (en) * | 2014-07-09 | 2014-10-01 | 湖南长笛龙吟竹业有限公司 | Bamboo and wood material drying tunnel kiln |
| CN104215052A (en) * | 2014-09-03 | 2014-12-17 | 江苏宇达环保科技股份有限公司 | SCR (Selective Catalytic Reduction) catalyst drying system |
-
2013
- 2013-12-06 CN CN201320795264.1U patent/CN203657385U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104075554A (en) * | 2014-07-09 | 2014-10-01 | 湖南长笛龙吟竹业有限公司 | Bamboo and wood material drying tunnel kiln |
| CN104075554B (en) * | 2014-07-09 | 2016-01-13 | 湖南长笛龙吟竹业有限公司 | A kind of bamboo and wood materials drying alley kiln |
| CN104215052A (en) * | 2014-09-03 | 2014-12-17 | 江苏宇达环保科技股份有限公司 | SCR (Selective Catalytic Reduction) catalyst drying system |
| CN104215052B (en) * | 2014-09-03 | 2016-04-20 | 江苏宇达环保科技股份有限公司 | A kind of SCR catalyst drying system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140618 Termination date: 20151206 |
|
| EXPY | Termination of patent right or utility model |