CN205909656U - Honeycombed denitrification catalyst dry kiln - Google Patents
Honeycombed denitrification catalyst dry kiln Download PDFInfo
- Publication number
- CN205909656U CN205909656U CN201620807302.4U CN201620807302U CN205909656U CN 205909656 U CN205909656 U CN 205909656U CN 201620807302 U CN201620807302 U CN 201620807302U CN 205909656 U CN205909656 U CN 205909656U
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- conveyer belt
- kiln
- denitrification catalyst
- metal heat
- hot
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Abstract
The utility model relates to a drying device specifically is honeycombed denitrification catalyst dry kiln, including the kiln body, the kiln is internal to have the conveyer belt, and articulated in proper order on the conveyer belt have a plurality of metal heat -conducting plates, and there is the feed inlet top of conveyer belt feed end, and there is the discharge gate below of conveyer belt discharge end, the below of conveyer belt also have the hot -blast main, the hot -blast main on have a plurality of hot air exitus, hot air exitus up. The utility model provides a honeycombed denitrification catalyst dry kiln, the metal heat -conducting plate on the conveyer belt is fallen to the denitration catalyst that needs to dry under the feed inlet, and the denitration catalyst is dried to the metal heat -conducting plate, the conveyer belt discharge end, the upset is poured out the denitration catalyst from the discharge gate, and the input material that can last carries out the drying to need not open the kiln body, the energy has been practiced thrift to the internal constancy of temperature that keeps of kiln.
Description
Technical field
This utility model is related to a kind of drying device, specially honeycomb type denitrification catalyst dry kiln.
Background technology
Need sufficiently to be dried before denitrating catalyst packaging, conventional drying mode is to adopt heater, device is kiln
Body formula, denitrating catalyst is put in container, and container is put in heater and dries, and opens kiln body and take out after drying, this dry
The every batch heating of dry device is unpacked, and in kiln body, hot-air just scatters and disappears, and during next batch re-dry, needs to reheat, and wastes energy
Source.
Utility model content
For above-mentioned technical problem, this utility model provides a kind of honeycomb type denitrification catalyst dry kiln of energy-conservation.Specifically
Technical scheme be:
Honeycomb type denitrification catalyst dry kiln, including kiln body, has conveyer belt, conveyer belt is hinged with successively multiple in kiln body
Metal heat-conducting plate, there is charging aperture the top of conveyer belt feed end, and there is discharging opening the lower section of conveyer belt discharge end；Described conveyer belt
Lower section also have warm-air pipe, described warm-air pipe has multiple hot-blast outlets, described hot-blast outlet is upward.
There is baffle plate the both sides of described conveyer belt.
Air outlet is arranged at described kiln body top, and described air outlet is connected with warm-air pipe by pipeline, forms circulation air path.
The honeycomb type denitrification catalyst dry kiln that this utility model provides, needs the denitrating catalyst dried from charging aperture
Drop to the metal heat-conducting plate on conveyer belt, metal heat-conducting plate, by drying denitration catalyst, conveyer belt discharge end, upset, will take off
Denox catalyst is poured out from discharging opening, and the input material that can continue is dried, and does not need to open holding in kiln body, kiln body
Temperature constant, has saved the energy.
Brief description
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Of the present utility model specific embodiment is described with reference to the drawings, as shown in figure 1, honeycomb type denitrification catalyst is dried
Kiln, including kiln body 1, has conveyer belt 3, conveyer belt 3 is hinged with multiple metal heat-conducting plates 5 successively, conveyer belt 3 feeds in kiln body 1
There is charging aperture 2 top at end, and there is discharging opening 4 lower section of conveyer belt 3 discharge end；The lower section of described conveyer belt 3 also has warm-air pipe
6, described warm-air pipe 6 has multiple hot-blast outlets 7, described hot-blast outlet 7 is upward.
There is baffle plate the both sides of described conveyer belt 3.
Air outlet is arranged at described kiln body 1 top, and described air outlet is connected with warm-air pipe 6 by pipeline 8, forms circulated air
Road.
The denitrating catalyst dried is needed to drop to the metal heat-conducting plate 5 conveyer belt 3, metal heat-conducting plate from charging aperture 2
5 by drying denitration catalyst.Metal heat-conducting plate 5 runs to conveyer belt 3 discharge end, upset, and denitrating catalyst is fallen from discharging opening 4
Go out.The hot blast that metal heat-conducting plate 5 is imported by warm-air pipe 6 in lower section is heated.
The air outlet of kiln body 1 is connected with warm-air pipe 6 by pipeline 8, and steam is circulated utilization.
Claims (3)
1. honeycomb type denitrification catalyst dry kiln, including kiln body (1) it is characterised in that: have conveyer belt (3) in kiln body (1), transmission
It is hinged with multiple metal heat-conducting plates (5) successively, there are charging aperture (2), conveyer belt (3) in the top of conveyer belt (3) feed end on band (3)
There is discharging opening (4) lower section of discharge end；The lower section of described conveyer belt (3) also has warm-air pipe (6), on described warm-air pipe (6)
There are multiple hot-blast outlets (7), described hot-blast outlet (7) is upward.
2. honeycomb type denitrification catalyst dry kiln according to claim 1 it is characterised in that: described conveyer belt (3)
There is baffle plate both sides.
3. honeycomb type denitrification catalyst dry kiln according to claim 1 and 2 it is characterised in that: described kiln body (1) top
There is air outlet in portion, and described air outlet is connected with warm-air pipe (6) by pipeline (8), forms circulation air path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620807302.4U CN205909656U (en) | 2016-07-29 | 2016-07-29 | Honeycombed denitrification catalyst dry kiln |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620807302.4U CN205909656U (en) | 2016-07-29 | 2016-07-29 | Honeycombed denitrification catalyst dry kiln |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205909656U true CN205909656U (en) | 2017-01-25 |
Family
ID=57802403
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620807302.4U Active CN205909656U (en) | 2016-07-29 | 2016-07-29 | Honeycombed denitrification catalyst dry kiln |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205909656U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115028294A (en) * | 2022-07-19 | 2022-09-09 | 华夏碧水环保科技股份有限公司 | Magnetic catalytic oxidation wastewater treatment system with recycling integration |
-
2016
- 2016-07-29 CN CN201620807302.4U patent/CN205909656U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115028294A (en) * | 2022-07-19 | 2022-09-09 | 华夏碧水环保科技股份有限公司 | Magnetic catalytic oxidation wastewater treatment system with recycling integration |
| CN115028294B (en) * | 2022-07-19 | 2024-02-20 | 华夏碧水环保科技股份有限公司 | Recycling integrated magnetic catalytic oxidation wastewater treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |