CN205718379U - Produce the boiler smoke waste heat recovery plant of organosilicon - Google Patents
Produce the boiler smoke waste heat recovery plant of organosilicon Download PDFInfo
- Publication number
- CN205718379U CN205718379U CN201620334143.0U CN201620334143U CN205718379U CN 205718379 U CN205718379 U CN 205718379U CN 201620334143 U CN201620334143 U CN 201620334143U CN 205718379 U CN205718379 U CN 205718379U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- pipe
- interconnecting part
- drying room
- boiler smoke
- 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.)
- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
This utility model relates to a kind of boiler smoke waste heat recovery plant producing organosilicon, and including a drying room, one first pipeline and a second pipe, the first pipeline and second pipe run through drying room；The left end of the first pipeline and second pipe is interconnected, and is defined as the first interconnecting part, and the first interconnecting part is connected with boiler flue gas outlet pipeline；The right-hand member of the first pipeline and second pipe is interconnected, and is defined as the second interconnecting part, and the second interconnecting part is connected with exhaust gas processing device；Being provided with multiple turbulent baffle in first pipeline, turbulent baffle is crisscross arranged in the first inner-walls of duct, and second pipe is provided with a control valve, controls valve between the first interconnecting part and drying room.The boiler smoke waste heat recovery plant of described production organosilicon passes through said structure, can effectively utilize the heat of boiler smoke, and make drying room heat, the raw material such as activated carbon, white carbon can be carried out high-temperature activation, its simple in construction, and can reduce production cost.
Description
Technical field
This utility model relates to a kind of boiler smoke waste heat recovery plant producing organosilicon, for field of organic silicon.
Background technology
At present, organosilicon needs to use the raw material such as activated carbon, white carbon in producing, and these raw materials need to carry out high-temperature activation process before use, in order to prevent these raw materials moisture absorption during storing, typically deposit in special drying room, the heat supply and existing drying room is required to individually be energized, causes production cost higher.
It is therefore desirable to design a kind of boiler smoke waste heat recovery plant producing organosilicon, to overcome the problems referred to above.
Utility model content
The purpose of this utility model is to overcome the defect of prior art, it is provided that a kind of boiler smoke waste heat recovery plant producing organosilicon reducing production cost.
This utility model is achieved in that
This utility model provides a kind of boiler smoke waste heat recovery plant producing organosilicon, and including a drying room, one first pipeline and a second pipe, described first pipeline and described second pipe run through described drying room；The left end of described first pipeline and described second pipe is interconnected, and is defined as the first interconnecting part, and described first interconnecting part is connected with boiler flue gas outlet pipeline；The right-hand member of described first pipeline and described second pipe is interconnected, and is defined as the second interconnecting part, and described second interconnecting part is connected with exhaust gas processing device；Being provided with multiple turbulent baffle in described first pipeline, described turbulent baffle is crisscross arranged in described first inner-walls of duct, and described second pipe is provided with a control valve, and described control valve is between described first interconnecting part and described drying room.
Further, described first pipeline and described second pipe be arranged in parallel.
Further, it is provided with current limliting block in described second interconnecting part.
Further, multiple turbulent baffles are uniformly arranged.
This utility model has the advantages that
It is provided with multiple turbulent baffle in described first pipeline, the flue gas making heat completes substantial amounts of heat exchange in drying room, then the temperature in drying room is improved, by arranging described control valve, can effectively control the admission velocity of flue gas, thus control the temperature in drying room, the boiler smoke waste heat recovery plant of described production organosilicon passes through said structure, can effectively utilize the heat of boiler smoke, and make drying room heat, the raw material such as activated carbon, white carbon can be carried out high-temperature activation, its simple in construction, and production cost can be reduced.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
The structural representation of the boiler smoke waste heat recovery plant producing organosilicon that Fig. 1 provides for this utility model embodiment.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, all other embodiments that those of ordinary skill in the art are obtained on the premise of not making creative work, broadly fall into the scope of this utility model protection.
Such as Fig. 1, this utility model embodiment provides a kind of boiler smoke waste heat recovery plant producing organosilicon, and including drying room 3,1 first pipeline 1 and a second pipe 2, described first pipeline 1 and described second pipe 2 run through described drying room 3.Wherein, described first pipeline 1 and described second pipe 2 be arranged in parallel.Described first pipeline 1 carries out heat exchange with the flue gas in described second pipe 2 inside described drying room 3, then makes drying room 3 internal temperature increase, and described drying room 3 is used for the raw material such as activated carbon, white carbon is carried out high-temperature activation,
Such as Fig. 1, the left end of described first pipeline 1 and described second pipe 2 is interconnected, and is defined as the first interconnecting part 4, and described first interconnecting part 4 is connected with boiler flue gas outlet pipeline.Described first pipeline 1 and described second pipe 2 is simultaneously entered from the flue gas of described boiler flue gas outlet pipeline heat out.
Such as Fig. 1, the right-hand member of described first pipeline 1 and described second pipe 2 is interconnected, and is defined as the second interconnecting part 5, and described second interconnecting part 5 is connected with exhaust gas processing device, described exhaust gas processing device, for absorbing the tail gas through heat exchange thoroughly, prevents it from entering air pollution environmental.Be provided with current limliting block 51 in described second interconnecting part 5, for time gas flow temperature discharge.
Such as Fig. 1, being provided with multiple turbulent baffle 11 in described first pipeline 1, described turbulent baffle 11 is crisscross arranged in described first pipeline 1 inwall, and described turbulent baffle 11 can strengthen the contact area of flue gas and inner-walls of duct, improves heat exchange efficiency.In this preferred embodiment, multiple turbulent baffles 11 are uniformly arranged.
Being provided with a control valve 6 on described second pipe 2, described control valve 6 is between described first interconnecting part 4 and described drying room 3.Described control valve 6 can effectively control the admission velocity of flue gas, thus controls the temperature in drying room 3.
In sum, the boiler smoke waste heat recovery plant of described production organosilicon passes through said structure, can effectively utilize the heat of boiler smoke, and make drying room 3 heat, the raw material such as activated carbon, white carbon can be carried out high-temperature activation, its simple in construction, and production cost can be reduced.
The foregoing is only preferred embodiment of the present utility model; not in order to limit this utility model; all within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (4)
1. the boiler smoke waste heat recovery plant producing organosilicon, it is characterised in that include a drying room, one first pipeline and a second pipe, described first pipeline and described second pipe run through described drying room；
The left end of described first pipeline and described second pipe is interconnected, and is defined as the first interconnecting part, and described first interconnecting part is connected with boiler flue gas outlet pipeline；
The right-hand member of described first pipeline and described second pipe is interconnected, and is defined as the second interconnecting part, and described second interconnecting part is connected with exhaust gas processing device；
Being provided with multiple turbulent baffle in described first pipeline, described turbulent baffle is crisscross arranged in described first inner-walls of duct, and described second pipe is provided with a control valve, and described control valve is between described first interconnecting part and described drying room.
2. the boiler smoke waste heat recovery plant producing organosilicon as claimed in claim 1, it is characterised in that: described first pipeline and described second pipe be arranged in parallel.
3. the boiler smoke waste heat recovery plant producing organosilicon as claimed in claim 1 or 2, it is characterised in that: it is provided with current limliting block in described second interconnecting part.
4. the boiler smoke waste heat recovery plant producing organosilicon as claimed in claim 1 or 2, it is characterised in that: multiple turbulent baffles are uniformly arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620334143.0U CN205718379U (en) | 2016-04-20 | 2016-04-20 | Produce the boiler smoke waste heat recovery plant of organosilicon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620334143.0U CN205718379U (en) | 2016-04-20 | 2016-04-20 | Produce the boiler smoke waste heat recovery plant of organosilicon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205718379U true CN205718379U (en) | 2016-11-23 |
Family
ID=57298652
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620334143.0U Expired - Fee Related CN205718379U (en) | 2016-04-20 | 2016-04-20 | Produce the boiler smoke waste heat recovery plant of organosilicon |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205718379U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107449287A (en) * | 2017-08-28 | 2017-12-08 | 太仓贝斯特机械设备有限公司 | Mould heating furnace waste heat recovery apparatus |
-
2016
- 2016-04-20 CN CN201620334143.0U patent/CN205718379U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107449287A (en) * | 2017-08-28 | 2017-12-08 | 太仓贝斯特机械设备有限公司 | Mould heating furnace waste heat recovery apparatus |
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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: 20161123 Termination date: 20180420 |
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| CF01 | Termination of patent right due to non-payment of annual fee |