CN205412566U - High temperature dust disposal recovery system - Google Patents
High temperature dust disposal recovery system Download PDFInfo
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- CN205412566U CN205412566U CN201620108239.5U CN201620108239U CN205412566U CN 205412566 U CN205412566 U CN 205412566U CN 201620108239 U CN201620108239 U CN 201620108239U CN 205412566 U CN205412566 U CN 205412566U
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Abstract
The utility model relates to a high temperature dust disposal recovery system, including gravity settling chamber, it advances the pipe to be equipped with waste gas on gravity settling chamber's the left side wall, the heat recovery case is connected through first gas -supply pipe in gravity settling chamber's top, be equipped with hot exchange pipe on the inner wall of heat recovery case, the top of heat recovery case is passed through the second gas -supply pipe and is connected the baffle -box, connect in parallel through the branch pipe and have first gas storage package in one side of second gas -supply pipe, all be connected with first pulse valve on the branch pipe of first gas storage package both sides, the top of baffle -box is passed through the third gas -supply pipe and is connected cyclone, the benefit blast gate is connected to one side of third gas -supply pipe, cyclone's top is passed through the fourth gas -supply pipe and is connected the sack cleaner, the fan is connected through the 5th gas -supply pipe in the right side of sack cleaner. The utility model discloses a high temperature dust disposal recovery system novel structure, through the combined action of a plurality of subassemblies, very big reduction in waste gas dust composition for the emission of waste gas reaches the environmental protection requirement.
Description
Technical field
This utility model relates to a kind of high-temperature dust and processes recovery system.
Background technology
China is a populous nation; it it is again the country that develops rapidly of an economy; 21 century is faced with the dual-pressure of economic growth and environmental conservation; the annual Fuel Consumption of China was 12-15 hundred million tons in recent years; wherein more than 80% directly burning for Thermal Equipments such as boilers; the sulfur dioxide of discharged from coal-fired boiler is 1400-1700 ten thousand tons; the city sulfur dioxide mean annual concentration of China 62.3% has exceeded national grade ii standard at present; acid rain all causes serious harm in many cities, and environmental pollution is the most serious.And oil burning boiler needs to consume substantial amounts of petroleum resources every year, cause the discharge of great amount of carbon dioxide, and containing a large amount of dust in the waste gas of fuel oil equipment and coal combustion equipment generation, environment is caused strong influence, is therefore badly in need of the high-temperature dust process recovery system that a kind of waste gas producing fuel oil equipment and coal combustion equipment processes.
Utility model content
For solving above-mentioned technical problem, this utility model provides a kind of high-temperature dust to process recovery system.
nullHigh-temperature dust of the present utility model processes recovery system，Including gravitational settling case，The left side wall of described gravitational settling case is provided with waste gas inlet pipe，The bottom of gravitational settling case is provided with the first ash bucket，The top of gravitational settling case connects energy recovery case by the first appendix，The inwall of energy recovery case is provided with heat-exchange tube，Heat-exchange tube be respectively arranged at two ends with water inlet pipe and outlet pipe，The bottom of energy recovery case is provided with the second ash bucket，The end of described first appendix is connected on the sidewall of the second ash bucket，The top of energy recovery case connects baffle-box by the second appendix，The side of the second appendix is parallel with the first gas storage bag by arm，It is respectively connected with the first pulse valve on the arm of the first gas storage bag both sides，The bottom of baffle-box is provided with the 3rd ash bucket，The top of baffle-box connects cyclone dust extractor by the 3rd appendix，The side of the 3rd appendix connects mends air-valve，The bottom of cyclone dust extractor is provided with the 4th ash bucket，The top of cyclone dust extractor connects sack cleaner by the 4th appendix，The bottom of sack cleaner is provided with the 5th ash bucket，The 5th appendix connecting fan is passed through on the right side of sack cleaner.
High-temperature dust of the present utility model processes recovery system, and the front side wall of described gravitational settling case is provided with observation window.
High-temperature dust of the present utility model processes recovery system, and the bottom of described 3rd ash bucket, the 4th ash bucket and the 5th ash bucket is equipped with gravity sensing valve.
High-temperature dust of the present utility model processes recovery system, the front side wall of described sack cleaner is provided with the second gas storage bag near top end, the top of the second gas storage bag connects some second pulse valves, and the gas outlet of the second pulse valve connects with the internal cavities of sack cleaner.
Compared with prior art the beneficial effects of the utility model are: high-temperature dust of the present utility model processes recovery system novel structure, by the common effect of multiple assemblies, greatly reduce Dust in waste gas so that the discharge meet the requirement of environmental protection of waste gas.
Accompanying drawing explanation
Fig. 1 is the structural representation that the high-temperature dust described in this utility model embodiment processes recovery system.
In figure:
1, gravitational settling case；2, waste gas inlet pipe；3, the first ash bucket；4, the first appendix；5, energy recovery case；6, heat-exchange tube；7, water inlet pipe；8, outlet pipe；9, the second ash bucket；10, the second appendix；11, baffle-box；12, arm；13, the first gas storage bag；14, the first pulse valve；15, the 3rd ash bucket；16, the 3rd appendix；17, cyclone dust extractor；18, air-valve is mended；19, the 4th ash bucket；20, the 4th appendix；21, sack cleaner；22, the 5th ash bucket；23, the 5th appendix；24, blower fan；25, observation window；26, gravity sensing valve；27, the second gas storage bag；28, the second pulse valve.
Detailed description of the invention
Below in conjunction with the accompanying drawings and embodiment, detailed description of the invention of the present utility model is described in further detail.Following example are used for illustrating this utility model, but are not limited to scope of the present utility model.
nullAs shown in Figure 1，A kind of high-temperature dust processes recovery system，Including gravitational settling case 1，The left side wall of described gravitational settling case 1 is provided with waste gas inlet pipe 2，The bottom of gravitational settling case 1 is provided with the first ash bucket 3，The top of gravitational settling case 1 connects energy recovery case 5 by the first appendix 4，The inwall of energy recovery case 5 is provided with heat-exchange tube 6，Heat-exchange tube 6 be respectively arranged at two ends with water inlet pipe 7 and outlet pipe 8，The bottom of energy recovery case 5 is provided with the second ash bucket 9，The end of described first appendix 4 is connected on the sidewall of the second ash bucket 9，The top of energy recovery case 5 connects baffle-box 11 by the second appendix 10，The side of the second appendix 10 is parallel with the first gas storage bag 13 by arm 12，It is respectively connected with the first pulse valve 14 on the arm 12 of the first gas storage bag 13 both sides，The bottom of baffle-box 11 is provided with the 3rd ash bucket 15，The top of baffle-box 11 connects cyclone dust extractor 17 by the 3rd appendix 16，The side of the 3rd appendix 16 connects mends air-valve 18，The bottom of cyclone dust extractor 17 is provided with the 4th ash bucket 19，The top of cyclone dust extractor 17 connects sack cleaner 21 by the 4th appendix 20，The bottom of sack cleaner 21 is provided with the 5th ash bucket 22，The 5th appendix 23 connecting fan 24 is passed through on the right side of sack cleaner 21.
High-temperature dust of the present utility model processes recovery system, and the front side wall of described gravitational settling case 1 is provided with observation window 25.
High-temperature dust of the present utility model processes recovery system, and the bottom of described 3rd ash bucket the 15, the 4th ash bucket 19 and the 5th ash bucket 22 is equipped with gravity sensing valve 26.
High-temperature dust of the present utility model processes recovery system, the front side wall of described sack cleaner 21 is provided with the second gas storage bag 27 near top end, the top of the second gas storage bag 27 connects some second pulse valves 28, and the gas outlet of the second pulse valve 28 connects with the internal cavities of sack cleaner 21.
High-temperature dust of the present utility model process recovery system is when specific works, and first waste gas input gravitational settling case, and gravitational settling case front is provided with observation panel, and lower section arranges ash bucket, for sedimentation and the cleaning of dust；Input energy recovery case after the output of gravitational settling case, energy recovery case is provided with heat-exchange tube along cabinet wall, utilizes the heat energy of tail gas to realize the recovery of heat energy；It is provided with ash bucket below energy recovery case, is used for settling big dust particle；Input baffle-box after the output of energy recovery case, be provided with ash bucket below baffle-box, be used for collecting dust, below ash bucket, be furnished with gravity sensing valve, the automatic ash-discharging when reaching setting weight；The side of the second appendix is parallel with the first gas storage bag by arm, and the arm of the first gas storage bag both sides is respectively connected with the first pulse valve, and Main Function is the dust being deposited in duct bottom to be carried out purging kick up；The dust kicked up falls in baffle-box in time, it is achieved segmentation, process in time, prevents dust secondary settlement；Inputting cyclone dust extractor after baffle-box output, above cyclone dust extractor, side is provided with air inlet, and cyclone dust extractor top is air outlet, it is the sedimentation of ash bucket, beneficially dust below cyclone dust extractor, below ash bucket, is provided with gravity sensing valve, when dust weight reaches setting weight, automatic ash-discharging；It is provided with benefit air-valve between baffle-box and cyclone dust extractor, by mending air-valve, cold wind is filled in system, reduce system temperature；Sack cleaner is inputted after cyclone dust extractor output, in the lower left of sack cleaner, air inlet is set, sack cleaner upper right side arranges air outlet, high temperature cloth bag is set inside sack cleaner, the pulsed deashing device being provided above being made up of the second gas storage bag and the second pulse valve of sack cleaner, set the burst length, reach, during the setting time, cloth bag is carried out jet, the dust being attached on cloth bag is blown down.The lower section of sack cleaner is provided with ash bucket, for keeping in the dust fallen in cloth bag.It is provided with gravity sensing valve in the lower section of ash bucket, when dust weight temporary in ash bucket reaches setting value, automatic ash-discharging；After sack cleaner output, through the effect of blower fan, by chimney qualified discharge.
The above is only preferred implementation of the present utility model; should be understood that; for those skilled in the art; on the premise of without departing from this utility model know-why; can also make some improvement and modification, these improve and modification also should be regarded as protection domain of the present utility model.
Claims (4)
- null1. a high-temperature dust processes recovery system，Including gravitational settling case (1)，It is characterized in that: the left side wall of described gravitational settling case (1) is provided with waste gas inlet pipe (2)，The bottom of gravitational settling case (1) is provided with the first ash bucket (3)，The top of gravitational settling case (1) connects energy recovery case (5) by the first appendix (4)，The inwall of energy recovery case (5) is provided with heat-exchange tube (6)，Heat-exchange tube (6) be respectively arranged at two ends with water inlet pipe (7) and outlet pipe (8)，The bottom of energy recovery case (5) is provided with the second ash bucket (9)，The end of described first appendix (4) is connected on the sidewall of the second ash bucket (9)，The top of energy recovery case (5) connects baffle-box (11) by the second appendix (10)，The side of the second appendix (10) is parallel with the first gas storage bag (13) by arm (12)，It is respectively connected with the first pulse valve (14) on the arm (12) of the first gas storage bag (13) both sides，The bottom of baffle-box (11) is provided with the 3rd ash bucket (15)，The top of baffle-box (11) connects cyclone dust extractor (17) by the 3rd appendix (16)，The side of the 3rd appendix (16) connects mends air-valve (18)，The bottom of cyclone dust extractor (17) is provided with the 4th ash bucket (19)，The top of cyclone dust extractor (17) connects sack cleaner (21) by the 4th appendix (20)，The bottom of sack cleaner (21) is provided with the 5th ash bucket (22)，The 5th appendix (23) connecting fan (24) is passed through on the right side of sack cleaner (21).
- High-temperature dust the most according to claim 1 processes recovery system, it is characterised in that: the front side wall of described gravitational settling case (1) is provided with observation window (25).
- High-temperature dust the most according to claim 1 processes recovery system, it is characterised in that: the bottom of described 3rd ash bucket (15), the 4th ash bucket (19) and the 5th ash bucket (22) is equipped with gravity sensing valve (26).
- High-temperature dust the most according to claim 1 processes recovery system, it is characterized in that: the front side wall of described sack cleaner (21) is provided with the second gas storage bag (27) near top end, the top of the second gas storage bag (27) connects some second pulse valves (28), and the gas outlet of the second pulse valve (28) connects with the internal cavities of sack cleaner (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108239.5U CN205412566U (en) | 2016-02-03 | 2016-02-03 | High temperature dust disposal recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620108239.5U CN205412566U (en) | 2016-02-03 | 2016-02-03 | High temperature dust disposal recovery system |
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| Publication Number | Publication Date |
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| CN205412566U true CN205412566U (en) | 2016-08-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620108239.5U Expired - Fee Related CN205412566U (en) | 2016-02-03 | 2016-02-03 | High temperature dust disposal recovery system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107511004A (en) * | 2017-10-13 | 2017-12-26 | 云南省烟草公司保山市公司 | Circulation dust collector |
| CN107899354A (en) * | 2017-12-20 | 2018-04-13 | 郑州赫恩电子信息技术有限公司 | It is a kind of that there is the energy saving emission-control equipment of heat recovery |
| CN108755222A (en) * | 2018-05-29 | 2018-11-06 | 孙爱芬 | A kind of retracting device of papermaking slurry |
-
2016
- 2016-02-03 CN CN201620108239.5U patent/CN205412566U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107511004A (en) * | 2017-10-13 | 2017-12-26 | 云南省烟草公司保山市公司 | Circulation dust collector |
| CN107899354A (en) * | 2017-12-20 | 2018-04-13 | 郑州赫恩电子信息技术有限公司 | It is a kind of that there is the energy saving emission-control equipment of heat recovery |
| CN108755222A (en) * | 2018-05-29 | 2018-11-06 | 孙爱芬 | A kind of retracting device of papermaking slurry |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 315202 Ningbo, Zhenhai District, camel street, Yongping West Road, room 168, No. 205 (metro core area), No. Patentee after: Zhejiang Yi Long Environmental Services Co., Ltd. Address before: 315400 Ningbo Province, Zhenhai District, Zhuang City, the streets of the Dragon Road, No., building 528, No. 4 Patentee before: ZHEJIANG XIANGNIU ENVIRONMENTAL PROTECTION AND TECHNOLOGY DEVELOPMENT CO., LTD. |
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| CP03 | Change of name, title or address | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20190203 |
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| CF01 | Termination of patent right due to non-payment of annual fee |