CN202361819U - Comprehensive waste heat utilization system on aluminum section production line - Google Patents
Comprehensive waste heat utilization system on aluminum section production line Download PDFInfo
- Publication number
- CN202361819U CN202361819U CN2011204766172U CN201120476617U CN202361819U CN 202361819 U CN202361819 U CN 202361819U CN 2011204766172 U CN2011204766172 U CN 2011204766172U CN 201120476617 U CN201120476617 U CN 201120476617U CN 202361819 U CN202361819 U CN 202361819U
- Authority
- CN
- China
- Prior art keywords
- production line
- furnace
- smoke
- valve
- aluminium
- 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
Links
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 92
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 50
- 239000002918 waste heat Substances 0.000 title abstract description 14
- 239000000779 smoke Substances 0.000 claims abstract description 57
- 238000001035 drying Methods 0.000 claims abstract description 30
- 230000032683 aging Effects 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 25
- 238000005266 casting Methods 0.000 claims abstract description 20
- 239000004411 aluminium Substances 0.000 claims description 84
- 235000019504 cigarettes Nutrition 0.000 claims description 33
- 238000007599 discharging Methods 0.000 claims description 26
- 241000208125 Nicotiana Species 0.000 claims description 10
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims description 10
- 230000005540 biological transmission Effects 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 46
- 239000003546 flue gas Substances 0.000 abstract description 46
- 239000007789 gas Substances 0.000 abstract description 11
- 239000000428 dust Substances 0.000 abstract description 8
- 238000000605 extraction Methods 0.000 abstract 1
- 238000011144 upstream manufacturing Methods 0.000 abstract 1
- 238000009826 distribution Methods 0.000 description 5
- 238000005453 pelletization Methods 0.000 description 4
- 239000000567 combustion gas Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 150000001398 aluminium Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000007630 basic procedure Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000505 pernicious Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model discloses a comprehensive waste heat utilization system on an aluminum section production line. A casting furnace, an aluminum ingot preheating chamber, a homogenizing furnace, an aluminum bar heating furnace, an aging oven, a curing furnace and a drying furnace on the aluminum section production line are communicated to form the comprehensive waste heat utilization system on the aluminum section production line through a flue gas delivery network consisting of a smoke exhaust pipeline, a smoke feed pipeline, a smoke delivery pipeline, a smoke exhaust valve, a smoke delivery valve, a safety valve, a heat exchanger, an air feeder and a smoke feed valve. By the system, waste heat in high-temperature flue gas exhausted from an upstream high temperature furnace on the aluminum section production line can be distributed in various downstream low temperature furnaces, and the waste heat in each furnace can be fully utilized by the downstream furnaces. By the system, the existing 250 cubic meters of gas required for producing each ton of aluminum sections is reduced to only 130 cubic meters of gas per ton, and the energy is saved by about 50 percent; and moreover, the gas consumption is reduced while the discharge of various pollution gases is reduced. By the system, the high-temperature flue gas converts into low-temperature flue gas to be discharged, and the cost of a flue gas dust extraction system is also reduced.
Description
Technical field
The utility model relates to a kind of bootstrap system, and in particular a kind of aluminium section bar production line residual heat integrative utilizes system.
Background technology
Production equipment on the existing aluminium section bar production line such as casting furnace, homogeneous stove, aging furnace etc., its high-temperature flue gas that produces in process of production all are directly or after dust pelletizing system is handled to discharge.The temperature of the high-temperature flue gas that casting furnace produces reaches 800-1000 ℃, and the temperature of the high-temperature flue gas that the homogeneous fire grate is put reaches about 600 ℃, and its temperature of high-temperature flue gas of aging furnace discharging also can reach 200 ℃.50% heat has nearly been taken away on the production line in the discharging of this high-temperature flue gas on the one hand, has caused a large amount of wastes of combustion gas, is unfavorable for the reduction of production cost; On the other hand, high-temperature flue gas directly discharges, and has a large amount of pernicious gases in the flue gas, is unfavorable for environmental protection, after dedusting, discharges, and high-temperature flue gas is very high to the requirement of dust pelletizing system, and the construction cost of dust pelletizing system is very expensive.
Therefore, prior art awaits to improve and development.
The utility model content
The purpose of the utility model is to provide a kind of aluminium section bar production line residual heat integrative to utilize system, and aluminium section bar production line high-temperature flue gas directly discharges the technical problem that the wasting of resources is huge, environmental protection is of a high price that causes in the above-mentioned prior art to solve.
The technical scheme of the utility model is following:
A kind of aluminium section bar production line residual heat integrative utilizes system; Comprise casting furnace, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven, smoke discharging pipe, send the smoke pipe road, tobacco transmission pipe, exhaust smoke valve, defeated cigarette valve, safety valve, heat exchanger, pressure fan and send the cigarette valve, on the outlet flue of casting furnace, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven, be provided with smoke discharging pipe; Advancing to be provided with on the mouth and send the smoke pipe road at aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven; The smoke discharging pipe of the high temperature furnace in said each stove and low temperature oven send annular smoke flue to cross described tobacco transmission pipe to be communicated with; Said exhaust smoke valve is arranged on the exhaust opening place of smoke discharging pipe; Said defeated cigarette valve and safety valve are arranged on the tobacco transmission pipe; Said pressure fan and send the cigarette valve to be arranged on said sending on the smoke pipe road, it is provided with the position and is followed successively by pressure fan, send the cigarette valve according to air supply direction.
Described aluminium section bar production line residual heat integrative utilizes system, wherein, also comprises heat exchanger, and said heat exchanger is arranged on sending on the smoke pipe road of said each stove.
Described aluminium section bar production line residual heat integrative utilizes system, wherein, also comprises water tank, and the smoke discharging pipe of said drying oven is inserted in the said water tank, and the smoke discharging pipe of said drying oven is provided with heat exchanger.
Described aluminium section bar production line residual heat integrative utilizes system, and wherein, the quantity of said casting furnace is at least one; The quantity of said aluminium ingot preheating chamber is at least one; The quantity of said homogeneous stove is at least one, and the quantity of said aluminium bar heating furnace is at least one, and the quantity of said aging furnace is at least one; The quantity of said curing oven is at least one, and the quantity of said drying oven is at least one.
Described aluminium section bar production line residual heat integrative utilizes system; Wherein, Also comprise monitoring system; Said monitoring system comprises central processing unit, data monitoring device and regulation device, and said data monitoring device and regulation device are arranged on said aluminium section bar production line residual heat integrative and utilize on each body of heater in the system, and said data monitoring device and regulation device electrically connect with central processing unit respectively.
Described aluminium section bar production line residual heat integrative utilizes system, and wherein, described supervising device comprises pressure monitor device and temperature monitor.
Described aluminium section bar production line residual heat integrative utilizes system, and wherein, described regulation device comprises exhaust smoke valve, defeated cigarette valve, safety valve, heat exchanger, pressure fan and send the cigarette valve.
The utility model through utilize smoke discharging pipe, send the smoke pipe road, tobacco transmission pipe, exhaust smoke valve, defeated cigarette valve, safety valve, heat exchanger, pressure fan and the flue gas transport net that send the cigarette valve to form be communicated with composition aluminium section bar production line residual heat integrative with the casting furnace on the aluminium section bar production line, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven and drying oven and utilize system.Waste heat in the high-temperature flue gas that this system can discharge the high temperature furnace at the upper reaches on the aluminium section bar production line is assigned in each low temperature oven of downstream, and the waste heat of each stove can both be made full use of by the downstream stove.This system will produce 250 cubic metres required gas quantity of aluminium section bar per ton now and be reduced to 130 cubic metres of combustion gas of per ton need, and energy-conservation nearly 50%.And, when reducing gas consumption, also reduced the discharge capacity of various dusty gas.The low-temperature flue gas that becomes of high-temperature flue gas discharges in this system, has equally also reduced the cost of flue gas dust collecting system.
Description of drawings
Fig. 1 is the structural representation that aluminium section bar production line residual heat integrative utilizes system in the utility model;
Fig. 2 is the structural representation that aluminium section bar production line residual heat integrative utilizes monitoring system in the system in the utility model;
Fig. 3 is that aluminium section bar production line residual heat integrative utilizes system works flow process figure in the utility model.
The specific embodiment
For the purpose, technical scheme and the advantage that make the utility model is clearer, clear and definite, below develop simultaneously embodiment to the utility model further explain with reference to accompanying drawing.
As aluminium section bar production line residual heat integrative in the said the utility model of Fig. 1 utilize the structural representation of system, this aluminium section bar production line residual heat integrative to utilize system to comprise casting furnace 1, aluminium ingot preheating chamber 2, homogeneous stove 3, aluminium bar heating furnace 4, aging furnace 5, curing oven 6, drying oven 7, smoke discharging pipe 8, send smoke pipe road 9, tobacco transmission pipe 10, exhaust smoke valve 11, defeated cigarette valve 12, safety valve 13, heat exchanger 14, pressure fan 15 and send cigarette valve 16.Among casting furnace 1, aluminium ingot preheating chamber 2, homogeneous stove 3, aluminium bar heating furnace 4, aging furnace 5, curing oven 6 and drying oven 7, except that 1 of casting furnace is provided with the smoke discharging pipe 8, all the other each stoves all corresponding setting have smoke discharging pipe 8 and send smoke pipe road 9.Sending between the smoke pipe road 9 of the smoke discharging pipe 8 of upper reaches stove and its adjacent downstream stove is communicated with through tobacco transmission pipe 10; Be casting furnace 1, homogeneous stove 3 and aging furnace 5 smoke discharging pipe 8 separately with aluminium ingot preheating chamber 2, aluminium bar heating furnace 4 and curing oven 6 separately send adjacent connection the between the smoke pipe road 9; Homogeneous stove 3, aluminium bar heating furnace 4 and curing oven 6 smoke discharging pipe 8 separately and homogeneous stove 3, aging furnace 5 and drying oven 7 separately send adjacent connection the between the smoke pipe road 9; The smoke discharging pipe of drying oven 7 directly discharges, and perhaps connects flue gas dust collecting system.Exhaust opening place at each smoke discharging pipe 8 is provided with exhaust smoke valve 11; Defeated cigarette valve 12 is arranged on each tobacco transmission pipe 10 with the needs of safety valve 13 according to native system control and distribution high-temperature flue gas; Heat exchanger 14, pressure fan 15 and send cigarette valve 16 to be arranged on each and send on the smoke pipe road, it is provided with the position relation with sending the cigarette direction to be followed successively by heat exchanger 14, pressure fan 15, sending cigarette valve 16.High-temperature flue gas is after heat exchanger 14 heat exchange, and the waste heat that wherein carries is sent in the stove of downstream through pressure fan 15.Wherein, the flue-gas temperature in the casting furnace 1 is near 1050 ℃, and the flue-gas temperature in the aluminium ingot preheating chamber 2 can reach 500 ℃; Flue-gas temperature in the homogeneous stove 3 can reach 600 ℃; Flue-gas temperature in the aluminium bar heating furnace 4 is about 500 ℃, and aging furnace 5 then has only about 200 ℃ with the flue-gas temperature in the curing oven 6, and the flue-gas temperature of drying oven 7 is about 80 ℃; After waste heat in the flue gas that drying oven is discharged heat exchanger capable of using transforms, be used for hot water.。
Aluminium section bar production line residual heat integrative utilizes the structural representation of monitoring system in the system in the utility model as shown in Figure 2; Aluminium section bar production line residual heat integrative utilizes and also comprises a monitoring system in the system, in order to detect the distribution that aluminium section bar production line residual heat integrative utilizes the temperature and pressure state in each stove and control high temperature cigarette in the system.This detection system comprises central processing unit 17; Casting furnace data detection device 18; Casting furnace regulation device 19; Aluminium ingot preheating chamber data monitoring device 20; Aluminium ingot preheating chamber regulation device 21; Homogeneous stove data monitoring device 22; Homogeneous stove regulation device 23; Aluminium bar heating furnace data monitoring device 24; Aluminium bar heating furnace regulation device 25; Aging furnace data monitoring device 26; Aging furnace regulation device 27; Curing oven data detection device 28; Curing oven regulation device 29; Drying oven data monitoring device 20 and drying oven regulation device 31.Above-mentioned data monitoring device just exists on existing aluminium section bar production line, like pressure monitor, temperature monitoring (not shown) etc., is installed on the aluminium section bar production line in each stove.Above-mentioned each regulation device is the exhaust smoke valve 11 shown in Fig. 1, defeated cigarette valve 12 in the utility model, send cigarette valve 16, safety valve 13, heat exchanger 14, pressure fan 15 etc.; After the data of data monitoring device monitoring in each stove; Data-signal is sent to central processing unit 17; Central processing unit 17 is made judgement and is sent operational order to each regulation device according to data-signal; Regulate the distribution of high temperature cigarette through the switch of controlling each regulation device, so that the data in each stove all are in normal condition on the production line.
As shown in Figure 3, aluminium section bar production line residual heat integrative utilizes system works flow process figure in the utility model, and this aluminium section bar production line residual heat integrative utilizes system under the control of its monitoring system, to carry out the distribution utilization of waste heat.Monitoring system is utilized its this residual heat integrative of regulation device control to utilize the switch of each valve in the system according to analysis result, thereby is carried out the distribution of waste heat through the data in each stove stove on the aluminium section bar production line are carried out monitoring analysis.Its basic procedure is following: 1, discharge from casting furnace near about 1000 ℃ high-temperature flue gas, can supply aluminium ingot preheating chamber, monitoring system through aluminium bar heating furnace and curing oven are used.Data in aluminium ingot preheating chamber, aluminium bar heating furnace and the curing oven are analyzed, and judge whether need advance cigarette.If need not advance cigarette, high-temperature flue gas is then directly discharged from casting furnace.2, the high-temperature flue gas about 500 ℃ in the aluminium ingot preheating chamber can supply homogeneous stove, aging furnace and drying oven to use, and monitoring system judges whether need advance cigarette through the data in homogeneous stove, aging furnace and the drying oven are analyzed.If need not advance cigarette, high-temperature flue gas is then directly discharged from the aluminium ingot heating furnace.3, the temperature of the high-temperature flue gas in the homogeneous stove can reach 600 ℃, can supply aluminium bar heating furnace and curing oven to use, and monitoring system judges whether need advance cigarette through the data in aluminium bar heating furnace and the curing oven are analyzed.If need not advance cigarette, high-temperature flue gas is then directly discharged from homogeneous stove stove.4, the high-temperature flue gas in the aluminium bar heating furnace also can reach 500 ℃, after flue gas flows out, can supply aging furnace and drying oven to use, and monitoring system judges through the data in aging furnace and the drying oven are analyzed whether it need advance cigarette.If do not need, high-temperature flue gas is then directly discharged from the aluminium bar heating furnace.5, the temperature of the high-temperature flue gas in the aging furnace is about 200 ℃, can directly discharge or directly supply with curing oven and use.6, the high-temperature flue gas in the curing oven also has only about 200 ℃, can directly discharge or directly supply with drying oven and use.7, last, the flue gas in the drying oven is then directly discharged or after dust pelletizing system is handled, is discharged.
Can find out by the foregoing description; The aluminium section bar production line residual heat integrative that the utility model provides utilizes system; Under the control of monitoring system; Through functors such as pressure fan, valve, heat exchangers, the waste heat in the high-temperature flue gas that can the upper reaches fire grate on the aluminium section bar production line be gone out is assigned in each stove of downstream, and the waste heat of each stove can both be made full use of by the downstream stove.Through calculating, this system can be reduced to 130 cubic metres of combustion gas of per ton need by 250 cubic metres the gas quantity that existing production aluminium section bar per ton is required, and energy-conservation nearly 50%.And, when reducing gas consumption, also reduced the discharge capacity of various dusty gas.In addition, the low-temperature flue gas that becomes of high-temperature flue gas discharges in this system, has equally also reduced the cost of flue gas dust collecting system.
Should be understood that the application of the utility model is not limited to above-mentioned giving an example, concerning those of ordinary skills; Can improve or conversion according to above-mentioned explanation; For example, the casting furnace in the native system, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven and drying oven, its quantity can be for more than two; Smoke conveying duct in corresponding this system also is set to network structure, thereby this system also can build up a residual heat integrative and utilizes net.In addition, drying oven smoke discharging pipe can also an external water tank, a heat exchanger is set on the smoke discharging pipe, the waste heat of the flue gas of discharging through the heat exchanger converter is used for hot water.All these improvement and conversion all should belong to the protection domain of the utility model accompanying claims.
Claims (7)
1. an aluminium section bar production line residual heat integrative utilizes system; It is characterized in that; Comprise casting furnace, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven, smoke discharging pipe, send the smoke pipe road, tobacco transmission pipe, exhaust smoke valve, defeated cigarette valve, safety valve, heat exchanger, pressure fan and send the cigarette valve, on the outlet flue of casting furnace, aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven, be provided with smoke discharging pipe; Advancing to be provided with on the mouth and send the smoke pipe road at aluminium ingot preheating chamber, homogeneous stove, aluminium bar heating furnace, aging furnace, curing oven, drying oven; The smoke discharging pipe of the high temperature furnace in said each stove and low temperature oven send annular smoke flue to cross described tobacco transmission pipe to be communicated with; Said exhaust smoke valve is arranged on the exhaust opening place of smoke discharging pipe; Said defeated cigarette valve and safety valve are arranged on the tobacco transmission pipe; Said pressure fan and send the cigarette valve to be arranged on said sending on the smoke pipe road, it is provided with the position and is followed successively by pressure fan, send the cigarette valve according to air supply direction.
2. aluminium section bar production line residual heat integrative according to claim 1 utilizes system, it is characterized in that, also comprises heat exchanger, and said heat exchanger is arranged on sending on the smoke pipe road of said each stove.
3. aluminium section bar production line residual heat integrative according to claim 1 utilizes system, it is characterized in that, also comprises water tank, and the smoke discharging pipe of said drying oven is inserted in the said water tank, and the smoke discharging pipe of said drying oven is provided with heat exchanger.
4. utilize system according to claim 1,2 or 3 described aluminium section bar production line residual heat integratives, it is characterized in that the quantity of said casting furnace is at least one; The quantity of said aluminium ingot preheating chamber is at least one; The quantity of said homogeneous stove is at least one, and the quantity of said aluminium bar heating furnace is at least one, and the quantity of said aging furnace is at least one; The quantity of said curing oven is at least one, and the quantity of said drying oven is at least one.
5. aluminium section bar production line residual heat integrative according to claim 1 utilizes system; It is characterized in that; Also comprise monitoring system; Said monitoring system comprises central processing unit, data monitoring device and regulation device, and said data monitoring device and regulation device are arranged on said aluminium section bar production line residual heat integrative and utilize on each body of heater in the system, and said data monitoring device and regulation device electrically connect with central processing unit respectively.
6. aluminium section bar production line residual heat integrative according to claim 5 utilizes system, it is characterized in that described supervising device comprises pressure monitor device and temperature monitor.
7. utilize system according to claim 5 or 6 described aluminium section bar production line residual heat integratives, it is characterized in that, described regulation device comprises exhaust smoke valve, defeated cigarette valve, safety valve, heat exchanger, pressure fan and send the cigarette valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204766172U CN202361819U (en) | 2011-11-25 | 2011-11-25 | Comprehensive waste heat utilization system on aluminum section production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204766172U CN202361819U (en) | 2011-11-25 | 2011-11-25 | Comprehensive waste heat utilization system on aluminum section production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202361819U true CN202361819U (en) | 2012-08-01 |
Family
ID=46573000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204766172U Expired - Fee Related CN202361819U (en) | 2011-11-25 | 2011-11-25 | Comprehensive waste heat utilization system on aluminum section production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202361819U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102410744A (en) * | 2011-11-25 | 2012-04-11 | 佛山市通润热能科技有限公司 | Waste heat comprehensive utilization system in aluminum profile production line |
-
2011
- 2011-11-25 CN CN2011204766172U patent/CN202361819U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102410744A (en) * | 2011-11-25 | 2012-04-11 | 佛山市通润热能科技有限公司 | Waste heat comprehensive utilization system in aluminum profile production line |
| CN102410744B (en) * | 2011-11-25 | 2013-10-16 | 佛山市通润热能科技有限公司 | Waste heat comprehensive utilization system in aluminum profile production line |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202511638U (en) | Device for recovering flue gas waste heat generated by industrial heat treatment | |
| CN104801174A (en) | Activated coke flue gas purification system | |
| CN102061396B (en) | Method and device for smelting recycled copper in reverberator | |
| CN102410744B (en) | Waste heat comprehensive utilization system in aluminum profile production line | |
| CN202361819U (en) | Comprehensive waste heat utilization system on aluminum section production line | |
| CN204007178U (en) | Heat-treatment furnace flue gas waste heat utilization device | |
| CN203784990U (en) | High-temperature low-oxygen combustion apparatus | |
| CN103063044B (en) | Rotary hearth furnace smoke waste heat utilization system and rotary hearth furnace fume afterheat Application way | |
| CN203007295U (en) | Novel blast-furnace hot blast stove exhaust gas classification recycle device | |
| CN107523663A (en) | A kind of control method of RECOVERY OF CONVERTER GAS | |
| CN204958401U (en) | Yellow phosphor furnace burner gas clean system | |
| CN204522739U (en) | A kind of activated coke flue gas purification system | |
| CN202157087U (en) | High-efficiency electric furnace steel making system | |
| CN204648986U (en) | A kind of board-like pair of preheater process system for gas burning lime kiln | |
| CN205957207U (en) | Utilize device of flue gas waste heat heating cold wind system | |
| CN104848674A (en) | Coal mine low concentration gas oxidation high temperature hot air and coal slime preparing and drying technology | |
| CN201753307U (en) | Combustion-supporting wind system for glass smelting kiln | |
| CN201666738U (en) | Pre-heated one section waste flue gas afterheat utilizing system of pellet grate machine | |
| CN201155799Y (en) | Plaster board organic heat carrier heating stove residual heat utilization device | |
| CN203342903U (en) | Energy-saving and emission-reduction device used for industrial vertical mill | |
| CN103968409A (en) | High-temperature low-oxygen combustion device | |
| CN203099869U (en) | Device using high-temperature smoke to heat baffle door sealing air | |
| CN203396251U (en) | Cooling air reusing device | |
| CN208238568U (en) | Aluminium melting furnace high temperature heat exchanger | |
| CN203132320U (en) | Oxygen enrichment energy-saving copper converting reverberating furnace |
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: 20120801 Termination date: 20141125 |
|
| EXPY | Termination of patent right or utility model |