CN201785440U - Heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace - Google Patents
Heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace Download PDFInfo
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- CN201785440U CN201785440U CN2010202982755U CN201020298275U CN201785440U CN 201785440 U CN201785440 U CN 201785440U CN 2010202982755 U CN2010202982755 U CN 2010202982755U CN 201020298275 U CN201020298275 U CN 201020298275U CN 201785440 U CN201785440 U CN 201785440U
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- annealing furnace
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- carbon restoration
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Abstract
The utility model provides a heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace; a carbon restoration section is arranged in the annealing furnace; a heating section, a quick-cooling section, an isothermal section and a slow-cooling section are sequentially arranged at the rear end of the carbon restoration section; a preheating section parallel to the slow-cooling section is connected on the side of the slow-cooling section; a heat circulation channel is further arranged between the preheating section and the slow-cooling section; and a heat exchange blower is mounted on the heat circulation channel. By adopting the annealing furnace provided by the utility model, not only be the product quality can improved in virtue of carbon restoration, but also the residual heat from high-temperature workpieces can be fully used for preheating the workpieces newly entering the furnace, so that the annealing furnace has high heat efficiency, small occupied area, good quality and high efficiency, and is energy-saving and environment-friendly.
Description
Technical field
The utility model relates to annealing furnace, relates in particular to a kind of carbon restoration recovery type heat continuous isothermal spheroidizing annealing furnace that can fully reclaim heat energy.
Background technology
In the prior art, the Spheroidizing Annealing of metallic substance or workpiece generally all heats in oxidizing atmosphere, cools off in air subsequently, such processing mode, oxidation and decarbonization had both taken place in its workpiece, and its heat energy can run off in process of cooling, had that quality is low, energy consumption big and defective such as contaminate environment.
The utility model content
The purpose of this utility model is to overcome the deficiency that prior art exists, and a kind of carbon restoration recovery type heat continuous isothermal spheroidizing annealing furnace that can fully reclaim heat energy is provided.
The purpose of this utility model is achieved through the following technical solutions:
Heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace, comprise body of heater and the fire door that is arranged at the body of heater both sides, characteristics are: be provided with the carbon restoration section in the described body of heater, the rear end of described carbon restoration section is disposed with heating zone, fast cold section, isothermal section and slow cooling section, the side of described slow cooling section is connected preheating section, preheating section parallels with the slow cooling section, and is provided with the thermal cycling passage between preheating section and slow cooling section, on the thermal cycling passage heat-exchange fan is installed.
Further, above-mentioned heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace wherein, is provided with the transport sector that is used to carry the guide rail of hopper motion and is used to drive the hopper motion in the described body of heater.
Further, above-mentioned heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace, wherein, the length of described carbon restoration section is 1.5 meters, and the length of heating zone is 3 meters, and fast cold section length is 1.5 meters, and the length of isothermal section is 3 meters, the length of slow cooling section is 6 meters.
Again further, above-mentioned heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace wherein, is provided with e Foerderanlage in the described thermal cycling passage.
The substantive distinguishing features of technical solutions of the utility model and progressive being mainly reflected in:
The utility model is rational in infrastructure, both can utilize carbon restoration to improve the quality of products, and can make full use of high temperature workpiece waste heat again and make preheating usefulness for the workpiece that newly advances stove, the thermo-efficiency height, floor space is little, and is high-quality and efficient, energy-conserving and environment-protective.
Description of drawings
Below in conjunction with accompanying drawing technical solutions of the utility model are described further:
Fig. 1: master of the present utility model looks synoptic diagram;
Fig. 2: schematic top plan view of the present utility model;
The B-B cross-sectional schematic of Fig. 3: Fig. 2.
The implication of each Reference numeral sees the following form among the figure:
Embodiment
As shown in Figure 1 and Figure 2, heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace, comprise body of heater 1 and the fire door 11 that is arranged at the body of heater both sides, be provided with the transport sector 8 that is used to carry the guide rail 12 of hopper motion and is used to drive the hopper motion in the body of heater, and be provided with the push rod that the promotion hopper moves on guide rail at the body of heater two ends; Be provided with carbon restoration section 2 in the body of heater, the rear end of carbon restoration section 2 is disposed with heating zone 3, fast cold section 4, isothermal section 5 and slow cooling section 6 (heat exchange zone), the length of carbon restoration section 2 is 1.5 meters, the length of heating zone 3 is 3 meters, fast cold section 4 length is 1.5 meters, the length of isothermal section 5 is 3 meters, and the length of slow cooling section 6 is 6 meters; The side of slow cooling section 6 is connected preheating section 7, as shown in Figure 3, preheating section 7 parallels with slow cooling section 6, and is provided with thermal cycling passage 9 between preheating section 7 and slow cooling section 6, heat-exchange fan 10 is installed on the thermal cycling passage 9, is provided with e Foerderanlage in the thermal cycling passage 9.
Side design in the slow cooling section has workpiece preheating combustion flue, promotes hopper preheating one by one by push rod, and preheating finishes the back by the correspondence position that transport sector makes it to enter feeding port is set in the body of heater.
Normal course of operation is as follows: imported into to heating zone 3 heating of annealing by transport sector 8 after carbon restoration section 2 is carried out carbon restorations when newly advancing workpiece.The experience heating insulation afterwards forward of the workpiece of the indoor new dish of then packing into of carbon restoration, workpiece pulsation.Fast cold section 4 enters isothermal section 5 nodularizations after fast cold, comes out of the stove via slow cooling section 6 (heat exchange zone) at last.Go into workpiece and the operation of aforementioned reverse direction with stylish, realize the waste heat heat production, reach temperature about 400 ℃, switch charging and can enter the carbon restoration chamber via carrying through heat exchange zone.Absorbed by when cooling off, putting into furnaceman's part, so the heat energy utilization rate of equipment greatly improves through the waste heat of high temperature workpiece.
In sum, the utility model is rational in infrastructure, can realize carbon restoration, and can make full use of annealing high temperature workpiece waste heat and make preheating usefulness for the workpiece that newly advances stove, the thermo-efficiency height, and the space availability ratio height, floor space is little, and is high-quality and efficient, energy-conserving and environment-protective.
What need understand is: the above only is a preferred implementation of the present utility model; for those skilled in the art; under the prerequisite that does not break away from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (4)
1. heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace, comprise body of heater (1) and be arranged at the fire door (11) of body of heater both sides, it is characterized in that: be provided with carbon restoration section (2) in the described body of heater, the rear end of described carbon restoration section (2) is disposed with heating zone (3), fast cold section (4), isothermal section (5) and slow cooling section (6), the side of described slow cooling section (6) is connected preheating section (7), preheating section (7) parallels with slow cooling section (6), and between preheating section (7) and slow cooling section (6), be provided with thermal cycling passage (9), heat-exchange fan (10) is installed on the thermal cycling passage (9).
2. heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace according to claim 1 is characterized in that: be provided with the transport sector (8) that is used to carry the guide rail (12) of hopper motion and is used to drive the hopper motion in the described body of heater.
3. heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace according to claim 1, it is characterized in that: the length of described carbon restoration section (2) is 1.5 meters, the length of heating zone (3) is 3 meters, the length of fast cold section (4) is 1.5 meters, the length of isothermal section (5) is 3 meters, and the length of slow cooling section (6) is 6 meters.
4. heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace according to claim 1 is characterized in that: be provided with e Foerderanlage in the described thermal cycling passage (9).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202982755U CN201785440U (en) | 2010-08-20 | 2010-08-20 | Heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace |
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CN2010202982755U CN201785440U (en) | 2010-08-20 | 2010-08-20 | Heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace |
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CN201785440U true CN201785440U (en) | 2011-04-06 |
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CN2010202982755U Expired - Fee Related CN201785440U (en) | 2010-08-20 | 2010-08-20 | Heat-recovery-type carbon restoration continuous isothermal spheroidized annealing furnace |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101906513A (en) * | 2010-08-20 | 2010-12-08 | 苏州工业园区振兴电炉有限公司 | Heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace |
-
2010
- 2010-08-20 CN CN2010202982755U patent/CN201785440U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101906513A (en) * | 2010-08-20 | 2010-12-08 | 苏州工业园区振兴电炉有限公司 | Heat recovery-type carbon restoration continuous isothermy spheroidizing annealing furnace |
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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: 20110406 Termination date: 20140820 |
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EXPY | Termination of patent right or utility model |