CN202494345U - Industrial furnace waste heat recovery system - Google Patents
Industrial furnace waste heat recovery system Download PDFInfo
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- CN202494345U CN202494345U CN2012200974611U CN201220097461U CN202494345U CN 202494345 U CN202494345 U CN 202494345U CN 2012200974611 U CN2012200974611 U CN 2012200974611U CN 201220097461 U CN201220097461 U CN 201220097461U CN 202494345 U CN202494345 U CN 202494345U
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- water
- heat exchanger
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- smoke exhaust
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- 239000002918 waste heat Substances 0.000 title claims abstract description 24
- 238000011084 recovery Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 132
- 239000000779 smoke Substances 0.000 claims abstract description 33
- 238000005338 heat storage Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 9
- 239000008399 tap water Substances 0.000 claims description 4
- 235000020679 tap water Nutrition 0.000 claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 7
- 239000003546 flue gas Substances 0.000 abstract description 7
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 206010022000 influenza Diseases 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
本实用新型公开了一种工业炉余热回收系统,包括总排烟通道以及连接在总排烟通道上的由一次、二次换热装置构成的余热回收装置,一次换热装置为串联在总排烟通道上的带有进出水口的气/水换热器,二次换热装置为带有一级进出水口和二级进出水口的水/水换热器;气/水换热器的出水口与水/水换热器的一级进水口相连通,水/水换热器的一级出水口与气/水换热器的进水口相连通;待加热冷水管路与水/水换热器的二级进水口相连通,水/水换热器的二级出水口经热水管路和与蓄热水池相连通。本实用新型的优点在于结构简单、余热利用率高,在有效的将工业炉烟气排放温度降至130℃左右的同时,还能得到60℃的热水来满足人们的供水和采暖需求。
The utility model discloses an industrial furnace waste heat recovery system, which comprises a total smoke exhaust channel and a waste heat recovery device connected to the total smoke exhaust channel, which is composed of a primary heat exchange device and a secondary heat exchange device. The air/water heat exchanger with water inlet and outlet on the smoke channel, the secondary heat exchange device is a water/water heat exchanger with primary water inlet and outlet and secondary water inlet and outlet; the water outlet of the air/water heat exchanger is connected to the The primary water inlet of the water/water heat exchanger is connected, the primary water outlet of the water/water heat exchanger is connected with the water inlet of the air/water heat exchanger; the cold water pipeline to be heated is connected with the water/water heat exchanger The secondary water inlet of the water/water heat exchanger is connected, and the secondary water outlet of the water/water heat exchanger is connected with the heat storage pool through the hot water pipeline. The utility model has the advantages of simple structure and high waste heat utilization rate. While effectively reducing the flue gas discharge temperature of the industrial furnace to about 130°C, it can also obtain hot water at 60°C to meet people's water supply and heating needs.
Description
技术领域 technical field
本实用新型涉及工业燃气(燃油)炉高温烟气的余热回收,尤其是涉及一种工业炉余热回收系统。 The utility model relates to waste heat recovery of high-temperature flue gas of industrial gas (fuel oil) furnaces, in particular to a waste heat recovery system of industrial furnaces.
背景技术 Background technique
目前中国90%的能源来自化工燃料,并且这种形式在短期内(15-20年)不会发生变化。由于中国是个资源贫乏的国家,需要大量进口能源以支撑高速经济发展的需要,而能源又很大程度上由发达国家通过期货市场控制,为了减少在能源问题上对别国的过分依赖,节能作为一项切实可行的策略受到政府的重视,并且提出了一种新的理念:“节能”也是一种重要能源。 At present, 90% of China's energy comes from chemical fuels, and this form will not change in the short term (15-20 years). Since China is a resource-poor country, it needs to import a large amount of energy to support the needs of rapid economic development, and energy is largely controlled by developed countries through the futures market. A practical strategy has been valued by the government, and a new concept has been put forward: "energy saving" is also an important energy source.
节约热能的突出方面就是回收和利用余热。工业燃气(燃油)炉在生产过程中产生的烟气经过工业炉一次余热利用之后的排烟温度仍然较高(可达350-700℃),将温度达350-700℃的烟气直接排放在大气中,既浪费了能源,又污染环境。如果能将排烟温度降至180℃(甚至更低)以下,则既可以达到节能减排、降低生产运行成本,又可以起到改善人民生活品质的目的。 A prominent aspect of thermal energy conservation is the recovery and utilization of waste heat. The exhaust gas temperature of the flue gas produced during the production process of the industrial gas (fuel) furnace is still high (up to 350-700°C) after the first waste heat utilization of the industrial furnace, and the flue gas with a temperature of 350-700°C is directly discharged in the The atmosphere not only wastes energy, but also pollutes the environment. If the exhaust gas temperature can be reduced to below 180°C (or even lower), it can not only achieve energy saving and emission reduction, reduce production and operation costs, but also improve the quality of life of the people.
目前国内大型的钢铁厂的焦炉可以做到利用余热进行发电。但同时我国还有大批规模不一的金属热处理炉,功率从数百到几千千瓦不等。由于热处理炉的热效率仅为50%左右,如何把这部分余热利用好有着非常重大的实际意义。 At present, the coke ovens of large-scale domestic iron and steel plants can use waste heat to generate electricity. But at the same time, there are a large number of metal heat treatment furnaces of different sizes in my country, with power ranging from hundreds to thousands of kilowatts. Since the thermal efficiency of the heat treatment furnace is only about 50%, how to make good use of this part of waste heat has very great practical significance.
发明内容 Contents of the invention
本实用新型的目的在于提供一种工业炉余热回收系统,它可以将工业炉生产中排放的高温烟气进行充分回收,达到很好的节能目的。 The purpose of the utility model is to provide an industrial furnace waste heat recovery system, which can fully recover the high-temperature flue gas discharged in the production of the industrial furnace, so as to achieve a good energy-saving purpose.
为实现上述目的,本实用新型可采取下述技术方案: In order to achieve the above object, the utility model can take the following technical solutions:
本实用新型所述的工业炉余热回收系统,包括与多个工业炉排烟道相连通的总排烟通道以及通过排烟风机连接在所述总排烟通道上的余热回收装置,所述余热回收装置由一次换热装置和二次换热装置构成;所述一次换热装置为通过控制阀串联在总排烟通道上的带有进出水口的气/水换热器,所述二次换热装置为带有一级进出水口和二级进出水口的水/水换热器;所述气/水换热器的出水口通过管路与水/水换热器的一级进水口相连通,所述水/水换热器的一级出水口通过管路及设置在所述管路上的循环泵与所述气/水换热器的进水口相连通;待加热冷水管路通过阀门与所述水/水换热器的二级进水口相连通,所述水/水换热器的二级出水口经热水管路和设置在该热水管路上的水泵与蓄热水池相连通。 The industrial furnace waste heat recovery system described in the utility model includes a total smoke exhaust channel connected with a plurality of industrial grate flues and a waste heat recovery device connected to the total smoke exhaust channel through a smoke exhaust fan. The recovery device is composed of a primary heat exchange device and a secondary heat exchange device; the primary heat exchange device is an air/water heat exchanger connected in series on the total smoke exhaust channel through a control valve, and the secondary heat exchange device The heat device is a water/water heat exchanger with primary water inlet and outlet and secondary water inlet and outlet; the water outlet of the air/water heat exchanger is connected with the primary water inlet of the water/water heat exchanger through a pipeline, The first-stage water outlet of the water/water heat exchanger communicates with the water inlet of the air/water heat exchanger through a pipeline and a circulating pump arranged on the pipeline; the cold water pipeline to be heated communicates with the water inlet through a valve. The secondary water inlet of the water/water heat exchanger is connected, and the secondary water outlet of the water/water heat exchanger is connected with the heat storage tank through the hot water pipeline and the water pump arranged on the hot water pipeline.
所述气/水换热器为热管换热器,所述水/水换热器为板式换热器。 The air/water heat exchanger is a heat pipe heat exchanger, and the water/water heat exchanger is a plate heat exchanger.
所述排烟风机后的总排烟通道和气/水换热器排烟口后部的排烟通道之间设置有旁路排烟支路,所述旁路排烟支路上设置有控制阀门。 A bypass smoke exhaust branch is set between the general smoke exhaust channel behind the exhaust fan and the smoke exhaust channel at the rear of the gas/water heat exchanger exhaust port, and a control valve is set on the bypass smoke exhaust branch.
所述待加热冷水管路包括并联在一起的自蓄水池引出的循环管路以及由自来水管网引入的补水管路。 The cold water pipeline to be heated includes a circulation pipeline drawn from a water storage tank and a supplementary water pipeline introduced from a tap water pipe network connected in parallel.
本实用新型的优点在于结构简单、余热利用率高,在有效的将工业炉烟气排放温度降至130℃左右的同时,还能得到60℃的热水来满足人们的供水和采暖需求。 The utility model has the advantages of simple structure and high waste heat utilization rate. While effectively reducing the flue gas discharge temperature of the industrial furnace to about 130°C, it can also obtain hot water at 60°C to meet people's water supply and heating needs.
附图说明 Description of drawings
图1是本实用新型的系统原理图。 Fig. 1 is the system schematic diagram of the utility model.
具体实施方式 Detailed ways
如图1所示,本实用新型所述的工业炉余热回收系统,包括与多个工业炉1排烟道相连通的总排烟通道2以及通过排烟风机3连接在总排烟通道2上的余热回收装置,所述余热回收装置由一次换热装置和二次换热装置构成;一次换热装置为通过控制阀4串联在总排烟通道2上的带有进出水口的热管气/水换热器5,二次换热装置为带有一级进出水口和二级进出水口的板式水/水换热器6;热管气/水换热器5的出水口通过管路与板式水/水换热器6的一级进水口相连通,板式水/水换热器6的一级出水口通过管路及设置在管路上的循环泵7和安全阀14与热管气/水换热器5的进水口相连通;并联在一起的自蓄水池9引出的循环管路12以及由自来水管网引入的补水管路13通过阀门与热管水/水换热器6的二级进水口相连通,板式水/水换热器6的二级出水口经热水管路和设置在该热水管路上的水泵8与蓄热水池9相连通;在排烟风机3后的总排烟通道和热管气/水换热器5排烟口后部的排烟通道之间设置有旁路排烟支路10,在旁路排烟支路10上设置有控制阀门11。
As shown in Figure 1, the industrial furnace waste heat recovery system described in the utility model includes a total
本实用新型工作时,将多台加热炉1的高温排烟汇流成一根总排烟通道2进行强制排烟,通过变频排烟风机3控制其排烟压力,把热管式换热器5串联到总排烟通道2上,换热器5的一对进出水口接软化水,用循环泵7使其通过换热器5循环进行换热,得到最高120℃的高温软化水;把高温软化水经板式换热器6进行二次换热,板式换热器6另外一对进出水口分别接自来水或蓄水池9,得到60℃左右的热水存入蓄水池9,供采暖或生活用。蓄水池9可以缓冲用水高峰期的压力。当蓄水池9中的热水已满,水温超过70℃时,可以关闭余热回收系统,通过旁路排烟支路10直接排走烟气。
When the utility model is working, the high-temperature smoke exhaust from
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| Application Number | Priority Date | Filing Date | Title |
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| CN2012200974611U CN202494345U (en) | 2012-03-15 | 2012-03-15 | Industrial furnace waste heat recovery system |
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| CN2012200974611U CN202494345U (en) | 2012-03-15 | 2012-03-15 | Industrial furnace waste heat recovery system |
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| CN202494345U true CN202494345U (en) | 2012-10-17 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103673649A (en) * | 2013-12-16 | 2014-03-26 | 机械工业第六设计研究院有限公司 | Waste heat recovery and comprehensive utilization system of industrial furnace group |
| CN104294013A (en) * | 2014-09-10 | 2015-01-21 | 浙江长兴正达电炉制造有限公司 | Continuous mesh belt tempering heating furnace |
| CN104294017A (en) * | 2014-09-10 | 2015-01-21 | 浙江长兴正达电炉制造有限公司 | Continuous mesh belt quenching furnace capable of recovering waste heat |
| CN105135898A (en) * | 2015-09-21 | 2015-12-09 | 宝钢发展有限公司 | Smoke energy cyclic utilization system of rotary hearth furnace |
| CN106435201A (en) * | 2016-10-09 | 2017-02-22 | 云南冶金新立钛业有限公司 | Reaction system used for producing high titanium slag |
| CN106796086A (en) * | 2014-06-04 | 2017-05-31 | 斯蒂-B及T集团股份公司 | For the heat exchanger of industrial furnace |
-
2012
- 2012-03-15 CN CN2012200974611U patent/CN202494345U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103673649A (en) * | 2013-12-16 | 2014-03-26 | 机械工业第六设计研究院有限公司 | Waste heat recovery and comprehensive utilization system of industrial furnace group |
| CN106796086A (en) * | 2014-06-04 | 2017-05-31 | 斯蒂-B及T集团股份公司 | For the heat exchanger of industrial furnace |
| CN104294013A (en) * | 2014-09-10 | 2015-01-21 | 浙江长兴正达电炉制造有限公司 | Continuous mesh belt tempering heating furnace |
| CN104294017A (en) * | 2014-09-10 | 2015-01-21 | 浙江长兴正达电炉制造有限公司 | Continuous mesh belt quenching furnace capable of recovering waste heat |
| CN105135898A (en) * | 2015-09-21 | 2015-12-09 | 宝钢发展有限公司 | Smoke energy cyclic utilization system of rotary hearth furnace |
| CN106435201A (en) * | 2016-10-09 | 2017-02-22 | 云南冶金新立钛业有限公司 | Reaction system used for producing high titanium slag |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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Granted publication date: 20121017 |