CN201417093Y - Waste heat boiler heat recovery system for glass production line - Google Patents
Waste heat boiler heat recovery system for glass production line Download PDFInfo
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- CN201417093Y CN201417093Y CN200920303022XU CN200920303022U CN201417093Y CN 201417093 Y CN201417093 Y CN 201417093Y CN 200920303022X U CN200920303022X U CN 200920303022XU CN 200920303022 U CN200920303022 U CN 200920303022U CN 201417093 Y CN201417093 Y CN 201417093Y
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- 239000002918 waste heat Substances 0.000 title claims abstract description 61
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 239000011521 glass Substances 0.000 title claims abstract description 22
- 238000011084 recovery Methods 0.000 title claims abstract description 20
- 230000001105 regulatory effect Effects 0.000 claims abstract description 13
- 239000012530 fluid Substances 0.000 claims abstract description 12
- 239000012528 membrane Substances 0.000 claims abstract description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 14
- 239000003546 flue gas Substances 0.000 claims description 14
- 239000011810 insulating material Substances 0.000 claims 1
- 238000010248 power generation Methods 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract description 3
- 238000010276 construction Methods 0.000 abstract description 2
- 230000009466 transformation Effects 0.000 abstract description 2
- 239000011449 brick Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000005338 heat storage Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture 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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- 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
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
本实用新型公开了一种热回收系统,尤其是涉及一种用于玻璃生产线的余热锅炉热回收系统,其余热利用效率更高。该系统在主烟道上的调节门与大闸门之间连接有余热烟道和余热锅炉,余热锅炉的工质管道的进口端和出口端连接热用户,在主烟道的入口端与调节门之间设置有主烟道过热器,主烟道过热器的工质管道的进口端和出口端分别连接余热锅炉工质管道出口端和热用户的工质管道入口端。在利用该余热发电的场合,可以使余热发电的功率提高10%~20%。主烟道过热器采用膜式换热片和刚性结构框构成的包墙式主烟道过热器,降低了玻璃生产线的投资成本,可广泛用于现有的玻璃生产线余热锅炉热回收系统的改造以及新的生产线的建造中。
The utility model discloses a heat recovery system, in particular to a heat recovery system for a waste heat boiler used in a glass production line, and the waste heat utilization efficiency is higher. In this system, a waste heat flue and a waste heat boiler are connected between the regulating door on the main flue and the large gate. A main flue superheater is arranged between them, and the inlet end and outlet end of the working fluid pipeline of the main flue superheater are respectively connected to the outlet end of the waste heat boiler working medium pipeline and the inlet end of the working medium pipeline of the heat user. In the case of using the waste heat to generate electricity, the power of the waste heat power generation can be increased by 10% to 20%. The main flue superheater adopts a wall-wrapped main flue superheater composed of membrane heat exchange fins and a rigid structural frame, which reduces the investment cost of the glass production line and can be widely used in the transformation of the heat recovery system of the waste heat boiler in the existing glass production line And new production lines are under construction.
Description
技术领域 technical field
本实用新型涉及一种热回收系统,尤其是涉及一种用于玻璃生产线的余热锅炉热回收系统。The utility model relates to a heat recovery system, in particular to a waste heat boiler heat recovery system used in a glass production line.
背景技术 Background technique
目前,现有用于玻璃生产线的余热锅炉与玻璃生产线的连接方式如图1所示,窑池产生的高温烟气通过蓄热池进行热交换后进入主烟道,再依次通过调节门、大闸门进入烟囱,靠烟囱的自然抽力排入大气。而排入大气的烟气带有较高的热量,为了充分利用这部分热力,达到节能减排的目的,在调节门后设置余热烟道,关闭大闸门。高温烟气通过蓄热池进入主烟道,通过调节门进入余热烟道,依次通过余热锅炉进口闸板门,余热锅炉,引风机,余热锅炉出口闸板门,最后进入烟囱排入大气。烟气的热量在通过余热锅炉时,交换给余热锅炉的工质,加热后的工质被送入汽轮发电机发电或者取暖等热用户。At present, the existing waste heat boiler used in the glass production line is connected to the glass production line as shown in Figure 1. The high-temperature flue gas generated by the kiln enters the main flue after heat exchange through the heat storage tank, and then passes through the regulating door and the large gate in turn. It enters the chimney and is discharged into the atmosphere by the natural suction of the chimney. The flue gas discharged into the atmosphere has relatively high heat. In order to make full use of this part of heat and achieve the purpose of energy saving and emission reduction, a waste heat flue is installed behind the regulating door and the large gate is closed. The high-temperature flue gas enters the main flue through the heat storage tank, enters the waste heat flue through the regulating door, passes through the waste heat boiler inlet shutter door, waste heat boiler, induced draft fan, waste heat boiler outlet shutter door, and finally enters the chimney and is discharged into the atmosphere. When the heat of the flue gas passes through the waste heat boiler, it is exchanged to the working fluid of the waste heat boiler, and the heated working medium is sent to heat users such as steam turbine generator for power generation or heating.
余热锅炉也称为热回收蒸汽发生器,和常规锅炉不同,余热锅炉中不发生燃烧过程,也没有燃烧相关的设备,从本质上讲,它只是一个燃气查?蒸汽的换热器。The waste heat boiler is also called heat recovery steam generator. Unlike conventional boilers, there is no combustion process in the waste heat boiler, and there is no combustion-related equipment. In essence, it is just a gas check? Steam heat exchanger.
上述现有的主烟道由耐火砖、保温砖、普通砖等组成,结构复杂,投资高。由于蓄热池出口温度较高大约600℃,如果耐火砖长期处于这样高的温度环境下,耐火砖的维护成本高,所以在玻璃生产线设计时,有意降低保温效果让热量部分散失,经实测到余热烟道接口点,主烟道的温度只有450~530℃,损失的热量非常大。Above-mentioned existing main flue is made up of refractory brick, insulation brick, common brick etc., and structure is complicated, and investment is high. Since the outlet temperature of the heat storage tank is about 600°C, if the refractory bricks are kept at such a high temperature for a long time, the maintenance cost of the refractory bricks will be high. Therefore, in the design of the glass production line, the heat preservation effect is intentionally reduced to allow part of the heat to be dissipated. According to actual measurements At the interface point of the waste heat flue, the temperature of the main flue is only 450-530°C, and the heat loss is very large.
实用新型内容 Utility model content
本实用新型所要解决的技术问题是提供一种用于玻璃生产线的余热利用效率更高的余热锅炉热回收系统。The technical problem to be solved by the utility model is to provide a waste heat boiler heat recovery system with higher waste heat utilization efficiency for a glass production line.
本实用新型解决其技术问题所采用的技术方案是:用于玻璃生产线的余热锅炉热回收系统,在主烟道上的调节门与大闸门之间连接有余热烟道和余热锅炉,余热锅炉的工质管道的出口端与主烟道过热器工质入口端连接,主烟道过热器工质出口端连接热用户,热用户的工质出口端与余热锅炉的工质入口端连接。The technical scheme adopted by the utility model to solve its technical problems is: the waste heat boiler heat recovery system used in the glass production line, the waste heat flue and the waste heat boiler are connected between the regulating door on the main flue and the large gate, and the waste heat boiler works The outlet end of the gas pipeline is connected with the working fluid inlet port of the main flue superheater, the working fluid outlet port of the main flue superheater is connected with the heat user, and the working fluid outlet port of the heat user is connected with the working fluid inlet port of the waste heat boiler.
进一步的是,主烟道过热器采用膜式换热片和刚性结构框构成的包墙式主烟道过热器。Furthermore, the main flue superheater adopts a wall-wrapped main flue superheater composed of membrane heat exchange fins and a rigid structural frame.
本实用新型的有益效果是:通过在主烟道的入口端与调节门之间设置主烟道过热器,充分利用这部分热量,将工质从饱和温度进一步加热至设计的过热温度,在保证压力和温度不变的情况下,有效的提高主蒸汽出力,从而提高整个动力装置的循环热效率或热用户的热使用效率。主烟道过热器设置在调节门前的主烟道位置,可取代玻璃生产线该处的主烟道,在利用该余热系统发电的场合,可以使余热发电的功率提高10%~20%。主烟道过热器采用膜式换热片和刚性结构框构成的包墙式主烟道过热器,使得该处不再使用耐火砖,保温砖,普通砖,降低了玻璃生产线的投资成本,可广泛用于现有的玻璃生产线余热锅炉热回收系统的改造以及新的生产线的建造中。The beneficial effects of the utility model are: by setting the main flue superheater between the inlet end of the main flue and the regulating door, this part of heat can be fully utilized to further heat the working fluid from the saturation temperature to the designed superheating temperature, ensuring Under the condition of constant pressure and temperature, the main steam output can be effectively increased, thereby improving the cycle heat efficiency of the entire power plant or the heat use efficiency of heat users. The main flue superheater is installed at the position of the main flue in front of the regulating door, which can replace the main flue of the glass production line. When the waste heat system is used to generate electricity, the power of waste heat power generation can be increased by 10% to 20%. The main flue superheater adopts a wall-wrapped main flue superheater composed of membrane heat exchange fins and a rigid structural frame, so that refractory bricks, insulation bricks, and ordinary bricks are no longer used here, which reduces the investment cost of the glass production line and can It is widely used in the transformation of the heat recovery system of the waste heat boiler of the existing glass production line and the construction of a new production line.
附图说明 Description of drawings
图1是现有的用于玻璃生产线的余热锅炉热回收系统的原理图;Figure 1 is a schematic diagram of an existing waste heat boiler heat recovery system used in a glass production line;
图2是本实用新型的用于玻璃生产线的余热锅炉热回收系统的原理图,图中箭头方向为烟气流动方向;Fig. 2 is a schematic diagram of the waste heat boiler heat recovery system used in the glass production line of the present invention, and the direction of the arrow in the figure is the direction of flue gas flow;
图3是本实用新型中的余热锅炉热回收系统的工质循环示意图,图中箭头方向为工质流动方向;Fig. 3 is a schematic diagram of the working medium circulation of the heat recovery system of the waste heat boiler in the present invention, and the direction of the arrow in the figure is the flow direction of the working medium;
图4是本实用新型中的主烟道过热器的横截面示意图。Fig. 4 is a schematic cross-sectional view of the main flue superheater in the utility model.
图中标记为:主烟道1、调节门2、大闸门3、余热烟道4、余热锅炉5、热用户6、主烟道过热器7、闸板门8。The marks in the figure are: main flue 1, regulating door 2, large gate 3, waste heat flue 4,
具体实施方式 Detailed ways
下面结合附图和实施例对本实用新型进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
如图1所示,现有的用于玻璃生产线的余热锅炉热回收系统,在主烟道1上的调节门2与大闸门3之间连接有余热烟道4和余热锅炉5,余热烟道4中的高温烟气通过余热锅炉5的烟气通道的过程中,烟气的热量交换给余热锅炉5的工质。余热锅炉5的工质管道的进口端和出口端连接热用户6,加热后的工质因此被送入汽轮发电机发电或者取暖等热用户。余热锅炉5通常采用水作为工质。As shown in Figure 1, in the existing waste heat boiler heat recovery system used in the glass production line, a waste heat flue 4 and a
为了提高余热利用效率,如图2~图4所示,本实用新型的热回收系统,在主烟道1的入口端与调节门2之间设置有主烟道过热器7,进一步将工质从饱和温度进一步加热至过热温度。余热锅炉5的工质管道的出口端与主烟道过热器7工质入口端连接,在主烟道1的入口端与调节门2之间设置有主烟道过热器7,主烟道过热器7的工质管道的进口端和出口端分别连接余热锅炉5工质管道出口端和热用户6的工质管道入口端。In order to improve the waste heat utilization efficiency, as shown in Fig. 2 to Fig. 4, the heat recovery system of the present invention is provided with a main flue superheater 7 between the inlet end of the main flue 1 and the regulating door 2, and further transfers the working fluid Further heating from saturation temperature to superheating temperature. The outlet end of the working medium pipeline of the
为了进一步降低玻璃生产线的投资成本和主烟道1的维修成本,同时提高其余热利用效率,如图4所示,主烟道过热器7采用膜式换热片和刚性结构框构成的包墙式主烟道过热器,从而取代玻璃生产线该处的主烟道1,同时,主烟道过热器7外表面采用轻型保温材料包裹,有利于隔热保温,进一步提高其余热利用效率。In order to further reduce the investment cost of the glass production line and the maintenance cost of the main flue 1, and at the same time improve the utilization efficiency of residual heat, as shown in Figure 4, the main flue superheater 7 adopts a wall consisting of membrane heat exchangers and rigid structural frames Type main flue superheater, thereby replacing the main flue 1 in the place of the glass production line. At the same time, the outer surface of the main flue superheater 7 is wrapped with light thermal insulation material, which is beneficial to heat insulation and heat preservation, and further improves the utilization efficiency of residual heat.
通常情况下,余热锅炉5的烟气进口端和出口端均设置有闸板门8,这些都是现有技术,这里不再赘述。Usually, both the flue gas inlet and outlet of the
在上述技术方案中,高温烟气的流程如图2所示。高温烟气进入蓄热池换热后,进入主烟道1上的主烟道过热器7,然后顺序通过调节门2、余热锅炉5前端的闸板门8、余热锅炉5,最后通过引风机抽入烟囱。In the above technical solution, the flow of high temperature flue gas is shown in Figure 2. After the high-temperature flue gas enters the heat storage tank for heat exchange, it enters the main flue superheater 7 on the main flue 1, then passes through the regulating door 2, the shutter door 8 at the front end of the
在上述技术方案中,余热锅炉热回收系统的工质循环工质流程如图3所示,工质由余热锅炉5中的给水泵抽入省煤器,与烟气进行热交换后进入汽包,汽包中的工质进入水冷蒸发器,与烟气进行热交换后,变成饱和水及饱和汽混合物进入汽包,饱和蒸汽工质从汽包顶进入主烟道前端设置的主烟道过热器7,进行热交换后变成过热工质,然后输入热用户6,如汽轮机做功带动发电机发电等,做功后的乏汽工质进入凝结器,被循环水冷却后变成凝结水,凝结水工质被凝结水泵抽入除氧器,除氧后的给水工质被给水泵又抽入省煤器,开始下一个工质循环。In the above technical scheme, the working fluid circulation process of the waste heat boiler heat recovery system is shown in Figure 3. The working fluid is pumped into the economizer by the feed water pump in the
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| CN200920303022XU CN201417093Y (en) | 2009-05-11 | 2009-05-11 | Waste heat boiler heat recovery system for glass production line |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102478232A (en) * | 2010-11-25 | 2012-05-30 | 江西永源节能环保科技有限公司 | Method for recycling heat energy of coke oven flue gas |
| CN103900387A (en) * | 2014-04-10 | 2014-07-02 | 天津华能北方热力设备有限公司 | Glass kiln waste heat recovery system |
| CN110345456A (en) * | 2019-01-02 | 2019-10-18 | 中冶华天工程技术有限公司 | Internal combustion engine smoke evacuation pre-cooling and UTILIZATION OF VESIDUAL HEAT IN integral system |
-
2009
- 2009-05-11 CN CN200920303022XU patent/CN201417093Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102478232A (en) * | 2010-11-25 | 2012-05-30 | 江西永源节能环保科技有限公司 | Method for recycling heat energy of coke oven flue gas |
| CN103900387A (en) * | 2014-04-10 | 2014-07-02 | 天津华能北方热力设备有限公司 | Glass kiln waste heat recovery system |
| CN103900387B (en) * | 2014-04-10 | 2015-12-30 | 天津华能北方热力设备有限公司 | The residual neat recovering system of glass furnace |
| CN110345456A (en) * | 2019-01-02 | 2019-10-18 | 中冶华天工程技术有限公司 | Internal combustion engine smoke evacuation pre-cooling and UTILIZATION OF VESIDUAL HEAT IN integral system |
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