CN204372879U - A kind of two medium waste heat boiler - Google Patents
A kind of two medium waste heat boiler Download PDFInfo
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- CN204372879U CN204372879U CN201420718767.3U CN201420718767U CN204372879U CN 204372879 U CN204372879 U CN 204372879U CN 201420718767 U CN201420718767 U CN 201420718767U CN 204372879 U CN204372879 U CN 204372879U
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- 239000002918 waste heat Substances 0.000 title claims abstract description 44
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000003546 flue gas Substances 0.000 claims abstract description 29
- 239000007789 gas Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000009776 industrial production Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 9
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
本实用新型提供了一种双介质余热锅炉,其既同时为工业生产提供过热蒸汽又能同时提供采暖用热水,因而能有效降低锅炉购置及运行成本,并能大大减少能源的耗费及污染排放。其包括余热锅炉烟道和汽包,余热锅炉烟道水平安装于支架上,余热锅炉烟道一端设有余热高温烟气进口、另一端设有烟气出口,烟气出口连接烟囱,余热锅炉烟道内沿烟气流动方向依次设置有过热器、蒸发器、省煤器,高温烟气自余热高温烟气进口进入余热锅炉烟道,依次冲刷所述过热器、蒸发器、省煤器的垂直管束后从烟气出口经所述烟囱排入大气,其特征在于:余热锅炉烟道内还设置有机热载体锅炉的对流段,有机热载体锅炉对流段设置于沿烟气流动方向的省煤器的后部。
The utility model provides a dual-medium waste heat boiler, which not only provides superheated steam for industrial production but also hot water for heating at the same time, thereby effectively reducing boiler purchase and operating costs, and greatly reducing energy consumption and pollution discharge . It includes waste heat boiler flue and steam drum. The waste heat boiler flue is installed horizontally on the bracket. One end of the waste heat boiler flue is provided with a waste heat high-temperature flue gas inlet, and the other end is equipped with a flue gas outlet. The flue gas outlet is connected to the chimney. A superheater, an evaporator, and an economizer are installed in the duct in sequence along the flow direction of the flue gas. The high-temperature flue gas enters the flue of the waste heat boiler from the waste heat high-temperature flue gas inlet, and flushes the vertical tube bundles of the superheater, evaporator, and economizer in sequence. Then it is discharged into the atmosphere from the flue gas outlet through the chimney. It is characterized in that: the convection section of the organic heat carrier boiler is also arranged in the flue of the waste heat boiler, and the convection section of the organic heat carrier boiler is arranged behind the economizer along the flow direction of the flue gas. department.
Description
技术领域 technical field
本实用新型涉及余热锅炉技术领域,具体为一种双介质余热锅炉。 The utility model relates to the technical field of waste heat boilers, in particular to a double-medium waste heat boiler.
背景技术 Background technique
余热锅炉是利用各种工业过程中的废气、废料或废液中的余热及其可燃物质燃烧后产生的热量把水加热到一定工质的锅炉,其因能大大提高燃料燃烧释放的热量的利用率而具有良好的节能作用。常规的余热锅炉多为单一传热介质,如余热蒸汽锅炉、余热有机热载体锅炉,但是在实际生产生活中,往往会出现既需要通过蒸汽锅炉产生过热蒸汽来作为生产动力,又需要通过热水锅炉提供热水用于采暖的情况,在此情形下若设置两台锅炉则不仅设备成本高,而且也导致能源耗费大,无法达到目前节能减排的要求。 The waste heat boiler is a boiler that uses the waste heat in waste gas, waste materials or waste liquid in various industrial processes and the heat generated by the combustion of combustible substances to heat water to a certain working medium, because it can greatly improve the use of heat released by fuel combustion It has a good energy-saving effect. Conventional waste heat boilers mostly use a single heat transfer medium, such as waste heat steam boilers and waste heat organic heat carrier boilers. The boiler provides hot water for heating. In this case, if two boilers are installed, not only the equipment cost is high, but also the energy consumption is large, which cannot meet the current energy saving and emission reduction requirements.
发明内容 Contents of the invention
针对上述问题,本实用新型提供了一种双介质余热锅炉,其既同时为工业生产提供过热蒸汽又能同时提供采暖用热水,因而能有效降低锅炉购置及运行成本,并能大大减少能源的耗费及污染排放。 In view of the above problems, the utility model provides a dual-medium waste heat boiler, which can provide superheated steam for industrial production and hot water for heating at the same time, thus effectively reducing boiler purchase and operating costs, and greatly reducing energy consumption. consumption and pollution.
其技术方案是这样的,其包括余热锅炉烟道和汽包,所述余热锅炉烟道水平安装于支架上,所述余热锅炉烟道一端设有余热高温烟气进口、另一端设有烟气出口,所述烟气出口连接烟囱,所述余热锅炉烟道内沿烟气流动方向依次设置有过热器、蒸发器、省煤器,高温烟气自所述余热高温烟气进口进入所述余热锅炉烟道,依次冲刷所述过热器、蒸发器、省煤器的垂直管束后从所述烟气出口经所述烟囱排入大气,其特征在于:所述余热锅炉烟道内还设置有机热载体锅炉的对流段,所述有机热载体锅炉对流段设置于沿烟气流动方向的所述省煤器的后部。 The technical solution is as follows: it includes a waste heat boiler flue and a steam drum. The waste heat boiler flue is installed horizontally on a bracket. Outlet, the flue gas outlet is connected to the chimney, and the waste heat boiler flue is provided with a superheater, an evaporator, and an economizer in sequence along the flue gas flow direction, and high-temperature flue gas enters the waste heat boiler from the waste heat high-temperature flue gas inlet The flue, which flushes the vertical tube bundles of the superheater, evaporator, and economizer in sequence, is discharged into the atmosphere from the flue gas outlet through the chimney, and is characterized in that an organic heat carrier boiler is also arranged in the flue of the waste heat boiler The convection section of the organic heat carrier boiler is arranged at the rear of the economizer along the flue gas flow direction.
其进一步特征在于: It is further characterized by:
所述有机热载体锅炉对流段的一端为出油口、另一端为回油口; One end of the convection section of the organic heat carrier boiler is an oil outlet, and the other end is an oil return port;
所述省煤器的出水口与所述汽包通过管道连接,所述汽包通过下降管、上升管与所述蒸发器连接形成循环回路,所述汽包通过上部蒸汽管道与所述过热器连接,所述过热器的蒸汽出口外接过热蒸汽母管。 The water outlet of the economizer is connected to the steam drum through a pipeline, and the steam drum is connected to the evaporator through a downcomer and an upcomer to form a circulation loop, and the steam drum is connected to the superheater through an upper steam pipeline. The steam outlet of the superheater is externally connected to the superheated steam main pipe.
本实用新型的双介质余热锅炉的有益效果在于:其结构简单,烟道内设置有两种受热面,因而通过前环节产生的高温烟气同时水、导热油两种介质进行加热,从而达到同是提供用于生产的过热蒸汽及用于生活供暖的热水的目的,有效减少锅炉购置运行成本,并能大大降低能源消耗和污染排放。 The beneficial effect of the dual-medium waste heat boiler of the present utility model lies in that its structure is simple, and there are two kinds of heating surfaces in the flue, so that the high-temperature flue gas generated in the previous link is heated by two media of water and heat-conducting oil at the same time, so as to achieve the same The purpose of providing superheated steam for production and hot water for domestic heating can effectively reduce boiler purchase and operation costs, and can greatly reduce energy consumption and pollution emissions.
附图说明 Description of drawings
图1为本实用新型双介质余热锅炉的示意图。 Fig. 1 is a schematic diagram of the dual-media waste heat boiler of the present invention.
具体实施方式 Detailed ways
见图1,本实用新型双介质余热锅炉包括余热锅炉烟道1和汽包2,余热锅炉烟道2水平安装于支架3上,余热锅炉烟道1一端设有余热高温烟气进口4、另一端设有烟气出口5,烟气出口5连接烟囱6,余热锅炉烟道1内沿烟气流动方向依次设置有过热器7、蒸发器8、省煤器9,高温烟气自余热高温烟气进口4进入余热锅炉烟道2内,依次冲刷过热器7、蒸发器8、省煤器9的垂直管束后从烟气出口5经烟囱6排入大气,余热锅炉烟道1内还设置有机热载体锅炉对流段10,有机热载体锅炉对流段10设置于沿烟气流动方向的省煤器9的后部;有机热载体锅炉对流段10的一端为出油口11、另一端为回油口12;省煤器9的出水口与汽包2通过管道13连接,汽包2通过下降管14、上升管15与蒸发器8连接形成循环回路,汽包2通过上部蒸汽管道16与过热器7连接,过热器7的过热蒸汽出口外接过热蒸汽母管。 As shown in Figure 1, the dual-media waste heat boiler of the present invention includes a waste heat boiler flue 1 and a steam drum 2. The waste heat boiler flue 2 is horizontally installed on a support 3. One end of the waste heat boiler flue 1 is provided with a waste heat high-temperature flue gas inlet 4 and the other One end is provided with a flue gas outlet 5, and the flue gas outlet 5 is connected to the chimney 6. The waste heat boiler flue 1 is provided with a superheater 7, an evaporator 8, and an economizer 9 in sequence along the flow direction of the flue gas. The gas inlet 4 enters the waste heat boiler flue 2, flushes the vertical tube bundles of the superheater 7, evaporator 8, and economizer 9 in sequence, and then is discharged into the atmosphere from the flue gas outlet 5 through the chimney 6. The convection section 10 of the heat carrier boiler, the convection section 10 of the organic heat carrier boiler is arranged at the rear of the economizer 9 along the flue gas flow direction; one end of the convection section 10 of the organic heat carrier boiler is the oil outlet 11, and the other end is the oil return port 12; the water outlet of the economizer 9 is connected to the steam drum 2 through the pipe 13, the steam drum 2 is connected to the evaporator 8 through the downcomer 14 and the upcomer 15 to form a circulation loop, and the steam drum 2 is connected to the superheater through the upper steam pipe 16 7, the superheated steam outlet of the superheater 7 is externally connected to the superheated steam main pipe.
下面具体描述一下本实用新型双介质余热锅炉的运行过程: The following specifically describes the operation process of the utility model dual-medium waste heat boiler:
烟气侧,前环节产生的高温烟气经余热高温烟气进口4进入余热锅炉烟道2内,并依次冲刷过热器7、蒸发器8、省煤器9的垂直管束以及有机热载体锅炉对流段10后经过烟气出口5排入烟囱6、最终排入大气; On the flue gas side, the high-temperature flue gas generated in the previous link enters the waste heat boiler flue 2 through the waste heat high-temperature flue gas inlet 4, and flushes the vertical tube bundles of the superheater 7, evaporator 8, economizer 9 and the convection flow of the organic heat carrier boiler in sequence. After the section 10, it is discharged into the chimney 6 through the flue gas outlet 5, and finally discharged into the atmosphere;
汽水侧,除氧水首先进入省煤器9并在省煤器9内吸收热量升温到略低于汽包压力下的饱和温度后进入汽包2,进入汽包2的水与汽包2内的饱和水混合后沿汽包2下方的下降管14进入蒸发器8从而吸收热量开始产汽,通常情况下进入蒸发器8的饱和水只有部分直接变成蒸汽,因而在蒸发器8内流动的是汽水混合物,汽水混合物通过上升管15离开蒸发器8进入汽包2并由汽包2上部的汽水分离装置分离,其中分离出的水落到汽包2内的水空间并再次通过下降管14进入蒸发器8吸收热量产生汽水混合物,而分离出的饱和蒸汽则通过上部蒸汽管道14进入过热器7内并吸收热量使饱和蒸汽变成过热蒸汽后从过热蒸汽出口流入过热蒸汽母管用于生产; On the soda water side, deoxygenated water first enters the economizer 9 and absorbs heat in the economizer 9 to raise the temperature to slightly lower than the saturation temperature under the pressure of the steam drum, then enters the steam drum 2, and enters the water in the steam drum 2 and the steam drum 2 After the saturated water is mixed, it enters the evaporator 8 along the downcomer 14 below the steam drum 2 to absorb heat and start to produce steam. Usually, only part of the saturated water entering the evaporator 8 directly turns into steam, so the amount of water flowing in the evaporator 8 It is a mixture of steam and water, which leaves the evaporator 8 through the riser pipe 15 and enters the steam drum 2 and is separated by the steam-water separation device on the upper part of the steam drum 2, where the separated water falls into the water space in the steam drum 2 and enters again through the downcomer 14 The evaporator 8 absorbs heat to generate a mixture of steam and water, and the separated saturated steam enters the superheater 7 through the upper steam pipe 14 and absorbs heat to make the saturated steam become superheated steam, and then flows into the superheated steam main pipe from the superheated steam outlet for production;
矿物导热油在有机热载体锅炉对流段内闭路循环,矿物油从回油口进入对流段再从出油口流出,经过过热器7、蒸发器8、省煤器9后的烟气再通过有机热载体锅炉对流段后温度降至约150℃,同时对有机热载体锅炉对流段内的矿物导热油加热,用来加热相应介质或提供生活采暖热水。 Mineral heat transfer oil circulates in a closed circuit in the convection section of the organic heat carrier boiler. The mineral oil enters the convection section from the oil return port and then flows out from the oil outlet. After passing through the superheater 7, evaporator 8, and economizer 9, the flue gas passes through the organic After the convection section of the heat carrier boiler, the temperature drops to about 150°C. At the same time, the mineral heat transfer oil in the convection section of the organic heat carrier boiler is heated to heat the corresponding medium or provide hot water for domestic heating.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104406144A (en) * | 2014-11-27 | 2015-03-11 | 江苏太湖锅炉股份有限公司 | Double-medium waste heat boiler |
CN105937759A (en) * | 2016-04-28 | 2016-09-14 | 上海光热实业有限公司 | ORC economizer for power plant smoke waste heat utilization, system and method |
CN113587076A (en) * | 2021-07-15 | 2021-11-02 | 宁波久丰热电有限公司 | Boiler steam-water system waste heat utilization device |
-
2014
- 2014-11-27 CN CN201420718767.3U patent/CN204372879U/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104406144A (en) * | 2014-11-27 | 2015-03-11 | 江苏太湖锅炉股份有限公司 | Double-medium waste heat boiler |
CN105937759A (en) * | 2016-04-28 | 2016-09-14 | 上海光热实业有限公司 | ORC economizer for power plant smoke waste heat utilization, system and method |
CN113587076A (en) * | 2021-07-15 | 2021-11-02 | 宁波久丰热电有限公司 | Boiler steam-water system waste heat utilization device |
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