CN115653706A - A steam turbine waste heat utilization system and its control method - Google Patents
A steam turbine waste heat utilization system and its control method Download PDFInfo
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- 239000002918 waste heat Substances 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 121
- 239000007921 spray Substances 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 8
- 238000010793 Steam injection (oil industry) Methods 0.000 claims description 6
- 238000005273 aeration Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 abstract description 6
- 230000007547 defect Effects 0.000 abstract 1
- 238000011084 recovery Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
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Abstract
Description
技术领域technical field
本发明涉及汽轮机余热回收利用技术领域,尤其是一种汽轮机余热利用系统及其控制方法。The invention relates to the technical field of steam turbine waste heat recovery and utilization, in particular to a steam turbine waste heat utilization system and a control method thereof.
背景技术Background technique
火电厂汽轮机做功带动发电机发动之后,会产生大量的高温乏汽。为了提高燃煤机组的整体效率,需要对高温乏汽的余热进行二次回收利用。现有的余热回收系统中通常是通过高温乏汽与低温水的热交换实现高温乏汽的余热回收,但是其回收率仅为30%~40%。After the steam turbine in the thermal power plant works to drive the generator to start, a large amount of high-temperature exhaust steam will be generated. In order to improve the overall efficiency of coal-fired units, secondary recovery and utilization of waste heat from high-temperature exhaust steam is required. In the existing waste heat recovery system, waste heat recovery of high temperature waste steam is usually realized through heat exchange between high temperature waste steam and low temperature water, but the recovery rate is only 30%-40%.
发明内容Contents of the invention
本发明要解决的技术问题是提供一种汽轮机余热利用系统及其控制方法,能够解决现有技术的不足,提高了火电厂汽轮机组的余热利用率。The technical problem to be solved by the present invention is to provide a steam turbine waste heat utilization system and its control method, which can solve the deficiencies of the prior art and improve the waste heat utilization rate of the steam turbine unit in a thermal power plant.
为解决上述技术问题,本发明所采取的技术方案如下。In order to solve the above technical problems, the technical solutions adopted by the present invention are as follows.
一种汽轮机余热利用系统,包括蒸汽喷射器,蒸汽喷射器的进气口与汽轮机低压缸排气管连接,蒸汽喷射器上连接有低温水进水管和高温水出水管,低温水进水管中的低温水在蒸汽喷射器中吸热变为高温水后从高温水出水管排出,蒸汽喷射器的出气口与吸热式热泵的低温热源进口相连,吸热式热泵的冷凝水排水管与低温水进水管相连,汽轮机低压缸排气管与吸热式热泵的高温热源进口相连,吸热式热泵上连接有低温水进水管和中温水出水管,低温水进水管的低温水在吸热式热泵中吸热变为中温水后从中温水出水管排出。A steam turbine waste heat utilization system, including a steam injector, the inlet of the steam injector is connected to the exhaust pipe of the low-pressure cylinder of the steam turbine, the steam injector is connected with a low-temperature water inlet pipe and a high-temperature water outlet pipe, and the low-temperature water inlet pipe The low-temperature water absorbs heat in the steam injector and turns into high-temperature water, and then it is discharged from the high-temperature water outlet pipe. The water inlet pipe is connected, the exhaust pipe of the low-pressure cylinder of the steam turbine is connected with the high-temperature heat source inlet of the heat-absorbing heat pump, and the low-temperature water inlet pipe and the medium-temperature water outlet pipe are connected to the heat-absorbing heat pump. Medium-temperature water is discharged from the medium-temperature water outlet pipe after the medium-heat absorption becomes medium-temperature water.
作为优选,所述蒸汽喷射器内安装有换热板,蒸汽喷射器进气口内侧端安装有喷汽头,换热板内设置有导流腔室,导流腔室的进液端与低温水进水管相连,导流腔室的出液端安装有喷水头,换热板上设置有若干个通槽,蒸汽喷射器的出气口上安装有汽水分离器。As a preference, a heat exchange plate is installed in the steam injector, a steam injection head is installed at the inner side of the air inlet of the steam injector, a diversion chamber is arranged in the heat exchange plate, and the liquid inlet end of the diversion chamber is connected to the low temperature The water inlet pipe is connected, the liquid outlet end of the diversion chamber is equipped with a water spray head, the heat exchange plate is provided with several through grooves, and the gas outlet of the steam ejector is equipped with a steam-water separator.
作为优选,所述换热板朝向喷汽头的一侧设置有若干个竖向的凹槽,凹槽与通槽交替排列,凹槽内安装有若干个相互分离的翅片,凹槽两侧设置有与通槽相连通的第一通孔。As a preference, the heat exchange plate is provided with several vertical grooves on the side facing the steam spray head, the grooves and through grooves are arranged alternately, and several fins separated from each other are installed in the grooves, and the two sides of the grooves A first through hole communicating with the through groove is provided.
作为优选,所述高温水出水管上安装有流量调节阀,通过高温水出水流量的控制,使蒸汽喷射器底部存储有一定量的高温水,喷汽头位于高温水液面一下,喷汽头上安装有曝气盘。As a preference, a flow regulating valve is installed on the high-temperature water outlet pipe. Through the control of the high-temperature water outlet flow, a certain amount of high-temperature water is stored at the bottom of the steam injector. The steam spray head is located below the high-temperature water liquid surface. Aeration discs are installed.
作为优选,所述喷水头包括并排设置的若干个喷水孔,相邻喷水孔的喷射方向相互交叉,全部喷水孔的喷射方向位于同一平面内。Preferably, the water spray head includes several water spray holes arranged side by side, the spray directions of adjacent water spray holes cross each other, and the spray directions of all the water spray holes are located in the same plane.
作为优选,所述汽水分离器内设置有螺旋导流管,螺旋导流管与汽水分离器的进口相连,螺旋导流管上均匀设置有若干个第二通孔,螺旋导流管外侧设置有单叶双曲面形状的弧形挡板,螺旋导流管的出口端设置有扩口,扩口位于弧形挡板内部。As a preference, a spiral guide tube is arranged inside the steam-water separator, and the spiral guide tube is connected to the inlet of the steam-water separator, and several second through holes are evenly arranged on the spiral guide tube, and the spiral guide tube is provided with a The arc-shaped baffle in the shape of a single-leaf hyperboloid, the outlet end of the spiral draft tube is provided with a flaring, and the flaring is located inside the arc-shaped baffle.
一种汽轮机余热利用系统的控制方法,包括以下步骤:A control method for a steam turbine waste heat utilization system, comprising the following steps:
汽轮机的高温乏汽从汽轮机低压缸排气管排出,进入蒸汽喷射器中与低温水进行第一次换热,制得高温水,经过第一次换热的低温乏汽进入吸热式热泵,利用高温乏汽作为驱动热源,低温乏汽与低温水进行第二次换热,制得中温水,吸热式热泵产生的冷凝水回流至低温水进水管循环使用。The high-temperature exhaust steam of the steam turbine is discharged from the exhaust pipe of the low-pressure cylinder of the steam turbine, and enters the steam injector for the first heat exchange with low-temperature water to produce high-temperature water. After the first heat exchange, the low-temperature exhaust steam enters the heat-absorbing heat pump, Using high-temperature exhaust steam as the driving heat source, low-temperature exhaust steam and low-temperature water conduct a second heat exchange to produce medium-temperature water, and the condensed water generated by the heat-absorbing heat pump is returned to the low-temperature water inlet pipe for recycling.
采用上述技术方案所带来的有益效果在于:本发明采用两级换热结构,充分回收乏汽中的热量。第一级换热采用蒸汽喷射接触换热方式,第二级换热采用热泵换热方式。对于蒸汽喷射器,本发明又进行了具有针对性的改进。本发明摒弃了蒸汽直接喷射换热的方式,首先将高温乏汽通入高温水中,进行第一次换热,从高温水中流出的高温乏汽流速降低,在换热板表面进行二次换热。由于换热板表面采用凹槽和通槽交替排列的方式,降低流速的高温乏汽可以与凹槽内的翅片充分接触换热,然后通过第一通孔和通槽流过换热板,降低高温乏汽在换热板区域产生的紊流。经过换热板的高温乏汽与喷水头喷出的水流进行第三次换热,喷水头的喷射可以生成水帘,从而进一步提高乏汽与水体的换热效率。经过三次低温换热后的乏汽通过汽水分离器分离水分后进入热泵,利用高温乏汽作为驱动热源,对低温乏汽进行第四次换热,从而充分利用乏汽热量。汽水分离器设计有内外两层分离结构,有效的提高汽水分离效率。The beneficial effect brought by the adoption of the above technical solution is that the present invention adopts a two-stage heat exchange structure to fully recover the heat in exhaust steam. The first-stage heat exchange adopts the steam injection contact heat exchange method, and the second-stage heat exchange adopts the heat pump heat exchange method. For the steam injector, the present invention has carried out targeted improvement. The present invention abandons the way of direct steam injection for heat exchange, and first passes the high-temperature exhaust steam into the high-temperature water for the first heat exchange, the flow rate of the high-temperature exhaust steam flowing out of the high-temperature water is reduced, and the second heat exchange is performed on the surface of the heat exchange plate . Since the surface of the heat exchange plate is alternately arranged with grooves and through grooves, the high-temperature exhaust steam with a reduced flow rate can fully contact the fins in the grooves for heat exchange, and then flow through the heat exchange plate through the first through holes and through grooves. Reduce the turbulent flow generated by high-temperature exhaust steam in the heat exchange plate area. The high-temperature exhaust steam passing through the heat exchange plate performs a third heat exchange with the water jetted from the sprinkler head, and the spray from the sprinkler head can form a water curtain, thereby further improving the heat exchange efficiency between the exhaust steam and the water body. After three times of low-temperature heat exchange, the exhaust steam passes through the steam-water separator to separate water and then enters the heat pump. The high-temperature exhaust steam is used as the driving heat source, and the low-temperature exhaust steam is subjected to the fourth heat exchange, so as to make full use of the heat of exhaust steam. The steam-water separator is designed with an inner and outer two-layer separation structure, which can effectively improve the steam-water separation efficiency.
附图说明Description of drawings
图1是本发明一个具体实施方式的结构图。Fig. 1 is a structural diagram of a specific embodiment of the present invention.
图2是本发明一个具体实施方式中蒸汽喷射器的结构图。Fig. 2 is a structural diagram of a steam injector in a specific embodiment of the present invention.
图3是本发明一个具体实施方式中换热板的局部放大图。Fig. 3 is a partially enlarged view of a heat exchange plate in a specific embodiment of the present invention.
图4是本发明一个具体实施方式中汽水分离器的结构图。Fig. 4 is a structural diagram of a steam-water separator in a specific embodiment of the present invention.
具体实施方式Detailed ways
参照图1-4,本发明一个具体实施方式包括蒸汽喷射器2,蒸汽喷射器2的进气口与汽轮机低压缸排气管1连接,蒸汽喷射器2上连接有低温水进水管3和高温水出水管4,低温水进水管3中的低温水在蒸汽喷射器2中吸热变为高温水后从高温水出水管4排出,蒸汽喷射器2的出气口与吸热式热泵5的低温热源进口相连,吸热式热泵5的冷凝水排水管6与低温水进水管3相连,汽轮机低压缸排气管1与吸热式热泵5的高温热源进口相连,吸热式热泵5上连接有低温水进水管3和中温水出水管7,低温水进水管3的低温水在吸热式热泵5中吸热变为中温水后从中温水出水管7排出。蒸汽喷射器2内安装有换热板8,蒸汽喷射器2进气口内侧端安装有喷汽头9,换热板8内设置有导流腔室10,导流腔室10的进液端与低温水进水管3相连,导流腔室10的出液端安装有喷水头11,换热板8上设置有若干个通槽12,蒸汽喷射器2的出气口上安装有汽水分离器13。换热板8朝向喷汽头9的一侧设置有若干个竖向的凹槽14,凹槽14与通槽12交替排列,凹槽14内安装有若干个相互分离的翅片15,凹槽14两侧设置有与通槽12相连通的第一通孔16。高温水出水管4上安装有流量调节阀17,通过高温水出水流量的控制,使蒸汽喷射器2底部存储有一定量的高温水,喷汽头9位于高温水液面一下,喷汽头9上安装有曝气盘18。喷水头11包括并排设置的若干个喷水孔19,相邻喷水孔19的喷射方向相互交叉,全部喷水孔19的喷射方向位于同一平面内。汽水分离器13内设置有螺旋导流管20,螺旋导流管20与汽水分离器13的进口相连,螺旋导流管20上均匀设置有若干个第二通孔21,螺旋导流管20外侧设置有单叶双曲面形状的弧形挡板22,螺旋导流管20的出口端设置有扩口23,扩口23位于弧形挡板22内部。With reference to Fig. 1-4, a specific embodiment of the present invention comprises
一种上述汽轮机余热利用系统的控制方法,包括以下步骤:A control method for the above steam turbine waste heat utilization system, comprising the following steps:
汽轮机的高温乏汽从汽轮机低压缸排气管1排出,进入蒸汽喷射器2中与低温水进行第一次换热,制得高温水,经过第一次换热的低温乏汽进入吸热式热泵5,利用高温乏汽作为驱动热源,低温乏汽与低温水进行第二次换热,制得中温水,吸热式热泵5产生的冷凝水回流至低温水进水管3循环使用。The high-temperature exhaust steam of the steam turbine is discharged from the exhaust pipe 1 of the low-pressure cylinder of the steam turbine, and enters the
本发明对于汽轮机高温乏汽的余热利用率可以达到45%~47%,有效的提高了汽轮机乏汽余热利用率,节约电厂运行成本。The invention can reach 45%-47% of the waste heat utilization rate of the high-temperature exhaust steam of the steam turbine, effectively improves the waste heat utilization rate of the exhaust steam of the steam turbine, and saves the operation cost of the power plant.
以上显示和描述了本发明的基本原理和主要特征和本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above. Those skilled in the industry should understand that the present invention is not limited by the above-mentioned embodiments. What are described in the above-mentioned embodiments and the description only illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention will also have Variations and improvements are possible, which fall within the scope of the claimed invention. The protection scope of the present invention is defined by the appended claims and their equivalents.
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| CN210663026U (en) * | 2019-10-14 | 2020-06-02 | 梁双荣 | Novel heating system |
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2022
- 2022-10-11 CN CN202211241387.0A patent/CN115653706B/en active Active
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| JPH11350920A (en) * | 1998-04-09 | 1999-12-21 | Osaka Gas Co Ltd | Exhaust heat recovery system |
| CN101240909A (en) * | 2008-03-19 | 2008-08-13 | 清华大学 | A steam injection heat pump heating system for recovering condensate waste heat in thermal power plants |
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