CN206129339U - Organic rankine cycle device - Google Patents
Organic rankine cycle device Download PDFInfo
- Publication number
- CN206129339U CN206129339U CN201621084382.1U CN201621084382U CN206129339U CN 206129339 U CN206129339 U CN 206129339U CN 201621084382 U CN201621084382 U CN 201621084382U CN 206129339 U CN206129339 U CN 206129339U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- surge tank
- turbine
- rankine cycle
- organic rankine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000012530 fluid Substances 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 7
- 239000002826 coolant Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000017525 heat dissipation Effects 0.000 abstract description 4
- 238000003303 reheating Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 15
- 238000010438 heat treatment Methods 0.000 description 10
- 238000010586 diagram Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及有机朗肯循环技术领域,尤其涉及一种有机朗肯循环装置。The utility model relates to the technical field of organic Rankine cycle, in particular to an organic Rankine cycle device.
背景技术Background technique
现有的低温有机朗肯循环发电装置包括依次连通的加热装置、蒸发器、稳压罐、透平、冷凝器、储液罐和工质泵,其中,工质泵将工质升压并输送至蒸发器加热,在启动阶段,工质流量较小,工质泵一般带有变频装置,即使变频也易出现工质泵出口压力和流量的波动,进而影响蒸发器换热效果,同时,由于工质流量逐渐升高,蒸发器的加热不一定均匀,导致工质流经蒸发器后可能还是气液两相流,不能直接进入汽轮机,而是先进入稳压罐,稳压罐的作用为:(1)对工质流量、压力波动进行缓冲,保证透平进汽均匀;(2)汽液分离,在启动阶段保证蒸发器流出的液态工质经液态导流管减压减温后回收至凝汽器。而当系统进入稳定负荷阶段,蒸发器出口为符合透平进口参数要求的蒸汽,此时系统流量和压力已趋于稳定,波动较小,稳压罐的作用不再明显,而稳压罐由于表面积较大,即使有保温层,也依然存在散热损失,而且稳压罐由于其中间容积,内部始终充满具有一定压力和温度的工质不能使用,导致热源利用率低。The existing low-temperature organic Rankine cycle power generation device includes a heating device, an evaporator, a surge tank, a turbine, a condenser, a liquid storage tank and a working medium pump connected in sequence, wherein the working medium pump boosts the pressure of the working medium and delivers To the heating of the evaporator, in the start-up stage, the flow rate of the working medium is small, and the working medium pump is generally equipped with a frequency conversion device. The flow rate of the working fluid gradually increases, and the heating of the evaporator is not necessarily uniform. As a result, the working fluid may still be a gas-liquid two-phase flow after passing through the evaporator. It cannot directly enter the steam turbine, but first enters the surge tank. The function of the surge tank is : (1) Buffer the flow and pressure fluctuations of the working medium to ensure that the turbine enters the steam evenly; (2) Separation of vapor and liquid, ensure that the liquid working medium flowing out of the evaporator is recovered after decompression and temperature reduction through the liquid guide pipe during the start-up phase to the condenser. And when the system enters the stable load stage, the outlet of the evaporator is steam that meets the requirements of the turbine inlet parameters. At this time, the flow and pressure of the system have become stable, and the fluctuation is small. The surface area is large, even if there is an insulation layer, there is still heat dissipation loss, and because of its intermediate volume, the surge tank is always filled with working fluid with a certain pressure and temperature and cannot be used, resulting in low heat source utilization.
因此,如何提供一种有机朗肯循环装置,以避免热损失,是目前本领域技术人员亟待解决的技术问题。Therefore, how to provide an organic Rankine cycle device to avoid heat loss is a technical problem to be solved urgently by those skilled in the art.
实用新型内容Utility model content
有鉴于此,本实用新型的目的在于提供一种机朗肯循环装置,以避免热损失。In view of this, the purpose of this utility model is to provide a machine Rankine cycle device to avoid heat loss.
为了达到上述目的,本实用新型提供如下技术方案:In order to achieve the above object, the utility model provides the following technical solutions:
一种有机朗肯循环装置,包括加热装置、蒸发器、稳压罐、透平、冷凝器、储液罐和工质泵,其中,所述加热装置用于为所述蒸发器提供热量,所述蒸发器通过第一管路与所述稳压罐连通,所述稳压罐通过第二管路与所述透平连通,所述透平通过第三管路与所述冷凝器连通,所述冷凝器通过第四管路与所述储液罐连通,所述储液罐通过第五管路与所述蒸发器连通,所述工质泵设置在所述第五管路上,还包括旁路管道,所述旁路管道与所述稳压罐并联,所述旁路管道的一端与所述第一管路连通,其另一端与所述第二管路连通,所述第一管路上设置有第一截止阀门,所述旁路管道上设置有第二截止阀门。An organic Rankine cycle device, comprising a heating device, an evaporator, a surge tank, a turbine, a condenser, a liquid storage tank and a working medium pump, wherein the heating device is used to provide heat for the evaporator, and the The evaporator communicates with the surge tank through a first pipeline, the surge tank communicates with the turbine through a second pipeline, and the turbine communicates with the condenser through a third pipeline, so The condenser communicates with the liquid storage tank through a fourth pipeline, the liquid storage tank communicates with the evaporator through a fifth pipeline, the working medium pump is arranged on the fifth pipeline, and includes a bypass A pipeline, the bypass pipeline is connected in parallel with the surge tank, one end of the bypass pipeline communicates with the first pipeline, and the other end communicates with the second pipeline, and on the first pipeline A first shut-off valve is set, and a second shut-off valve is set on the bypass pipeline.
优选的,上述第二截止阀门为电动阀门。Preferably, the above-mentioned second cut-off valve is an electric valve.
优选的,上述冷凝器上设置有冷却塔,所述冷却塔的冷却介质为水。Preferably, the above-mentioned condenser is provided with a cooling tower, and the cooling medium of the cooling tower is water.
优选的,上述工质泵为气动泵。Preferably, the above-mentioned working medium pump is a pneumatic pump.
本实用新型提供的有机朗肯循环装置,包括加热装置、蒸发器、稳压罐、透平、冷凝器、储液罐和工质泵,其中,所述加热装置用于为所述蒸发器提供热量,所述蒸发器通过第一管路与所述稳压罐连通,所述稳压罐通过第二管路与所述透平连通,所述透平通过第三管路与所述冷凝器连通,所述冷凝器通过第四管路与所述储液罐连通,所述储液罐通过第五管路与所述蒸发器连通,所述工质泵设置在所述第五管路上,还包括旁路管道,所述旁路管道与所述稳压罐并联,所述旁路管道的一端与所述第一管路连通,其另一端与所述第二管路连通,所述第一管路上设置有第一截止阀门,所述旁路管道上设置有第二截止阀门。The organic Rankine cycle device provided by the utility model includes a heating device, an evaporator, a surge tank, a turbine, a condenser, a liquid storage tank and a working medium pump, wherein the heating device is used to provide the evaporator with heat, the evaporator communicates with the surge tank through the first pipeline, the surge tank communicates with the turbine through the second pipeline, and the turbine communicates with the condenser through the third pipeline The condenser communicates with the liquid storage tank through the fourth pipeline, the liquid storage tank communicates with the evaporator through the fifth pipeline, and the working medium pump is arranged on the fifth pipeline, It also includes a bypass pipeline, the bypass pipeline is connected in parallel with the surge tank, one end of the bypass pipeline communicates with the first pipeline, and the other end communicates with the second pipeline, and the first A first shut-off valve is set on a pipeline, and a second shut-off valve is set on the bypass pipeline.
那么当系统进入稳定负荷阶段,蒸发器出口为符合透平进口参数要求的蒸汽,此时系统流量和压力已趋于稳定,波动较小,稳压罐的作用不再明显时,关闭第一截止阀门,开启第二截止阀门,使得工质不再通过稳压罐,而是从旁路管道直接通过,蒸发器流出的蒸汽将绕过稳压罐,直接流经旁路管道进入透平中,避免了对稳压罐内工质的再加热,减少了稳压罐的散热损失,从而避免热损失。Then when the system enters the stable load stage, the outlet of the evaporator is steam that meets the requirements of the turbine inlet parameters. At this time, the flow and pressure of the system have tended to be stable, the fluctuation is small, and the function of the surge tank is no longer obvious, close the first cut-off valve, open the second cut-off valve, so that the working fluid no longer passes through the surge tank, but directly through the bypass pipe, and the steam flowing out of the evaporator will bypass the surge tank and directly flow into the turbine through the bypass pipe. The reheating of the working medium in the surge tank is avoided, and the heat dissipation loss of the surge tank is reduced, thereby avoiding heat loss.
附图说明Description of drawings
为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description These are some embodiments of the present utility model. Those skilled in the art can also obtain other drawings based on these drawings without any creative work.
图1为本实用新型实施例提供的有机朗肯循环装置的结构示意图。Fig. 1 is a schematic structural diagram of an organic Rankine cycle device provided by an embodiment of the present invention.
上图1中:In Figure 1 above:
加热装置1、蒸发器2、第一截止阀门3、旁路管道4、稳压罐5、第二截止阀门6、透平7、冷凝器8、冷却塔9、储液罐10、工质泵11。Heating device 1, evaporator 2, first shut-off valve 3, bypass pipeline 4, surge tank 5, second shut-off valve 6, turbine 7, condenser 8, cooling tower 9, liquid storage tank 10, working medium pump 11.
具体实施方式detailed description
为使本实用新型实施例的目的、技术方案和优点更加清楚,下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the utility model more clear, the technical solutions in the embodiments of the utility model will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the utility model. Obviously, the described The embodiments are some embodiments of the present utility model, but not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of the present utility model.
请参考图1,图1为本实用新型实施例提供的有机朗肯循环装置的结构示意图。Please refer to FIG. 1 , which is a schematic structural diagram of an organic Rankine cycle device provided by an embodiment of the present invention.
本实用新型实施例提供的有机朗肯循环装置,包括加热装置1、蒸发器2、稳压罐5、透平7、冷凝器8、储液罐10和工质泵11,其中,加热装置1用于为蒸发器2提供热量,蒸发器2通过第一管路与稳压罐5连通,稳压罐5通过第二管路与透平7连通,透平7通过第三管路与冷凝器8连通,冷凝器8通过第四管路与储液罐10连通,储液罐10通过第五管路与蒸发器2连通,工质泵11设置在第五管路上,还包括旁路管道4,旁路管道4与稳压罐5并联,旁路管道4的一端与第一管路连通,其另一端与第二管路连通,第一管路上设置有第一截止阀门3,旁路管道4上设置有第二截止阀门6。The organic Rankine cycle device provided by the embodiment of the utility model includes a heating device 1, an evaporator 2, a surge tank 5, a turbine 7, a condenser 8, a liquid storage tank 10 and a working medium pump 11, wherein the heating device 1 Used to provide heat for the evaporator 2, the evaporator 2 communicates with the surge tank 5 through the first pipeline, the surge tank 5 communicates with the turbine 7 through the second pipeline, and the turbine 7 communicates with the condenser through the third pipeline 8, the condenser 8 communicates with the liquid storage tank 10 through the fourth pipeline, the liquid storage tank 10 communicates with the evaporator 2 through the fifth pipeline, and the working fluid pump 11 is arranged on the fifth pipeline, which also includes a bypass pipeline 4 , the bypass pipeline 4 is connected in parallel with the surge tank 5, one end of the bypass pipeline 4 communicates with the first pipeline, and the other end communicates with the second pipeline, the first shut-off valve 3 is arranged on the first pipeline, and the bypass pipeline 4 is provided with a second cut-off valve 6 .
那么当系统进入稳定负荷阶段,蒸发器2出口为符合透平进口参数要求的蒸汽,此时系统流量和压力已趋于稳定,波动较小,稳压罐5的作用不再明显时,关闭第一截止阀门3,开启第二截止阀门6,使得工质不再通过稳压罐5,而是从旁路管道4直接通过,蒸发器2流出的蒸汽将绕过稳压罐5,直接流经旁路管道4进入透平7中,避免了对稳压罐5内工质的再加热,减少了稳压罐5的散热损失。Then when the system enters the stable load stage, the outlet of the evaporator 2 is steam that meets the requirements of the turbine inlet parameters. At this time, the system flow and pressure have tended to be stable, the fluctuation is small, and the function of the surge tank 5 is no longer obvious. One cut-off valve 3, open the second cut-off valve 6, so that the working medium no longer passes through the surge tank 5, but directly passes through the bypass pipe 4, and the steam flowing out of the evaporator 2 will bypass the surge tank 5 and directly flow through The bypass pipeline 4 enters the turbine 7, avoiding the reheating of the working fluid in the surge tank 5, and reducing the heat dissipation loss of the surge tank 5.
其中,第二截止阀门6为电动阀门,主要是鉴于高温环境,手动的不安全。Wherein, the second cut-off valve 6 is an electric valve, mainly because it is unsafe to operate manually in view of the high temperature environment.
其中,冷凝器8上设置有冷却塔9,冷却塔9的冷却介质为水,工质泵11为气动泵。Wherein, the condenser 8 is provided with a cooling tower 9, the cooling medium of the cooling tower 9 is water, and the working medium pump 11 is a pneumatic pump.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本实用新型。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本实用新型的精神或范围的情况下,在其它实施例中实现。因此,本实用新型将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments enables those skilled in the art to realize or use the utility model. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to these embodiments shown herein, but will conform to the widest scope consistent with the principles and novel features disclosed herein.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621084382.1U CN206129339U (en) | 2016-09-27 | 2016-09-27 | Organic rankine cycle device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621084382.1U CN206129339U (en) | 2016-09-27 | 2016-09-27 | Organic rankine cycle device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206129339U true CN206129339U (en) | 2017-04-26 |
Family
ID=58571510
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621084382.1U Expired - Fee Related CN206129339U (en) | 2016-09-27 | 2016-09-27 | Organic rankine cycle device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206129339U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111894685A (en) * | 2020-08-12 | 2020-11-06 | 广州达都动力科技有限公司 | Steam turbine capable of controlling rotating speed of power generation shaft |
-
2016
- 2016-09-27 CN CN201621084382.1U patent/CN206129339U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111894685A (en) * | 2020-08-12 | 2020-11-06 | 广州达都动力科技有限公司 | Steam turbine capable of controlling rotating speed of power generation shaft |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104266250B (en) | Hydraulic damping type wind heating system | |
CN206129339U (en) | Organic rankine cycle device | |
CN102192555A (en) | Air compressor waste heat recovery and utilization system | |
CN202811282U (en) | Circulating air compressor heat recovery hot water delivery control system | |
CN104329127B (en) | Multi-unit joint expansion system | |
CN203796527U (en) | Direct air cooling unit evacuation pipeline cooling system with absorption heat pump | |
CN207268554U (en) | A heat pump unit | |
CN105698241B (en) | A kind of method of 150MW high back pressures thermal power plant unit circulation pump of heat-supply network operation | |
CN204922936U (en) | Low pressure economizer connected system | |
CN205560278U (en) | Diffused argon gas recovery device | |
CN204244061U (en) | Cooling system for wind turbine converter equipment | |
CN204438296U (en) | Industrial smoke UTILIZATION OF VESIDUAL HEAT IN joint network system | |
CN207422527U (en) | Cooling water circulation system | |
CN204290611U (en) | Steam turbine open water system | |
CN204619688U (en) | A reabsorbent optimization device | |
CN206290976U (en) | A kind of remote device for increasing steam conveying capacity | |
CN205895774U (en) | Hydraulic oil cooling device | |
CN202382224U (en) | Boiler flue gas waste heat recovery system | |
CN203717358U (en) | Afterheat recycling system for air compressor | |
CN208845241U (en) | A spiral channel steam turbine | |
CN103498799A (en) | Water pump device with self-absorption function | |
CN206300372U (en) | A kind of tower type solar energy thermal power generation fused salt heat absorption circulatory system | |
CN203248243U (en) | External circulating water cooling system of diesel generator | |
CN209546891U (en) | A cooling tower device for a vacuum dampening machine | |
CN202547491U (en) | Physical cleaning device for air compressor heat exchanger |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170426 Termination date: 20190927 |