CN105927301A - Organic rankine cycle flue gas waste heat recovery system - Google Patents
Organic rankine cycle flue gas waste heat recovery system Download PDFInfo
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- CN105927301A CN105927301A CN201610280999.9A CN201610280999A CN105927301A CN 105927301 A CN105927301 A CN 105927301A CN 201610280999 A CN201610280999 A CN 201610280999A CN 105927301 A CN105927301 A CN 105927301A
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- organic rankine
- evaporimeter
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K13/00—General layout or general methods of operation of complete plants
- F01K13/02—Controlling, e.g. stopping or starting
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K21/00—Steam engine plants not otherwise provided for
- F01K21/04—Steam engine plants not otherwise provided for using mixtures of steam and gas; Plants generating or heating steam by bringing water or steam into direct contact with hot gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
- F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
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- Combustion & Propulsion (AREA)
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- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The invention discloses an organic Rankine cycle flue gas waste heat recovery system, and belongs to the technical field of waste heat utilization. The organic Rankine cycle flue gas waste heat recovery system comprises an organic Rankine system and a flue gas processing system, and further comprises a flow distribution protection system and a control system. The flow distribution protection system and the flue gas processing system are connected with the organic Rankine system in parallel through a three-way valve I and communicate with a flue gas channel. The flow distribution protection system is arranged and used as an auxiliary system for conducting flow distribution on the amount of flue gas entering the system, and therefore the amount of the flue gas and heat which pass through the main system, namely, the organic Rankine system can be kept stable all the time, the system can be in the stable running state all the time, and the problems that because all parts of the system are in the overheated or high-load running state for a long time, the service life of the parts is influenced and cost is increased are solved; and meanwhile, control is conducted on the whole waste heat recovery process through the control system, control over the system can be more efficient, accurate and intelligent, and the waste heat utilization efficiency and quality are higher.
Description
Technical field
The invention belongs to technical field of waste heat utilization, be specifically related to a kind of to there is defencive function, can the organic Rankine of stable operation follow
Ring flue gas waste heat recovery system.
Background technology
Substantial amounts of middle-low temperature heat is there is, if directly being set by boiler or condensation in the chemical industries such as oil, metallurgy, iron and steel
Standby by substantial amounts of, in the flue gas of low temperature, discharge of wastewater to environment, although so releasing substantial amounts of heat, but not only can
Cause huge energy waste, the most also can cause serious environmental thermal pollution.Recycle these residual heat resources, on the one hand can
To improve the utilization rate for primary energy, on the other hand the environmental thermal pollution problem in chemical industry can also be alleviated.It addition,
The low-grade heat source of other abundant forms is there is also, such as geothermal energy, solar energy, biomass energy etc. in China.Along with the energy is endangered
Increasingly sharpening of machine and environmental problem, the most gradually causes the attention of people to the utilization of these low-grade energies.
Organic Rankine bottoming cycle (ORC) system is as a kind of effective ways reclaiming low grade heat energy, and compensate for water as working medium is bright
It agree the defect of circulation, when reclaiming low grade heat energy, there is higher efficiency, therefore have the most wide application prospect.But
In system operation, certain interference and fluctuation can be there is, so the unstability that system is run can be caused, such as evaporimeter
The phenomenons such as acting is uprushed, heat source side is overheated, condensation end quantity of circulating water is not enough, cause system generated energy generation deviation, meeting time serious
Causing equipment to be stopped transport, not only the operation to system has an impact, and the life-span of system equipment can be caused to reduce, to system economy
For be a kind of huge challenge.
For the problems referred to above, it is necessary to existing organic rankine cycle system is improved, propose one and may insure that system begins
It is in the protection scheme of even running state eventually.
Summary of the invention
In view of this, it is an object of the invention to provide a kind of organic Rankine bottoming cycle flue gas waste heat recovery system with defencive function,
System can be made to be in more stable running status all the time, it is to avoid various parts is chronically at overheated and high loaded process state shadow
Ring its life-span and the problem increasing cost.
It is an object of the invention to be achieved through the following technical solutions:
A kind of organic Rankine bottoming cycle flue gas waste heat recovery system, including organic Rankine system and smoke processing system, it is characterised in that:
Also including divided current system and control system, described divided current system, smoke processing system are bright with organic by triple valve I
Willing system forms parallel connection and connects with exhaust gases passes,
Described organic Rankine system includes evaporimeter I, condenser I, device for storing liquid I, decompressor I and TRT I, described steaming
Sending out device I and be provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, described condenser I is provided with working medium import, working medium
Outlet, cooling water inlet and coolant outlet,
The gas approach of described evaporimeter I connects with triple valve I, and its exhanst gas outlet connects with smoke processing system, forms waste heat
Absorption circuit I；The working medium import of described evaporimeter I connects with device for storing liquid I, its sender property outlet and decompressor I and TRT
I connects, the working medium inlet communication of decompressor I and condenser I, and the sender property outlet of condenser I connects with device for storing liquid I, is formed
UTILIZATION OF VESIDUAL HEAT IN closed circuit I；
Described divided current system includes evaporimeter II, condenser II, device for storing liquid II, decompressor II and TRT II, institute
State evaporimeter II and be provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, described condenser II be provided with working medium import,
Sender property outlet, cooling water inlet and coolant outlet,
The gas approach of described evaporimeter II connects with triple valve I, and its exhanst gas outlet connects with smoke processing system, forms waste heat
Absorption circuit II；The working medium import of described evaporimeter II connects with device for storing liquid II, its sender property outlet and decompressor II and generating dress
Putting II connection, the working medium inlet communication of decompressor II and condenser II, the sender property outlet of condenser II connects with device for storing liquid II,
Form UTILIZATION OF VESIDUAL HEAT IN closed circuit II；
The working medium of triple valve II, described triple valve II and condenser I it is provided with on the pipeline that described evaporimeter I and decompressor I is connected
Inlet communication,
Triple valve III, described triple valve III and condenser II it is provided with on the pipeline that described evaporimeter II and decompressor II is connected
Working medium inlet communication,
Described exhaust-heat absorption loop I, exhaust-heat absorption loop II, heat utilization closed circuit I, heat utilization closed circuit II and threeway
Multiple check-valves, flow control valve and stop valve it is provided with smoke processing system on the pipeline that valve I connects,
Described control system includes being controlled triple valve I, triple valve II, triple valve III, flow control valve and stop valve
Multiple PLC.
Further, also include that overtemperature prote system, described overtemperature prote system include being arranged on evaporimeter I on the I of exhaust-heat absorption loop
And preheater between smoke processing system, it is arranged on returning between device for storing liquid I and evaporimeter I on UTILIZATION OF VESIDUAL HEAT IN closed circuit I
Hot device and be arranged on the spray working medium attemperator on device for storing liquid I and evaporimeter I connecting pipeline, described preheater respectively with liquid storage
Device I and regenerator connection, described regenerator connects with condenser I and TRT I respectively.
Further, described control system also includes being arranged on evaporimeter I, the two ends of evaporimeter II and decompressor I, decompressor II
The pressure sensor of front end and temperature sensor.
Further, between described preheater and device for storing liquid I, be provided with circulating pump group, described evaporimeter II and device for storing liquid II it
Between be provided with circulating pump.
Further, described circulating pump group includes two circulating pumps in parallel.
Further, described control system also includes being arranged in each loop of recovery system the multiple flowmeters being connected with PLC.
Further, described control system also includes the PLC master control platform being connected with each PLC.
Further, gas or liquid or charge of flowable solids are included by the heat source medium in exhaust gases passes entrance system.
The invention has the beneficial effects as follows:
Exhaust gas volumn in entrance system is shunted as subsystem by the present invention by arranging divided current system, so that passing through
The exhaust gas volumn of main system organic Rankine system, heat remain stable, make system be in more stable running status all the time, keep away
Exempt from various parts to be chronically at overheated and high loaded process state and affect its life-span and increase the problem of cost, meanwhile, by control
Whole waste heat recovery process is controlled by system processed, makes the control to system more efficient, accurate, intelligent, utilization rate of waste heat
Higher with quality, it addition, also by overtemperature prote system to instantaneous high-temperature and the control of continuous high temperature, make system run more steady.
Other advantages, target and the feature of the present invention will be illustrated to a certain extent in the following description, and
To a certain extent, will be apparent to those skilled in the art based on to investigating hereafter, or can
To be instructed from the practice of the present invention.The target of the present invention and other advantages can be realized by description below
And acquisition.
Accompanying drawing explanation
In order to make the object, technical solutions and advantages of the present invention clearer, below in conjunction with accompanying drawing, the present invention is made into one
The detailed description of step, wherein:
Fig. 1 is the structural representation of the organic Rankine bottoming cycle flue gas waste heat recovery system of invention.
Description of reference numerals:
1-organic Rankine system；2-smoke processing system；3-divided current system；4-overtemperature prote system；5-control system；6-
Triple valve I；7-exhaust gases passes；8-evaporimeter I；9-condenser I；10-device for storing liquid I；11-decompressor I；12-generates electricity
Device I；13-UTILIZATION OF VESIDUAL HEAT IN closed circuit I；14-evaporimeter II；15-condenser II；16-device for storing liquid II；17-decompressor
II；18-TRT II；19-exhaust-heat absorption loop I；20-exhaust-heat absorption loop II；21-heat utilization closed circuit II；22-is only
Return valve；23-flow control valve；24-stop valve；25-circulating pump group；26-preheater；27-regenerator；28-sprays working medium attemperator；
29-circulating pump；30-PLC master control platform；31-triple valve II；32-triple valve III；33-triple valve IV；34-triple valve V；35-
Flowmeter；P-pressure sensor；T-temperature sensor.
Detailed description of the invention
Hereinafter with reference to accompanying drawing, the preferred embodiments of the present invention are described in detail.Should be appreciated that preferred embodiment
Only for the explanation present invention rather than in order to limit the scope of the invention.
As it can be seen, the present embodiment organic Rankine bottoming cycle flue gas waste heat recovery system, including organic Rankine system 1 and fume treatment
System 2, it is characterised in that: also include divided current system 3, overtemperature prote system 4 and control system 5, divided current system
3, smoke processing system 2 is in parallel with organic Rankine system 1, meanwhile, at divided current system 3, flue gas by triple valve I 6
Reason system 2, organic Rankine system 1 all connect with exhaust gases passes 7, wherein, and divided current system 3 and smoke processing system 2
It is positioned at the same connector of triple valve I 6, the flue gas flow entering organic Rankine system 1 can be adjusted by triple valve I 6,
Many divided current systems 3 that is partly into, thus realize the protection to main system organic Rankine system,
Concrete, organic Rankine system includes evaporimeter I 8, condenser I 9, device for storing liquid I 10, decompressor I 11 and generating dress
Putting I 12, evaporimeter I 8 and be provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, condenser I 9 is provided with working medium and enters
Mouth, sender property outlet, cooling water inlet and coolant outlet, the gas approach of evaporimeter I 9 connects with triple valve I, and its flue gas goes out
Mouth connects with smoke processing system, forms exhaust-heat absorption loop I 19；The working medium import of evaporimeter I 8 connects with device for storing liquid I 10,
Its sender property outlet connects with decompressor I 11 and TRT I 12, the working medium inlet communication of decompressor I 11 and condenser I 9,
The sender property outlet of condenser I 9 connects with device for storing liquid I 10, forms UTILIZATION OF VESIDUAL HEAT IN closed circuit I 13；
Divided current system includes evaporimeter II 14, condenser II 15, device for storing liquid II 16, decompressor II 17 and TRT
II 18, evaporimeter II are provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, condenser II be provided with working medium import,
Sender property outlet, cooling water inlet and coolant outlet, the gas approach of evaporimeter II connects with triple valve I, its exhanst gas outlet with
Smoke processing system connects, and forms exhaust-heat absorption loop II 20；The working medium import of evaporimeter II connects with device for storing liquid II, its work
Matter outlet connects with decompressor II and TRT II, the working medium inlet communication of decompressor II and condenser II, condenser II's
Sender property outlet connects with device for storing liquid II, forms UTILIZATION OF VESIDUAL HEAT IN closed circuit II 21；
In the present embodiment, in exhaust-heat absorption loop I 19, exhaust-heat absorption loop II 20, heat utilization closed circuit I 13, heat utilization
Multiple check-valves 22, flow control valve it is provided with smoke processing system on the pipeline that closed circuit II 21 and triple valve I connects
23 and stop valve 24,
Overtemperature prote system include being arranged on the I of exhaust-heat absorption loop the preheater 26 between evaporimeter I and smoke processing system,
The regenerator 27 that is arranged on UTILIZATION OF VESIDUAL HEAT IN closed circuit I between device for storing liquid I and evaporimeter I and be arranged on device for storing liquid I
With the spray working medium attemperator 28 on evaporimeter I connecting pipeline, preheater 26 connects with device for storing liquid I and regenerator 27 respectively,
Regenerator 27 connects with condenser I and TRT I respectively.
Further, between preheater and device for storing liquid I, it is provided with circulating pump group 25, arranges between evaporimeter II and device for storing liquid II
Circulating pump 29, circulating pump 29, circulating pump group 25 is had to be centrifugation frequency pump or a combination thereof, drive cycle fluid by circulating pump
UTILIZATION OF VESIDUAL HEAT IN closed circuit circulates, thus realizes UTILIZATION OF VESIDUAL HEAT IN, in the present embodiment, circulating pump group include two in parallel from
Heart variable frequency pump, one, as standby, can be improved the security of system.
In the present embodiment, the pipeline that evaporimeter I and decompressor I is connected is provided with triple valve II 31, triple valve II 31 and condensation
The working medium inlet communication of device I；Triple valve III 32, triple valve III 32 it is provided with on the pipeline that evaporimeter II and decompressor II is connected
Working medium inlet communication with condenser II；It is provided with triple valve IV 33 between two circulating pumps in parallel and device for storing liquid I；Spray
Triple valve V 34 is set between working medium attemperator and evaporimeter I, regenerator；
Control system includes multiple PLC and a PLC master control platform 30, and the present embodiment PLC is 6 altogether,
Being respectively PLC1, PLC2, PLC3, PLC4, PLC5, PLC6, its major control object: PLC1 controls triple valve
I；PLC2 controls triple valve II；PLC3 controls triple valve III；PLC4 controls triple valve IV；PLC5 controls triple valve V；
PLC6 controls the circulating pump between evaporimeter II and device for storing liquid II, and meanwhile, PLC also will be to being arranged on recovery system
Flowmeter 35, flow control valve, stop valve, pressure sensor and temperature sensor in each loop are controlled.
In the present embodiment, it is provided with pressure sensor P and temperature sensor T at the two ends of evaporimeter I and evaporimeter II, with
Time, also it is provided with pressure sensor and temperature sensor in the front end of decompressor I and decompressor II, can be respectively to by evaporation
Device I, evaporimeter II, decompressor I and decompressor II actual flow or heat are monitored, thus reach preferable duty.
The operation of the present embodiment and the process of control:
Low-temperature waste heat flue gas enters system, PLC1 control triple valve I and open, flue gas thermal source is divided into two parts, major part
Flue gas enters organic Rankine bottoming cycle main system, and remainder flue gas enters in divided current system, heat source side cigarette does not occurs in system
During the situation that tolerance is not enough, divided current system is in stable running status all the time, when exhaust gas volumn occurs abnormal:
1. heat source side generation transient state overtemperature situation: when short time (i.e. transient state) overheat condition occurs in heat source side, system can be made to steam
Send out temperature suddenly to rise, so that decompressor I acting is fluctuated, thus affect generator I traveling comfort, occurring
During this type of phenomenon, in system, PLC5 will automatically control spray working medium attemperator spray into by measuring heat source side inlet temperature and flow
A certain amount of supercooling working medium, increases system evaporator amount of work；But owing to spraying into Biological process, cause flow to be uprushed, then by PLC2
By measuring two ends temperature, pressure and flow, control triple valve II and open, open flow control valve, it is ensured that the flow uprushed is not
Decompressor can be produced impact.
2. heat source side generation stable state overtemperature situation: when long-time (i.e. stable state) overheat condition occurs in heat source side, PLC5 in system
Will be by measuring heat source side inlet temperature and flow, control spray working medium attemperator sprays into and working medium is quantitatively subcooled, and PLC2 will be controlled simultaneously
Triple valve II processed opens, and opens flow control valve, keeps the stable operation of decompressor.
3. heat source side generation shortage of heat situation: when shortage of heat occurs in heat source side, control is disconnected divided current system by system,
Flue gas is made only to flow into organic Rankine bottoming cycle main system, it is ensured that exhaust gas volumn is sufficient.Disconnection divided current system step: first PLC3
Control triple valve III to open, make working medium be bypassed to condenser II, simultaneously close off decompressor II and generator II, treat system
After middle Temperature of Working declines, PLC6 control stop valve and pump cuts out, then divided current system will be closed, and treat heat
After source heat abundance, to wait to reopen.
Exhaust gas volumn in entrance system is shunted as subsystem by the present embodiment by arranging divided current system, so that logical
Cross the exhaust gas volumn of main system organic Rankine system, heat remains stable, makes system be in more stable running status all the time,
Avoid various parts to be chronically at overheated and high loaded process state affect its life-span and increase the problem of cost, pass through meanwhile
Whole waste heat recovery process is controlled by control system, makes the control to system more efficient, accurate, intelligent, it addition, the most logical
Cross overtemperature prote system to instantaneous high-temperature and the control of continuous high temperature, make system run more steady.
As the improvement of the present embodiment, include gas or liquid or flowable solid by the heat source medium in exhaust gases passes entrance system
Body, such as the middle low temperature waste gas produced in industrial process or waste water, and geothermal energy or other low-grade solid energy etc..
As the improvement of the present embodiment, the cycle fluid of system is that non-azeotrope mixes organic working medium, and its thermodynamic property is stable, profit
In the stability and the security that improve system.
As the improvement of the present embodiment, the decompressor in system is turbo-expander, it is ensured that system stability reliability service.
It also have the advantage that
1. the present invention adds some infrastructure devices on the basis of original organic rankine cycle system, it is ensured that evaporation is occurring in system
When thermal agitation crossed by device, maintain the stable operation of system；
2. system uses spray working medium attemperator, effectively utilizes device resource originally in system, and effectively serves control evaporation
The effect of temperature；
3. being also a set of organic rankine cycle system on the divided current system parenchyma that system uses, controlling its start and stop can be effective
Control flue gas flow, it is ensured that the stability that main system is run；
4. select ripe turbo-expander, it is ensured that system reliability service；
5. the system reform is relatively easy, and engineering difficulty is relatively low.
Finally illustrating, above example is only in order to illustrate technical scheme and unrestricted, although with reference to preferably
The present invention has been described in detail by embodiment, it will be understood by those within the art that, can be to the skill of the present invention
Art scheme is modified or equivalent, and without deviating from objective and the scope of the technical program, it all should be contained at this
In the middle of bright right.
Claims (8)
1. an organic Rankine bottoming cycle flue gas waste heat recovery system, including organic Rankine system and smoke processing system, it is characterised in that:
Also including divided current system and control system, described divided current system, smoke processing system pass through triple valve I with organic
Rankine system is in parallel and connects with exhaust gases passes,
Described organic Rankine system includes evaporimeter I, condenser I, device for storing liquid I, decompressor I and TRT I, described evaporation
Device I is provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, and described condenser I is provided with working medium import, working medium
Outlet, cooling water inlet and coolant outlet,
The gas approach of described evaporimeter I connects with triple valve I, and its exhanst gas outlet connects with smoke processing system, forms waste heat and inhales
Regain road I；The working medium import of described evaporimeter I connects with device for storing liquid I, its sender property outlet and decompressor I and TRT
I connects, and the working medium inlet communication of decompressor I and condenser I, the sender property outlet of condenser I connects with device for storing liquid I, shape
Become UTILIZATION OF VESIDUAL HEAT IN closed circuit I；
Described divided current system includes evaporimeter II, condenser II, device for storing liquid II, decompressor II and TRT II, described steaming
Sending out device II and be provided with gas approach, exhanst gas outlet, working medium import and sender property outlet, described condenser II is provided with working medium import, work
Matter outlet, cooling water inlet and coolant outlet,
The gas approach of described evaporimeter II connects with triple valve I, and its exhanst gas outlet connects with smoke processing system, forms waste heat and inhales
Regain road II；The working medium import of described evaporimeter II connects with device for storing liquid II, its sender property outlet and decompressor II and generating dress
Putting II connection, the working medium inlet communication of decompressor II and condenser II, the sender property outlet of condenser II connects with device for storing liquid II,
Form UTILIZATION OF VESIDUAL HEAT IN closed circuit II；
Being provided with triple valve II on the pipeline that described evaporimeter I and decompressor I is connected, the working medium of described triple valve II and condenser I is entered
Mouth connection,
The work of triple valve III, described triple valve III and condenser II it is provided with on the pipeline that described evaporimeter II and decompressor II is connected
Matter inlet communication,
Described exhaust-heat absorption loop I, exhaust-heat absorption loop II, heat utilization closed circuit I, heat utilization closed circuit II and triple valve
Multiple check-valves, flow control valve and stop valve it is provided with smoke processing system on the pipeline that I connects,
Described control system includes being controlled many to triple valve I, triple valve II, triple valve III, flow control valve and stop valve
Individual PLC.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: also include overtemperature prote
System, it is pre-that described overtemperature prote system includes being arranged on the I of exhaust-heat absorption loop between evaporimeter I and smoke processing system
Hot device, the regenerator being arranged on UTILIZATION OF VESIDUAL HEAT IN closed circuit I between device for storing liquid I and evaporimeter I and be arranged on liquid storage
Device I and the spray working medium attemperator on evaporimeter I connecting pipeline, described preheater connects with device for storing liquid I and regenerator respectively
Logical, described regenerator connects with condenser I and TRT I respectively.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: described control system is also
Pass including the pressure sensor of front end and temperature being arranged on evaporimeter I, the two ends of evaporimeter II and decompressor I, decompressor II
Sensor.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: described preheater and storage
It is provided with circulating pump group between liquid device I, between described evaporimeter II and device for storing liquid II, is provided with circulating pump.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 4, it is characterised in that: described circulating pump group bag
Include two circulating pumps in parallel.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: described control system is also
Including being arranged in each loop of recovery system the multiple flowmeters being connected with PLC.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: described control system is also
Including the PLC master control platform being connected with each PLC.
Organic Rankine bottoming cycle flue gas waste heat recovery system the most according to claim 1, it is characterised in that: entered by exhaust gases passes
Enter the heat source medium in system and include gas or liquid or charge of flowable solids.
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Cited By (1)
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| CN108036288A (en) * | 2017-11-20 | 2018-05-15 | 江苏太湖锅炉股份有限公司 | The crossed configuration of more waste heat boilers |
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| CN103206317A (en) * | 2013-04-24 | 2013-07-17 | 哈尔滨广瀚新能动力有限公司 | Cascaded recycling system for waste heat of internal combustion generating set |
| CN103306764A (en) * | 2013-07-05 | 2013-09-18 | 重庆大学 | Kalina circulating system with two-phase expansion machine |
| CN103670558A (en) * | 2013-12-27 | 2014-03-26 | 天津大学 | Internal combustion engine waste heat recovery system adopting double-pressure multistage expansion reheating |
| CN103953405A (en) * | 2014-05-05 | 2014-07-30 | 碧海舟（北京）石油化工设备有限公司 | Waste heat power generation system utilizing organic Rankine cycle |
| CN105443174A (en) * | 2016-01-07 | 2016-03-30 | 上海维尔泰克螺杆机械有限公司 | Cascade type organic Rankine cycle system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108036288A (en) * | 2017-11-20 | 2018-05-15 | 江苏太湖锅炉股份有限公司 | The crossed configuration of more waste heat boilers |
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