CN204536022U - The heat exchange of system, the proving installation of drag characteristic emulation is utilized for smoke discharging residual heat - Google Patents
The heat exchange of system, the proving installation of drag characteristic emulation is utilized for smoke discharging residual heat Download PDFInfo
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- CN204536022U CN204536022U CN201520232192.9U CN201520232192U CN204536022U CN 204536022 U CN204536022 U CN 204536022U CN 201520232192 U CN201520232192 U CN 201520232192U CN 204536022 U CN204536022 U CN 204536022U
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Abstract
The utility model discloses a kind of for smoke discharging residual heat utilize system heat exchange, drag characteristic emulation proving installation, comprise centrifugal blower, test section, simulation component and measurement mechanism, wherein: test section comprises flue gas heat-exchange unit simulation test section and preheating of air test section; Centrifugal blower is arranged at air inlet, and the air outlet of centrifugal blower is divided into two-way by pipeline, and a road is provided with flue gas heat-exchange unit simulation test section; Separately be provided with preheating of air test section on the way; Pipeline is outside equipped with simulation component, simulation component comprises expansion tank and water bath with thermostatic control, the inlet tube and outlet tube of water bath with thermostatic control is connected with the inlet tube and outlet tube of flue gas heat-exchange unit simulation test section heat-exchanging tube bundle to be determined, preheating of air test section heat-exchanging tube bundle respectively, form recirculated water closed-loop, water bath with thermostatic control is provided with constant temperature water tank ebullator.
Description
Technical field
The utility model relate to a kind of for smoke discharging residual heat utilize system heat exchange, drag characteristic emulation proving installation.
Background technology
In recent years, China's electric power installed capacity speedup is swift and violent, by the end of the year 2013, whole nation electric power installation total volume has reached 12.47 hundred million kilowatts, wherein thermoelectricity accounts for 69% of national total installation of generating capacity, and estimate to account for more than 80% of gross generation at China's thermoelectricity generated energy in 2015, therefore " energy-saving and emission-reduction " of Large-scale fire-electricity unit are the important energy source policies of country always, and each power plant is faced with energy-conservation great potential.In every loss of boiler, flue gas loss is maximum one, reduces exhaust gas temperature and has important practical significance for energy-saving and emission-reduction.Current exhaust gas temperature is generally 120-140 DEG C, and exhaust gas temperature often reduces by 10 ~ 20 DEG C, and boiler thermal output improves about 0.6% ~ 1%, the corresponding coal 1.2% ~ 2.4% of consumption less.Research at present about smoke discharging residual heat utilization is a lot, can introduce steam heat regenerative system as backheat heat, for adding Hot gas turbine condensate water, or by heating air preheater import cold air to introduce boiler, all have certain energy-saving effect.
In " utilizing smoke discharging residual heat to heat air preheater import cold air to introduce boiler energy-saving system ", at back-end ductwork and air preheater cool air inlet, all heat-exchanging tube bundle is set, in back-end ductwork, adopt fume afterheat to heat low-temperature water heating, and adopt by the low-temperature water heating heating cold air heated before air preheater cool air inlet, therefore in two parts heat interchanger, the selection of heat-exchanging tube bundle is very important, and the measurement of heat-exchanging tube bundle heat exchange, drag characteristic is particularly important.
At present, although the theoretical research " utilizing smoke discharging residual heat to heat air preheater import cold air to introduce boiler energy-saving system " is very abundant, practical engineering experience is still not enough, and especially power plant's site environment is complicated, a lot of position is not suitable for installing measuring point, and measurement is installed restricted; Some measurement mechanism aged deterioration, causes measurement result inaccurate; Do not measure the testing table of two heat interchanger heat exchange, drag characteristic intuitively.
Utility model content
The utility model in order to solve the problem, propose a kind of for smoke discharging residual heat utilize system heat exchange, drag characteristic emulation proving installation, this device on the basis meeting power plant's each equipment flow field similarity principle, simplify system, ensure measurement accuracy; According to flowing, the heat transfer characteristic of power plant system actual condition analog machine, system is emulated.
To achieve these goals, the utility model adopts following technical scheme:
Utilize the heat exchange of system, a proving installation for drag characteristic emulation for smoke discharging residual heat, comprise centrifugal blower, test section, simulation component and measurement mechanism, wherein:
Described test section comprises flue gas heat-exchange unit simulation test section and preheating of air test section;
Centrifugal blower is arranged at air inlet, and the air outlet of centrifugal blower is divided into two-way by pipeline, and a road is provided with flue gas heat-exchange unit simulation test section; Separately be provided with preheating of air test section on the way;
Pipeline is outside equipped with simulation component, simulation component: water bath with thermostatic control, the inlet tube and outlet tube of water bath with thermostatic control is connected with the inlet tube and outlet tube of flue gas heat-exchange unit simulation test section heat-exchanging tube bundle to be determined, preheating of air test section heat-exchanging tube bundle respectively, form recirculated water closed-loop, water bath with thermostatic control is provided with constant temperature water tank ebullator;
Together with the air that the air of preheating of air test section discharge and flue gas heat-exchange unit simulation test section are discharged outside discharge chamber, the parameter of measurement mechanism measurement test section, and be transferred to data acquisition unit.
Described measurement mechanism comprises pitot tube, electronic micro-manometer and spinner-type flowmeter, wherein, flue gas heat-exchange unit simulation test section and preheating of air test section rear end respectively arrange a pitot tube, and pitot tube connects electronic micro-manometer, is provided with spinner-type flowmeter between water circulating pump and preheating of air test section.
The inlet tube and outlet tube of described water bath with thermostatic control is connected with total inlet tube and outlet tube of the heat-exchanging tube bundle to be determined of flue gas heat-exchange unit simulation test section and preheating of air test section respectively, forms recirculated water closed-loop; The air channel regulation gate valve of heat-exchanging tube bundle to be measured is opened, and another air channel regulation gate valve closes.
The mean wind speed of the current stabilization xsect of test section measured by described pitot tube and microbarograph, and before and after flue gas heat-exchange unit simulation test section and preheating of air test section both sides set temperature sensor, with data acquisition unit by time determination test section import and export wind-warm syndrome.
Described water bath with thermostatic control is connected with heat-exchanging tube bundle and supplies water to heat-exchanging tube bundle through centrifugal water pump, spinner-type flowmeter, the connection inlet tube and outlet tube of water bath with thermostatic control between heat-exchanging tube bundle installs water inlet, leaving water temperature sensors, with data acquisition unit by time determination test section import and export water temperature.
Based on an emulation testing experimental technique for said apparatus, specifically comprise the following steps:
(1) water bath with thermostatic control water-filling, and be heated to design temperature;
(2) open water pump, slow running, until the intrafascicular air of developmental tube is emptying, high-speed cruising water pump, until stable conditions;
(3) blower fan is opened, and the air channel flashboard of standard-sized sheet heat-exchanging tube bundle to be measured, maximum wind velocity runs half an hour, treats stable conditions, and the time period that the heating arrangement reading water bath with thermostatic control is frequently opened, for checking water side draught heat and the thermal equilibrium adding heat;
(4) read the water side of data acquisition unit and the out temperature of air side, and adopt " nine grids " method, obtain with pitot tube and microbarograph measurement the mean wind speed obtaining xsect;
(5) aperture of flashboard is regulated, after stable conditions, under repetition (4) step obtains different wind speed, the out temperature of water side and air side, and the mean wind speed of xsect.
(6) process experimental data, remove test bad point, calculate the coefficient of heat transfer of heat-exchanging tube bundle.
In described step (2), stable conditions is that water side import and export pipeline section thermometric is identical.
In described step (5), stable conditions is for running more than 30min.
In described step (6), test bad point is the point of thermal equilibrium error more than 10%.
The beneficial effects of the utility model are: the power plant for energy conservation smoke discharging residual heat for " utilizing smoke discharging residual heat to heat air preheater import cold air to introduce boiler energy-saving system " utilizes system to carry out analog simulation, on the basis meeting power plant's each equipment flow field similarity principle, simplification system, can ensure measurement accuracy; Simulate flowing, the heat transfer characteristic of each equipment according to power plant system actual condition, system is emulated; Heat exchange, the drag characteristic test of each heat-exchanging tube bundle can be carried out at this experiment table; For the heat-exchanging tube bundle of power plant's Practical Project design, run provide reliable test figure basis.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein, A-air inlet; B-blower fan; D-flue gas heat-exchange unit simulation test section; F-preheating of air test section; J-can set temperature and record the heat time electrical heating water bath with thermostatic control; K-constant temperature water tank ebullator; L-controllable register valve; M-exhaust outlet; N-data acquisition unit; 1-8-electric thermo-couple temperature measuring point; 9-12-pitot tube; 13-14-electronic micro-manometer; 15-spinner-type flowmeter.
Embodiment:
Below in conjunction with accompanying drawing and embodiment, the utility model is described in further detail.
As shown in Figure 1, the device in this test platform comprise centrifugal blower B, air channel regulating gate, flue gas heat-exchange unit simulation test section D, preheating of air test section F, can set temperature and record the heat time electrical heating water bath with thermostatic control J, the supporting ebullator of water bath with thermostatic control, data acquisition unit N; Measurement mechanism comprises pitot tube, electronic micro-manometer, air channel measuring point temperature sensor, recirculated water measuring tempeature sensor, spinner-type flowmeter.
This platform can measure flue gas heat-exchange unit simulation test section heat-exchanging tube bundle, the heat exchange of preheating of air test section heat-exchanging tube bundle, drag characteristic, during measurement, respectively the inlet tube and outlet tube of water bath with thermostatic control is connected with total inlet tube and outlet tube of heat-exchanging tube bundle to be determined respectively, forms recirculated water closed-loop; The air channel regulation gate valve of heat-exchanging tube bundle to be measured is opened, and another air channel regulation gate valve closes.
" nine grids " method of employing, obtains with pitot tube and microbarograph measurements the mean wind speed obtaining current stabilization xsect, and at heat-exchanging tube bundle test section priority both sides set temperature sensor, with data acquisition unit by time determination test section import and export wind-warm syndrome.
Can to be connected with heat-exchanging tube bundle with the self-control electrical heating water bath with thermostatic control of record heat time and to supply water to heat-exchanging tube bundle through centrifugal water pump, spinner-type flowmeter by set temperature, the connection inlet tube and outlet tube of water bath with thermostatic control between heat-exchanging tube bundle installs water inlet, leaving water temperature sensors, with data acquisition unit by time determination test section import and export water temperature.
Water bath with thermostatic control adopts electrically heated mode, has the function of heating pipe built-in Shu Yunhang timing, accurately can calculate electrical heating power, for heat Balance Calculation; Can regulating thermostatic coolant-temperature gage voluntarily, precision can reach ± and 0.5 DEG C.
In actual measurement, measure in accordance with the following steps:
(1) water bath with thermostatic control water-filling, and be heated to design temperature;
(2) open water pump, slow running, until the intrafascicular air of developmental tube is emptying, high-speed cruising water pump, until stable conditions (it is identical that pipeline section thermometric is imported and exported in water side);
(3) blower fan is opened, and the air channel flashboard of standard-sized sheet heat-exchanging tube bundle to be measured, maximum wind velocity runs half an hour, treats stable conditions, and the time period that the heating arrangement reading water bath with thermostatic control is frequently opened, for checking water side draught heat and the thermal equilibrium adding heat;
(4) read the water side of data acquisition unit and the out temperature of air side, and adopt " nine grids " method, obtain with pitot tube and microbarograph measurement the mean wind speed obtaining xsect;
(5) aperture of flashboard is regulated, after stable conditions (30min), under repetition (4) step obtains different wind speed, the out temperature of water side and air side, and the mean wind speed of xsect.
(6) process experimental data, remove test bad point (thermal equilibrium error is more than 10%), calculate the coefficient of heat transfer of heat-exchanging tube bundle.
By reference to the accompanying drawings embodiment of the present utility model is described although above-mentioned; but the restriction not to the utility model protection domain; one of ordinary skill in the art should be understood that; on the basis of the technical solution of the utility model, those skilled in the art do not need to pay various amendment or distortion that creative work can make still within protection domain of the present utility model.
Claims (5)
1. utilize the heat exchange of system, a proving installation for drag characteristic emulation for smoke discharging residual heat, it is characterized in that: comprise centrifugal blower, test section, simulation component and measurement mechanism, wherein:
Described test section comprises flue gas heat-exchange unit simulation test section and preheating of air test section;
Centrifugal blower is arranged at air inlet, and the air outlet of centrifugal blower is divided into two-way by pipeline, and a road is provided with flue gas heat-exchange unit simulation test section; Separately be provided with preheating of air test section on the way;
Pipeline is outside equipped with simulation component, simulation component: water bath with thermostatic control, the inlet tube and outlet tube of water bath with thermostatic control is connected with the inlet tube and outlet tube of flue gas heat-exchange unit simulation test section heat-exchanging tube bundle to be determined, preheating of air test section heat-exchanging tube bundle respectively, form recirculated water closed-loop, water bath with thermostatic control is provided with constant temperature water tank ebullator;
Together with the air that the air of preheating of air test section discharge and flue gas heat-exchange unit simulation test section are discharged outside discharge chamber, the parameter of measurement mechanism measurement test section, and be transferred to data acquisition unit.
2. utilize the heat exchange of system, the proving installation of drag characteristic emulation for smoke discharging residual heat as claimed in claim 1, it is characterized in that: described measurement mechanism comprises pitot tube, electronic micro-manometer and spinner-type flowmeter, wherein, flue gas heat-exchange unit simulation test section and preheating of air test section rear end respectively arrange a pitot tube, pitot tube connects electronic micro-manometer, is provided with spinner-type flowmeter between water circulating pump and preheating of air test section.
3. utilize the heat exchange of system, the proving installation of drag characteristic emulation for smoke discharging residual heat as claimed in claim 1, it is characterized in that: the inlet tube and outlet tube of described water bath with thermostatic control is connected with total inlet tube and outlet tube of the heat-exchanging tube bundle to be determined of flue gas heat-exchange unit simulation test section and preheating of air test section respectively, forms recirculated water closed-loop; The air channel regulation gate valve of heat-exchanging tube bundle to be measured is opened, and another air channel regulation gate valve closes.
4. utilize the heat exchange of system, the proving installation of drag characteristic emulation for smoke discharging residual heat as claimed in claim 2, it is characterized in that: the mean wind speed of the current stabilization xsect of test section measured by described pitot tube and microbarograph, and before and after flue gas heat-exchange unit simulation test section and preheating of air test section both sides set temperature sensor, with data acquisition unit by time determination test section import and export wind-warm syndrome.
5. utilize the heat exchange of system, the proving installation of drag characteristic emulation for smoke discharging residual heat as claimed in claim 1, it is characterized in that: described water bath with thermostatic control is connected with heat-exchanging tube bundle and supplies water to heat-exchanging tube bundle through centrifugal water pump, spinner-type flowmeter, the connection inlet tube and outlet tube of water bath with thermostatic control between heat-exchanging tube bundle installs water inlet, leaving water temperature sensors, with data acquisition unit by time determination test section import and export water temperature.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520232192.9U CN204536022U (en) | 2015-04-16 | 2015-04-16 | The heat exchange of system, the proving installation of drag characteristic emulation is utilized for smoke discharging residual heat |
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| CN201520232192.9U CN204536022U (en) | 2015-04-16 | 2015-04-16 | The heat exchange of system, the proving installation of drag characteristic emulation is utilized for smoke discharging residual heat |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104729871A (en) * | 2015-04-16 | 2015-06-24 | 山东大学 | Heat-exchange and resistance characteristic simulation testing device used for exhaust smoke waste heat utilizing system |
| CN104777008A (en) * | 2015-04-16 | 2015-07-15 | 山东大学 | Performance simulation testing experimental device for power plant smoke waste heat utilizing system |
-
2015
- 2015-04-16 CN CN201520232192.9U patent/CN204536022U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104729871A (en) * | 2015-04-16 | 2015-06-24 | 山东大学 | Heat-exchange and resistance characteristic simulation testing device used for exhaust smoke waste heat utilizing system |
| CN104777008A (en) * | 2015-04-16 | 2015-07-15 | 山东大学 | Performance simulation testing experimental device for power plant smoke waste heat utilizing system |
| CN104777008B (en) * | 2015-04-16 | 2018-04-06 | 山东大学 | A kind of power-plant flue gas afterheat utilizing system performance simulation experimental apparatus for testing |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150805 Termination date: 20160416 |
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| CF01 | Termination of patent right due to non-payment of annual fee |