CN105222116B - The cloud observing and controlling steam generator system of intelligent monitoring water loss - Google Patents
The cloud observing and controlling steam generator system of intelligent monitoring water loss Download PDFInfo
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- CN105222116B CN105222116B CN201510602555.8A CN201510602555A CN105222116B CN 105222116 B CN105222116 B CN 105222116B CN 201510602555 A CN201510602555 A CN 201510602555A CN 105222116 B CN105222116 B CN 105222116B
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Abstract
The invention provides a kind of steam generator system, monitoring and diagnosis controller can calculate the water loss of boiler with the quality sum of sewer by calculating quality of steam with the ratio of the quality of the water of input boiler, if the water loss for calculating exceedes the upper limit, monitoring and diagnosis controller then sends alarm；The monitoring and diagnosis controller and cloud server data cube computation, so that the data transfer that will be monitored is to cloud server, cloud server is connected with client, the data that client can be monitored by cloud server.Client of the present invention can in time grasp the ruuning situation of boiler water loss, it is possible in time by client, prevent due to the substantial amounts of thermal waste that boiler water loss is caused.
Description
Technical field
The invention belongs to field of boilers, belong to F22 fields.
Background technology
Traditional boiler blow-out system includes home server.Home server receives the information that controller sends, and passes through
The operating scheme that pre-set control programs and parameter are obtained in home server, the operation side that controller is obtained according to home server
Case control steam generator system operation, the i.e. operation of steam generator system can only be obtained according to default control program and parameter in home server
The operating scheme operation arrived.However, system for field complex is changeable, when the operating scheme that home server is obtained cannot meet
, it is necessary to attendant arrives at control program and parameter that scene updates home server during the demand of field conditions, so as to local
Server is met the operating scheme of field conditions, it is impossible to neatly adjust the control program and parameter in home server.
The content of the invention
The water loss rate that the present invention passes through every boiler of monitor in real time, and above-mentioned dynamic relationship is taken by high in the clouds in real time
Business device sends client to, and client can in time grasp boiler blow-out system ruuning situation, it is possible in time by client
The adjustment of parameters sewage is carried out, is prevented due to the substantial amounts of thermal waste that boiler blow-out system failure is caused.
To achieve these goals, technical scheme is as follows：
A kind of steam generator system, including monitoring and diagnosis controller and boiler,
The boiler includes the flowmeter, pressure gauge and the thermometer that are arranged on steam (vapor) outlet pipeline, is exported for measuring
The flow velocity of steam, pressure and temperature；The flowmeter, pressure gauge and thermometer carry out data company with monitoring and diagnosis controller respectively
Connect, so as to by measure data transfer give monitoring and diagnosis controller, in monitoring and diagnosis controller according to measurement vapor (steam) temperature,
Pressure, the quality of steam of flow relocity calculation unit interval；
The boiler includes being arranged on the blow-off pipe of boiler-steam dome lower end, and blowoff valve, blowoff valve one end are set on blow-off pipe
Connecting valve adjusting means, adjustment mechanism for valve and monitoring and diagnosis controller carry out data cube computation, so as to by valve opening data
Monitoring and diagnosis controller is passed to, while receiving instruction from monitoring and diagnosis controller, the aperture of blowoff valve is adjusted；
Flowmeter is further included on the blow-off pipe, the flow of blowdown is measured；The flowmeter is controlled with monitoring and diagnosis
Device carries out data cube computation, and to pass data to monitoring and diagnosis controller, monitoring and diagnosis controller calculates list according to flowmeter
The blowdown quality of position time；
Flowmeter is set on the water inlet manifold of the boiler, for detect enter boiler in flow, the flowmeter with
Monitoring and diagnosis controller carries out data cube computation, to give monitoring and diagnosis controller, monitoring and diagnosis control by the data transfer for measuring
Device enters the quality of the water of boiler according to the flow rate calculation unit interval of measurement；
Monitoring and diagnosis controller can be by calculating the quality sum and the water of input boiler of quality of steam and sewer
The ratio of quality calculates the water loss of boiler, if the water loss for calculating exceedes the upper limit, monitoring and diagnosis controller then sends report
Alert prompting；
The monitoring and diagnosis controller and cloud server data cube computation, so that the data transfer that will be monitored is to cloud service
Device, cloud server is connected with client, the data that client can be monitored by cloud server.
Preferably, data below is sent to cloud server by monitoring and diagnosis controller：
Quality of steam, the quality of sewer, the quality of the water of input boiler；
Quality of steam and blowdown quality sum；
Quality of steam and blowdown quality sum and the ratio of the quality of the water of input boiler；
Cloud server is by above-mentioned data transfer to client；
If the water loss for calculating exceedes the upper limit, client then sends alarm.
Preferably, setting afterheat heat exchanger on the blow-off pipe, the afterheat heat exchanger is convector, described to dissipate
Hot device includes upper header and lower collector pipe, connects radiating tube between the upper header and lower collector pipe, the radiating tube include base tube with
And positioned at the fin of matrix periphery, the cross section of the base tube is isosceles triangle, the fin includes the first fin
With the second fin, first fin is stretched out from isosceles triangle drift angle, second fin include from etc.
Multiple fin for extending outwardly where two waists of lumbar triangle shape and the multiple stretched out from the first fin dissipate
Backing, the second fin extended to same direction is parallel to each other, the end shape that first fin, the second fin extend
Into the second isosceles triangle；The substrate tube sets first fluid passage, and the first fin inside sets second fluid
Passage, the first fluid passage and second fluid channel connection.
Preferably, second fin is relative to the face specular where the first fin center line, adjacent institute
The distance of the second fin stated is L1, and the base length of the isosceles triangle is W, the waist of second isosceles triangle
Length is S, meets equation below：
L1/S*100=A*Ln (L1/W*100)+B* (L1/W)+C, wherein Ln is logarithmic function, and A, B, C are coefficient, 0.68
<A<0.72,22<B<26,7.5<C<8.8；
0.09<L1/S<0.11,0.11<L1/W<0.13
4mm<L1<8mm
40mm <S<75mm
45mm <W<85mm
The drift angle of isosceles triangle is a, 110 °<a<160°.
Compared with prior art, steam generator system of the invention has the following advantages：
1）The water loss amount that the present invention passes through monitor in real time boiler, and above-mentioned dynamic relationship is passed through into cloud service in real time
Device sends client to, and client can in time grasp steam generator system ruuning situation, prevents from being caused because boiler water loss is excessive
Substantial amounts of thermal waste.
2）The present invention develops a kind of heat exchanger of new UTILIZATION OF VESIDUAL HEAT IN, and its structure is optimized, and reaches and most saves
Heat transfer effect.
Brief description of the drawings
Fig. 1 is the schematic diagram that drainage of the present invention is automatically controlled；
Fig. 2 is the main structure diagram of radiator one embodiment of the present invention；
Fig. 3 is the main structure diagram of radiator one embodiment of the present invention；
Fig. 4 is the schematic diagram of the right side observation of Fig. 2；
Fig. 5 is the sectional drawing of the fin of providing holes；
Fig. 6 is the schematic flow sheet of cloud computing control of the present invention.
Reference is as follows：
1 drum, 2 afterheat heat exchangers, 3 flowmeters, 4 pressure gauges, 5 thermometers, 6 Water Test Kits, 7 adjustment mechanism for valve, 8
Blowoff valve, 9 valves, 10 adjustment mechanism for valve, 11 flowmeters, 12 CSRC diagnosing controllers, 13 cloud servers, 14 clients
End, 15 base tubes, 16 first fluid passages, 17 first fin, 18 second fin, 19 second fin, 20 first waists, 21
Second waist, 22 bases, 23 holes, 24 second fluid passages.
Specific embodiment
Specific embodiment of the invention is described in detail below in conjunction with the accompanying drawings.
Herein, if without specified otherwise, being related to formula, "/" represents division, and "×", " * " represent multiplication.
A kind of boiler thermodynamic system, the boiler thermodynamic system includes at least one boiler, for producing steam, the pot
Stove carries out data cube computation with monitoring and diagnosis controller 12, so that the operation to boiler is monitored.The monitoring and diagnosis controller
12 with the data cube computation of cloud server 13, so as to will monitor data transfer to cloud server, cloud server 13 and client
End 14 connects, the various information that client 14 can be monitored by cloud server.
Preferably, client can control the operation of steam generator system with input data.
As shown in figure 1, the boiler includes automatically controlling drainage, the drainage that automatically controls is produced according to boiler
Raw quantity of steam and the water of input boiler are automatically controlled.If the ratio between the water of quantity of steam and input boiler is small
In lower numerical limit, then monitoring and diagnosis controller 12 automatically controls reduction blowdown flow rate.If quantity of steam with input boiler water it
Between ratio be more than limit value, then monitoring and diagnosis controller 12 automatically control increase blowdown flow rate.Specific control system is as follows：
As shown in figure 1, the boiler includes the flowmeter 3, pressure gauge 4 and the thermometer 5 that are arranged on steam (vapor) outlet pipeline,
Flow velocity, pressure and temperature for measuring output steam.The flowmeter 3, pressure gauge 4 and thermometer 5 respectively with monitoring and diagnosis
Controller 12 carries out data cube computation, so that the data transfer that will be measured is to monitoring and diagnosis controller 12, in monitoring and diagnosis controller
Middle vapor (steam) temperature, pressure, the quality of steam of flow relocity calculation unit interval according to measurement.
The boiler includes being arranged on the blow-off pipe of the lower end of boiler-steam dome 1, and blowoff valve 8, blowoff valve 8 one are set on blow-off pipe
Connecting valve adjusting means 7 is held, adjustment mechanism for valve 7 carries out data cube computation with monitoring and diagnosis controller 20, so that valve is opened
Degrees of data passes to monitoring and diagnosis controller 20, while receiving instruction from monitoring and diagnosis controller 20, adjusts opening for blowoff valve 8
Degree.
Flowmeter 11 is further included on the blow-off pipe, the flow of blowdown is measured.The flowmeter 11 and monitoring and diagnosis
Controller 20 carries out data cube computation, to pass data to monitoring and diagnosis controller 20.Monitoring and diagnosis controller 20 is according to stream
Gauge calculates the blowdown flow rate of unit interval, so as to calculate blowdown quality.Blowdown quality can be using the close of the sewer of experience
Spend to calculate, it is also possible to specifically call the data stored in controller 20 to calculate by measuring blowdown temperature water quality.
Flowmeter is set on the water inlet manifold of the boiler, for detect enter boiler in flow, the flowmeter with
Monitoring and diagnosis controller 20 carries out data cube computation, so that the data transfer that will be measured is to monitoring and diagnosis controller 20, monitoring and diagnosis
Controller 20 enters the flow of the water of boiler according to the flow rate calculation unit interval of measurement, so as to calculate the quality of water outlet.Water
Quality can be calculated using the density of water, it is also possible to the number stored in controller 20 is specifically called by measuring the temperature of water
According to calculating.
Certainly, into boiler water be both circulating water pipe and filling pipe water summation.Preferably, can be in moisturizing
Flowmeter with the data cube computation of monitoring and diagnosis controller 20 is respectively provided with pipe and circulating water pipe, by both calculate flows it
With, thus the unit of account time enter the total water of boiler.The present invention can be using various control strategy come control of sewage disposal amount.
One preferred control strategy is：Quality of steam and the quality of the water of input boiler that monitoring and diagnosis controller 20 is calculated
Ratio be less than lower limit, then show that blowdown rate is too high, thus monitoring and diagnosis controller 20 by adjustment mechanism for valve 7 automatically adjust
The aperture of small blowoff valve 8.By aforesaid operations, blowdown can be avoided excessive, cause the waste of the energy.If quality of steam with it is defeated
Enter the ratio of quality of the water of boiler more than higher limit, then show that blowdown rate is too low, the life-span of boiler may be influenceed, then monitor
Diagnosing controller 20 improves the aperture of blowoff valve 8 by adjustment mechanism for valve 7 automatically.
Monitoring and diagnosis controller 20 passes quality of steam, the quality of input boiler water and its ratio, the aperture of blowoff valve 39
Cloud server 13 is sent to, cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of blowoff valve 8 according to the data for obtaining, and be passed by cloud server 13
Monitoring and diagnosis controller 20 is passed, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller.
If preferably, in the case of the aperture maximum of blowoff valve 8, the quality of quality of steam and the water of input boiler
Ratio is still more than higher limit, then client can give a warning, and points out whether drainage breaks down.
If preferably, in the case of the closing of blowoff valve 8, the ratio of quality of steam and the quality of the water of input boiler
Lower limit is still less than, then client can give a warning, points out whether drainage breaks down.
One preferred control strategy be the water of the blowdown that monitoring and diagnosis controller 20 is detected by flowmeter 11 quality with
When the ratio for being input into the quality of the water of boiler exceedes the upper limit, then show that blowdown flow rate is excessive, therefore monitoring and diagnosis controller 20 passes through
Adjustment mechanism for valve 7 turns the aperture of blowoff valve 8 down automatically.If the matter of the water of the quality of the water of the blowdown of detection and input boiler
When the ratio of amount exceedes lower limit, then show that blowdown flow rate is too small, therefore monitoring and diagnosis controller 20 is automatic by adjustment mechanism for valve 7
Tune up the aperture of blowoff valve 8.By so setting, it is to avoid the water quality in drum is too poor, in order to avoid cause the corrosion of boiler-steam dome.
Monitoring and diagnosis controller 20 is by the quality of the water of blowdown, the quality of the water of input boiler and its ratio, blowoff valve 8
Aperture is sent to cloud server 13, and cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of blowoff valve 8 according to the data for obtaining, and be passed by cloud server 13
Monitoring and diagnosis controller 20 is passed, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller 20.
If in the case of the aperture maximum of blowoff valve, the ratio of the quality of the quality of the water of blowdown and the water of input boiler
Lower limit is still less than, then client can give a warning；
If in the case of the closing of blowoff valve, the quality of the water of blowdown is with the ratio of the quality of the water of input boiler still
More than higher limit, then client can give a warning.
One preference policy, the drum 1 also includes Water Test Kits 6, to measure the water quality in drum.The water quality point
Analyzer 6 carries out data cube computation with monitoring and diagnosis controller 20, and to receive the data of measurement, the data according to measurement are to blowoff valve
8 carry out aperture control.If the as shown by data water quality of measurement is excessively poor, such as a certain index exceeds the data upper limit, then need to carry out
Timely blowdown, therefore monitoring and diagnosis controller 20 is by the automatic aperture for tuning up blowoff valve 8 of adjustment mechanism for valve 7.If measurement
As shown by data water quality it is good, then monitoring and diagnosis controller 20 is by the automatic aperture for turning blowoff valve 8 down of adjustment mechanism for valve 7.Must
Even blowoff valve can be closed in the case of wanting.
Monitoring and diagnosis controller 20 will measure drum in water quality data, blowoff valve 8 aperture be sent to cloud server
13, cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of blowoff valve 8 according to the data for obtaining, and be passed by cloud server 13
Monitoring and diagnosis controller 20 is passed, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller 20.
One preference policy, sets Water Test Kits on blow-off line（It is not shown）, to measure the water in blow-off pipe
Matter.The Water Test Kits carries out data cube computation with monitoring and diagnosis controller 20, to receive the data of measurement, according to measurement
Data carry out aperture control to blowoff valve.If the as shown by data water quality of measurement is excessively poor, such as a certain index exceeds the data upper limit,
Then need to carry out timely blowdown, therefore monitoring and diagnosis controller 20 tunes up opening for blowoff valve 8 automatically by adjustment mechanism for valve 7
Degree.If the as shown by data water quality of measurement is good, monitoring and diagnosis controller 20 turns blowoff valve down automatically by adjustment mechanism for valve 7
8 aperture.Even blowoff valve can be closed in the case of necessity.
Monitoring and diagnosis controller 20 will measure blow-off pipe in water quality data, blowoff valve 8 aperture be sent to cloud service
Device 13, cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of blowoff valve 8 according to the data for obtaining, and be passed by cloud server 13
Monitoring and diagnosis controller 20 is passed, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller 20.
Preferably, waste heat utilization heat exchanger 2 is connected on the blow-off line, to make full use of the heat of sewage.Change
The low-temperature receiver inlet tube of hot device 2 sets valve 9, and the valve 9 is connected with adjustment mechanism for valve 10, adjustment mechanism for valve 10 with monitor
Diagnosing controller 20 carries out data cube computation, so that the aperture data transfer of valve 9 is connect to monitoring and diagnosis controller 20 and simultaneously
The instruction of monitored diagnosing controller 20.If the blowdown flow rate of the measurement of monitoring and diagnosis controller 20 increases, monitoring and diagnosis control
Device 20 increases the aperture of valve 9 by adjustment mechanism for valve 10, to increase the low-temperature receiver amount into heat exchanger 2, keeps heat exchanger 2 defeated
The temperature of the low-temperature receiver for going out is constant, while avoiding low-temperature receiver from overheating.If the blowdown flow rate of the measurement of monitoring and diagnosis controller 20 is reduced, supervise
Control diagnosing controller 20 reduces the aperture of valve 9 by adjustment mechanism for valve 10, to reduce the low-temperature receiver amount into heat exchanger 2, protects
The temperature for holding the low-temperature receiver of the output of heat exchanger 2 is constant, while avoiding low-temperature receiver heating effect too poor.Preferably, the heat exchanger 2 can
To set multiple.
The aperture of the valve 9 of measurement, the aperture data of blowoff valve 8 are sent to cloud server by monitoring and diagnosis controller 20
13, cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of valve 9 according to the data for obtaining, and be transmitted by cloud server 13
To monitoring and diagnosis controller 20, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller 20.
Used as preference policy, monitoring and diagnosis controller 20 can be by calculating quality of steam with blowdown quality sum and input
The ratio of the quality of the water of boiler calculates the water loss of boiler.If the water loss for calculating exceedes the upper limit, monitoring and diagnosis control
Device 20 then sends alarm.
Monitoring and diagnosis controller 20 by quality of steam, blowdown quality, input boiler water quality and its quality of steam with
Blowdown quality sum is sent to cloud server 13 with the ratio data of the quality of the water of input boiler, and cloud server 13 will be upper
Data transfer is stated to client 14.
If the water loss for calculating exceedes the upper limit, client 13 then sends alarm.
As preference policy, water-level gauge is set in drum 1（It is not shown）, the water-level gauge and monitoring and diagnosis controller 20
Data cube computation is carried out, so that measurement data is passed into monitoring and diagnosis controller 20.Monitoring and diagnosis controller 20 is according to measurement
The height of water level change of data unit of account time, so as to calculate the mass change of the water unit interval in drum 1.Monitoring is examined
Disconnected controller 20 adjusts the aperture of blowoff valve 8 according to the change of steam production, the water of boiler input and drum water.
If the quality of steam that monitoring and diagnosis controller 20 is calculated is plus the mass change sum of the water of boiler-steam dome 1 and the water of input boiler
The ratio of quality be less than lower limit less than certain numerical value, then show that blowdown rate is too high, therefore monitoring and diagnosis controller 20 passes through
Adjustment mechanism for valve 7 turns the aperture of blowoff valve 8 down automatically.By aforesaid operations, blowdown can be avoided excessive, cause the wave of the energy
Take.By increase steam water-level detect, further increase measurement data it is accurate.
The mass change of the water unit interval in water level, drum 1 that monitoring and diagnosis controller 20 will be measured, steam are produced
Amount, the water of boiler input and quality of steam are plus the mass change sum of the water of boiler-steam dome 1 and the matter of the water of input boiler
The ratio data of amount is sent to cloud server 13, and cloud server 13 is by above-mentioned data transfer to client 14.
Client 14 can be input into the numerical value of the aperture of valve 9 according to the data for obtaining, and be transmitted by cloud server 13
To monitoring and diagnosis controller 20, the aperture of blowoff valve is adjusted manually by monitoring and diagnosis controller 20.
As preference policy, monitoring and diagnosis controller 20 can by calculate quality of steam, the variable quality of drum water with
Blowdown quality three sum calculates the water loss of boiler with the ratio of the quality of the water of input boiler.If the water loss for calculating
More than the upper limit, monitoring and diagnosis controller 20 then sends alarm.
Monitoring and diagnosis controller 20 is by quality of steam, the variable quality of drum water and blowdown quality and its quality of steam, vapour
The variable quality of Bao Shui is sent to cloud service with blowdown quality three sum with the ratio data of the quality of the water of input boiler
Device 13, cloud server 13 is by above-mentioned data transfer to client 14.
If the water loss for calculating exceedes the upper limit, client 13 then sends alarm.
Preferably, setting the temperature of measurement drum reclaimed water and the device of drum pressure, described device and monitoring and diagnosis control
The data cube computation of device processed 20, monitoring and diagnosis controller 20 calculates the mass change of drum reclaimed water according to the temperature and pressure of measurement.It is logical
The quality of excess temperature and calculation of pressure water so that result is more accurate.
The temperature of drum reclaimed water and drum pressure data are sent to cloud server 13, high in the clouds by monitoring and diagnosis controller 20
Server 13 is by above-mentioned data transfer to client 14.
Preferably, setting the device of measurement vapor (steam) temperature and pressure, described device and monitoring and diagnosis controller in drum
20 data cube computations, monitoring and diagnosis controller 20 according to measurement temperature and pressure and drum in height of water level, calculate drum in
The quality of steam.So, in calculating above, according to the mass change of steam, the quality of output steam and drum in drum
The conjunction of the mass change three of reclaimed water carrys out the aperture of control of sewage disposal valve with the size of the ratio of the quality of the water of input boiler.So
So that result of calculation is more accurate.
Equally, be also required to when the loss for calculating water by the mass change of steam in drum, the quality of output steam and
The mass change and blowdown flow rate sum of drum reclaimed water are contrasted with boiler input water.
Preferably, thermometer can be set on blow-off pipe, monitoring and diagnosis controller 20 is according to the water temperature of blowdown, water
The quality of the water of the blowdown of composition and flow relocity calculation unit interval.
Preferably, the temperature, pressure of steam and the relation data of density are prestored in monitoring and diagnosis controller 20,
To calculate quality of steam.The temperature and density relationship data of water can also be prestored, while calculating the quality of drum reclaimed water.
The relation of temperature, composition and density for sewage is also prestored in lower monitoring and diagnosis controller 20.
Above-mentioned all of measurement data and calculating data can be sent to high in the clouds by monitoring and diagnosis controller 20
Server 13, cloud server 13 is by above-mentioned data transfer to client 14.Client can obtain the letter of system operation in time
Breath.
Preferably, heat exchanger is convector.Certain sewage is heated in being directly entered convector,
As shown in Figure 1.Certainly, after the recirculated water in radiator can also be exchanged heat by heat exchanger and sewer, it is recycled to heating
Radiator is heated.
The radiator includes upper header and lower collector pipe, and radiating tube, such as Fig. 2,3 are connected between the upper header and lower collector pipe
Shown, the radiating tube includes base tube 15 and the fin 17-19 positioned at base tube periphery, as shown in Figure 2,3, the base tube
Cross section is isosceles triangle, and the fin includes the first fin 17 and the second fin 18,19, first fin
17 stretch out from isosceles triangle drift angle, and second fin 18,19 includes two waist institutes from isosceles triangle
The multiple fin 18 for extending outwardly and the multiple fin 19 stretched out from the first fin, to same direction
The second fin 18,19 for extending is parallel to each other, for example, as illustrated, from the second waist of isosceles triangle 21（The waist on the left side）To
Second fin 18,19 of outer extension is parallel to each other, from the first waist of isosceles triangle 20（Waist on the right of i.e.）For stretching out
Two fin 18,19 are parallel to each other, and the end that first fin 17, the second fin 18,19 extend forms the second isosceles
Triangle, as shown in Fig. 2 the length of the waist of the second isosceles triangle is S；The inside of the base tube 15 sets first fluid passage
16, the inside of first fin 17 sets second fluid passage 24, and the first fluid passage 17 and second fluid passage connect
Logical 24.For example, as described in Figure 2, in the connection of isosceles triangle corner position.
General radiating tube is all surrounding or both sides set fin, but is found in engineering, contacted with wall
Generally heat convection effect is bad for the fin of side, because relatively poor, therefore this hair that air flows in wall side
It is bright that isosceles triangle base 22 is set to plane, therefore when fin is installed, can be directly tight with wall by plane
Contact, compared with other radiators, can greatly save installing space, it is to avoid the waste in space, while taking special dissipating
Backing form, it is ensured that meet optimal radiating effect.
Preferably, second fin 18,19 is relative to the face specular where the center line of the first fin 17, i.e.,
Relative to the face specular where the line at the midpoint where the summit and base of isosceles triangle.
Preferably, the second fin extends perpendicular to two waists of the second isosceles triangle.
In the case that the length on the side of isosceles triangle is certain, the first fin 17 and the second fin 18,19 are more long, then
Heat transfer effect is better in theory, is found in process of the test, when the first fin and the second fin reach certain length
Wait, then heat transfer effect just increases very unobvious, be primarily due to increase with the first fin and the second fin length, dissipating
The temperature of backing end is also more and more lower, with temperature reduction to a certain extent, then heat transfer effect can be caused unobvious, opposite to go back
The cost that increased material and the space for occupying for considerably increasing radiator, meanwhile, in heat transfer process, if the second radiating
Spacing between piece is too small, also easily causes the deterioration of heat transfer effect, because with the increase of radiating length of tube, air rose
Boundary layer is thickening in journey, and boundary layer mutually coincides between causing abutting fins, deteriorates heat transfer, and radiating length of tube is too low or the
Spacing between two fin causes greatly very much heat exchange area to reduce, and have impact on the transmission of heat, therefore in the second adjacent radiating
Between the length and heat sink length of the distance of piece, the length of side of isosceles triangle, the first fin and the second fin
Meet a size relationship for optimization.
Therefore, the present invention optimal is dissipated by what thousands of test datas of multiple various sizes of radiators were summed up
The dimensionally-optimised relation of hot device.
The distance of described the second adjacent fin is L1, and the base length of the isosceles triangle is W, described second
The length of the waist of isosceles triangle is S, and the relation of above-mentioned three meets equation below：
L1/S*100=A*Ln (L1/W*100)+B* (L1/W)+C, wherein Ln is logarithmic function, and A, B, C are coefficient, 0.68
<A<0.72,22<B<26,7.5<C<8.8；
0.09<L1/S<0.11,0.11<L1/W<0.13
4mm<L1<8mm
40mm <S<75mm
45mm <W<85mm
The drift angle of isosceles triangle is a, 110 °<a<160°.
Preferably, base tube length is L, 0.02<W/L<0.08,800mm<L<2500mm.
Preferably, A=0.69, B=24.6, C=8.3.
It should be noted that adjacent second fin apart from L1 be counted since the center of the second fin away from
From as shown in Figure 1.
By being tested again after result of calculation, by calculating the numerical value on border and median, the result of gained is basic
Upper to be matched with formula, substantially within 3.54%, maximum relative error is no more than 3.97% to error, and mean error is
2.55%。
Preferably, the distance of described the second adjacent fin is identical.
Preferably, the width of the first fin is greater than the width of the second fin.
Preferably, the width of the first fin is b1, and the width of the second fin is b2, wherein 2.2*b2<b1<3.1*
b2;
Preferably, 0.9mm<b2<1mm,2.0mm<b1<3.2mm.
Preferably, the width of second fluid passage is 0.85-0.95 times of the width of the second fin, preferably
0.90-0.92 times.
Width b1, b2 herein refers to the mean breadth of fin.
Preferably, the providing holes 23 on the first and/or second fin, for destroying laminar sublayer.Main cause is
Two fin are mainly exchanged heat by the convection current of air, and air carries out the stream of free convection from the bottom up of the second fin
Dynamic, during air flows upwards, the thickness in boundary layer constantly becomes big, in addition finally result in adjacent second fin it
Between boundary layer overlapped, this kind of situation can cause heat exchange deterioration.Therefore boundary layer can be destroyed by providing holes 9,
So as to augmentation of heat transfer.
Preferably, the shape in hole 23 is semicircle or circular.
Preferably, the whole fin of the insertion of hole 23.
As one preferably, along the direction of the flowing of air, i.e., from the bottom of radiator to the top of radiator, hole 23
Area constantly increase.Main cause is the direction along the flowing of air, and the thickness in boundary layer constantly increases, therefore logical
The area for setting and being continuously increased hole 23 is crossed, can cause constantly to increase the destructiveness in boundary layer, so that augmentation of heat transfer.
Preferably, the hole 23 of maximum area is 1.25-1.37 times of minimum area, preferably 1.32 times.
As one preferably, along the direction of the flowing of air, i.e., from the bottom of radiator to the top of radiator, hole 23
Density（That is quantity）Constantly increase.Main cause is the direction along the flowing of air, and the thickness in boundary layer constantly increases
Greatly, therefore by setting the density in ever-increasing hole 23, can cause constantly to increase the destructiveness in boundary layer, so that
Augmentation of heat transfer.
Preferably, the most close local density in hole 23 is 1.26-1.34 times of most thin local density, preferably 1.28
Times.
As one preferably, on same second fin, from fin root（I.e. with the connecting portion of base tube 15）To radiating
Between piece top, the area in each hole 239 constantly diminishes.Main cause is the temperature of fin from fin root to fin top
Degree constantly declines, therefore the thickness in boundary layer is constantly reduced, the area in the hole 23 by setting change, it is possible to achieve destruction
The thickness of the diverse location in boundary layer, so as to save material.
Preferably, the PTAT example relation in the change of the area in hole 23 and fin.
As one preferably, on same second fin, from fin root（I.e. with the connecting portion of base tube 1）To fin
Between top, the density in hole 23 is constantly reduced.Main cause is that, from fin root to fin top, the temperature of fin is continuous
Decline, therefore the thickness in boundary layer is constantly reduced, the density in the hole 23 by setting change, it is possible to achieve destruction boundary layer
The thickness of diverse location, so as to save material.
Preferably, the PTAT example relation in the change of the density in hole 23 and fin.
Preferably, for the width b2 between the second fin it is changed according to certain rule, specific rule is
From the base angle of isosceles triangle to drift angle, the width of the second fin 18 extended from two waists of isosceles triangle is increasingly
Greatly, from the drift angle of isosceles triangle to the end of the first fin 17, the second fin 19 extended from the first fin 18 is wide
Degree is less and less.Main cause is the second fin set in waist, and heat dissipation capacity gradually increases from base angle to drift angle, therefore is needed
Increase the area of radiating, therefore the area of dissipation by increasing the width of fin to increase fin.Similarly, along first
Fin 18, from bottom to end, the quantity of radiating is fewer and feweri, therefore the corresponding area for reducing fin.By such
Set, can greatly improve radiating efficiency, while greatly material-saving.
Preferably, from the base angle of isosceles triangle to drift angle, from the second radiating that two waists of isosceles triangle extend
The increased amplitude of the width of piece 18 is increasing, from the drift angle of isosceles triangle to the end of the first fin 17, from the first radiating
The amplitude that the width of the second fin 19 that piece 17 extends is reduced is less and less.It is found through experiments that, by above-mentioned setting, with increase
Or reduction amplitude is identical compares, it is possible to increase about 16% radiating effect.Therefore there is good radiating effect.
Although the present invention is disclosed as above with preferred embodiment, the present invention is not limited to this.Any art technology
Personnel, without departing from the spirit and scope of the present invention, can make various changes or modifications, therefore protection scope of the present invention should
It is defined when by claim limited range.
Claims (2)
1. a kind of steam generator system, including monitoring and diagnosis controller and boiler,
The boiler includes the flowmeter, pressure gauge and the thermometer that are arranged on steam (vapor) outlet pipeline, for measuring output steam
Flow velocity, pressure and temperature；The flowmeter, pressure gauge and thermometer carry out data cube computation with monitoring and diagnosis controller respectively,
To give monitoring and diagnosis controller by the data transfer for measuring, vapor (steam) temperature, pressure in monitoring and diagnosis controller according to measurement
Power, the quality of steam of flow relocity calculation unit interval；
The boiler includes being arranged on the blow-off pipe of boiler-steam dome lower end, and blowoff valve, the connection of blowoff valve one end are set on blow-off pipe
Adjustment mechanism for valve, adjustment mechanism for valve and monitoring and diagnosis controller carry out data cube computation, so as to by valve opening data transfer
Monitoring and diagnosis controller is given, while receiving instruction from monitoring and diagnosis controller, the aperture of blowoff valve is adjusted；
Flowmeter is further included on the blow-off pipe, the flow of blowdown is measured；The flowmeter enters with monitoring and diagnosis controller
Row data cube computation, to pass data to monitoring and diagnosis controller, when monitoring and diagnosis controller calculates unit according to flowmeter
Between blowdown quality；
Flowmeter is set on the water inlet manifold of the boiler, for detecting the flow entered in boiler, the flowmeter and monitoring
Diagnosing controller carries out data cube computation, to give monitoring and diagnosis controller, monitoring and diagnosis controller root by the data transfer for measuring
Enter the quality of the water of boiler according to the flow rate calculation unit interval of measurement；
Monitoring and diagnosis controller can be by calculating quality of steam with blowdown quality sum and the ratio of the quality of the water of input boiler
Value calculates the water loss of boiler, if the water loss for calculating exceedes the upper limit, monitoring and diagnosis controller then sends alarm；
The monitoring and diagnosis controller and cloud server data cube computation, so that the data transfer that will be monitored is to cloud server,
Cloud server is connected with client, the data that client can be monitored by cloud server.
2. data below is sent to cloud server by steam generator system as claimed in claim 1, monitoring and diagnosis controller：
Quality of steam, blowdown quality, the quality of the water of input boiler；
Quality of steam and blowdown quality sum；
Quality of steam and blowdown quality sum and the ratio of the quality of the water of input boiler；
Cloud server is by above-mentioned data transfer to client；
If the water loss for calculating exceedes the upper limit, client then sends alarm.
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| CN107143840B (en) * | 2017-05-22 | 2018-08-17 | 中北大学 | A kind of steam boiler system of intelligent control blowdown reference data |
| CN108954287B (en) * | 2017-06-05 | 2019-07-23 | 中北大学 | A kind of cloud computing steam boiler system controlling vapour-liquid current stabilization |
| CN108980810B (en) * | 2017-06-05 | 2020-04-17 | 中北大学 | Cloud computing intelligent control vibration and noise reduction boiler system |
| CN107218589B (en) * | 2017-07-18 | 2019-02-22 | 中北大学 | A kind of boiler system automatically controlling the blowdown of cloud computing pH value |
| CN107289440B (en) * | 2017-07-18 | 2019-02-22 | 中北大学 | A kind of boiler system of cloud computing intelligent control of sewage disposal speed |
| CN107289439B (en) * | 2017-07-18 | 2018-08-14 | 中北大学 | The boiler system of cloud computing intelligent control of sewage disposal time |
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| RU2214559C1 (en) * | 2002-06-25 | 2003-10-20 | Ульяновский государственный технический университет | Drum boiler-operation method |
| CN201475975U (en) * | 2009-07-03 | 2010-05-19 | 大连汇能技术服务有限公司 | Boiler automatic sewage drainage device |
| CN203421666U (en) * | 2013-07-12 | 2014-02-05 | 重庆中节能三峰能源有限公司 | Water quality monitoring sewage discharge system for steam boiler |
| CN104791881A (en) * | 2015-05-11 | 2015-07-22 | 山东理工大学 | Heat and power cogeneration system intelligently monitoring heat consumption through cloud server |
| CN104896572A (en) * | 2015-05-11 | 2015-09-09 | 山东理工大学 | Boiler system for monitoring by using cloud server |
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| US8646415B2 (en) * | 2009-03-18 | 2014-02-11 | Ex-Tar Technologies | System and method for zero liquid discharge |
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Patent Citations (5)
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|---|---|---|---|---|
| RU2214559C1 (en) * | 2002-06-25 | 2003-10-20 | Ульяновский государственный технический университет | Drum boiler-operation method |
| CN201475975U (en) * | 2009-07-03 | 2010-05-19 | 大连汇能技术服务有限公司 | Boiler automatic sewage drainage device |
| CN203421666U (en) * | 2013-07-12 | 2014-02-05 | 重庆中节能三峰能源有限公司 | Water quality monitoring sewage discharge system for steam boiler |
| CN104791881A (en) * | 2015-05-11 | 2015-07-22 | 山东理工大学 | Heat and power cogeneration system intelligently monitoring heat consumption through cloud server |
| CN104896572A (en) * | 2015-05-11 | 2015-09-09 | 山东理工大学 | Boiler system for monitoring by using cloud server |
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