CN103196128B - Power station boiler heating surface design method - Google Patents
Power station boiler heating surface design method Download PDFInfo
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- CN103196128B CN103196128B CN201310108856.6A CN201310108856A CN103196128B CN 103196128 B CN103196128 B CN 103196128B CN 201310108856 A CN201310108856 A CN 201310108856A CN 103196128 B CN103196128 B CN 103196128B
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Abstract
The invention discloses a power station boiler heating surface design method. The power station boiler heating surface design method is only suitable for smoke temperature deviation and fixing and comprises the steps: first, confirming a smoke temperature deviation factor of each screen according to smoke side temperature deviation curves on the same section; second, confirming steam deviation curves according a given header size and a leading-in and leading-out mode of a heating surface pipe from a header, and obtaining a steam deviation factor of each screen; third, performing superposition of the smoke temperature deviation factors and the steam deviation factors to obtain comprehensive deviation factor of each screen; and fourth, adjusting selected materials for heating surface according to the comprehensive deviation factor of each screen and performing different design, wherein good materials are used for screens with large deviation, and poor materials can be used for screens with small deviation.
Description
Technical field
The present invention relates to boiler plant field, especially a kind of optimization be applicable to the fixing heating surface method for designing of flue gas deviation.
Background technology
In Power Station Boiler Heating Surface, there is thermal deviation.Thermal deviation refer to and tubulation group in the working medium enthalpy of every pipe increase different phenomenons.The degree available heat deviation factor of thermal deviation represents, the ratio that in heating surface parallel transistor, indivedual pipe working medium enthalpys increasings increase with the average enthalpy of pipe in parallel.Ratio is that 1 expression does not have deviation; Ratio is greater than 1 expression overgauge, and enthalpy increases excessive; Ratio is less than 1, represents that enthalpy increases too small.The reason that the thermal deviation of heating surface produces is the flow direction inequality of working medium side and the heating power inequality of fume side.The reason that causes heating surface thermal deviation is that heat absorption is uneven, structure is uneven, mass flow discrepancy.Heated face structure is inconsistent, and caloric receptivity, flow are all had to impact, so, conventionally the main cause that produces thermal deviation is summed up as to heat absorption inequality and two aspects of mass flow discrepancy.
(1) the uneven aspect of absorbing heat.
1) inconsistent along stove cross direction flue-gas temperature, flue gas flow rate, cause the pipe heat absorption situation of diverse location different.
2) flame full level in stove is poor, or flame kernel deflection.
3) the local slagging scorification of heating surface or dust stratification, can make the heat absorption between pipe seriously uneven.
4) convection superheater or reheater, because pipe pitch difference is excessive or when maintenance slices off indivedual pipes and do not repair, forms flue gas " corridor ", and its adjacent tube caloric receptivity is increased.
5) outer race tube of pendant superheater or reheater, recepts the caloric large compared with the caloric receptivity of other pipe.
(2) mass flow discrepancy aspect:
1) pipe arranged side by side, because the actual inner diameter of pipe inconsistent (pipe flattening, outstanding overlap, the foreign material obstruction etc. in commissure) causes the flow resistance of each pipe arranged side by side in different size, makes mass flow discrepancy.
2) header is different from the connected mode of introducing fairlead, causes that pipe arranged side by side two ends pressure reduction is different, causes mass flow discrepancy.Modern boiler adopts multitube to draw header more, in the hope of also tubulation flow is basically identical.
Therefore in boiler design, the mobile flue gas deviation of bringing of flue gas, make the design of boiler heating surface very difficult, effectively control deviation is one of effective method of guaranteeing safe operation of the boiler, and we also can guarantee that boiler has larger security at heating surface by the design of optimizing heating surface.
Summary of the invention
The present invention relates to a kind of heating surface method for designing of optimization, the understanding of this method for designing based on to flue gas deviation, is applicable to the situation that fume side temperature deviation curve is comparatively fixed.The boiler of for example tangential firing, no matter boiler capacity size, its fume side temperature deviation curve by heating surface is substantially fixing.
In order to realize object of the present invention, technical scheme of the present invention is:
A kind of Power Station Boiler Heating Surface method for designing, described method is only applicable to flue-gas temperature deviation and fixes, and the step of described method for designing is:
The first step, determines the flue-gas temperature deviation factor of each screen according to the fume side temperature deviation curve on same section;
Second step, the mode that leads in/out header according to given header size and heating surface pipe, determines steam aberration curve, obtains the steam deviation factor of each screen;
The 3rd step, superposes flue-gas temperature deviation factor and steam deviation factor, obtains the comprehensive deviation coefficient of each screen;
The 4th step, according to the comprehensive deviation coefficient of each screen, adjusts the selection of heating surface, carries out difference design, and the screen that deviation is large has been selected material, and the screen selection that deviation is little can be slightly poor.
Use this method for designing, effectively control deviation, when guaranteeing safe operation of the boiler, makes boiler design more economical.
Brief description of the drawings
Fig. 1 is conventional heating surface schematic diagram;
Fig. 2 is heating surface schematic diagram of the present invention;
Fig. 3 is fume side temperature deviation curve synoptic diagram;
Fig. 4 is header and heating surface work schematic diagram.
Description of reference numerals: the pipe 4 on pipe joint 3, screen in import header 1, outlet header 2, header.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation, but the present invention is not limited to following embodiment.
If Fig. 1 is conventional heating surface schematic diagram, according to conventional method design, screen 1 is all identical design to screen 8 all screens, and width is identical, and highly identical, material is identical.
On same section, flue-gas temperature is not identical, has the crest of flue-gas temperature and the trough of flue-gas temperature, and the aberration curve of such flue-gas temperature can obtain or practical experience acquisition by numerical simulation.As shown in Figure 3.
Deviation between heating surface screen is that the difference of the extraction location in header due to flue gas deviation and different screen pipe causes.When the bore of header is determined, the mode that leads in/out determines that between rear its screen, steam aberration curve is also substantially definite.
Heating surface is because the difference of the heat absorption of Internal and external cycle pipe and circulation area, tube length between the different pipes with screen causes with the deviation of screen.
In the time carrying out heating surface design, must consider deviation and same deviation of shielding between screen simultaneously, could really guarantee the security of heating surface.
If adopt conventional method for designing, heating surface for the difference screen on same section is not carry out differentiation consideration, although only several limited screens are in the highest flue gas deviation region, but the flue gas deviation of choosing when the design of all heating surfaces must be also flue gas deviation maximum on this section, designs so uneconomical.In addition, in considering flue gas deviation, the deviation (comprising with the steam deviation between steam deviation and the screen of screen) of the steam side that consideration may exist, if two kinds of deviations are not effectively superposeed, and two kinds of deviations are considered separately to selection design, although its final result is the security of having guaranteed heating surface, loses certain economy.
Below method for designing involved in the present invention is elaborated:
Embodiment 1
Embodiment: in horizontal flue, taking 8 screens as example, suppose that each screen size is identical, material is identical, with header to lead in/out mode identical.
The first step, determines the flue-gas temperature deviation factor of each screen according to the fume side temperature deviation curve on same section;
Be illustrated in figure 3 fume side temperature deviation curve synoptic diagram, below for the ease of understanding, imagined a form in addition, data are roughly put into form.
Table 1
| Position | Screen 1 | Screen 2 | Screen 3 | Screen 4 | Screen 5 | Screen 6 | Screen 7 | Screen 8 |
| Flue-gas temperature DEG C | 1120 | 1130 | 1150 | 1125 | 1105 | 1120 | 1150 | 1100 |
| Flue-gas temperature deviation factor α | 0.9956 | 1.0044 | 1.0222 | 1 | 0.9822 | 0.9956 | 1.0222 | 0.9777 |
As table 1, obtaining the mean temperature of flue gas outside eight screens is 1125 DEG C, and deviation factor roughly can be regarded as the temperature in certain screen outside and the ratio of mean temperature.As, the temperature of screen 4 is 1125 DEG C, deviation factor is 1, there is no deviation; The temperature of screen 3 is the highest, is 1150 DEG C, is overgauge, and operating mode is the most severe; The temperature of screen 8 is minimum, is 1100 DEG C, is minus deviation, and operating mode is least severe.
Certainly the calculating in actual design process is more more complex than above-mentioned, but general principle is the same.
Second step, determines steam aberration curve (can obtain flow deviation curve in given header size with after leading in/out mode), obtains the steam deviation factor of each screen.
Header characterization of size is length, inside radius.It is multiple that working medium enters the introducing mode of header, and as introduce at two ends, two ends introduce and add mid portion and introduce, many small tubes are introduced, etc.; The lead-out mode that corresponding working medium goes out header also has multiple, and as drawn at two ends, two ends are drawn and added mid portion and draw, and many small tubes are drawn).Determine when header size, lead in/out mode definite, steam deviation factor has just been determined.
Suppose that header introducing mode is that introduce at two ends, according to the experience of our actual design, we have roughly supposed the steam deviation factor as following table:
Table 2
| Position | Screen 1 | Screen 2 | Screen 3 | Screen 4 | Screen 5 | Screen 6 | Screen 7 | Screen 8 |
| Steam deviation factor β | 0.97 | 0.98 | 1 | 1.02 | 1.03 | 1 | 0.98 | 0.97 |
As table 2, the roughly implication of steam deviation factor is: the total flow of supposing 8 screens is 800 tons/hour, and the flow of average every screen is 100 tons.Deviation factor β is 1 o'clock, there is no deviation, shield 3 and screen 6 flow be 100 tons/hour, the deviation factor of screen 1 is 0.97, belongs to minus deviation, flow is 97 tons/hour, screen 5 is overgauge, flow is 103 tons/hour.When flow is large, the heat of taking away is many, and the temperature of screen declines many.
The 3rd step, superposes flue-gas temperature deviation factor and steam deviation factor, obtains comprehensive deviation coefficient;
The length of supposing screen is 10000 millimeters, Ping Chang unit's millimeter.
Table 3
How to superpose, have the account form of multiple stack, illustrate for an example of simplifying.
For example shielding 1 flue-gas temperature deviation factor α is 0.9956, the temperature that is it is on the low side with respect to the mean temperature of 8 screens, if elongated its length, shield the resistance of working medium is increased, flow just declines, caloric receptivity declines, and the temperature of screen will rise, and increases enough length and can allow the temperature of screen reach mean temperature (note: when screen lengthens, also phase strain is large for the heat-absorbent surface of screen, caloric receptivity also can increase, and for the purpose of simplifying the description, puts aside this impact herein).Eliminate deviation factor α, the temperature of screen reaches the mean temperature of 8 screens, and rule of thumb, screen is long to be inversely proportional to α.Tentative standard screen length is 10000 millimeters, in the time of α=0.9956, and the corresponding long L=10000/ of screen α=10044 millimeter after elimination deviation factor α.
The steam deviation factor β of screen 1 is 0.97, the flow that is it is on the low side with respect to the average discharge of 8 screens, if so its length is shortened, shield the resistance of working medium is reduced, flow just increases, and caloric receptivity increases, the corresponding rising of the temperature (note: now the endotherm area of screen also diminishes of screen, caloric receptivity also can diminish, and for the purpose of simplifying the description, does not temporarily consider this impact herein).Eliminate deviation factor β, allow the flow of screen equal the average discharge of 8 screens, rule of thumb, screen is long to be directly proportional to β.Tentative standard screen length is 10000 millimeters, the corresponding long L=10000 of screen β=9700 millimeter after elimination deviation factor β.
After stack, eliminate after deviation factor α and β, shield long L=9700+10044 ?10000=9744 millimeter.
Comprehensive deviation coefficient is substantially equal to beta/alpha, and screen 1 comprehensive deviation coefficient equals 0.97/0.9956=0.9743, eliminates after deviation factor α and β, shield long L=10000 × 0.9743 millimeter=9743 millimeters, with 9744 millimeters approaching, in the error range of permission.
Calculating in certain actual additive process is more more complex than above-mentioned narration, but general principle is the same, and be the impact of considering variety of factors, deviation factor α and β are not only considered, also consider the situation that affects on endotherm area when screen increases or shortens, certainly also have other factors, the present invention just for example understands method and the factor of stack.
The 4th step, by shortening and lengthen the length of screen, offsets deviation between the screen forming due to flue gas deviation and steam deviation, obtains outlet temperature comparatively uniformly.
Table 4
According in table 4, the screen after elimination deviation factor α and β is long, and standard screen progress row is increased or shortened, and can obtain outlet temperature comparatively uniformly.For example shield 1, can be from 10000 millimeters, adjust to 9744 millimeters.
Method for designing used in the present invention is for the flue gas deviation existing on same section, and its flue gas bias property is the design that substantially fixing characteristic is carried out heating surface personalization, the heating surface in region heating surface that on same section, flue-gas temperature is high and the low region of flue-gas temperature is adopted to different design principles, guarantee to there is higher economy in retaining enough margins of safety.
Method for designing of the present invention is first to determine the flue-gas temperature deviation factor of each screen according to fume side temperature deviation curve on same section, obtain the steam deviation factor of each screen according to steam aberration curve (given header size and lead in/out mode can obtain flow deviation curve) simultaneously, flue-gas temperature deviation factor and steam deviation factor are superposeed, obtain the flow passing through of each screen, due to the existence of deviation, although the heating surface of its each screen is identical, be that resistance is identical, but the flow by each screen is not identical, cause its outlet temperature to have deviation.Obtaining after deviation factor, we can, by shortening and lengthen the length of screen, adjust the resistances of different screens, offset deviation between the screen forming due to flue gas deviation and steam deviation, obtain outlet temperature comparatively uniformly.
Adopt method used in the present invention in guaranteeing that each screen screen all has safe enough nargin, to obtain good economy, because be not that each screen screen is all to design according to worst operating mode.
The design of certain every a slice screen is the personalized difficulty that can increase design all, and we also can will similarly shield and carry out standardized design on the basis of personalized designs, to security, economy and standardization are carried out to orderly combination.Certainly do not consider that standardization also allows.
By calculating the coefficient of the steam deviation between flue gas deviation on same section and screen, adjust the length of heating surface, carry out the adjustment of deviation, obtain outlet temperature comparatively uniformly.Because the height of difference screen is not identical, need to guarantee that the heating surface area of final (in fact) is identical with theoretic design-calculated area.If different, need to re-start after heating power calculates and re-start selection calculating.
Embodiment 2
Embodiment 2 is identical with first three step of embodiment 1.Obtaining after comprehensive deviation coefficient, improving the material class of the screen that deviation is large and keep out the deviation that may exist, this kind of method do not eliminated in esse deviation, but personalized design can be guaranteed certain economy in guaranteeing security.
The 4th step, by calculating the coefficient of the steam deviation between flue gas deviation on same section and screen, adjusts the selection of heating surface, carries out the design of deviation screen, and the screen that deviation is large has been selected material, and the screen selection that deviation is little can be slightly poor.
As table 4, the comprehensive deviation of screen be less than 1 for minus deviation, be greater than 1 be overgauge, no matter be overgauge or minus deviation, comprehensive deviation is larger with the absolute value of 1 difference, the temperature of the interior working medium of screen is higher, operating mode is poorer.The deviation here refers to greatly the absolute value of the difference of comprehensive deviation and 1.For example, the comprehensive deviation coefficient of screen is 1.0486, and the comprehensive deviation of screen 5 and 1 difference are 0.0486, absolute value maximum in 8 screens, and operating mode is the poorest.Therefore, comprehensive deviation is that the screen of 1 left and right is that a basic material is chosen on basis, the maximum annex of absolute value select a good material, absolute value is at the medium material that selects of middle annex.For example, basic material can select common stainless steel, and the trade mark is as SA-213TP347H; Medium material selects meticulous stainless steel, and the trade mark is as SA-213TP347HFG; Good material selects super stainless steel, and the trade mark is as SA-213. δ 304H.
The standard of selection is here taken into account thermal conductivity taking high temperature resistant as major parameter standard, withstand voltage, wearability and life-span length; Standard according to this, common stainless steel, meticulous stainless steel, super stainless steel, material improves successively.
Embodiment 3
Embodiment 3 is identical with first three step of embodiment 1.
The 4th step, is obtaining after deviation factor, and we can be by the size of perforate in header, regulate the design resistance of every screen, thereby regulate the working medium flow of every screen, offset deviation between the screen forming due to flue gas deviation and steam deviation, obtain outlet temperature comparatively uniformly.
As shown in Figure 4, working medium enters import header 1 from two ends, have hole in header, is welded with pipe joint 3 on hole, and pipe joint 3 connects the pipe 4 of heating surface.Perforate is large, and internal diameter of pipe joint is also corresponding large.Working medium heats laggard inlet/outlet header 2 on heating surface, flows out from outlet header two ends.In the time that perforate becomes large, also phase strain is large for the internal diameter of pipe joint, fluid resistance force diminishes herein.
In the time that the comprehensive deviation coefficient of screen is minus deviation, the resistance that shows to a certain extent screen is large, need to increase the perforate (perforate in header is connected with the pipe of screen) in header, perforate becomes large resistance and reduces, flow velocity can increase, and flow increases, and caloric receptivity increases, temperature drop increases, and makes screen in safe range.When the comprehensive deviation coefficient of screen is while being overgauge, show that the resistance of screen is little, need to reduce the perforate in header, the perforate resistance that diminishes increases, and flow velocity can reduce, and flow reduces, and caloric receptivity reduces, and temperature drop reduces, and screen is still in the scope of safety.
Embodiment 4
Embodiment 4 is identical with first three step of embodiment 1.Can consider embodiment 1 and embodiment 3 to combine, the length adjustment and the header perforate adjustment that are about to screen combine.
The 4th step, according to the comprehensive deviation coefficient of each screen, in the situation that each heating surface heat absorption total amount is constant, by adjusting the size of perforate in header and adjusting the length of shielding, the design resistance of every screen of comprehensive adjustment, thereby regulate the working medium flow of every screen, offset comprehensive deviation between the screen forming due to flue gas deviation and steam deviation, make the steam exit temperature of each screen even.
The comprehensive benefit of adjusting is, can not make the perforate difference in the excessive or header of the length difference of each screen excessive.
Embodiment 5
Embodiment 5 is identical with first three step of embodiment 1.It is also conceivable that embodiment 1, embodiment 2 and embodiment 3 are combined, combine by the length adjustment of screen, adjustment and the header perforate adjustment of materials variances.
The 4th step, according to the comprehensive deviation coefficient of each screen, in the situation that each heating surface heat absorption total amount is constant, by adjusting size, the materials variances of screen and the length of adjustment screen of perforate in header, the design resistance of every screen of comprehensive adjustment, thereby regulate the working medium flow of every screen, carry out comprehensive deviation between screen that partial offset forms due to flue gas deviation and steam deviation, make the steam exit temperature of each screen even; Unmatched part comprehensive deviation is passed through to adjust the selection (adjusting the materials variances of screen) of heating surface simultaneously, carry out the design of deviation screen, the screen that deviation is large has been selected material, and the screen selection that deviation is little can be slightly poor.
Claims (1)
1. a Power Station Boiler Heating Surface method for designing, described method is only applicable to flue-gas temperature deviation and fixes, and it is characterized in that:
The first step, determines the flue-gas temperature deviation factor of each screen according to the fume side temperature deviation curve on same section;
Second step, the mode that leads in/out header according to given header size and heating surface pipe, determines steam aberration curve, obtains the steam deviation factor of each screen;
The 3rd step, superposes flue-gas temperature deviation factor and steam deviation factor, obtains the comprehensive deviation coefficient of each screen;
The 4th step, according to the comprehensive deviation coefficient of each screen, adjusts the selection of heating surface, carries out difference design, and the screen that deviation is large has been selected material, and the screen selection that deviation is little can be slightly poor.
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| JP2002221303A (en) * | 2001-01-24 | 2002-08-09 | Babcock Hitachi Kk | Method of measuring furnace interior side temperature of membrane panel |
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| CN101832541A (en) * | 2010-05-14 | 2010-09-15 | 上海发电设备成套设计研究院 | Method for self-searching optimal thermal deviation working condition of boiler superheter and reheater of power station |
| CN101832544A (en) * | 2010-05-14 | 2010-09-15 | 上海发电设备成套设计研究院 | Method for online monitoring thermal deviations of final superheater and final reheater of boiler of power station |
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