CN204788892U - Cold die test bench based on CFB boiler - Google Patents
Cold die test bench based on CFB boiler Download PDFInfo
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- CN204788892U CN204788892U CN201520494575.3U CN201520494575U CN204788892U CN 204788892 U CN204788892 U CN 204788892U CN 201520494575 U CN201520494575 U CN 201520494575U CN 204788892 U CN204788892 U CN 204788892U
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Abstract
The utility model discloses a cold die test bench based on CFB boiler, this cold die test bench is including the test box, send out the material device, separator, the returning charge device, the air -blower, the draught fan, the test box is including the air inlet room that feeds through in proper order, close looks compartment, the dilute phase compartment, the downstream chamber, it feeds through with close looks compartment to send out the material device, and can change through a regulation material device sends out material speed, separator's air inlet and downstream chamber's intercommunication, separator's backward flow mouth and the entry of returning charge device intercommunication, separator's discharge port and draught fan are connected, the export and the close looks compartment of returning charge device feed through, the air -blower is connected with the air inlet room, and can change the fluidization wind speed through adjusting the air -blower, can simulate out the flow field of CFB boiler well, facilitate for developing flow field research.
Description
Technical field
The utility model relates to CFB Simulation of Boiler experimental technique field, particularly a kind of cold model experiment platform based on CFB boiler.
Background technology
Recirculating fluidized bed (being called for short CFB) boiler is a kind of novel clean coal-burning facility grown up in the last thirty years, there is pollutant emission and control cost that low, fuel wide accommodation, peak modulation capacity are strong, burning efficiency advantages of higher, particularly for burning of coal inferior, there is good energy saving standard usefulness.The technology that Combustion technology of circulating fluidized is most some commercial potential in clean coal technology, pollution emission control cost is minimum, simultaneously because coal adaptability is strong, also be the most effective means of a large amount of gangues that coal production brings of dissolving, therefore obtain and use widely.In order to realize the optimization of Circulating Fluidized Bed Boiler, the flow field in Circulating Fluidized Bed Boiler must be studied, thus designing a set of test unit of Study on Flow Field that facilitates particularly necessary.
Utility model content
Based on this, the utility model is the defect overcoming prior art, provides a kind of cold model experiment platform based on CFB boiler, can simulate the flow field of CFB boiler, be convenient to the carrying out of Study on Flow Field.
Its technical scheme is as follows:
A kind of cold model experiment platform based on CFB boiler, comprise test casing, issuance of materials device, tripping device, material-returning device, fan blower, induced draft fan, described test casing comprises the inlet air plenum be communicated with successively, emulsion zone room, dilute phase compartment, downstream chamber, described issuance of materials device is communicated with emulsion zone room, and by regulating issuance of materials device can change issuance of materials speed, the air intake opening of described tripping device is communicated with downstream chamber, the refluxing opening of described tripping device is communicated with the entrance of material-returning device, the escape hole of described tripping device is connected with induced draft fan, the outlet of described material-returning device is communicated with emulsion zone room, described fan blower is connected with inlet air plenum, and by regulating air blast function to change fluidising air velocity.
Wherein in an embodiment, the sidewall of described emulsion zone room, dilute phase compartment adopts transparent or semitransparent material to make.
Wherein in an embodiment, the sidewall of described emulsion zone room, dilute phase compartment adopts organic glass to make.
Wherein in an embodiment, the described cold model experiment platform based on CFB boiler also comprises some glass microballoons, and the density of glass microballoon is 2.4-2.6g/cm
3, the diameter of glass microballoon is less than 8mm.
Wherein in an embodiment, described tripping device is whirlwind separator.
Wherein in an embodiment, described material-returning device is U-shaped material returning device.
Wherein in an embodiment, described inlet air plenum and emulsion zone room, emulsion zone room and dilute phase compartment, to be removably connected by flange between dilute phase compartment and downstream chamber.
Wherein in an embodiment, the described cold model experiment platform based on CFB boiler also comprises supporting construction frame, and described test casing is vertically arranged on supporting construction frame.
Wherein in an embodiment, the described cold model experiment platform based on CFB boiler also comprises control device, and described control device is electrically connected with issuance of materials device, material-returning device, fan blower, induced draft fan respectively.
The utility model also provides a kind of three dimensional flow simulation method based on CFB boiler, can simulate the three-dimensional flow field based on cold model experiment platform, obtains the mobilism flow process of particle.The method comprises the following steps:
Set up the computation model for simulating cold model experiment platform flow field;
Stress and strain model is carried out to described computation model, obtains corresponding grid model;
The initial boundary conditions of described grid model is set;
According to being provided with the grid model after initial boundary conditions, the algorithm simulation of CPFD numerical simulation is adopted to go out three-dimensional flow field;
Three-dimensional flow field and cold model experiment platform flow field are contrasted, if both deviations are greater than predetermined value, then repeats above-mentioned steps.
Below the advantage of preceding solution or principle are described:
The above-mentioned cold model experiment platform based on CFB boiler, material is sent in emulsion zone room through issuance of materials device, fan blower is blown in inlet air plenum, be entrained in test casing to move upward by air after goods fluid and arrive dilute-phase zone room and downstream chamber, at the differing heights of test casing, part bulky grain along the landing of test cabinet wall, will form the Inner eycle of material; Less particle enters in tripping device with air and is separated, and the bulky grain of the overwhelming majority is separated to get off, and is again got back in emulsion zone by material-returning device, forms the outer circulation of material; And the bottom that the bulky grain of non-fluidisation is deposited on test casing becomes bed material wait fluidisation, issuance of materials speed and fluidising air velocity can regulate, and can simulate the flow field of CFB boiler well, provide convenient for carrying out Study on Flow Field.
The above-mentioned three dimensional flow simulation method based on CFB boiler, the CPFD numerical simulation algorithm simulation of employing advanced person goes out the three-dimensional flow field based on cold model experiment platform, direct contrast verification is carried out with the practical flow field of cold model experiment platform after drawing three-dimensional flow field, ensure the accuracy of analog result, the optimization for CFB boiler provides technical guidance.
Accompanying drawing explanation
Fig. 1 is the structural representation of the cold model experiment platform based on CFB boiler described in the utility model embodiment.
Description of reference numerals:
1, casing is tested, 2, issuance of materials device, 3, tripping device, 4, material-returning device, 5, supporting construction frame, 10, inlet air plenum, 11, emulsion zone room, 12, dilute phase compartment, 13, downstream chamber, 30, air intake opening, 31, refluxing opening, 32, escape hole.
Embodiment
Below embodiment of the present utility model is described in detail:
As shown in Figure 1, the cold model experiment platform based on CFB boiler described in the present embodiment, comprise test casing 1, issuance of materials device 2, tripping device 3, material-returning device 4, fan blower (not shown), induced draft fan (not shown), described test casing 1 comprises the inlet air plenum 10 be communicated with successively, emulsion zone room 11, dilute phase compartment 12, downstream chamber 13, described issuance of materials device 2 is communicated with emulsion zone room 11, and by regulating issuance of materials device 2 can change issuance of materials speed, the air intake opening 30 of described tripping device 3 is communicated with downstream chamber 13, the refluxing opening 31 of described tripping device 3 is communicated with the entrance of material-returning device 4, the escape hole 32 of described tripping device 3 is connected with induced draft fan, the outlet of described material-returning device 4 is communicated with emulsion zone room 11, described fan blower is connected with inlet air plenum 10, and by regulating air blast function to change fluidising air velocity.The above-mentioned cold model experiment platform based on CFB boiler, material is sent in emulsion zone room 11 through issuance of materials device 2, fan blower is blown in inlet air plenum 10, be entrained in test casing 1 to move upward by air after goods fluid and arrive dilute-phase zone room 12 and downstream chamber 13, at the differing heights of test casing 1, part bulky grain along the landing of test casing 1 inwall, will form the Inner eycle of material; Less particle enters in tripping device 3 with air and is separated, and the bulky grain of the overwhelming majority is separated to get off, and is again got back in emulsion zone by material-returning device 4, forms the outer circulation of material; And the bottom that the bulky grain of non-fluidisation is deposited on test casing 1 becomes bed material wait fluidisation, issuance of materials speed and fluidising air velocity can regulate, and can simulate the flow field of CFB boiler well, provide convenient for carrying out Study on Flow Field.
In the present embodiment, the sidewall of described emulsion zone room 11, dilute phase compartment 12 adopts transparent or semitransparent material to make, and facilitates the flow field situation in observation test casing 1.Preferably, the sidewall of described emulsion zone room 11, dilute phase compartment 12 adopts organic glass to make, and adopts methenyl choloride to bond, be easy to assembly between sidewall, solid and reliable.
The cold model experiment platform based on CFB boiler described in the present embodiment also comprises some glass microballoons, the density of glass microballoon is 2.4-2.6g/cm3, the diameter of glass microballoon is less than 8mm, and the material used with glass microballoon simulated field, can keep the tidiness of whole device.Certainly, fine sand also can be used as material, dissimilar material all should within protection domain of the present utility model.Described inlet air plenum 10 and emulsion zone room 11, emulsion zone room 11 and dilute phase compartment 12, to be removably connected by flange between dilute phase compartment 12 and downstream chamber 13, easy accessibility.Be lined with rubber sheet gasketing between flange, ensure air tight.
As shown in Figure 1, described tripping device 3 is whirlwind separator.Tripping device 3 is one of key equipments of cycle fluidized-bed combustion boiler, the layout of its structure influence boiler and volume.The whirlwind separator structure that the present embodiment adopts is simple, and material is organic glass, has the advantage that pressure drop is low and separation efficiency is high.Described material-returning device 4 is U-shaped material returning device.Material returning device is the another critical component in Circulating Fluidized Bed Boiler, and it is loopback of material device, is again air-stopper, prevents air reverse flow in material returning device, ensures normal circulation in bed.Our material returning device of employing of this testing table is U-shaped material returning device, it is a small-sized fluidized bed, being regulated by air quantity makes it keep bubbling fluidized bed state, granule materials in bed suspends, when being suspended into overflow vent place, relying on run by gravity to emulsion zone room 11, completing feed back process, the stock column formed at lower riser end encloses gas, makes material not flow back to whirlwind separator.
In the present embodiment, the described cold model experiment platform based on CFB boiler also comprises supporting construction frame 5, described test casing 1 is vertically arranged on supporting construction frame 5, supporting construction frame 5 is formed by connecting by ∠ 50 × 50 × 3 angle steel bolt, supporting construction frame 5 designs by GB50017-2003 " Code for design of steel structures ", shockproofly presses 8 degree of designs.
The described cold model experiment platform based on CFB boiler also comprises control device, and described control device is electrically connected with issuance of materials device 2, material-returning device 4, fan blower, induced draft fan respectively.Control device described in the present embodiment adopts PLC to control, and has the function such as data acquisition, storage.
A) issuance of materials, First air and returning charge are controlled;
B) test casing 1 vacuum cavitations, maintain test casing 1 negative pressure within the specific limits; .
C) bed of material differential pressure controls;
D) security interlocking protection.
Security interlocking protection major consideration:
Boot sequence is: induced draft fan → fan blower → issuance of materials device 2.
Stopping order is: issuance of materials device 2 → fan blower → induced draft fan.
If any one in fan blower, induced draft fan, issuance of materials device 2 occurs tripping operation, all should interlock and stop corresponding motor.
Table 1 cold model experiment platform designing and calculating summary sheet
Cold model experiment platform overall height based on CFB boiler is 3220mm (more than ground), floor area 1865mm × 880mm, and arrangement is indoor layout.Test casing 1 overall height 2940mm, floor area 1200mm × 610mm, adopt sectionally smooth join combination.
The utility model also provides a kind of three dimensional flow simulation method based on CFB boiler, can simulate the three-dimensional flow field based on cold model experiment platform, obtains the mobilism flow process of particle.The method comprises the following steps:
Step 1: set up the computation model for simulating cold model experiment platform flow field; Consider the reliability of computation model, the present embodiment has selected standard k-ε turbulent flow modeling cold model experiment platform flow field;
Step 2: carry out stress and strain model to described computation model, obtains corresponding grid model; The shape of grid division and total grid number can be diversified;
Step 3: the initial boundary conditions that described grid model is set; Initial boundary conditions specifically comprises component and states of matter, issuance of materials speed, the fluidising air velocity of material;
Step 4: according to being provided with the grid model after initial boundary conditions, adopts the algorithm simulation of CPFD numerical simulation to go out three-dimensional flow field; The utility model proposes to adopt CPFD numerical simulation algorithm to carry out Circulating Fluidized Bed Boiler numerical simulation calculation in the world first, and the optimization for industrialization recirculating fluidized bed provides important technological means;
Step 5: three-dimensional flow field and cold model experiment platform flow field are contrasted, if both deviations are greater than predetermined value, then repeats above-mentioned steps, finally analyze according to three-dimensional flow field, according to analysis result, Circulating Fluidized Bed Boiler is transformed.
The above-mentioned three dimensional flow simulation method based on CFB boiler, the CPFD numerical simulation algorithm simulation of employing advanced person goes out the three-dimensional flow field based on cold model experiment platform, direct contrast verification is carried out with the practical flow field of cold model experiment platform after drawing three-dimensional flow field, ensure the accuracy of analog result, the optimization for CFB boiler provides technical guidance.
The utility model adopts CPFD algorithm to carry out Circulating Fluidized Bed Boiler fluidization process visual research, and CPFD simulates granule polyphasic flow based on EulerianLagrangian framework.Although by the spatial gradient of grain volume fraction, EulerianLagrangian model can simulate the Stress between particles near compacted grains stream, if but consider type and the size distribution of particle, continuity equation by complex because need to solve continuity equation and the equation of momentum to the solid-phase of each type and yardstick.EulerianLagrangian model a kind ofly solves the comparatively economic method of particulate heterogeneous stream, and its considers the grain type of relative broad range, yardstick and speed etc.However, for the situation that grain volume fraction is higher, intergranular collision frequency is high, and it is also unpractical for adopting the Lagrangian method of real meaning to calculate collision.
CPFD technological borrowing MP-PIC (multiphaseparticle-in-cell) method, carried out dual treatment method to Particle Phase, namely particle was both considered to be continuous medium, was also considered to be discrete bodies.Rock frame stress gradient (being difficult to calculate each particle in compacted grains stream) is processed into the gradient on fluid grid, is then interpolated on discrete particle body; Other attributes of Particle Phase then calculate in the position of discrete particle.CPFD defines a kind of interpolation operator, and this operator computing velocity is high, and can ensure the conservation of the overall situation and local.Like this, CPFD method eliminate to the implicit solution of high calculated amount dependence-grid on particle method corresponding force calculate required for; The more important thing is, being coupled together, for designer provides the numerical solution that a robustness is excellent of Particle Phase and fluid-phase implicit expression.
CPFD method is different from traditional counting fluid mechanics part, be both detailed huge difference considering particle and fluid, the kinetic characteristic of true process particle, turn avoid the particle contacts retrieval of pole time-consuming, adopts between ripe granular kinetic theory count particles and act on.Meanwhile, CPFD method creatively proposes " count particles " concept.So-called " count particles ", on Lagrangian method basic " fluid micellar " concept, is extended to Particle Phase and is formed " particle micelle ".Among one " count particles ", contain multiple true particle, these true particles have identical material property, physical motion and chemical change.
The computation schema of CPFD method, be constantly switch under Euler's system and Lagrangian system, this switching is different from the coupling of distinct element method two solvers.In CPFD method, fluid-phase and Particle Phase all calculate in same solver, utilize the alternate interpolation operator of original creation to ensure the conservativeness of stability and the switching calculated.
Therefore, CPFD method is a kind of " mixing " numerical method, integrates the advantage of Euler's two-fluid model and Lagrangian discrete model, for the research of technical grade fluidization problem provides brand-new technological means.
What CPFD method solved is three-dimensional fluid-phase and Particle Phase system of equations.In CPFD method, have employed the concept of count particles, namely represent the particle (grain size, particle density etc.) much with identical particle attribute by a count particles.The concept of count particles is that the one that grain flow calculates is similar to, and as in fluid-phase numerical evaluation, represents the information of all fluid particles in physical space with controlling mean value on volume.Have employed the method for above-mentioned count particles, numerical simulation granule number scale can reach numerical particle up to a million.
Each technical characteristic of the above embodiment can combine arbitrarily, for making description succinct, the all possible combination of each technical characteristic in above-described embodiment is not all described, but, as long as the combination of these technical characteristics does not exist contradiction, be all considered to be the scope that this instructions is recorded.
The above embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to utility model patent scope.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.
Claims (9)
1. the cold model experiment platform based on CFB boiler, it is characterized in that, comprise test casing, issuance of materials device, tripping device, material-returning device, fan blower, induced draft fan, described test casing comprises the inlet air plenum be communicated with successively, emulsion zone room, dilute phase compartment, downstream chamber, described issuance of materials device is communicated with emulsion zone room, and by regulating issuance of materials device can change issuance of materials speed, the air intake opening of described tripping device is communicated with downstream chamber, the refluxing opening of described tripping device is communicated with the entrance of material-returning device, the escape hole of described tripping device is connected with induced draft fan, the outlet of described material-returning device is communicated with emulsion zone room, described fan blower is connected with inlet air plenum, and by regulating air blast function to change fluidising air velocity.
2. the cold model experiment platform based on CFB boiler according to claim 1, is characterized in that, the sidewall of described emulsion zone room, dilute phase compartment adopts transparent or semitransparent material to make.
3. the cold model experiment platform based on CFB boiler according to claim 2, is characterized in that, the sidewall of described emulsion zone room, dilute phase compartment adopts organic glass to make.
4. the cold model experiment platform based on CFB boiler according to claim 1, is characterized in that, also comprise some glass microballoons, and the density of glass microballoon is 2.4-2.6g/cm
3, the diameter of glass microballoon is less than 8mm.
5. the cold model experiment platform based on CFB boiler according to claim 1, is characterized in that, described tripping device is whirlwind separator.
6. the cold model experiment platform based on CFB boiler according to claim 1, is characterized in that, described material-returning device is U-shaped material returning device.
7. the cold model experiment platform based on CFB boiler according to any one of claim 1-6, is characterized in that, described inlet air plenum and emulsion zone room, emulsion zone room and dilute phase compartment, is removably connected by flange between dilute phase compartment and downstream chamber.
8. the cold model experiment platform based on CFB boiler according to claim 7, is characterized in that, also comprise supporting construction frame, and described test casing is vertically arranged on supporting construction frame.
9. the cold model experiment platform based on CFB boiler according to claim 7, is characterized in that, also comprise control device, and described control device is electrically connected with issuance of materials device, material-returning device, fan blower, induced draft fan respectively.
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| Application Number | Priority Date | Filing Date | Title |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104977150A (en) * | 2015-07-09 | 2015-10-14 | 广东电网有限责任公司电力科学研究院 | Cold mold testing bench based on CFB boiler and three-dimensional flow field stimulation method |
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2015
- 2015-07-09 CN CN201520494575.3U patent/CN204788892U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104977150A (en) * | 2015-07-09 | 2015-10-14 | 广东电网有限责任公司电力科学研究院 | Cold mold testing bench based on CFB boiler and three-dimensional flow field stimulation method |
| CN104977150B (en) * | 2015-07-09 | 2018-11-09 | 广东电网有限责任公司电力科学研究院 | Three dimensional flow simulation method based on CFB boiler |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 |