Cylindrical Cyclon Separator-6

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Cylindrical Cyclone Separator Tanaka Lab.

description

Cylindrical Cyclon Separator-6

Transcript of Cylindrical Cyclon Separator-6

  • Cylindrical Cyclone Separator Tanaka Lab.

  • Analysis Condition Cf.article

    (Akiyama) Analysis Condition

    Analysis Program FrontFlow/blue Fluent 15.0 Xflow2014

    Time Unsteady Steady/ Unsteady Unsteady

    Analysis Model LES

    SST k-, LES Standard k- Standard k-

    WMLES

    Element Number 17,000,000

    820,000/ 7,900,000 4,000,000

    Element Structure Hexa

    Tetra, Hexa Octant tree

    Inlet 9.47 [m/s] Re = 4.38104

    Outlet 0 [Pa]

    Tanaka Kazuhiro Lab 2

    Z=0

  • Tangential Velocity

    0.0

    1.0

    2.0

    -0.5 0.0 0.5

    u / U

    IN

    x/D

    z/D=-2.43 z/D=-3.57 2.0

    0.0

    1.0

    -0.5

    u / U

    IN

    0.0 0.5

    x/D

    Exp LES Akiyama SST k- k- k- XFLOW LES(FLUENT)

    Comparisons of computed and measured tangential velocity in Z/D=-2.43, -3.57

    An analysis result of XFLOW is the closest to experimental value in each model.

    SST k-, k-, k- model computed steady-state analysis.

    LES (FLUENT) approximately 50% are overestimated in comparison with experimental value.

    Tanaka Kazuhiro Lab 3

  • Axial Velocity

    -0.5 w

    / U

    IN

    0.0

    0.5

    1.0

    -0.5 0.0 0.5

    x/D

    z/D=-3.57

    w /

    UIN

    -0.5

    0.0

    0.5

    1.0

    -0.5 0.0 0.5

    x/D

    z/D=-2.43

    In five models, a tendency of XFLOW make advances in comparison with an experimental data in z/d=-2.43 , z/d=-3.57.

    Exp LES Akiyama SST k- k- k- XFLOW LES(FLUENT)

    Comparisons of computed and measured axial velocity in Z/D=-2.43, -3.57

    Tanaka Kazuhiro Lab 4

  • Comparison of Tangential Velocity (Steady) u /UIN

    0 2.5 x

    y

    x y

    z

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    Flow

    A tendency seems similar and can catch a whirlpool core clearly qualitatively.

    Cf.article x

    y

    x

    z u /UIN

    0 2.5

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Computed

    LES(FLUENT)

    Tanaka Kazuhiro Lab 5

  • Comparison of Axial Velocity (Steady)

    Flow

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5 x

    y

    x

    y

    x

    z

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5

    x y

    z

    A tendency comes closer qualitatively.

    Cf.article

    LES(FLUENT)

    Computed

    Tanaka Kazuhiro Lab 6

  • Comparison of Tangential Velocity (Steady) u /UIN

    0 2.5 x

    y

    x y

    z

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    Flow

    x

    y

    x

    z u /UIN

    0 2.5

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    The circumferential high-speed flow around the central axis of the spiral whirl core could not be confirmed.

    Cf.article Computed

    SST k-

    Tanaka Kazuhiro Lab 7

  • Comparison of Axial Velocity (Steady)

    Flow

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5 x

    y

    x y

    z

    x

    y

    x

    z

    -0.5 1.5

    w/UIN

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    The flow suddenly damps below at z/D=-2.43, and the high-speed upswing around the central axis could not be confirmed.

    Cf.article Computed

    SST k-

    Tanaka Kazuhiro Lab 8

  • Comparison of Tangential Velocity (Steady) u /UIN

    0 2.5 x

    y

    x y

    z

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    Flow

    x

    y

    x

    z u /UIN

    0 2.5

    The high-speed circumferential flow around the central axis of the spiral whirlpool could not be confirmed.

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Standard k-

    Computed Cf.article

    Tanaka Kazuhiro Lab 9

  • Comparison of Axial Velocity (Steady)

    Flow

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5 x

    y

    x y

    z

    x

    y

    x

    z

    -0.5 1.5

    w/UIN

    The flow suddenly damps below at z/D=-2.43, and the high-speed upswing around the central axis could not be confirmed.

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Standard k-

    Computed Cf.article

    Tanaka Kazuhiro Lab 10

  • Comparison of Tangential Velocity (Steady) u /UIN

    0 2.5 x

    y

    x y

    z

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    Flow

    x

    y

    x

    z u /UIN

    0 2.5

    I cannot confirm the high-speed turning speed of the central axis circumference of the spiral whirlpool.

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Standard k-

    Computed Cf.article

    Tanaka Kazuhiro Lab 11

  • Comparison of Axial Velocity (Steady)

    Flow

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5 x

    y

    x y

    z

    x

    y

    x

    z

    -0.5 1.5

    w/UIN

    The flow suddenly damps below at z/D=-2.43, and the high-speed upswing around the central axis could not be confirmed.

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Standard k-

    Computed Cf.article

    Tanaka Kazuhiro Lab 12

  • Comparison of Tangential Velocity at t=3.0[s]

    The influence through difference of the calculation lattice can be seen, but the circumferential velocity distributions comes closer qualitatively.

    LES(XFLOW)

    x

    y

    x y

    z

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    Flow

    Cf.article u /UIN 0 2.5 x

    y

    x

    z

    Computed

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    0 2.5

    u/UIN

    Tanaka Kazuhiro Lab 13

  • Comparison of Axial Velocity at t=3.0[s]

    The flow comes closer qualitatively. Because the width of contour cannot be controlled, the comparison is difficult.

    x y

    z

    LES(XFLOW)

    Flow

    z/D = -2.43

    Vortex Table

    z/D = -3.57

    z/D = -0.335

    w/UIN

    -0.5 1.5 x

    y

    x y

    z

    x

    y

    x

    z

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    Computed Cf.article -0.5 1.5

    w/UIN

    Tanaka Kazuhiro Lab 14

  • Comparison between XFLOW and FLUENT

    x

    y

    x

    z

    u /UIN

    0 2.5

    z/D = -2.43

    z/D = -3.57

    z/D = -0.335

    7,900,000element

    0 2.5

    u/UIN

    XFLOW FLUENT 3,900,000 element

    Because line-formed distributions are seen in XFLOW, so XFLOW realizes higher precision than FLUENT.

    Tanaka Kazuhiro Lab 15

  • Conclusion

    Using each model of the numerical analysis, the comparison between the experimental values, used for the article of Akiyama and the calculated values through XFLOW and FLUENT.

    The vortex core of the spiral whirlpool could not arrive at to a vortex table in SST k-, Standard k-, Standard k- model, even the phenomena could be seen in the experiment of Akiyama.

    In all calculation models, XFLOW gives the closest results with the experimental value quantitatively.

    Tanaka Kazuhiro Lab 16

    conclusions

  • Stairmand Cyclone Separator Tanaka Lab.

  • Cf. Article

    Derksen, J.J., Separation Performance Predictions of a Stairmand High-Efficiency Cyclone, AIChE Journal, Vol. 49, No. 6 (2003), pp. 1359-1371.

    0.2D

    0.36D 0.51D

    0.62D

    D = 0.29 [m]

    0.14D 1.5D

    D 0.5D 0.84D 0.52D

    2.5D 2D 4D 1.5D

    0.37D D D 0.5D

    Inlet Outlet

    Swirl Stop

    Feed Chamber Vortex Finder Dust Collection Box x

    z y

    x

    z y

    Tanaka Kazuhiro Lab 18

  • Analysis Condition

    3.25D

    Measurement Location

    x

    z

    y

    Cf. article (Derksen) Analysis Condition

    Analysis Program - Fluent 15.0 Xflow2014

    Time Unsteady Steady/ Unsteady Unsteady

    Analysis Model LES

    SST k-, LES Standard k- Standard k-

    WMLES

    Element Number 7,700,000

    380,000/ 8,800,000

    100,000/ 9,300,000

    Element Structure Hexa Hexa Octant tree

    Inlet 16.1 [m/s] Re 2.8105

    Outlet

    = 0 0 [Pa] Tanaka Kazuhiro Lab 19

  • Tangential Velocity and Axial Velocity

    -2

    -1

    0

    1

    2

    -1 0 1

    Location x/R

    Velo

    city

    u/U

    in

    -0.5

    0

    0.5

    1

    -1 0 1

    Location x/R Ve

    loci

    ty u

    z/Uin

    Steady Viscosity model 3,800,000element(FLUENT)

    LES Darksen Exp Hoekstra

    SST k-

    Realizable k-e

    RNG k-e

    RSM

    Standard k-

    LES Darksen Exp Hoekstra

    SST k-

    Realizable k-e

    RNG k-e

    RSM

    Standard k-

    -2

    -1

    0

    1

    2

    -1 0 1-0.5

    0

    0.5

    1

    -1 0 1

    Tanaka Kazuhiro Lab 20

    The evaluation of tangential velocity near the wall is not appropriate. The distribution of axial velocity is much different at the center of pipe, compared with experimental result.

  • Tangential Velocity and Axial Velocity Unsteadyt = 0.735 [s] LES 8,800,000 element(FLUENT)

    Location x/R

    Velo

    city

    u/U

    in

    Location x/R

    Velo

    city

    uz/U

    in

    -2

    -1

    0

    1

    2

    -1 0 1

    LES Darksen Exp Darksen

    LES(FLUENT)

    LES Darksen Exp Darksen

    LES(FLUENT) XFLOW XFLOW

    -0.5

    0

    0.5

    1

    -1 0 1

    100,000 element(XFLOW)

    Tanaka Kazuhiro Lab 21

    The gap of the peak values is caused by unsteady flow analysis. The results of XFLOW are instantaneous values.

    The difference of axial velocity is caused by strong unsteadiness of the vortex core of the spiral whirlpool.

  • Tangential Velocity and Axial Velocity Average(Time) (1[s]~3[s]) WMLES 9,300,000element(XFLOW)

    LES Darksen Exp Darksen

    LES Darksen Exp Darksen

    0 -2

    0.5 -0.5

    2

    0

    x/D

    /

    Xflow Xflow

    0 -0.5

    0.5 -0.5

    1

    0

    x/D

    w/

    0.75D

    Measurement location

    Tanaka Kazuhiro Lab 22

    Both of tangential velocity and axial velocity correspond to experimental result qualitatively. The peak value of tangential velocity is 25% bigger than the experimental result in our evaluation. The peak value of axial velocity is 10% bigger than the experimental result in our evaluation.

  • The time required in the XFLOW analysis

    Analysis Element number time Simulation

    time CPU(core) Analysis

    Stairmand cyclone 9,300,000 Unsteady 3.0[s] 40(20) 180[h]

    Stairmand cyclone 100,000 Unsteady 10.0[s] 8 6[h]

    Akiyama cyclone 3,920,000 Unsteady 3[s] 16 140[h]

    Stairmand cyclone 8,800,000 Unsteady 5[s] 20 168[h]

    Stairmand cyclone 3,800,000 Unsteady 5[s] 20 72[h]

    Akiyama cyclone 7,900,000 Unsteady 3[s] 20 168[h]

    Unsteady analysis only

    Tanaka Kazuhiro Lab 23

    XFLO

    W

    FLUEN

    T

  • Conclusion

    Tanaka Kazuhiro Lab 24

    The analysis through LES of XFLOW realizes unsteady motion of inside flow correctly.

    The results of XFLOW LES shows that the velocity near the wall is different from the experimental results because of influence of boundary condition and calculation lattice.

    Even though LES XFLOW result with 9,300,000 element still has a little gap compared with the experiments, but the LES result and peak values agree with the experiments qualitatively.

    Conclusions

    Cylindrical Cyclone SeparatorAnalysis ConditionTangential VelocityAxial VelocityComparison of Tangential Velocity (Steady)Comparison of Axial Velocity (Steady)Comparison of Tangential Velocity (Steady)Comparison of Axial Velocity (Steady)Comparison of Tangential Velocity (Steady)Comparison of Axial Velocity (Steady)Comparison of Tangential Velocity (Steady)Comparison of Axial Velocity (Steady)Comparison of Tangential Velocity at t=3.0[s]Comparison of Axial Velocity at t=3.0[s]Comparison between XFLOW and FLUENTConclusionStairmand Cyclone SeparatorCf. ArticleAnalysis ConditionTangential Velocity and Axial VelocityTangential Velocity and Axial VelocityTangential Velocity and Axial VelocityThe time required in the XFLOW analysisConclusion