non-ideal effects in compressible swirling flows

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Non-Ideal Effects in Compressible Swirling Flows 3 rd International Seminar on NICFD Delft, The Netherlands F. Tosto, A. Giuffre’, P. Colonna, M. Pini Propulsion and Power, Delft University of Technology The information in this document is the property of TU Delft and may not be copied or communicated to a third party without prior written consent 11/11/2020

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Page 1: Non-Ideal Effects in Compressible Swirling Flows

Non-Ideal Effects in

Compressible Swirling Flows

3rd International Seminar on NICFD

Delft, The Netherlands

F. Tosto, A. Giuffre’, P. Colonna, M. Pini

Propulsion and Power, Delft University of Technology

The information in this document is the property of TU Delft and may not be

copied or communicated to a third party without prior written consent 11/11/2020

Page 2: Non-Ideal Effects in Compressible Swirling Flows

Background1

Limited knowledge of NICFD

effects on turbomachinery

β€’ efficiency

β€’ operability

choking instability

𝑒 π‘’π‘šπ‘’πœƒ

Page 3: Non-Ideal Effects in Compressible Swirling Flows

NICFD effects: isentropic exponent 𝛾𝑝𝑣

Dilute gas state: 𝛾𝑝𝑣 β†’ 𝛾, with 𝛾 > 1

2

𝛾𝑝𝑣 = βˆ’π‘£

𝑝

πœ•π‘

πœ•π‘£π‘ 

CO2CO2MM

Page 4: Non-Ideal Effects in Compressible Swirling Flows

Relevance of NICFD effects on losses3

Efficiency can

differ of up to ~πŸ’%

Giuffre’ and Pini, β€œDesign guidelines for axial turbines operating with non-ideal compressible flows”, JEGTP, 2020, article in press

Page 5: Non-Ideal Effects in Compressible Swirling Flows

Problem Statement4

No existing knowledge on quantitative impact of NICFD effects on

β€’ Choking conditions

β€’ Flow deviation in post and pre-expansion processes

Page 6: Non-Ideal Effects in Compressible Swirling Flows

Scope of Research

β€’ Assess variation of flow deviation as 𝒇(πœΈπ’‘π’—)

β€’ Assess impact of πœΈπ’‘π’— on choking in turbomachinery

5

Page 7: Non-Ideal Effects in Compressible Swirling Flows

Methodology: 2-steps Approach6

1β€’ Theoretical analysis on

Swirling Flow

2β€’ Verification and

validation through CFD

Page 8: Non-Ideal Effects in Compressible Swirling Flows

7

Theoretical Analysis

Page 9: Non-Ideal Effects in Compressible Swirling Flows

Corrected mass flow per unit area (1)8

absolute

Mach number

= 𝑀 cos 𝛼meridional

Mach number

𝑀 π‘€π‘š

π‘€πœƒ

Assumption: 𝛾𝑝𝑣 = π‘π‘œπ‘›π‘ π‘‘

αˆΆπ‘šπ‘π‘œπ‘Ÿπ‘Ÿ β‰ƒπ‘€π‘š

1 +𝛾𝑝𝑣 βˆ’ 1

2𝑀2

𝛾𝑝𝑣+1

2(π›Ύπ‘π‘£βˆ’1)

Page 10: Non-Ideal Effects in Compressible Swirling Flows

Corrected mass flow per unit area (2)9

absolute

Mach number

= ΰ·œπ‘’πœƒswirl parameter

𝑒 π‘’π‘šπ‘’πœƒ

Assumption: 𝛾𝑝𝑣 = π‘π‘œπ‘›π‘ π‘‘

αˆΆπ‘šπ‘π‘œπ‘Ÿπ‘Ÿ ≃ 1 +𝛾𝑝𝑣 βˆ’ 1

2𝑀2

𝑀2

1 +𝛾𝑝𝑣 βˆ’ 1

2𝑀2

βˆ’π‘’πœƒ

𝛾𝑝𝑣,𝑑𝑍𝑑𝑅𝑇𝑑

2

Page 11: Non-Ideal Effects in Compressible Swirling Flows

Investigated Processes10

𝛾𝑝𝑣 > 𝛾 𝛾𝑝𝑣 < 𝛾

CO2MM

Page 12: Non-Ideal Effects in Compressible Swirling Flows

Influence of 𝛾𝑝𝑣 on Choking11

Choking: π‘€π‘š = 1

𝑀 𝛾𝑝𝑣

𝛾𝑝𝑣 > 𝛾 𝛾𝑝𝑣 < 𝛾

Page 13: Non-Ideal Effects in Compressible Swirling Flows

Exemplary Post – Expansion in Turbine12

Horizontal line at constant αˆΆπ‘šπ‘π‘œπ‘Ÿπ‘Ÿ (A-B-C)

β€’ Point B: sonic throat (𝑀 = 1)

β€’ Point C: post-expansion final state (𝑀 = 1.8)

β€’ Deviation angle increases if πœΈπ’‘π’— decreases

Page 14: Non-Ideal Effects in Compressible Swirling Flows

Exemplary Expansion in Supersonic Turbine13

Vertical line at constant π‘€π‘š (D-B-E)

β€’ Constant flow coefficient

β€’ Negligible post-expansion

β€’ βˆ† αˆΆπ’Žπ’„π’π’“π’“ increases if πœΈπ’‘π’— decreases

β€’ Larger area variation to accommodate larger

volumetric flow ratio 𝛼 = πœŒπ‘‘,𝑖𝑛/πœŒπ‘œπ‘’π‘‘

Page 15: Non-Ideal Effects in Compressible Swirling Flows

14

CFD Verification

Page 16: Non-Ideal Effects in Compressible Swirling Flows

Test Cases & Numerical Setting15

3D transonic stator vanes

Spatial discretization: 2nd order

Turbulence: π‘˜ βˆ’ πœ” SST (y+ ≀ 1)

Fluid mesh: 5M points

Look-up table: 2.5M (iMM) - 4M (niMM) points

iMM

niMM

iMM: 𝛽𝑑𝑠 = 2.0 βˆ’ 2.8 βˆ’ 3.4

niMM: 𝛽𝑑𝑠 = 1.8 βˆ’ 2.7 βˆ’ 3.8

Page 17: Non-Ideal Effects in Compressible Swirling Flows

Results16

β€’ 1D model qualitatively in line with CFD if sufficiently far from chocking

β€’ Large deviation in volumetric flow ratio

- iMM: 𝛼𝑑𝑠 = 2.2 βˆ’ 3.1 βˆ’ 3.8- niMM: 𝛼𝑑𝑠 = 1.6 βˆ’ 4.0 βˆ’ 6.9

iMM

D

B

C

niMM

D

B

C

Page 18: Non-Ideal Effects in Compressible Swirling Flows

Physical Insights17

β€’ 𝛾𝑝𝑣 < 𝛾 β†’ larger area variation to accommodate larger 𝛼 at given 𝛽

β€’ 𝛾𝑝𝑣 < 𝛾 β†’ larger flow deviation in convergent blade channels

iMM, 𝛼𝑑𝑠 = 3.8 niMM , 𝛼𝑑𝑠 = 6.9

Page 19: Non-Ideal Effects in Compressible Swirling Flows

Take-Away Messages

β€’ Expansions characterized by πœΈπ’‘π’— < 𝜸 lead to earlier choking and

larger flow deviation when fixing 𝛽𝑑𝑠

β€’ Turbines operating with flow 𝛾𝑝𝑣 < 𝛾 (ORC) more susceptible to

reach complete choking operability/efficiency issues

β€’ Research hypothesis:

choice of convergent-divergent nozzle driven by ability to control

flow deviation and extend operating range

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Page 20: Non-Ideal Effects in Compressible Swirling Flows

Ongoing & Future Work

β€’ Verify hypothesis by

- Investigate expansion in convergent-divergent nozzles

β€’ Pre-expansion at compressor inlet

β€’ Analysis of compression processes

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Page 21: Non-Ideal Effects in Compressible Swirling Flows

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Further info upon request @

[email protected] & co-workers!