TFAWS August 21-25, 2017 NASA Marshall Space Flight Center MSFC - - PowerPoint PPT Presentation

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TFAWS August 21-25, 2017 NASA Marshall Space Flight Center MSFC - - PowerPoint PPT Presentation

TFAWS Active Thermal Paper Session AN INNOVATIVE METHODOLOGY FOR ERROR ANALYSIS OF THERMO-FLUID SYSTEMS David Dodoo-Amoo, Julio Mendez, Mookesh Dhanasar, Frederick Ferguson North Carolina A&T State University Presented By David


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SLIDE 1

TFAWS

MSFC โˆ™ 2017

Presented By

David Dodoo-Amoo

AN INNOVATIVE METHODOLOGY FOR ERROR ANALYSIS OF THERMO-FLUID SYSTEMS

David Dodoo-Amoo, Julio Mendez, Mookesh Dhanasar, Frederick Ferguson North Carolina A&T State University

Thermal & Fluids Analysis Workshop TFAWS 2017 August 21-25, 2017 NASA Marshall Space Flight Center Huntsville, AL

TFAWS Active Thermal Paper Session

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SLIDE 2

Governing Equations

  • Conservation of Mass :

๐œ– ๐œ๐ต ๐œ–๐‘ข + ๐œ– ๐œ๐‘ฃ๐ต ๐œ–๐‘ฆ = 0

  • Conservation of Momentum :

๐œ– ๐œ๐‘ฃ๐ต ๐œ–๐‘ข + ๐œ– ๐œ๐‘ฃ2 + ๐‘ž ๐ต ๐œ–๐‘ฆ โˆ’ ๐‘ž ๐‘’๐ต ๐‘’๐‘ฆ = 0

  • Conservation of Energy :

๐œ– ๐œ๐‘“๐‘ˆ๐ต ๐œ–๐‘ข + ๐œ– ๐œ๐‘“๐‘ˆ + ๐‘ž ๐‘ฃ๐ต ๐œ–๐‘ฆ = 0

TFAWS 2017 โ€“ August 21-25, 2017

2

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SLIDE 3

Governing Equations- Non Dimensional

  • Conservation of Mass :

๐œ– าง ๐œ าง ๐ต ๐œ– าง ๐‘ข + ๐œ– าง ๐œเดค ๐‘ฃ าง ๐ต ๐œ– าง ๐‘ฆ = 0

  • Conservation of Momentum :

๐œ– าง ๐œเดค ๐‘ฃ าง ๐ต ๐œ– าง ๐‘ข + ๐œ– ๐œ– าง ๐‘ฆ าง ๐œ าง ๐ต เดค ๐‘ฃ2 + เดค ๐‘ˆ ๐›ฟ โˆ’ าง ๐œเดค ๐‘ˆ ๐›ฟ ๐‘’ าง ๐ต ๐‘’ าง ๐‘ฆ = 0

  • Conservation of Energy :

๐œ– ๐œ– าง ๐‘ข าง ๐œ าง ๐‘“๐‘ˆ าง ๐ต + ๐œ– ๐œ– าง ๐‘ฆ าง ๐œเดค ๐‘ฃ าง ๐ต าง ๐‘“๐‘ˆ + เดค ๐‘ˆ = 0

Where

าง ๐‘“๐‘ˆ โ‰

าง ๐‘“ ๐›ฟโˆ’1 + ๐›ฟ 2 เดค

๐‘ฃ2

TFAWS 2017 โ€“ August 21-25, 2017

3

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SLIDE 4

Vector Form

TFAWS 2017 โ€“ August 21-25, 2017

4

๐œ–๐‘‰ ๐œ–๐‘ข + ๐œ–๐บ ๐œ–๐‘ฆ โˆ’ ๐ป = 0 Where the vectors, U, F and G are defined as

๐‘‰ = ๐œ๐ต ๐œ๐‘ฃ๐ต ๐œ๐‘“๐‘ˆ๐ต , ๐บ = ๐œ๐‘ฃ๐ต ๐œ๐ต ๐‘ฃ2 + ๐‘ˆ

๐›ฟ

๐œ๐‘ฃ๐ต ๐‘“๐‘ˆ + ๐‘ˆ , ๐ป =

๐œ๐‘ˆ ๐›ฟ ๐‘’๐ต ๐‘’๐‘ฆ

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SLIDE 5

5

๐ต ๐‘ฆ = 1.0 + 2.2(๐‘ฆ โˆ’ 1.5)2

Problem ID1: Anderson Nozzle Isentropic Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

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SLIDE 6

6

๐ต ๐‘ฆ = 1.0 + 2.2(๐‘ฆ โˆ’ 1.5)2

Problem ID1: Anderson Nozzle Isentropic Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= 2.0๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’2

Outflow Conditions

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SLIDE 7

7

๐ต ๐‘ฆ = 1.0 + 2.2(๐‘ฆ โˆ’ 1.5)2

Problem ID2: Anderson Nozzle Shock Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

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SLIDE 8

8

๐ต ๐‘ฆ = 1.0 + 2.2(๐‘ฆ โˆ’ 1.5)2

Problem ID2: Anderson Nozzle Shock Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘ข

= ๐œ๐‘—๐‘›๐‘๐‘ฆโˆ’1 0.1520 ๐‘ˆ๐‘—๐‘›๐‘๐‘ฆโˆ’1

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SLIDE 9

9

๐ต ๐‘ฆ = 1.0 + 5.3 ๐‘๐‘๐‘ก| ๐‘ฆ โˆ’ 1.5 |

Problem ID3: Absolute Nozzle Isentropic Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

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SLIDE 10

10

๐ต ๐‘ฆ = 1.0 + 5.3 ๐‘๐‘๐‘ก| ๐‘ฆ โˆ’ 1.5 |

Problem ID3: Absolute Nozzle Isentropic Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= 2.0๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’2

Outflow Conditions

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SLIDE 11

11

๐ต ๐‘ฆ = 1.0 + 5.3 ๐‘๐‘๐‘ก| ๐‘ฆ โˆ’ 1.5 |

Problem ID4: Absolute Nozzle Isentropic Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

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SLIDE 12

12

๐ต ๐‘ฆ = 1.0 + 5.3 ๐‘๐‘๐‘ก| ๐‘ฆ โˆ’ 1.5 |

Problem ID4: Absolute Nozzle Isentropic Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘ข

= ๐œ๐‘—๐‘›๐‘๐‘ฆโˆ’1 0.1520 ๐‘ˆ๐‘—๐‘›๐‘๐‘ฆโˆ’1

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SLIDE 13

13

๐ต ๐‘ฆ = 1.0 + 2.2 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ โ‰ค 1.5 ๐ต ๐‘ฆ = 1.0 + 0.2223 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ > 1.5

Problem ID5: Feng Nozzle Isentropic Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

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SLIDE 14

14

๐ต ๐‘ฆ = 1.0 + 2.2 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ โ‰ค 1.5 ๐ต ๐‘ฆ = 1.0 + 0.2223 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ > 1.5

Problem ID5: Feng Nozzle Isentropic Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= 2.0๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’2

slide-15
SLIDE 15

15

๐ต ๐‘ฆ = 1.0 + 2.2 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ โ‰ค 1.5 ๐ต ๐‘ฆ = 1.0 + 0.2223 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ > 1.5

Problem ID6: Feng Nozzle Shock Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 เต— 0.59 ๐œ๐ต 1.0

๐‘ฆ๐‘๐‘๐‘ 

0 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 เต— 0.59 ๐œ๐ต 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 1.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 เต— 0.59 ๐œ๐ต 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

๐‘ฆ๐‘๐‘๐‘  โ‰ฅ 1.5

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

slide-16
SLIDE 16

16

๐ต ๐‘ฆ = 1.0 + 2.2 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ โ‰ค 1.5 ๐ต ๐‘ฆ = 1.0 + 0.2223 ๐‘ฆ โˆ’ 1.50 2 ๐‘”๐‘๐‘  ๐‘ฆ > 1.5

Problem ID6: Feng Nozzle Shock Flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Inflow Conditions Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 0.48 ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1

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17

๐ต ๐‘ฆ = 1.5643 + 0.3883tanh(8๐‘ฆ โˆ’ 4)

Problem ID7: Hoffmann Nozzle Isentropic flow

Initial Conditions

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

๐œ ๐‘ฃ ๐‘ˆ ๐‘—

๐‘ข=0

= 0.395 1.5 ร— 0.6897 0.6897 0 โ‰ค ๐‘Œ๐‘๐‘๐‘  โ‰ค 1

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SLIDE 18

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๐ต ๐‘ฆ = 1.5643 + 0.3883tanh(8๐‘ฆ โˆ’ 4)

Problem ID7: Hoffmann Nozzle Isentropic flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ 1 = 0.395 1.5 ร— 0.6897 0.6897 ๐œ ๐‘ฃ ๐‘ˆ ๐ฝ๐‘›๐‘๐‘ฆ

๐‘œ

= 2 ๐œ ๐‘ฃ ๐‘ˆ ๐ฝ๐‘›๐‘๐‘ฆโˆ’1

๐‘œ

โˆ’ ๐œ ๐‘ฃ ๐‘ˆ ๐ฝ๐‘›๐‘๐‘ฆโˆ’2

๐‘œ

Inflow Conditions

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๐ต ๐‘ฆ = 1.5643 + 0.3883tanh(8๐‘ฆ โˆ’ 4)

Problem ID8: Hoffmann Nozzle Shock flow

Initial Conditions

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

๐œ ๐‘ฃ ๐‘ˆ ๐‘—

๐‘ข=0

= 0.395 1.5 ร— 0.6897 0.6897 0 โ‰ค ๐‘Œ๐‘๐‘๐‘  โ‰ค 1

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SLIDE 20

20

๐ต ๐‘ฆ = 1.5643 + 0.3883tanh(8๐‘ฆ โˆ’ 4)

Problem ID8: Hoffmann Nozzle Shock flow

TFAWS 2017 โ€“ August 21-25, 2017

Quasi 1-D Problems

Outflow Conditions

๐œ ๐‘ฃ ๐‘ˆ 1 = 0.395 1.5 ร— 0.6897 0.6897

Inflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐ฝ๐‘›๐‘๐‘ฆ

๐‘œ

= ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 0.5081 ร— ๐‘ˆ๐‘—๐‘›๐‘๐‘ฆ ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1

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SLIDE 21

21

๐ต ๐‘ฆ = 2.0 ๐‘”๐‘๐‘  โˆ’ 1.0 โ‰ค ๐‘ฆ < โˆ’0.5 , 0.5 โ‰ค ๐‘ฆ โ‰ค 1.0 ๐ต ๐‘ฆ = 1.0 + ๐‘ก๐‘—๐‘œ2 ๐œŒ๐‘ฆ ๐‘”๐‘๐‘  โˆ’ 0.5 โ‰ค ๐‘ฆ < 0.5 ,

Problem ID9 : Feng 2nd Nozzle Isentropic Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 0.3 1.0 ๐‘ฆ๐‘๐‘๐‘  ๐‘ฆ๐‘๐‘๐‘  < โˆ’0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 0.7 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

โˆ’ 0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 1.5 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  โ‰ค 1.0

Quasi 1-D Problems

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SLIDE 22

22

๐ต ๐‘ฆ = 2.0 ๐‘”๐‘๐‘  โˆ’ 1.0 โ‰ค ๐‘ฆ < โˆ’0.5 , 0.5 โ‰ค ๐‘ฆ โ‰ค 1.0 ๐ต ๐‘ฆ = 1.0 + ๐‘ก๐‘—๐‘œ2 ๐œŒ๐‘ฆ ๐‘”๐‘๐‘  โˆ’ 0.5 โ‰ค ๐‘ฆ < 0.5 ,

Problem ID9: Feng 2nd Nozzle Isentropic Flow

Inflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= 2.0๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ฃ ๐‘—๐‘›๐‘๐‘ฆโˆ’2 2.0๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 โˆ’ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’2

Outflow Conditions

Quasi 1-D Problems

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SLIDE 23

23

๐ต ๐‘ฆ = 2.0 ๐‘”๐‘๐‘  โˆ’ 1.0 โ‰ค ๐‘ฆ < โˆ’0.5 , 0.5 โ‰ค ๐‘ฆ โ‰ค 1.0 ๐ต ๐‘ฆ = 1.0 + ๐‘ก๐‘—๐‘œ2 ๐œŒ๐‘ฆ ๐‘”๐‘๐‘  โˆ’ 0.5 โ‰ค ๐‘ฆ < 0.5

Problem ID10: Feng 2nd Nozzle Shock Flow

Initial Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 0.3 1.0 ๐‘ฆ๐‘๐‘๐‘  ๐‘ฆ๐‘๐‘๐‘  < โˆ’0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 1.0 โˆ’ 0.366 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5 0.7 1.0 โˆ’ 0.167 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 0.5

๐‘ฆ๐‘๐‘๐‘ 

โˆ’ 0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  < 0.5 ๐œ ๐‘ฃ ๐‘ˆ ๐‘ฆ๐‘๐‘๐‘ 

๐‘ข=0

= 0.634 โˆ’ 0.3879 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5 1.5 0.833 โˆ’ 0.3507 ๐‘ฆ๐‘๐‘๐‘  โˆ’ 1.5

๐‘ฆ๐‘๐‘๐‘ 

0.5 โ‰ค ๐‘ฆ๐‘๐‘๐‘  โ‰ค 1.0

Quasi 1-D Problems

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SLIDE 24

24

๐ต ๐‘ฆ = 2.0 ๐‘”๐‘๐‘  โˆ’ 1.0 โ‰ค ๐‘ฆ < โˆ’0.5 , 0.5 โ‰ค ๐‘ฆ โ‰ค 1.0 ๐ต ๐‘ฆ = 1.0 + ๐‘ก๐‘—๐‘œ2 ๐œŒ๐‘ฆ ๐‘”๐‘๐‘  โˆ’ 0.5 โ‰ค ๐‘ฆ < 0.5 ,

Problem ID10: Feng 2nd Nozzle Shock Flow

Inflow Conditions

๐œ ๐‘ฃ ๐‘ˆ ๐‘—=1

๐‘ข

= 1.0 2.0๐‘ฃ2 โˆ’ ๐‘ฃ3 1.0 ๐œ ๐‘ฃ ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆ

๐‘œ

= ๐œ ๐‘—๐‘›๐‘๐‘ฆโˆ’1 0.43 ๐‘ˆ ๐‘—๐‘›๐‘๐‘ฆโˆ’1

Outflow Conditions

Quasi 1-D Problems

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SLIDE 25

Locations where Exact Solutions are known เต— ๐‘ˆ0 ๐‘ˆโˆ— , เต— ๐‘„0 ๐‘„โˆ— , ๐‘โˆ—

๐‘ผ๐Ÿ ๐‘—๐‘ก ๐‘‘๐‘๐‘œ๐‘ก๐‘ข๐‘๐‘œ๐‘ข, แˆถ ๐’ ๐‘—๐‘ก ๐‘‘๐‘๐‘œ๐‘ก๐‘ข๐‘๐‘œ๐‘ข

  • Pointwise (Throat)
  • Distributed ( Entire Nozzle )
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SLIDE 26

Problem ID1 and ID2

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SLIDE 27

TFAWS 2017 โ€“ August 21-25, 2017

27

Problem ID3 and ID4

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SLIDE 28

TFAWS 2017 โ€“ August 21-25, 2017

28

Problems ID5 and ID6

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SLIDE 29

TFAWS 2017 โ€“ August 21-25, 2017

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Problem ID7 and ID8

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SLIDE 30

TFAWS 2017 โ€“ August 21-25, 2017

30

Problem ID9 and ID10

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SLIDE 31

TFAWS 2017 โ€“ August 21-25, 2017

31

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SLIDE 32

TFAWS 2017 โ€“ August 21-25, 2017

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Problem ID1 and ID2

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SLIDE 33

TFAWS 2017 โ€“ August 21-25, 2017

33

Problem ID3 and ID4

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SLIDE 34

TFAWS 2017 โ€“ August 21-25, 2017

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Problem ID5 and ID6

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SLIDE 35

TFAWS 2017 โ€“ August 21-25, 2017

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Problem ID7 and ID8

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SLIDE 36

TFAWS 2017 โ€“ August 21-25, 2017

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Problem ID9 and ID10

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SLIDE 37

TFAWS 2017 โ€“ August 21-25, 2017

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Grid Independence Grid Comparison

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SLIDE 38

TFAWS 2017 โ€“ August 21-25, 2017

38

Grid Independence Grid Comparison

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SLIDE 39

TFAWS 2017 โ€“ August 21-25, 2017

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Table 1. Table of Error for Isentropic Problems

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SLIDE 40

TFAWS 2017 โ€“ August 21-25, 2017

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Table 2. Table of Error for Shock Problems

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SLIDE 41

CONCLUSIONS

  • The results show that the maximum error was 6.78%

and occurred at the throat of the nozzle with an acute throat gradient.

  • The standard solution can therefore be used in place of

an analytical solution for the purpose of error analysis

TFAWS 2017 โ€“ August 21-25, 2017

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