Ground Based Fuel Tank Inerting - PowerPoint PPT Presentation

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Ground Based Fuel Tank Inerting

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Adams Mark Hotel - St. Louis, MS. Modeling Inert Gas. Distribution in Commercial ... Focus of Testing was to Find Best Method of Depositing NEA ... – PowerPoint PPT presentation

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Title: Ground Based Fuel Tank Inerting


1
Modeling Inert Gas Distribution in
Commercial Transport Aircraft Fuel Tanks
William M CavageProject Manager - Fuel Tank
Inerting FAA AAR-440, Fire Safety RD Branch
22nd AIAA Aerodynamic Measurement Technology and
Ground Testing Conference June 24th-26th, 2002
Adams Mark Hotel - St. Louis, MS
2
Outline
  • Background
  • Equipment Procedures
  • B-747SP Ground Test Article
  • 24 Scale Tank
  • Data Analysis
  • Modeling Methods
  • Results
  • Summary

3
Background
  • Ongoing FAA Rulemaking Seeks to Improve on the
    Existing and Future Fuel Tank Safety
  • Consistent Accident Trends are a Concern
  • Focus of Concern is on Heated Center Wing Tanks
    (CWTs)
  • Fuel Tank Inerting is a Well Established Method
    of Reducing/Eliminating Ullage Vapor Flammability
  • Has Been Meet with Resistance by Industry Leaders
  • FAA Would Like to Develop Cost Effective Methods
    of Modeling Inert Gas Distribution in Commercial
    Transport Fuel Tanks

4
Equipment
  • Boeing 747SP Full-Scale Inerting Test Article
  • Decommissioned from Airline Service and Purchased
    by the FAA for Ground Testing Only
  • All Major Systems Fully Operational
  • Has Independent Power for Test Equipment and
    Instrumentation
  • Full Complement of Ground Service Equipment
  • Aircraft Modified to Study Inerting
  • Inert Gas Deposit System Installed on Aircraft
  • Inerts CWT from Ground Source of Nitrogen
    Enriched Air (NEA)
  • Instrumentation
  • Gas Sample Tubing at 8 Locations for Oxygen/THC
    Analysis
  • 32 Thermocouples in Tank (Ullage, Fuel, Walls,
    Floor, and Ceiling)

5
Boeing 747SP Aircraft
6
Boeing 747-100/SP Center Wing Tank
7
Boeing 747SP CWT Top Diagram
8
Equipment
  • Scale Tank Test Article
  • 24 Scale Model of Boeing 747 SP CWT was Built
    from 3/4 Inch Plywood By Scaling Drawings from
    Shepherd Report
  • Spars and Spanwise Beams Simulated with ¼ Inch
    Plywood Installed in Slats with Scaled
    Penetration Holes
  • Vent System Simulated with PVC Tubing Plumbed to
    an Aluminum Vent Channel Plumbed Similar to
    Aircraft
  • Instrumentation
  • Oxygen Sensor in Each Bay and in One Vent Channel
    Plumbed in Unique Sample Drafting Method
    Returned to Each Bay
  • Thermocouple in Each Bay
  • Variable NEA Manifold Allowed for NEA to be
    Deposited in Any and All Bays of the Tank at
    Different Flow Rates

9
Scale Plywood CWT Model
10
Procedures
  • 24 Scale Tank Testing
  • Series of Tests Done to Examine Different Deposit
    Schemes
  • Deposited Different Amounts of NEA in Different
    Bays to Determine the most Efficient Method of
    Deposit in a Half Blocked Venting Configuration
  • All Work Presented is for 95 NEA and 128 CFH
    Total Flow Rate
  • Focus of Testing was to Find Best Method of
    Depositing NEA
  • Boeing 747SP Full-Scale Inerting Testing
  • Series of Tests Done to Examine the Efficiency of
    Inerting
  • Single Deposit (Optimal from Scale Testing)and
    Venting Case
  • Tested for Different Day and Operational
    Conditions
  • All Work Presented is for 95 NEA and 140 CFM
    Total Flow Rate with ACMs Running (Vertical
    Mixing Stimulated)
  • Focus of Testing was on Operational Effects and
    Predictability

11
Data Reduction Analysis
  • Volumetric Tank Exchange is the Ratio of the
    Volume of Deposited Gas to the Volume of the Tank
  • This Gives a Dimensionless Quantity of Inert Gas
    Given the Volume of the Tank
  • Average Tank Oxygen Concentration
  • This Gives a Representation of the Tank Oxygen
    Constituency Given Varying Oxygen Concentrations
    in Different Bays

12
Inert Gas Distribution Engineering Model
  • Model Calculates Inert Gas Distribution in 6 Bay
    Tank, in terms of Oxygen Concentration Evolution,
    Given NEA Purity and Bay Deposit Flow Rates
  • Based on Original Single Bay Inerting Model, by
    FAA CSTA for Fuel Systems, which Tracks Oxygen In
    and Out of Each Bay Assuming Perfect Mixing
    During the Time Step
  • Assumes an Outward Flow Pattern and Splits Flow
    into a Bay to Adjacent Bays Using Out Flow Area
    Relationships
  • Basic Formula for Volume of Oxygen in a Bay

13
Assumed Engineering Model Flow Pattern
Flow Out
Bay 1
Bay 2
Bay 4
Flow In
Bay 3
Flow Out
Bay 5
Bay 6
14
CFD Model
  • A CFD Model was Developed with the Analysis
    Package FLUENT
  • Used the Fluent CFD Solver Which Uses a Finite
    Volume Method Where the General Conservation
    (transport) Equation (Mass, Momentum, Energy,
    etc.) is Solved for Each Finite Volume
  • Has Ability to Track Fluid Species (O2
    Concentration) at Given Locations
  • Model was Solved Using a Laminar Flow Throughout
    (Oxygen Evolution is Based Entirely on Flow
    Diffusion)
  • For Administrative Reasons, Model was Developed
    of the Scale Tank and not Full-Scale Test Article
  • The Model Developed had Approximately 700K Cells
    and Ran on Several Platforms Over a Weekend.

15
Results - Full Scale Comparison
  • Scale Tank Test Data Compares Well with
    Full-Scale Test Article Data
  • Bay 4 Does Not Compare Well for Any Modeling
    Method
  • Engineering Model Compares Fair
  • Trend Data Very Good but Some Bays have Large
    Discrepancy in Some Bay Oxygen Concentration
    Values when Compared with Full-Scale Data
  • CFD Model Comparisons Initially Poor
  • Trend Data Marginal with Large Discrepancies in
    Some Bay Oxygen Concentration Values when
    Compared with Full-Scale Data
  • Subsequent Data Has Much Better Agreement

16
Scale Tank Data Comparison
17
Engineering Model Data Comparison
18
CFD Model Data Comparison
19
Modeling Methods Compared
20
Results - Mock Trade Study
  • Comparing Scale Tank Test Article Data with
    Engineering Model Data for Different Deposit
    Scenarios Has Mixed Results
  • Bay to Bay Oxygen Concentration Comparisons Vary
    for Different Deposit Scenarios
  • The Average Oxygen Concentration Trend Data for
    the Different Deposit Scenarios is Consistently
    Biased High for the Engineering Model Except for
    the Single Deposit Case
  • This Results in a Discrepancy Between Which
    Deposit Method is Optimal (Most Efficient) for
    Each Modeling Method

21
Engineering Model Compared with Scale Tank
22
Engineering Model Compared with Scale Tank
23
Full-Scale Data Compared with Modeling Methods
24
Summary
  • Scale Tank Testing Produced Good Results when
    Compared with the Good Mixing Full-Scale
    Testing
  • Cost Effective Modeling Method
  • Simple Engineering Modeling Methods Can Produce
    Fair Results in a Very Cost Effective Way
  • Additional Work Needed to Improve Model
  • Additional Research Required to Resolve
    Discrepancies between Engineering Model and Scale
    Tank for for Multiple Deposits
  • CFD Data Labor/Resource Intensive and Eventually
    Resulted in Good Comparison to Full-Scale Data
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