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Analytical Technique for Composite Storage Tank

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Presentation on theme: "Analytical Technique for Composite Storage Tank"— Presentation transcript:

1 Analytical Technique for Composite Storage Tank
Design Factor Specification NHA Annual Hydrogen Conference 2008 March 30 - April 4, Sacramento, CA Vladimir M. Shkolnikov, Ph.D., CTC Kevin L. Klug, Ph.D., CTC

2 AGENDA COMPOSITE OVERWRAPPED PRESSURE VESSELS
DEVELOPMENTAL GOALS & REQUIREMENTS ACCOMPLISHMENTS TO DATE CONCERNING ISSUES REQUIREMENTS VARIANCE DETERIORATIVE FACTORS OF OPERATION DESIGN STRENGTH RECONCILIATION TECHNIQUES EXEMPLIFIED SERVICEABILITY ASSESSMENT DESIGN FACTOR SPECIFICATION

3 Composite Overwrapped Pressure Vessels (COPV)
COPV Type 3, metal-lined composite reinforced cylinder with load-sharing liner that alone cannot resist the operating pressure, normally termed full-wrapped. COPV Type 2, metal-lined composite reinforced cylinder with load-sharing liner that alone can withstand the operating pressure, normally termed hoop-wrapped. Proprietary

4 DOE Goals & Requirements
Develop and demonstrate viable hydrogen storage technologies for on-board and off-board applications By 2010: Develop and verify hydrogen storage systems achieving 2 kWh/kg (6 wt%), 1.5 kWh/L, $4/kWh, and 30 g/L; storage tank purchased capital cost $500/kg H2; ambient -30/50ºC + full solar load; min/max delivery temperature -40/85ºC; life (1/4 tank to full) 1000 cycles By 2015: Develop and verify hydrogen storage systems achieving 3 kWh/kg (9 wt%), 2.7 kWh/L, $2/kWh, and >35 g/L; storage tank purchased capital cost $300/kg H2; ambient -40/60ºC + full solar load; min/max delivery temperature -40/85ºC; life (1/4 tank to full) 1500 cycles.

5 COPV Type 3 Designed and produced by HyPerComp Engineering, Inc.
(Brigham City, UT) for DOE project with CTC COPV-3 prototype with aluminum liner for on-board application Capacity: 7.75 L (0.30 kg H2) Mean burst test pressure: 25.4 Ksi Intended service pressure: 10.0 Ksi Hydrogen weight efficiency: 5.2% (6 wt% for 2010) Hydrogen volumetric efficiency: 38.7 g/L (30.0 g/L for 2010) Estimated cost: $4,700/kg H2 ($500/kg H2 for 2010). Proprietary

6 COPV Type 2 Designed and produced by HyPerComp Engineering, Inc.
(Brigham City, UT) for DOE project with CTC COPV-2 prototype with steel liner for off-board application Capacity: 15.1 L (0.44 kg H2) Mean burst test pressure: 15.5 Ksi Intended service pressure: 6.2 Ksi Hydrogen weight efficiency: 2.4% (6 wt% for 2010) Hydrogen volumetric efficiency: 29.2 g/L (30.0 g/L for 2010) Estimated cost: $641/kg H2 ($500/kg H2 for 2010) Proprietary

7 Concerning Issues The DOE goals and requirements, while presenting good reference points for COPV advancement, are incomplete in terms of design criteria for verification of long-term COPV capability Polymer Matrix Composites (PMC) typically exhibit enhanced sensitivity to time-variable parameters of force - temperature exposure that should be taken into account Existing standards / codes don’t provide design guidance sufficient to characterize serviceability and/or properly select a design factor for COPVs subjected to changeable operational exposure.

8 Requirements Variance
Criteria Material CGA [1] ISO [2] DOT [3] Stress ratios: Burst/test (Burst/service) Aramid FRP 2.0 (3.0) 2.1 (3.51) 2.04 (3.4) Carbon FRP 1.5 (2.25) 2.0 (3.34) Glass FRP 2.33 (3.5) 2.4 (4.01) Service life 30 years 30 + years 15 years CGA C -19 FRP-3.– Guideline for Filament-Wound Composite Cylinders with Nonloadsharing Liners, Second Edition. Compressed Gas Association, Inc., 2002 ISO : Gas Cylinders of Composite Construction - Specification and Test Methods - Part 2: Fully Wrapped Fiber Reinforced Composite Gas Cylinders With Load-sharing Metal Liners, 2002 DOT-CFFC. Appendix A. Basic Requirements for Fully Wrapped Carbon-Fiber Reinforced Aluminum Lined Cylinders Proprietary

9 Principal Objective Improve methodology for serviceability * characterization and specification of design factors to ensure proper long-term performance of COPVs. * Prerequisite quality of service accomplished within a specified timeframe.

10 Deteriorative Factors of Operation
Over-the-road bulk transportation Stationary accumulators for gas generation and/or collection sites Stationary storage for forecourt dispensing sites As an end-user’s vehicular fuel tank. These applications imply a variety of duty cycles and loading factors which will affect long-term structural performance of composite wrap jacket of COPV.   Storage tanks will be employed for assorted engineering systems of Hydrogen Infrastructure including: Proprietary

11 Deteriorative Factors of Operation
* A fabrication technique in which COPV is subjected to high pressure, causing the metal liner to yield and resulting in its compressive residual stresses. The goal of autofrettage is to increase the liner’s durability. Proprietary

12 Temperature Factor Possible Effects
Temperature may affect the composite jacket of COPV in several ways: As a direct deteriorative factor of thermal-mechanical fatigue Via increase of pressure of the contained gaseous hydrogen Inducing additional interface pressure between the jacket and load-sharing liner due to difference in thermal expansion of the jacket and liner materials. Proprietary

13 Temperature Factor Outside Ambient Temperature
Off-board storage tanks can sit at any climatic zone either above ground, on, or underground. This entails a wide variety of outside ambient temperatures during operation as no temperature control is present. Filling stations in North America Proprietary

14 Temperature Factor Pressure-Temperature-Density Interdependency*
H2 density vs. pressure & temperature Pressure increase due to H2 heating * - NIST Standard Reference Database, Proprietary

15 Temperature Factor Fast Filling • Warming up
The approximation is based on experimental data* regarding pressure & temperature changing over filling time and is to be utilized within COPV serviceability assessment. Approximated P,T = f (time) * - Eihusen, J. A., Application of Plastic-Lined Composite pressure vessels for Hydrogen Storage, GD Armament and Technical Products, Lincoln, NE Proprietary

16 Temperature Factor Thermal Expansion
Thermal expansion vs. temperature* Possible outcomes The difference in thermal expansion may affect jacket-liner interface pressure either increasing or decreasing the jacket stressing and resulting respectively with: Liner’s elastic instability and Reduction of residual after autofrettage pressure possibly affecting the interface bonding (when the tank is empty). Either case lowers liner’s functionality. * - Marquardt, E.D., Le, J.P., and Radebaugh, R., Cryogenic Material Properties Database, NIST, The 11th International Cryocooler Conference, Keystone, CO, June 20-22, 2000. Proprietary

17 Structural Design Reconciliation Conventional Technique
Allowed stress corresponds to stress ratio specified in COPV Design Guidance Knock - down coefficients ki represent partial deteriorative influence of operational loading factors: repetitive/sustained Force (pressure), elevated Temperature, Humidity, Aggressive environment, and UV irradiation among possible others Safety factor is a function of design uncertainties: actual Operational conditions, imperfection of utilized computer Model, and scattering of Properties of a real material system utilized within COPV structure Guide for Building and Classing Naval Vessels, Part 1: Hull and Structures, Chapter 4: Composites, ABS, July 15, 2004 Smirnova, M.K., Paliy, O.M., Spiro, V.E., Principles of Strength Criteria Specification for Ship Structures of PMC, Mechanics of Polymer Materials, Riga, Latvia, March, 1984, p Proprietary

18 Structural Design Reconciliation Advanced Technique
Durability under assorted loading: for Pijk fraction of service exposure to ijk loading conditions (i - category of operational exposure regarding j - load case under k - temperature) Durability under ijk exposure in terms of Kinetic Theory of Fracture Accumulated micro-damage (deterioration) with Bailey’s Integral Proprietary

19 Fatigue data actual and standardized
Serviceability Assessment Technique Experimental Verification Fatigue data actual and standardized Actual loading: Single loading rates 0.3…13.0 MPa/s (43.5…885 psi/s) Cycling frequencies 0.03 … 0.50 Hz Maximal cyclic stress (0.6 … 0.8) SU Temperature … 30°C (66 … 86°F) Base-line loading: Cycling frequency 0.1Hz Stress range 0.1 Temperature 20°C (68°F) * - Lavrov A.V. and Shkolnikov, V.M., Experimental Research of Fatigue of Thick-walled PMC Structures, Structural Application of PMC, Russian Society of Naval Engineers, v. 510, St. Petersburg, Russia: 1991, p.4-15. Proprietary

20 Serviceability Assessment Technique Influence of Loading Waveform
Typical cyclic loading waveforms Glass FRP fatigue performance under Cycling frequency 0.1Hz Stress range 0.1 Proprietary

21 Burst pressure in function of loading profile & rate
Serviceability Assessment Technique Single (Burst Pressure) Loading Evaluation Burst pressure in function of loading profile & rate Proprietary

22 Serviceability Assessment Exemplified Operational Profiles
* Per CGA C-19 – FRP-3 – Guideline ** Once per week *** Fraction of service life (%) except as otherwise noted Proprietary

23 Serviceability Assessment Prorated Influence of Service Loading
Severe loading conditions Proprietary

24 Serviceability Assessment Prorated Influence of Service Loading
Mild loading conditions Proprietary

25 Serviceability Assessment Prorated Influence of Test Loading
* - Autofrettage pressure is included into all loading profiles and is referred as Load case #1 Per Test Protocol of CGA C-19 – FRP-3 – Guideline Proprietary

26 Serviceability Assessment Prorated Influence of Test Loading
Proprietary

27 Serviceability Assessment Prorated Influence of Test Loading
Proprietary

28 Serviceability Assessment Summary
* Continuous service with stress ratio δP = 3.5 ** To endure 30-year continuous service Proprietary

29 Serviceability Assessment Summary (continued)
Loading parameters significantly affect length of COPV service life and should be taken into account Notable mismatch between computed and specified stress ratios substantiates the need for improvement of the design methodology The nomenclature of design qualification tests should be selected corresponding to assigned COPV operation Not being reconciled against actual / assigned operational conditions COPV’s serviceability might be either greater or lower than required. Proprietary

30 Design Factor Specification
It is possible to specify the knock-down factors on a pro-rata basis employing the proposed serviceability assessment technique Safety factor should be added to cover the multiple uncertainties in loading parameters, PMC properties, and COPV computer modeling Safety margin should be aligned with a selected loading profile; when this is close to actual or anticipated loading conditions, the safety margin might be reduced. Proprietary

31 Conclusion Remarks The outlined technique meets the demand and is applicable regarding both operation and testing The technique is also capable to specify a testing protocol adequately to the required COPV durability and to support COPV health monitoring in service Dependable data on fatigue parameters of employed structural materials are needed to fulfill the serviceability assessments The technique will somewhat complicate the conventional design reconciliation procedure; however, this extra effort will be paid off with increased performance predictability and ensured operational safety. Proprietary

32 ACKNOWLEDGEMENTS The presented work is performed under R&D project sponsored by the U.S. DOE, award # DE- FC36-04GO14229. The sponsorship and guidance for this project provided by Monterey Gardiner and Paul Bakke of the DOE are gratefully acknowledged. The presented work has benefited from support of David K. Moyer and Eileen M. Schmura of CTC, former and current managers of the project, respectively. Proprietary

33 Thank you Questions / Comments?
CONTACT INFO: Dr. Vladimir M. Shkolnikov Tel: (814) Dr. Kevin L. Klug Tel: (910) Thank you Proprietary

34 Back-up Proprietary

35 Project Relevance Hydrogen Regional Infrastructure Program in Pennsylvania
Hydrogen Fuel Cells Infrastructure and Technology (HFCIT) Program Multi-Year Research, Development and Demonstration Plan (MYRD&DP)

36 COPV-3 Prototype The selected COPV-3 has an aluminum (6061-T6) liner fully wrapped by fiber/epoxy PMC. The intermediate modulus Toray T K carbon fiber is chosen for PMC wrapping jacket. Proprietary

37 COPV-2 Prototype Commercial grade Toray T700 12K and Epon 828, an epoxy resin were selected for the PMC jacket. High strength chromium molybdenum steel (34CRM04) alloy is the liner’s material. Proprietary


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