boce propan-butan

Executive Summary Background: In 2004, the first US DOT exemptions were issued to bring composite cylinders to the US marketplace. The cylinders have been used successfully in Europe for many years in many applications. However, a working group of the National Propane Gas Association (NPGA) identified many differences between typical US and European applications and sought additional information on vaporization rates to insure the viability of composite cylinders for use in the United States. The intention of the project was to obtain a baseline comparison of vaporization rates at fixed conditions for composite, steel, and aluminum nominal 20-lb cylinders currently available on the US market. With the assistance of the principal investigator (Petersen Engineering), the task force developed a method of test in accordance with ANSI style and format to measure the ability of a container to conduct heat from the ambient to the liquid portion of LP-Gas to prolong the availability of LP-Gas vapor at a pressure that is suitable for the application. The NPGA working group then set out to establish the specific conditions that would yield the pertinent information for the test cylinders. These conditions include ambient temperature, relative humidity, cylinder fill level, and BTU draw rate. The specific conditions were selected to provide data at real-life conditions for a typical US application, outdoor cooking on a large barbecue grill in a moderate to cold climate. Testing: Tests were conducted on four cylinders, of varying construction, to determine their relative ability to supply LP-Gas at a constant flow rate. Tests were conducted at prescribed ambient temperatures, initial charge, and flow rates. Data were recorded at regular intervals; cylinder pressure, LP-gas temperature as well as pressures and temperatures associated with the flow through fixed orifices. Cylinder pressure and temperature were charted. Conclusions based on testing:

The purpose of the test was to measure the ability of a container to conduct heat from the ambient to the liquid LP-gas by correlating it with the interval of time at a constant withdrawal rate to reach a vapor pressure level (15 psig) identified as being unable to support most US applications at constant ambient conditions. In all tests, the aluminum cylinder (propane charge 9.5 lbs) maintained a higher vapor pressure level for the longest period of time. The linerless composite cylinder (propane charge 9.1 lbs) had the shortest interval to the 15 psig termination point, partially due to the lower initial charge.

In the 60 F tests, the lined composite cylinder (propane charge 10.6 lbs) mimicked the steel cylinder (propane charge 9.5 lbs) performance almost exactly, with averaging less than 1% difference in performance. The differences between the lined composite and steel cylinders were more pronounced in the 30 F tests, with approximately 15%

Executive Summary difference in the total time to reach the 15 psig threshold, with the lined composite cylinder providing more prolonged availability of LP-gas vapor.

Additional comments from Petersen Engineering: In interpreting the results, consideration needs to be given to the slightly different initial charges; based on 20% of the water capacity. The greater initial mass of LP-Gas in the larger cylinders will naturally prolong their ability to deliver vapor. After an initial review, the task force requested a statement of performance based on a normalized charge; relating the results as if the cylinders had the same mass charge rather than a charge based on 20% of water capacity. Appendix I was amended to include a calculation; adjusting the minutes of withdrawal, assuming a 10 pound charge. The average minutes to vaporize LP-Gas at 80,000 BTU/HR for a 10 pound charge are;

Temperature 60F 30FSteel 57 29

Aluminum 64 32 Lined Composite 52 31

Linerless Composite 47 27 Others should be able to repeat the results if they utilize the same equipment and test protocol – including the test environment within another closely controlled ‘outer environment’. This two shell environment simplified the temperature control at the test cylinders. Instrumentation and data recording methods can be varied without sacrificing the end results; however, data interpretation is easier if the data are collected automatically. A variation of the test protocol would be a relative comparison of a ‘Subject’ cylinder to a ‘Reference’ cylinder; varying materials of construction, container size or charge. This would require the ‘Subject’ and ‘Reference’ cylinders to be tested at the same time and in the same environment. The environment would not have to be controlled, (although it should be recorded). This approach would be practical if particular appliances were a part of the test.

Petersen Engineering

Petersen Engineering [email protected] 3115 Pine Street (903) 793-8581 Texarkana, TX Fax – (630) 282-0587

The Comparative Vaporization Rates of Composite, Steel, and

Aluminum Grill Cylinders

The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill Cylinders

Table of Contents

Item Page1

Executive Summary 1Report: Introduction 5 Description of the tests 5 Pertinent data for the containers 6 Target pre-determined flow rate and ambient temperature 6 Piping schematic 6 Equipment description (other than piping) 6 Photographic documentation of test apparatus 8 Recorded data and calculated flow rate at timed intervals 8Appendices: Appendix A; NPGA letter describing test requirements 9 Appendix B; Test procedure 17 Appendix C; Orifice calibration 19 Appendix D; Container descriptions 24 Appendix E; Piping schematic 25 Appendix F; Data acquisition channel assignment and pressure transducer description 27 Appendix G; Photo log of test equipment and test setup 28 Appendix H; Collected data and flow calculations 45 Appendix I; Summary of test results 65 Appendix J; Charts of pressure data 66 Appendix K; Charts of temperature data 70

1 Page number refers to overall page number. Individual reports or appendices may have individual page numbers.


Page 1 of 4

Introduction

Tests were conducted on four cylinders, of varying construction, to determine their relative ability to supply LP-gas at a constant flow rate. Tests were conducted at prescribed ambient temperatures, initial charge and flow rates. Data were recorded at regular intervals; cylinder pressure, LP-gas temperature as well as pressures and temperatures associated with the flow through fixed orifices. Cylinder pressure and temperature data were charted.

Description of the tests.

The test parameters were described in a letter from the NPGA, dated December 11, 2004; copy attached as Appendix A. Basic requirements were described in the Test Method for Determining the Vaporization Capacity of an LP-Gas Container standard.

In brief, the tests were conducted at 60F and 30F. The cylinders were charged, by weight, to 20% of their water capacity – slightly less than half of their maximum allowable charge of 42%. LP-gas was withdrawn at a flow rate equal to 80,000 BTU/Hr. The tests were stopped when the individual cylinder vapor pressures dropped to 15 PSIG. After completing the withdrawal, the cylinders were allowed to recover to an ambient condition. Weight, pressure and temperature were recorded at the stabilized (final) condition. The data were reviewed to verify compliance with the test requirements. Each test was conducted twice to verify repeatability (4 tests total). Data were recorded every 30 seconds, using a data acquisition system; 9 channels for temperature and 12 channels for pressure. Type K thermocouples were used to record temperature. Pressure transducers were used to record pressure. Analog pressure gauges were used for setup and to monitor the test. A more extensive equipment description is included in this report, below. The test procedure is described in Appendix B. This procedure reflects the particular method and equipment used. Fixed orifices were used as flow control elements. Each orifice was calibrated using a positive displacement meter; with a regulated inlet pressure flowing through the orifice, into the meter and out to the atmosphere. Orifice calibration test results are attached as Appendix C. Each fixed orifice had a flow rate corresponding to inlet pressure, temperature and pressure drop. Actual regulator and orifice differential


Page 2 of 4

pressures as well as orifice inlet temperature were used to calculate the deviation from target flow rates. Corrections were based on ideal gas laws and defined on the first page of Appendix C (bottom). The correction limits, per the test protocol, was 0.95-1.05 (1.00 infers no correction). Test data were reviewed with the calculations performed for each set of data (2/Min.).

Pertinent data for the containers

Containers were obtained from four manufacturers. The two metal containers were 47.6 pound water capacity (21.6 L); or nominal 20 pound LPG cylinders. The lined composite cylinder was slightly smaller, 45.5 pound water capacity (20.7 L). The linerless composite cylinder was larger; 52.9 pound water capacity (marked 24 L). A more extensive description is attached on Appendix D. Dimensional data for the metal cylinders were taken from the manufacturer’s web sites. Some dimensional data for the composite cylinders was obtained from the manufacturers or their web site. Other dimensional data was taken directly from exemplar composite cylinders (e.g. wall thickness).

Target pre-determined flow rate and ambient temperature

The target flow rate was 80,000 BTU/Hr. Assuming 2,516 BTU/FT³, this equates to 37.8 FT³/HR at standard temperature (60F) and pressure (atmospheric). Tests were conducted with a 60F and 30F ambient temperature. Each test was conducted twice to insure repeatability.

Piping schematic

A piping schematic is shown on Appendix E. This schematic does not describe instrumentation connections or the environment for the test (see below).

Equipment description (other than piping)

The outer environment for the cylinders consisted of a room, approximately 12’ by 24’. The room was well insulated and sealed except for two access doors. The temperature for this room was controlled via conventional HVAC controls (only AC was used) with 60F as the control temperature for all tests. The inner environment consisted of a walk-in freezer; nominally 6’ by 6’, interior dimensions – 5’ 2” by 5’2” with a 5’ 11” ceiling. Use of the freezer for the 60F tests (door open & freezer not operating) dampened temperature swings associated with normal temperature control cycling.


Page 3 of 4

The 30F tests were conducted with the freezer temperature set at 30F (and the outer environment still at 60F). The freezer was subdivided (top & bottom), separating the cylinders from the recirculating fan; again to dampen temperature swings due to temperature control cycling. A heater, in the form of four 100 watt light bulbs, was used as a heater; cycled to offset the localized cooling/refrigeration due to vapor withdrawal from the cylinders. The LPG vapor and instrumentation lines exited the freezer via a small conduit to the outer environment. Thermocouple lines went directly to the data acquisition unit. Vapor pressure lines went to pressure transducers which, in turn sent voltage signals to the data acquisition unit. The data acquisition/switch unit was an Agilent Technologies 34970A. Thermocouple leads and pressure transducer voltages were gathered into two HP34901A twenty channel MUX with T/C compensation. The 34970A would record data every 30 seconds; switching across the channels with ~12 milliseconds between channels. Actual time stamps for each individual recording are included in the raw data. As indicated above, thermocouple leads went directly to the MUX/switch unit since it has an internal reference and algorithm for temperature. The pressure transducers output was a voltage signal; nominally 0.5-5.5 volts DC – for a zero to full scale pressure input. Each transducer was calibrated against a ‘master’ gauge, and re-zeroed before each test. A more complete description of the channel assignment and pressure transducers is included in Appendix F. Transducer gain and offset values for each test is included in the appendix. Four sets of analog pressure gauges were used for monitoring the tests. These gauges were not used for data acquisition. Each set of gauges consisted of;

• WIKA Type 111.25, 4½ ” gauge, 0-160 PSIG (for cylinder pressure) • Magnehelic 0-15” WC gauge (for regulator pressure) • Magnehelic 0-2” WC gauge (for back pressure after the orifice)

‘Master’ gauges used for calibrating the pressure transducers;

• Heise 901A, 400 PSIG x 0.1, S/N S9-20659 (for cylinder pressure transducers)

• Dwyer 475-1 Digital Manometer, 20" WC x 0.01, S/N N21G51 (for regulator & orifice dP pressure transducers)

Electronic scale used to determine pre/post gross cylinder weight and tare weight; Mettler Toledo, Model 8213, S/N 2872919-2XW, 100 LB x 0.02.

Appendix A Page 1 of 8

December 14, 2004 Mr. James A. Petersen Petersen Engineering 3115 Pine Street Texarkana, TX 75503-4041 Dear Jim: The National Propane Gas Association (NPGA) invites you to bid on a project to determine the comparative vaporization rates of composite, steel, and aluminum grill cylinders as outlined herein. Bid packages are due to the NPGA no later than February 28, 2005. As you may know, several manufacturers anticipate the release of composite cylinders on the US market by the end of 2004. At this time, NPGA does not feel there is sufficient information about the performance of these cylinders to fully understand the market potential. The intention of this project is to obtain a baseline comparison of vaporization rates at fixed conditions for composite, steel and aluminum nominal 20-lb cylinders on the US market. NPGA has established interest from the Propane Education and Research Council for this work, and intends to present a formal funding request for the winning bidder. Scope of Work: The successful bidder will provide a complete report of testing in accordance with the draft method of test provided by NPGA and as modified herein.

1. Ambient Temperature at start of test (including stabilization period as required in Section 11 of the draft test method)

a. 30° ± 2° F b. 60° ± 2° F

2. Relative Humidity – The relative humidity level shall be recorded at the start of the test and controlled to within ± 10% of its initial value for the duration.

3. Cylinder Fill Level at start of test – 20% of stated water capacity for each cylinder. Cylinders must be filled from the same source tank to avoid any difference in propane composition between the cylinder contents.

4. Initial BTU draw rate – 80,000 BTUH ± 5% 5. Cylinders to be tested

a. Steel b. Aluminum c. Lined Composite cylinder d. Linerless Composite cylinder


6. Number of tests – Each cylinder shall be tested twice at each condition and shall be evacuated between tests such that the cylinder weight is within 1% of its initial tare weight established prior to testing.

7. Valves and Connections – The test cylinders shall be tested with non-OPD, POL outlet valves.

8. Data recording – Data shall be recorded at intervals no greater than 5 minutes.

9. End pressure level – The tests shall be terminated when the vapor pressure reaches 15 psi. Each cylinder shall be weighed at the conclusion of the test to determine the approximate amount of fuel remaining in the cylinder. The final weight and estimated amount of fuel remaining shall be included in the final report for each test.

The Bid Package: The bid package should be submitted in both hard copy and electronic format, and should include: 1. Statement of Project: Background information, anticipated results, identification and qualifications of essential personnel, status of essential personnel (employee, consultant or contractor to winning bidder). The project statement should demonstrate that the bidder has a firm understanding of the scope and intent of the project. 2. Projected Timeline: Commencement date, completion date, key project stages and activities, final report due date. 3. Budget and Statement of Costs: direct costs, salaries, overhead, and subcontractor costs, fees, and expenses. Once a bidder has been selected by the NPGA , the bid package will be expanded and submitted by NPGA to the Propane Education and Research Council Research and Development Advisory Committee (RDAC) as a formal funding request on behalf of the winning bidder. If you need further information on the project or bid package, please feel free to contact me at (202) 466-7200 or [email protected]. Best Regards,

Denise Beach Codes & Standards Engineer


Test Method for Determining the Vaporization Capacity of an LP-Gas Container ASTM D XXXX-YY 1. Scope

1.1 As LP-gas is utilized from a container, the remaining liquid cools due to vaporization. This test method is a measure of the ability of a container to conduct heat from the ambient to the liquid portion of LP-gas to prolong the availability of LP-gas vapor at a pressure that is suitable for the application.

1.2 This standard is limited to natural convection heating from the ambient and the conduction of that heat to the LP-gas liquid. It does not address forced air convection or radiation heating.

1.3 This method may be used to compare containers of different materials as well as geometries; size and shape.

1.4 The values stated in SI units are to be regarded as the standard. The values given in parentheses are for information only.

1.5 This standard does not purport to address all of the safety concerns associated with its use. It is the responsibility of the user of this standard to establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use. 2. Reference Documents

2.1 ASTM Standards: D 1835 Standard Specification for Liquefied Petroleum (LP) Gases D 2598 Standard Practice for Calculation of Certain Physical Properties of

Liquefied Petroleum (LP) Gases from Compositional Analysis [add reference standards for temperature and humidity measurement]

2.2 Other Documents: US DOT regulations; 49 CFR § 178, Specifications for Packagings ASME Boiler & Pressure Vessel Code

3. Terminology

3.1 Vaporization – When used in this standard, vaporization means the transition from liquid to vapor at saturated conditions.

3.2 Vaporization capacity – When used in this standard, vaporization capacity means the ability to vaporize liquid at a pressure usable for a particular application.

3.3 LP-gas – liquefied petroleum gas. Commercial propane or butane consisting mostly propane or butane as well as minor amounts of other LP-gases (See ASTM D 1835 and Section 7).

3.4 Container – When used in this standard, container means a pressure vessel suitable for commercial propane. Typically, these containers are designed and manufactured to the requirements of 49 CFR § 178 or the ASME Boiler & Pressure Vessel Code.


4. Summary of Test Method 4.1 LP-gas is withdrawn from a charged container, in a constant

temperature environment, at a pre-determined flow rate. The LP-gas vapor pressure is recorded at regular intervals until it drops to a predetermined value. 5. Significance and Use 5.1 LP-gas containers are manufactured utilizing a variety of materials and geometries. This method will provide a basis for modeling (predicting) the capability of a particular container design to vaporize sufficient vapor for a particular application. 5.2 Vaporization tends to reduce the temperature and vapor pressure of the remaining LP-gas. When the temperature of the remaining liquid is less than the environment, heat is conducted through the container walls and into the liquid. 5.3 This heat transfer from the ambient will somewhat counter the heat loss due to vaporization. The heat transfer from the ambient is limited by the temperature differential, wetted area of the container and the ability of the container shell to conduct heat. 5.4 When a container with insufficient vaporization capability is used, the available vapor pressure drops quickly and limits the time for a particular application; heating, cooking etc. 6. Apparatus 6.1 General – Since the test involves the withdrawal and measurement of LP-gas, the apparatus shall be suitable for LP-gas at the pressures involved.

6.2 Test Room – A room or chamber capable of maintaining a constant temperature, ± 2 °C (±3.6 °F), throughout the duration of the test. The test room shall be of sufficient size to allow at least .15 m (6.0 in.) from the outside of the test container(s) to any exterior wall and .3 m (12 in.) between containers. The surface in contact with the base of the test container shall be non-conducting (e.g. wood). Normal lighting, that does not radiate significant heat to the container, may be used for illumination. HVAC ducting shall not direct forced air onto the test container. 6.3 Thermometer – Any thermometer, thermocouple or other means capable of measuring temperature from -40 to 40 °C ±1 °C (-40 to 104 °F ±1.8 °F) throughout the duration of the test. 6.4 Pressure Gauge – Any pressure sensing device capable of measuring pressure from 0 to 1724 kPa gauge, ± 14 kPa (0 to 250 psig ±2 psi) throughout the duration of the test. 6.5 Flow Meter – Any means of determining a flow rate at ± 5% of the predetermined flow. The apparatus may be; fixed orifice, variable area flowmeters, mass flowmeters, positive displacement meters, scales or other means giving appropriate results. 6.6 Hygrometer – Any means of measuring the relative humidity of the ambient at the test temperature.


6.7 Piping – The piping shall be sized to prevent undue restriction at the vaporization flow.

6.8 Test container – The subject container for the test. 7. Materials 7.1 Commercial LP-gas, with a minimum propane content of 95%, shall be used for the test.

7.2 If the makeup (fractional composition of LP-gases) is not determined, the pressure/temperature shall be recorded before and after the test (See Calibration and Procedure below).

7.3 The pressure/temperature relationship of the LP-gas shall reflect a mixture with a pressure not more than an equivalent 95% propane – 5% ethane mixture nor less than a 95% – 2.5% butane mixture. 8. Hazards 8.1 Refillable LP-gas containers are typically prohibited from indoor utilization1. LP-gas containers utilize pressure relief devices that will vent flammable gas in the event of an overpressure situation – such as from a fire. This vented gas can contribute significant fuel to a preexisting fire.

8.2 It is assumed the procedure will include the burning of LP-gas outside of the test room. Since the procedure withdraws flammable gas from the container and through measurement apparatus, appropriate means shall be in place to prevent the unexpected ignition of fugitive gas. 9. Preparation of Apparatus

9.1 Test Room – the temperature of the test room shall be set and allowed to stabilize for 6 hours before the test.. A schematic of the test room shall be included in the Report. A typical schematic is shown in Appendix B.

9.2 Piping schematic – a piping schematic shall be prepared to describe the arrangement of devices and fittings. This schematic shall be included in the Report. A typical schematic is shown on Appendix A.

9.3 Thermometer – LP-Gas temperature measurement shall be in the liquid, in a thermo well (in the liquid) or insulated and outside the base of metal containers. Alternately, LP-Gas temperature may be inferred from a pressure/temperature relationship, as described in 10.1 below.

9.4 Pressure gauge – Vapor pressure will be measured at the container service valve outlet, before any pressure regulation or significant restrictions. The pressure tap shall be designed such that flow will not bias the pressure measurement.

9.5 Flow meter – In-line flow measurement devices may be placed anywhere in the piping; assuming there are no branches in the piping. If a fixed orifice is used, it shall be pre-qualified at the starting test conditions using LP-Gas vapor.

9.6 Test Container –

1 See NFPA 58 for exceptions.


9.6.1 Record pertinent data. Pertinent data for the test container shall include2;

Manufacturer Model or part number Serial number Manufacture date Container class and pressure designation, (e.g. DOT 4BA240) Container material(s) Container outside diameter, height and end configuration (e.g.

spherical or elliptical) Container shell thickness Tare weight (TW) Water capacity (WC) Service valve manufacturer, model and manufacture date3

9.6.2 Charge the container with LP-gas, noting the final gross weight. In no event shall a container be charged with more than 42% of its water capacity, by weight. 10. Calibration

10.1 LP-gas pressure/temperature relationship. If the construction or material of the test container make direct temperature measurement impractical, a pressure/temperature relationship may be utilized; based on the fractional composition of the LP-gases or the stabilized pressure/temperature relationship before and after the test (average). If used, calculations of the pressure/temperature relationship shall be part of the Report4.

10.2 Flow meter. If direct reading flowmeters are not utilized, flow measurement may be based on some combination of fixed restrictions, pressure, mass or volume over time. The combination must be adequately described in the Report so that it can be recreated. Calibration tests must be included in the Report. 11. Conditioning 11.1 Before the test, allow the temperature of the charged container to stabilize at the specified test room control ambient temperature. Record the pressure at the stabilized temperature. Container(s) shall not be placed closer than 0.15 m (6.0 in.) from any exterior wall and not closer than .3 m (12 in.) from each other. 12. Procedure

12.1 Before commencing the test, initial conditions to be recorded include; LP-gas vapor pressure Ambient temperature

2 Manufacturer’s drawings may be referenced for pertinent container information 3 In consideration of high flow rates during the test, the service valve may be replaced with a service valve having a minimum passage diameter not exceeding 7.9 mm (0.312 inch) 4 See ASTM D 2598


LP-gas temperature (if practical; see 10.1 above) Relative humidity Initial weights and pressures associated with flow rate

measurement 12.2 Initiate the pre-determined flow and record at regular intervals;

LP-gas vapor pressure Ambient temperature LP-gas temperature (if practical; see 10.1 above) Container weight if used for flow rate

12.3 Record visual observations on frost formation, including time when frost is first observed, approximate frosted surface area at regular intervals

12.4 Stop the test when vapor pressure drops to a predetermined level and record final values for:

LP-gas vapor pressure Ambient temperature LP-gas temperature (if practical; see 10.1 above) Relative humidity

12.5 Note variations in flow rate measurements if/when they occur 12.6 At the conclusion of the test, allow the container to stabilize in temperature and record the pressure (see 10.1 above) and gross weight of the container, ensuring that the container is free of condensate and frost. 13. Calculation or Interpretation of Results 13.1 Conversion from mass flow rate to volumetric flow rate at Standard Temperature and Pressure5 (STP) is as follows6: 1 Kg/Hr = 0.527 m³/Hr at STP or (1 Lbm/Hr = 8.45 Ft³/Hr at STP) or

1 Kg/m³ = 0.0624 LBm/Ft³ 13.2 Interpretation shall be limited to noting comparison of one container’s vaporization capacity to another. 14. Report

14.1 The report shall include; Description of the test, including reference to this standard and any

deviations from the standard. Pertinent data for the container from 9.6.1 Target pre-determined flow rate Target ambient temperature Piping schematic Equipment description Photographic documentation of test apparatus Recorded data as required in Section 12 at timed intervals Calculated or measured flow rate at timed intervals

5 STP conditions: Temperature = 15.5 C (60F) and Pressure = 101.3 kPa (1 atm, 14.7 psia, 0 psig) 6 The conversion is based on pure propane and considered sufficiently accurate.


15. Precision and Bias [under revision]

15.1 Precision – The following criteria should be used for judging the acceptability of results (95% confidence): 15.1.1 Repeatability – the difference between two test results obtained by the same operator with the same apparatus under constant operating conditions on identical test cylinders would in the normal and correct operation of the test method, exceed the following value only in one case in twenty: Time; 5% norm 15.1.2 Reproducibility – the difference between two single and independent results obtained by different operators working in different locations on identical test cylinders and using identical LP-gas would in the long run, in the normal and correct operation of the test method, exceed the following value only in one case in twenty: Time; 10% norm 15.2 Bias – The test for vaporization capacity is useful as a basis for predicting how a container will perform in conditions that would seldom be the same as the test conditions. There is no acceptance criteria for vaporization capacity, hence bias is not a consideration.

16. Keywords 16.1 vaporization; vaporization capacity; LP-gas; propane; butane; container; heat transfer; convection; temperature; pressure; flow

NPGA Vaporization Study Test Protocol

Appendix B Page 1 of 2

The procedure below reflects the test requirements described in the NPGA letter, (noted below as ‘Ltr.’), dated December 14, 2004, for the vaporization study. Within the Letter, reference is made to a proposed standard, (noted below as ‘Std’). Activities are divided as follows;

• Test room preparation. • Cylinder preparation • Test procedure • Documentation and report of test

Test room preparation:

1. Assemble cold environment room. 2. Test environment temperature controls. 3. Assemble analog gauge bank 4. Assemble pressure transducer bank 5. Assign data recording channels (P & T) 6. Calibrate pressure transducers 7. Assemble gas piping for calibration 8. Calibrate fixed orifices 9. Document fixed orifice calibration 10. Assemble & leak test gas flare piping;

o Vapor pressure line; cylinder to pressure regulator o Temperature regulation piping; heat sink o Regulator & orifice piping; regulator to orifice, including

thermocouple o Line to flare stand; poly line o Flare stand; ball valve & flare pipe mounted on stand

Cylinder preparation:

1. Receive cylinders 2. Record marked cylinder data. [Std. 9.6.1] 3. Refit cylinders with thermocouple equipped service valves. 4. Weigh cylinders to determine new tare weight. 5. Pressurize cylinders to verify pressure integrity. 6. Purge air from cylinders to < 2.5%.

Test procedure:

1. Fill cylinders to 100-110% of pretest gross weight; 20% of WC. [Letter, Scope item 3]

2. Weigh cylinders. 3. Adjust cylinder weights to pretest gross weight, ±1%. [Letter Scope, item

3] 4. Place cylinders in environment. 5. Connect cylinders to piping. 6. Connect thermocouples. 7. Connect vapor pressure taps to analog gauges.

NPGA Vaporization Study Test Protocol

Appendix B Page 2 of 2

8. Open cylinder service valves. 9. Verify instrumentation & pressure connections. 10. Verify cylinders are at prescribed initial temperature. 11. Record initial relative humidity, % & ambient temperature. 12. Begin data recording; 2/Min. [Ltr. Item 8] 13. Initiate flow; 80,000 BTUH, (32 SCFH). [Ltr. Item 3] 14. Ignite gas at flare. 15. Monitor cylinder vapor pressure. 16. Stop flow from individual cylinders when vapor pressure drops to

predetermined level; 15 psig. [Ltr. Item 9] 17. Stop data recording when the vapor pressure from all cylinders has

dropped to predetermined level. [Ltr. Item 9] 18. Record final relative humidity, %. [Std. 12.4] 19. After cylinders have stabilized in temperature, (within 1° F of ambient),

record vapor pressure. [Std. 12.6] 20. Close cylinder service valves. 21. Remove thermocouples & instrumentation connections from cylinders. 22. Disconnect piping from cylinders. 23. Weigh cylinders with residual gas. [Std. 12.6] 24. Empty cylinders. 25. Weigh empty cylinders. [Ltr. Item 9] 26. Verify final tare weight of cylinders is within 1% of initial tare weight. [Ltr.

Item 6] 27. Repeat test as required in NPGA Letter. [Ltr. Item 6]

Documentation and report of test:

• Determine weight of gas vaporized during test (initial weight minus final weight).

• Download recorded data to PC. • Calculate vapor withdrawal at intervals to verify target draw ± 5%. [Ltr.

Item 3] • Note any deviations from test protocol. • Prepare Piping schematic. [Std. 9.2] • Prepare report. [Std. 14]

Orifice calibration

Reference:Crane Flow of Fluids Through Valves, Fittings, and Pipe. Technical Paper No. 410 , 18th Printing -- 1979 (page 3-5)

For compressible flow:q’h = 24,700 Y (d1

2 C)/S g (SQRT(∆P ρ1))q’h -- rate of flow, in cubic feet per hour at standard conditions (14.7 psia and 60F)

Y -- net expansion factor for compressible flow through orificesd1 -- internal diameter of orificeC -- flow coefficient for orifices and nozzles

S g Specific gravity of a gas relative to air @ STD= M/29 = 44/29 = 1.52

∆P -- differential pressure across orificeρ1 -- density of gas, pounds per cubic foot (orifice inlet)

Using test data, (a), to correct to target flow rate, (b);∆Pb = ∆Pa ÷ (q’ha ÷ q’hb)2

q’hb = 80,000 ÷ 2516 = 31.8 SCFHc3h8

Orf # ∆Pb ∆Pa q’ha q’hb Avg.4101 11.09 12.76 34.1 31.84101 10.50 9.85 30.8 31.84101 11.34 10.50 30.6 31.84102 14.08 12.45 29.9 31.84102 14.53 11.84 28.7 31.84103 11.54 11.98 32.4 31.84103 11.55 12.90 33.6 31.84104 14.07 12.52 30.0 31.84104 13.88 11.86 29.4 31.8

Deviation from ideal flow based on test data, (based on ideal gas);

q'htest/q'h = [(∆PORF-test / ∆PORF )*((PREG-test+406.78)/(PREG+406.78)*(520/(TR-test+460))]

10.977

14.303

11.545

13.971

Appendix C Orifice Calibration Summary

Orifice calibration

Equipment used:Orifice; Brass orifice; 1/8 NPT with a #41 hole. Marked "4101"

Pcyl; Heise 901A, 400 PSIG x 0.1, S/N S9-20659T; Fluke 52 II, S/N 77260153

Regul;ator; ECII Model 404B4 regulator, date code '09D97'P1; Dwyer 475-1 Digital Manometer, 20" WC x 0.01, S/N N21G51P2; Dwyer Magnehelic, 2003C, 3" WC x 0.1, S/N 40607NH22Q; Equimeter, Model S-275, S/N 6117609

Time: Radio Shack 'Sports', Catalog No. 63-5016 (stopwatch)Brass orifice; 1/8 NPT with a #41 hole.

Commercial LP-gas flowed through a fixed orifice6/12/2005 Run 1 6/12/2005 Run 2

Start End Avg. Start End Avg. Start End Avg.Pcyl 101 88 94.5 122 106.6 114.3 105.6 91 98.3Tcyl 79.1 70.8 75.0 70.8 62 66.4

Preg, IN WC 9.9 9.8 9.85 10.55 10.5 10.525 12.8 12.71 12.755Preg, psi 0.357 0.353 0.35524 0.380 0.379 0.37959 0.462 0.458 0.46001

Treg 60.3 53.5 56.9 78 66.9 72.45 74.8 68 71.4

ρlpg , lb/ft^3 0.122 0.114 0.115 (calc'd from ALLPROPS¹;P2 orifice IN WC 0.25 0.25 0.25 0.55 0.7 0.625 0.32 0.3 0.31ρlpg , lb/ft^3

@ STD 0.11834 (calc'd from ALLPROPS; f(p,T))S g 1.517

16-Feb-05time, sec 0 55 114 177 237 295 351 415 474 530 584time, Hr 0 0.01528 0.03167 0.04917 0.06583 0.08194 0.0975 0.11528 0.13167 0.14722 0.162222Cu. Ft. 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0Flow rate, q’h 32.7 31.6 30.5 30.4 30.5 30.8 30.4 30.4 30.6 30.8

6/12/2005 Run 1time, sec 0 61 123 180 234 295 357 413 467 529 589time, Hr 0 0.01694 0.03417 0.05 0.065 0.08194 0.09917 0.11472 0.12972 0.14694 0.163611Cu. Ft. 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0Flow rate, q’h 29.5 29.3 30.0 30.8 30.5 30.3 30.5 30.8 30.6 30.6

6/12/2005 Run 2time, sec 0 55 110 161 210 266 319 371 419 475 528time, Hr 0 0.01528 0.03056 0.04472 0.05833 0.07389 0.08861 0.10306 0.11639 0.13194 0.146667Cu. Ft. 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0Flow rate, q’h 32.7 32.7 33.5 34.3 33.8 33.9 34.0 34.4 34.1 34.1

16-Feb-05

¹ ALLPRPOPS Property Package, Version 6/4/96. Developed by the Center for Applied Thermodynamic Studies, University of Idaho. Moscow, ID 83844-1011. Program used to calculate gas density, based on temperature and pressure. Thes values are used in flow corrections described in the first page of this Appendix.

Appendix C Orifice for Cylinder 1 4101

Orifice calibration

13-Jun-05



Regul;ator; ECII Model 404B4 regulator, date code '09D97'P1; Dwyer 475-1 Digital Manometer, 20" WC x 0.01, S/N N21G51P2; Dwyer Magnehelic, 2001C, 1" WC x 0.02, S/N R80614RI126Q; Equimeter, Model S-275, S/N 6117609

Time: Radio Shack 'Sports', Catalog No. 63-5016 (stopwatch)

Commercial LP-gas flowed through a fixed orifice

Run 1 Run 2Start End Avg. Start End Avg.

Pcyl 117 99.5 108.25 98.3 81.4 89.85Tcyl 76.2 67.3 71.75 66.3 57.2 61.75

Preg, IN WC 11.89 11.78 11.835 12.47 12.42 12.445Preg, psi 0.429 0.425 0.42683 0.450 0.448 0.44883

Treg 79 69 74 70 68 69

P2 orifice IN WC 0.25 0.25 0.25 0.25 0.25 0.25 Brass orifice; 1/8 NPT with a #41 hole.ρlpg , lb/ft^3

@ STD 0.11834 (calc'd from ALLPROPS¹; f(p,T))S g 1.517

Run 1time, sec 0 66 131 192 249 315 280 440 498 563 628time, Hr 0 0.018333 0.03639 0.05333 0.06917 0.0875 0.07778 0.12222 0.13833 0.15639 0.1744444Cu. Ft. 0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0Flow rate, q’h 27.3 27.5 28.1 28.9 28.6 38.6 28.6 28.9 28.8 28.7


¹ ALLPRPOPS Property Package, Version 6/4/96. Developed by the Center for Applied Thermodynamic Studies, University of Idaho. Moscow, ID 838441011. Program used to calculate gas density, based on temperature and pressure. Thes values are used in flow corrections described in the first page of this Appendix.


Orifice calibration

13-Jun-05






Run 1Start End Avg. Start End Avg.

Pcyl 85.2 68.8 77 67.3 54.1 60.7Tcyl 58.8 49.1 47.7 36.4 42.05

Preg, IN WC 12.9 12.9 12.9 12 11.95 11.975Preg, psi 0.465 0.465 0.46524 0.433 0.431 0.43188

Treg 75.7 70 72.85 70 70 70Brass orifice; 1/8 NPT with a #41 hole.

P2 orifice IN WC 0.25 0.3 0.275 0.28 0.28 0.25ρlpg , lb/ft^3

@ STD 0.11834 (calc'd from ALLPROPS¹; f(p,T))S g 1.517





Orifice calibration

13-Jun-05






Run 1 Run 2Start End Avg. Start End Avg.

Pcyl 62.1 46.1 54.1 44.4 34.4 39.4Tcyl 43.3 33.3 38.3 32 23.7 27.85

Preg, IN WC 11.85 11.87 11.86 12.52 12.51 12.52Preg, psi 0.427 0.428 0.42773 0.452 0.451 0.451

Treg 68 74 71 75 75 75P2 orifice IN WC 0.25 0.25 0.25 0.25 0.25 0.25 Brass orifice; 1/8 NPT with a #41 hole.

ρlpg , lb/ft^3 0.122 (calc'd from ALLPROPS¹; f(p,T))ρlpg , lb/ft^3 @

STD 0.11834 (calc'd from ALLPROPS; f(p,T))S g 1.517





The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill CylindersCylinder data

Cylinder IdentificationGeneric designationModel or part numberSerial numbers H3946802 H3983372 055539C 055472C 000953372 000953376 000952066 000952470 4018705 4018193Manufacture date Aug-04 Sep-04Container class and pressure designation

Container material(s)

Container outside diameter, height and end configuration Container shell thicknessTare weight (TW) (marking as rec'd)Tare weight (TW) (actual w test valve) 18.04 13.68 12.62 12.78Water capacity (WC)Test charge (20% of WC) 9.5 9.5 10.6Target gross weight before test 27.5 23.2 23.2 21.9

52.9 (24 L)

11.7 (5.3 KG)18

47.6

13.6

47.6

0.078" Minimum (per spec) 0.140" Minimum (per spec)

Not indicated

10504

45.5

Jul-05Jun-05

Shell (measured): 0.15-0.21" wall Shell (measured): 0.18-0.30 wall

12.4

9.1

12.65" OD 17.98" OL Shell; 12.244"OD, 14.38" HT, Ellip. ends. Shell (measured):11.8"/12.3"/11.9" OD, 14.25" H

Cylinder 4Linerless Composite cylinder

LC-20

May-05

DOT E 13105-294

composite; undisclosed

Lined Composite cylinderCylinder 1 Cylinder 2 Cylinder 3

12.16" OD, 17.56" OL, 2:1 elliptical ends

12.25" OD 20.6" OAH, sherical ends Shell (measured): 11.4" OD 0.15-.21", 18.12" tall

DOT 4BA240

Steel

Steel

DOT 4E240

Aluminum

Aluminum

Composite; polymeric liner, filament wound fibre glass & resin shell, injection moulded outer casing

Appendix D

(1) (2) (3) (4) (5)

Cylinder and Valve

Valve Connection and Piezo Tap for Vapor Pressure

Line Exiting Freezer to Heat

ExchangerShutoff Valve at Heat Exchanger Heat Exchanger

30/60F Environment 60F Environment (Walk in Freezer) (Outer Room) (6)

Line to Regulator

(10) (9) (8) (7)Flare Stand Orifice Piezo Tap

Outdoors

Regulator & Piezo Tap Shutoff Valve & Fixed Orifice

Appendix E Piping Schematic Page 1 of 2

Vaporization StudyPiping SchematicItem No.

(1)

(2)

(3) Line Exiting Freezer to Heat Exchanger(a) PE tubing; 1/4" OD x 0.175" ID -- 15' long(b) End connections; 1/4" compression x NPT

(4)(5)

(e) ~ 5 gallons water -- heat source for cold vapor.(6) Line to Regulator

(a) PE tubing; 3/8" OD x 1/4" ID -- 10' long(b) End connections; 3/8" compression x NPT

(7) Regulator & Piezo Tap(a) Regulator: ECII Model 404B4, 2 stage regulator, 1/4" x 1/2"(b) 1/2 NPT short nipple(c) 1/2 Sch 40 tee, nylon(d) 1/2 x 1/8 NPT reducer, nylon(e) 1/8 MNPT x 1/8 Swagelok adapter (for 1/8 thermocouple probe)(f) 1/2 Sch 40 nipple, 12" long, PVC - drilled midway; 8 holes, 1/8' dia.(g) 1/2 repair (tee) coupling, PVC(h) 1/2 x 1/4 adapter, PE(i) 1/4 NPT x 1/4 tube (push in) connector (for regulator P tap)

(8) Shutoff Valve & Fixed Orifice(a) 1/2 NPT ball valve, 1/2 psi(b) 1/2 MNPT x 5/8" barb connector (~1/4" ID)(c) 1/4 x 1/8 NPT reducer(d) 1/8 NPT fitting -- drilled to #41 orifice (see orifice calibration Appendix D)(e) 3/4" OD - 5/8" ID vinyl tubing, ~2" long, (goes onto barbs & over orifice)

(9) Orifice Piezo Tap(a) 2 - 5/8" barb x 3/4" fitting, nylon(b) 2 - 3/4 NPT coupler, PVC(c) 3/4" Sch 40 nipple, 12" long, PVC - drilled midway; 8 holes, 1/8' dia.(d) 3/4" repair (tee) coupling, PVC(e) 3/4 x 1/4 NPT adapter, PE(f) 1/4 NPT x 1/4 tube (push in) connector (for orifice dP tap)

(10) Flare Stand(a) 25' - 3/4" OD x 5/8" ID vinyl tubing(b) 3/4 NPT ball valve, 1/2 ps(c) 4' - 3/4 Sch 40 steel pipe

(b) 2 - Flare connections; 1/2 NPT x 3/8 flare(c) 20' - 3/8"copper tubing, Type K (ends flared & coiled inside bucket)(d) 5 gallon plastic bucket & lid. Lid modified to accept flare fitting.

(f) Piezo liner; PE tubing -- 3/8" OD x 1/4" ID, 4 holes, ~1/16 dia. drilled midway.

Shutoff Valve at Heat Exchanger: Ball valve -- 1/4 NPS, 600 WOGHeat Exchanger(a) 2 - 1/2 FNPT elbows, brass

(a) Cylinder descriptions; see Appendix CCylinder & Cylinder Valve

(b) Valve; TWHC cylinder valve for 100# cylinder. Valve modified by adding 1/4" copper 'dip tube' -- sealed. Thermocouples inserted into copper tubing and crimped in place. Thermocouples used to monitor LPG liquid temperature.Valve Connection and Piezo Tap for Vapor Pressure

(e) 1/8 MNPT x 1/8 tube (push in) connector

(a) Commercially available soft nose POL with 0.25" Internal bore(b) 2 - 1/4" short brass nipples, Sch. 40, ~2" long(c) 1/4", Sch. 40, brass tee(d) 1/4 x 1/8 NPT adapter

Appendix E Piping Material List Page 2 of 2

Vaporization StudyData Acquisition Channel Assignment:

Agilent 34970A Data Acquisition / Switch Unit and 2 HP34901A 20 Channel MUX with T/C Compensation

HP 100 channelsCh. 101-109Channel Cyl. Recording Units Location

K T'couple; Chrom

el-Alumel

wire; 24 gauge

Internal to cylinder, ~1" from bottom

T'couple end

Twisted

Wire length to DA unit

20 Ft.

101 1 T F102 2 T F103 3 T F104 4 T F

K T'couple; Chrom

el-Alumel

wire; 24 gauge

Internal to cylinder, ~1" from bottom

Regulator outlet, internal to piping

10 Ft.

1/8" Dia.

Probe

Twisted

20 Ft.

105 1 T F106 2 T F107 3 T F108 4 T F109 Amb. T F Cyl. Area

HP 200 channels Excitation voltage; 13.91 VDC via RadioShack Power Supply Cat. No. 22-507Ch. 201-21222 gauge, stranded

Channel Cyl. RecordingOmega Press.

Transducer S/N Units Gain Offset Gain Offset Gain Offset Gain Offset201 1 PX242A-150G5V 16.14 -27.63 16.14 -27.63 16.14 -27.13 16.14 -27.53202 2 PX242A-150G5V 16.19 -27.15 16.19 -27.65 16.19 -27.05 16.19 -27.85203 3 PX242A-150G5V 16.29 -28.53 16.49 -29.11 16.49 -28.51 16.49 -29.11204 4 PX242A-150G5V 16.31 -28.67 16.31 -28.77 16.31 -28.57 16.31 -28.87205 1 162PC01G 0430364 3.200 -5.494 3.200 -5.494 3.200 -5.494 3.200 -5.494206 2 142PC01D 05134-26 3.103 -5.674 3.103 -5.674 3.103 -5.674 3.103 -5.674207 3 142PC01D 03153-113 3.134 -5.294 3.134 -5.294 3.134 -5.294 3.134 -5.294208 4 142PC01D 03153-083 3.141 -5.354 3.141 -5.354 3.141 -5.354 3.141 -5.354209 1 142PC01D 03153-085 3.135 -5.394 3.135 -5.394 3.135 -5.794 3.135 -5.394210 2 142PC01D 03153-029 3.146 -5.774 3.146 -5.774 3.146 -5.774 3.146 -5.774211 3 142PC01D 03153-030 3.137 -6.014 3.137 -6.014 3.137 -6.014 3.137 -6.014212 4 142PC01D 03153-042 3.145 -5.374 3.145 -5.374 3.145 -5.374 3.145 -5.374

Vapor

Pressure

Regulator

Pressure

Orifice

dP

30F Test25-Sep-05 27-Sep-05 17-Oct-05 19-Oct-05

PS

IGIN

W (Inches W

ater C

olumn)

K T'couple; Chrom

el-Alumel

wire; 24 gauge

60F Test

Regulator outlet, internal to piping

10 Ft.20 Ft.

1/8" Dia.

Probe

1/8" Dia. Probe

Appendix F


Appendix G Page 1 of 17

vap01.JPG Cylinders tested

vap02.JPG Composite cylinder shells



vap03.JPG Composite cylinder shells

vap04.JPG Cylinder 4 shell



vap05.JPG Cylinder 3 shell

vap05a.JPG Test valve with thermocouple connector



vap05b.JPG Test valve & OEM valve

vap05c.JPG Test valve & cylinder 3



vap06.jpg Test shed (outer room)

vap07.JPG Outer room, test setup



vap07a.JPG Scaling cylinder after test

vap08.JPG Cylinders located in walk-in freezer



vap09.JPG POL piezo connection

vap09a.JPG Lines & thermoucouples routed through freezer wall



vap09b.JPG Heat exchanger coil

vap10.JPG Analog gauges, heat exchangers & regulator board



vap11.JPG Data aquisition unit & analog gauge bank

vap12.JPG Rear connections to pressure transducers



vap13.JPG Pressure transducers

vap14.JPG Regulator & orifice bank



vap14a.JPG Flare stand

vap15.JPG Regulator, orifice & piezo pressure taps



vap16.JPG Piezo pressure tap

vap17.JPG Shutoff valve & orifice



vap18.JPG Shutoff valve & orifice

vap19.JPG Orifice located inside barbed fitting



vap20.JPG Orifice calibration setup

vap21.JPG Orifice calibration setup



vap22.JPG Test cylinders; ~20 minutes after completion of 60F test

vap23.JPG Frost lines on metal cylinders



vap24.JPG Frost line on Cylinder 1



101 (C)102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Time TimeMin Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Min Cyl 1 Cyl 2 Cyl 3 Cyl 40.0 60.9 60.2 60.8 61.0 59.1 58.9 59.5 59.7 61.6 0.0 95.7 95.4 98.9 97.90.5 60.6 59.8 60.6 60.7 57.7 57.3 58.6 58.4 61.5 0.5 88.6 87.8 91.9 89.81.0 60.4 59.8 59.5 60.4 56.4 56.4 57.5 56.9 61.6 1.0 86.3 85.4 89.8 86.71.5 59.8 59.2 58.8 59.8 55.4 55.5 56.4 55.9 61.6 1.5 84.7 83.9 89.4 84.62.0 59.4 58.8 58.5 59.3 54.9 54.9 55.7 55.3 61.6 2.0 83.6 82.7 88.6 83.02.5 58.6 58.2 58.0 58.3 54.2 54.4 55.1 54.7 61.6 2.5 82.6 81.7 87.7 81.63.0 58.3 57.7 57.3 57.9 53.9 54.0 54.6 54.3 61.7 3.0 81.6 80.8 86.9 80.33.5 57.7 57.2 56.8 57.0 53.4 53.6 54.1 53.9 61.6 3.5 80.7 80.0 86.0 80.44.0 57.1 56.7 56.3 56.4 53.2 53.6 53.8 53.6 61.7 4.0 79.8 79.2 85.1 79.74.5 56.4 56.0 55.8 55.6 52.9 53.4 53.4 53.4 61.7 4.5 78.9 78.4 84.2 78.85.0 55.9 55.7 55.1 54.8 52.7 53.2 53.1 53.3 61.9 5.0 78.1 77.7 83.3 77.55.5 55.2 55.1 54.7 54.1 52.5 53.0 52.8 53.1 61.8 5.5 77.3 77.0 82.5 76.46.0 54.6 54.6 54.2 53.5 52.4 52.9 52.7 52.9 61.9 6.0 76.4 76.3 81.6 75.26.5 54.1 54.0 53.6 52.7 52.3 52.7 52.4 52.7 61.8 6.5 75.6 75.5 80.8 74.17.0 53.5 53.5 53.1 52.1 52.2 52.6 52.3 52.6 61.9 7.0 74.8 74.7 80.0 73.17.5 52.9 53.0 52.5 51.2 52.0 52.3 52.0 52.4 61.7 7.5 74.0 74.0 79.1 72.18.0 52.2 52.6 52.1 50.6 52.0 52.3 51.9 52.3 61.7 8.0 73.1 73.2 78.3 71.08.5 51.7 51.9 51.5 49.9 51.7 52.0 51.6 52.1 61.6 8.5 72.2 72.5 77.4 69.99.0 51.0 51.6 50.9 49.3 51.7 52.0 51.6 52.0 61.6 9.0 71.4 71.6 76.6 69.29.5 50.3 50.7 50.3 48.3 51.5 51.7 51.3 51.8 61.5 9.5 70.5 70.9 75.8 68.410.0 49.9 50.5 49.7 47.6 51.4 51.6 51.3 51.7 61.5 10.0 69.8 70.2 75.0 67.410.5 49.0 49.6 49.2 46.8 51.3 51.4 51.1 51.6 61.3 10.5 68.9 69.5 74.3 66.611.0 48.6 49.5 48.6 46.1 51.2 51.4 51.0 51.5 61.3 11.0 68.1 68.9 73.4 65.611.5 47.6 48.5 47.9 45.2 51.0 51.2 50.8 51.3 61.2 11.5 67.2 68.2 72.6 64.912.0 47.3 48.3 47.5 44.6 51.1 51.2 50.7 51.4 61.1 12.0 66.4 67.4 71.8 64.412.5 46.6 47.5 46.9 43.7 50.9 51.0 50.6 51.3 61.0 12.5 65.5 66.6 71.0 64.213.0 45.9 47.1 46.5 42.9 51.0 51.0 50.6 51.2 60.9 13.0 64.7 65.9 70.2 63.913.5 45.1 46.4 45.6 42.0 50.8 50.9 50.3 51.1 60.9 13.5 63.9 65.3 69.4 63.614.0 44.7 46.0 45.3 41.2 50.9 50.9 50.3 51.1 60.8 14.0 63.1 64.8 68.5 62.914.5 44.2 45.4 44.6 40.3 50.8 50.8 50.2 51.0 60.8 14.5 62.2 64.2 67.8 62.215.0 43.7 45.0 44.1 39.6 50.8 50.8 50.1 51.0 60.7 15.0 61.5 63.4 67.0 61.415.5 42.9 44.4 43.4 38.7 50.7 50.7 50.1 50.9 60.6 15.5 60.7 62.7 66.2 60.516.0 42.2 43.6 42.7 37.8 50.6 50.6 50.0 50.8 60.5 16.0 59.9 62.1 65.3 59.616.5 41.5 43.4 42.3 37.1 50.7 50.6 50.0 50.9 60.4 16.5 59.1 61.4 64.5 58.817.0 40.8 42.7 41.7 36.2 50.6 50.5 50.0 50.9 60.4 17.0 58.3 60.7 63.8 57.917.5 40.3 42.2 41.1 35.5 50.8 50.6 50.0 50.9 60.3 17.5 57.5 60.0 63.0 57.018.0 39.7 41.7 40.5 34.7 50.7 50.6 49.9 50.8 60.4 18.0 56.7 59.3 62.2 56.118.5 38.9 41.1 39.8 33.8 50.7 50.5 49.9 50.9 60.3 18.5 56.0 58.7 61.5 55.319.0 38.3 40.6 39.4 33.1 50.8 50.7 50.0 51.0 60.4 19.0 55.2 58.1 60.7 54.319.5 37.4 39.9 38.7 32.2 50.9 50.6 50.1 51.1 60.3 19.5 54.4 57.4 59.9 53.420.0 37.0 39.5 38.2 31.4 51.0 50.8 50.1 51.3 60.4 20.0 53.6 56.9 59.2 52.420.5 36.4 39.0 37.6 30.5 51.0 50.8 50.2 51.4 60.4 20.5 52.9 56.3 58.3 51.621.0 35.6 38.4 36.9 29.7 51.2 50.9 50.2 51.4 60.5 21.0 52.1 55.7 57.6 50.721.5 35.3 37.8 36.4 29.0 51.4 51.1 50.4 51.6 60.5 21.5 51.4 55.0 56.8 49.922.0 34.6 37.2 35.8 28.0 51.5 51.1 50.4 51.8 60.4 22.0 50.6 54.4 56.0 49.022.5 33.8 36.8 35.2 27.1 51.6 51.2 50.5 51.8 60.5 22.5 50.0 53.8 55.3 48.023.0 33.2 36.2 34.7 26.5 51.8 51.4 50.7 52.0 60.6 23.0 49.2 53.2 54.6 47.223.5 32.6 35.7 34.0 25.6 51.8 51.4 50.8 52.2 60.6 23.5 48.5 52.5 53.8 46.324.0 31.8 34.9 33.3 24.7 51.9 51.5 50.9 52.3 60.6 24.0 47.8 51.9 53.1 45.424.5 31.2 34.4 32.8 23.9 52.2 51.7 51.1 52.5 60.6 24.5 47.1 51.3 52.3 44.525.0 30.5 34.0 32.1 23.0 52.3 51.9 51.2 52.6 60.6 25.0 46.4 50.8 51.6 43.6

Temperature, Degrees Fahrenheit Cylinder Pressure, PSIG

Appendix H-1 60 F 050925.xls Temperature and Cylinder Pressure Dta


101 (C)102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Time TimeMin Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Min Cyl 1 Cyl 2 Cyl 3 Cyl 4


25.5 30.2 33.5 31.5 22.2 52.5 51.9 51.4 52.8 60.6 25.5 45.7 50.1 50.9 42.726.0 29.3 32.8 31.0 21.3 52.6 52.1 51.5 53.0 60.7 26.0 45.0 49.6 50.1 41.826.5 28.7 32.5 30.3 20.3 52.7 52.2 51.6 53.2 60.6 26.5 44.4 49.0 49.4 40.927.0 28.1 32.1 29.8 19.5 52.9 52.4 51.9 53.4 60.8 27.0 43.7 48.4 48.7 40.027.5 27.4 31.5 29.1 18.6 53.0 52.5 51.9 53.4 60.8 27.5 43.0 47.9 47.9 39.228.0 26.7 30.6 28.5 17.7 53.2 52.6 52.0 53.6 60.8 28.0 42.4 47.3 47.2 38.328.5 26.1 30.1 27.9 16.9 53.4 52.8 52.2 53.9 60.8 28.5 41.8 46.7 46.5 37.429.0 25.3 29.8 27.2 15.9 53.5 52.9 52.2 53.9 60.9 29.0 41.1 46.2 45.7 36.629.5 24.9 29.2 26.7 15.2 53.7 53.1 52.5 54.3 60.9 29.5 40.5 45.6 45.0 35.830.0 24.2 28.8 26.0 14.1 53.9 53.2 52.7 54.3 60.9 30.0 39.8 45.1 44.3 34.930.5 23.5 28.2 25.4 13.1 53.9 53.2 52.8 54.5 60.9 30.5 39.2 44.5 43.6 34.131.0 22.7 27.6 24.9 12.4 54.2 53.4 53.0 54.7 61.0 31.0 38.6 44.0 42.8 33.231.5 22.1 27.2 24.1 14.0 54.2 53.6 53.1 54.9 61.0 31.5 37.9 43.5 42.1 32.432.0 21.3 26.8 23.6 10.6 54.6 53.8 53.4 55.1 61.1 32.0 37.3 42.9 41.4 31.632.5 20.9 26.1 23.0 9.5 54.7 54.0 53.5 55.3 61.0 32.5 36.7 42.4 40.7 30.833.0 20.1 25.7 22.2 8.5 54.9 54.1 53.7 55.4 60.9 33.0 36.1 41.9 40.0 29.933.5 19.5 25.1 21.7 7.6 55.0 54.2 53.8 55.6 60.9 33.5 35.5 41.4 39.3 29.234.0 18.7 24.6 20.9 6.5 55.1 54.3 53.9 55.8 60.8 34.0 34.9 40.9 38.5 28.434.5 18.1 24.2 20.4 5.7 55.3 54.5 54.1 55.9 60.8 34.5 34.3 40.4 37.9 27.635.0 17.6 23.5 19.7 4.8 55.3 54.5 54.1 56.0 60.6 35.0 33.7 39.9 37.2 26.835.5 17.0 22.9 19.0 3.8 55.3 54.5 54.2 56.1 60.6 35.5 33.1 39.3 36.5 26.036.0 16.2 22.3 18.5 2.9 55.4 54.6 54.3 56.1 60.5 36.0 32.5 38.8 35.9 25.336.5 15.4 21.7 17.7 1.8 55.4 54.6 54.4 56.2 60.5 36.5 32.0 38.3 35.2 24.537.0 14.9 21.6 17.0 1.0 55.5 54.7 54.5 56.3 60.4 37.0 31.4 37.8 34.5 23.737.5 14.2 20.6 16.3 -0.2 55.4 54.7 54.5 56.4 60.3 37.5 30.8 37.3 33.9 23.038.0 13.4 20.2 15.5 -1.2 55.5 54.7 54.6 56.4 60.1 38.0 30.2 36.8 33.3 22.238.5 12.9 19.7 15.1 -2.1 55.6 54.7 54.7 56.5 60.0 38.5 29.6 36.3 32.6 21.539.0 12.1 19.2 14.2 -3.2 55.6 54.8 54.7 56.5 59.9 39.0 29.1 36.0 32.0 20.839.5 11.4 18.6 13.6 -4.3 55.5 54.7 54.6 56.5 59.7 39.5 28.5 35.4 31.4 20.040.0 10.8 18.3 12.9 -5.1 55.7 54.7 54.8 56.7 59.7 40.0 28.0 34.9 30.7 19.340.5 10.0 17.7 12.2 -6.2 55.6 54.8 54.8 56.7 59.6 40.5 27.5 34.4 30.1 18.641.0 9.3 16.9 11.5 -7.3 55.6 54.7 54.8 56.7 59.4 41.0 26.9 34.0 29.4 17.941.5 8.5 16.4 10.9 -8.3 55.7 54.8 54.9 56.8 59.4 41.5 26.3 33.5 28.8 17.142.0 7.8 15.8 10.0 -9.3 55.7 54.7 55.0 56.8 59.3 42.0 25.7 33.0 28.2 16.542.5 7.3 15.4 9.3 -10.3 55.7 54.7 55.0 56.9 59.1 42.5 25.2 32.5 27.6 15.843.0 7.0 15.3 8.8 -11.4 55.7 54.8 55.1 57.0 59.0 43.0 24.7 32.1 27.0 15.143.5 6.0 14.5 7.9 -11.5 55.7 54.8 55.1 57.0 58.9 43.5 24.2 31.6 26.344.0 5.3 13.8 -11.1 55.7 54.8 55.1 57.1 58.7 44.0 23.6 31.2 26.144.5 4.5 13.3 6.2 -10.8 55.7 54.9 55.1 57.0 58.5 44.5 23.1 30.7 25.745.0 3.8 12.9 5.6 -10.5 55.9 54.9 55.2 57.2 58.6 45.0 22.5 30.3 25.145.5 3.2 12.4 4.8 -10.3 55.9 54.9 55.3 57.2 58.8 45.5 22.1 29.9 24.546.0 2.4 11.8 4.0 -10.2 56.0 55.0 55.3 57.3 58.8 46.0 21.5 29.5 23.946.5 1.8 11.2 3.2 -10.0 56.0 55.1 55.4 57.3 58.8 46.5 21.1 29.1 23.347.0 0.7 10.6 2.5 -9.9 56.1 55.1 55.6 57.4 58.8 47.0 20.6 28.6 22.647.5 0.1 10.3 1.9 -9.5 56.3 55.3 55.7 57.5 58.8 47.5 20.0 28.2 22.148.0 -0.5 9.7 1.1 -9.3 56.4 55.4 55.8 57.6 58.8 48.0 19.5 27.9 21.548.5 -1.3 9.0 0.3 -9.2 56.5 55.5 55.9 57.6 58.7 48.5 19.0 27.5 20.849.0 -2.2 8.5 -0.4 -9.1 56.6 55.5 56.0 57.7 58.8 49.0 18.6 27.1 20.249.5 -2.5 8.3 -1.0 -8.8 56.9 55.7 56.2 57.9 58.9 49.5 18.1 26.7 19.650.0 -3.2 7.7 -1.9 -8.6 56.9 55.8 56.3 57.9 58.9 50.0 17.6 26.3 19.050.5 -3.8 7.3 -2.7 -8.5 57.1 55.9 56.4 57.9 58.8 50.5 17.2 25.9 18.5



101 (C)102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Time TimeMin Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Min Cyl 1 Cyl 2 Cyl 3 Cyl 4


51.0 -4.7 6.9 -3.5 -8.4 57.2 56.0 56.5 58.0 58.9 51.0 16.7 25.6 18.051.5 -5.5 6.3 -4.4 -8.2 57.4 56.1 56.7 58.1 58.9 51.5 16.3 25.2 17.452.0 -6.0 5.8 -4.9 -7.9 57.5 56.3 56.9 58.2 59.0 52.0 15.8 24.8 16.952.5 -6.9 5.3 -5.6 -7.8 57.7 56.5 57.1 58.2 58.9 52.5 15.4 24.4 16.453.0 -7.7 4.7 -6.6 -7.7 57.8 56.6 57.1 58.3 59.0 53.0 14.9 24.1 15.853.5 -7.9 4.1 -7.4 -7.6 57.8 56.7 57.2 58.4 59.0 53.5 23.7 15.354.0 -7.1 3.7 -7.9 -7.3 57.9 56.8 57.5 58.5 59.1 54.0 23.4 14.754.5 -6.7 3.3 -8.7 -7.2 57.9 56.9 57.6 58.6 59.1 54.5 23.055.0 -6.5 2.6 -9.5 -7.2 58.0 57.1 57.7 58.7 59.1 55.0 22.755.5 -6.0 2.2 -9.8 -7.0 58.1 57.1 57.7 58.6 59.0 55.5 22.456.0 -5.4 2.0 -9.3 -6.7 58.2 57.3 57.7 58.8 59.2 56.0 22.056.5 -5.3 1.1 -9.2 -6.6 58.3 57.4 57.7 58.9 59.2 56.5 21.757.0 -5.0 0.6 -9.1 -6.6 58.3 57.5 57.8 59.0 59.2 57.0 21.457.5 -4.6 0.2 -8.9 -6.4 58.4 57.6 57.8 59.0 59.2 57.5 21.058.0 -4.2 -0.3 -8.6 -6.1 58.6 57.8 57.9 59.1 59.3 58.0 20.758.5 -3.9 -0.8 -8.6 -6.0 58.6 57.9 57.9 59.1 59.4 58.5 20.459.0 -3.5 -1.2 -8.5 -5.9 58.7 58.0 57.9 59.2 59.4 59.0 20.159.5 -3.1 -1.5 -8.3 -5.6 58.9 58.1 58.0 59.4 59.4 59.5 19.860.0 -2.8 -2.1 -8.2 -5.6 58.9 58.2 58.1 59.4 59.5 60.0 19.560.5 -2.5 -2.7 -8.1 -5.4 59.0 58.3 58.2 59.5 59.5 60.5 19.261.0 -2.2 -3.2 -8.0 -5.3 59.1 58.4 58.2 59.6 59.5 61.0 18.961.5 -1.9 -3.5 -7.9 -5.1 59.2 58.6 58.3 59.7 59.6 61.5 18.762.0 -1.5 -3.9 -7.7 -5.0 59.4 58.6 58.4 59.7 59.7 62.0 18.462.5 -1.2 -4.6 -7.6 -4.8 59.4 58.7 58.4 59.8 59.7 62.5 18.163.0 -0.7 -5.0 -7.4 -4.7 59.5 58.9 58.6 59.9 59.7 63.0 17.863.5 -0.5 -5.4 -7.4 -4.5 59.6 59.0 58.6 60.0 59.7 63.5 17.564.0 -0.2 -5.9 -7.3 -4.4 59.7 59.0 58.7 60.0 59.7 64.0 17.364.5 0.3 -6.2 -7.0 -4.2 59.9 59.2 58.8 60.1 59.9 64.5 17.065.0 0.4 -6.6 -6.9 -4.1 59.8 59.2 58.8 60.2 59.9 65.0 16.765.5 0.8 -7.2 -6.9 -4.0 60.0 59.3 58.9 60.2 59.9 65.5 16.466.0 1.3 -7.5 -6.6 -3.7 60.1 59.6 59.1 60.4 60.0 66.0 16.266.5 1.5 -8.0 -6.6 -3.6 60.3 59.5 59.2 60.4 60.0 66.5 15.967.0 1.8 -8.3 -6.5 -3.5 60.2 59.6 59.2 60.4 60.1 67.0 15.667.5 2.2 -8.9 -6.2 -3.3 60.4 59.8 59.3 60.5 60.1 67.5 15.468.0 2.5 -9.3 -6.2 -3.2 60.5 59.9 59.3 60.5 60.1 68.0 15.168.5 2.8 -9.8 -6.1 -3.1 60.5 59.9 59.4 60.6 60.1 68.5 14.8



205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)

212 (INW) Orf 1 Orf 2 Orf 3 Orf 4

TimeMin Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 40.0 0.0 0.0 0.0 0.0 0.0 -0.1 0.0 0.10.5 11.1 14.4 11.9 14.2 10.7 14.3 11.7 14.1 1.00 1.02 1.02 1.021.0 11.0 14.3 11.8 14.1 10.6 14.2 11.6 14.0 1.00 1.01 1.02 1.021.5 11.0 14.3 11.7 14.1 10.6 14.2 11.6 14.0 1.00 1.01 1.02 1.022.0 10.9 14.2 11.7 14.0 10.6 14.1 11.6 13.9 1.00 1.01 1.02 1.022.5 10.9 14.2 11.6 14.0 10.5 14.1 11.5 13.9 1.00 1.01 1.02 1.023.0 10.9 14.2 11.6 14.0 10.5 14.1 11.5 13.9 1.00 1.01 1.02 1.023.5 10.9 14.1 11.6 14.0 10.5 14.0 11.5 13.9 1.00 1.01 1.02 1.024.0 10.9 14.2 11.6 14.0 10.5 14.1 11.4 13.9 1.00 1.01 1.02 1.024.5 10.9 14.1 11.5 14.0 10.5 14.1 11.4 13.9 1.00 1.01 1.02 1.025.0 10.9 14.1 11.5 14.0 10.5 14.0 11.4 13.9 1.00 1.01 1.02 1.025.5 10.9 14.1 11.5 14.0 10.5 14.0 11.4 13.9 1.00 1.01 1.02 1.026.0 10.9 14.1 11.5 13.9 10.5 14.0 11.4 13.9 1.00 1.01 1.02 1.026.5 10.9 14.1 11.5 13.9 10.5 14.0 11.4 13.8 1.00 1.01 1.02 1.027.0 10.9 14.1 11.5 13.9 10.5 14.0 11.3 13.8 1.00 1.01 1.02 1.027.5 10.8 14.1 11.5 13.9 10.5 14.0 11.3 13.9 1.00 1.01 1.02 1.028.0 10.8 14.1 11.5 14.0 10.5 14.0 11.3 13.9 1.00 1.01 1.02 1.028.5 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.029.0 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.9 1.00 1.01 1.02 1.029.5 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0210.0 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0210.5 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0211.0 10.8 14.1 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0211.5 10.8 14.0 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0212.0 10.8 14.0 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0212.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0213.0 10.8 14.0 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0213.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0214.0 10.8 14.0 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0214.5 10.8 14.0 11.4 13.9 10.4 14.0 11.3 13.8 1.00 1.01 1.02 1.0215.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0215.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0216.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0216.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0217.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0217.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0218.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0218.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0219.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0219.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0220.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0220.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0221.0 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0221.5 10.8 14.0 11.4 13.9 10.4 13.9 11.3 13.8 1.00 1.01 1.02 1.0222.0 10.8 14.0 11.4 13.9 10.4 13.9 11.2 13.7 1.00 1.01 1.02 1.0222.5 10.8 14.0 11.4 13.9 10.4 13.9 11.2 13.7 1.00 1.01 1.02 1.0223.0 10.8 14.0 11.4 13.8 10.4 13.9 11.3 13.7 1.00 1.01 1.02 1.0223.5 10.8 13.9 11.4 13.9 10.4 13.9 11.2 13.8 1.00 1.01 1.02 1.0224.0 10.8 14.0 11.4 13.9 10.4 13.9 11.2 13.8 1.00 1.01 1.02 1.0224.5 10.8 14.0 11.3 13.8 10.4 13.9 11.2 13.7 1.00 1.01 1.01 1.0225.0 10.8 13.9 11.4 13.8 10.3 13.9 11.2 13.7 1.00 1.01 1.01 1.0125.5 10.8 13.9 11.3 13.9 10.4 13.9 11.2 13.8 1.00 1.01 1.01 1.0226.0 10.7 13.9 11.3 13.8 10.4 13.9 11.2 13.8 1.00 1.01 1.01 1.01

Flow deviation (1.00=target); f(P, T)

Orifice Differential Pressure, IN. WCRegulator Pressure, IN. WC

Appendix H-1 60 F 050925.xls Regulator/Orifice Pressure Data and Flow Calcs


205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)


TimeMin Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 4



26.5 10.7 13.9 11.3 13.9 10.3 13.9 11.2 13.7 0.99 1.01 1.01 1.0127.0 10.7 14.0 11.3 13.8 10.4 13.9 11.2 13.7 0.99 1.01 1.01 1.0127.5 10.7 13.9 11.3 13.8 10.4 13.8 11.2 13.7 0.99 1.01 1.01 1.0128.0 10.7 13.9 11.3 13.8 10.4 13.8 11.2 13.7 0.99 1.01 1.01 1.0128.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.8 0.99 1.01 1.01 1.0129.0 10.7 13.9 11.3 13.8 10.4 13.8 11.2 13.7 0.99 1.00 1.01 1.0129.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.01 1.01 1.0130.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.01 1.01 1.0130.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0131.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0131.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0132.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0132.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0133.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0133.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0134.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0134.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0135.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0135.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0136.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0136.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0137.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0137.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0138.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.01 1.0138.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0039.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0039.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0040.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0040.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0041.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0041.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0042.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0042.5 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0043.0 10.7 13.9 11.3 13.8 10.3 13.8 11.2 13.7 0.99 1.00 1.00 1.0043.5 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0044.0 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0044.5 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0045.0 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0045.5 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0046.0 10.7 13.9 11.3 10.3 13.8 11.2 0.99 1.00 1.0046.5 10.7 13.9 11.3 10.3 13.8 11.1 0.99 1.00 1.0047.0 10.7 13.8 11.3 10.3 13.8 11.2 0.99 1.00 1.0047.5 10.7 13.8 11.3 10.3 13.8 11.2 0.99 1.00 1.0048.0 10.7 13.8 11.3 10.3 13.8 11.2 0.99 1.00 1.0048.5 10.7 13.8 11.3 10.3 13.8 11.2 0.98 1.00 1.0049.0 10.7 13.8 11.3 10.3 13.7 11.2 0.99 1.00 1.0049.5 10.7 13.8 11.3 10.3 13.8 11.2 0.98 1.00 1.0050.0 10.7 13.8 11.2 10.3 13.8 11.2 0.98 1.00 1.0050.5 10.7 13.8 11.2 10.3 13.8 11.1 0.98 1.00 1.0051.0 10.7 13.8 11.3 10.3 13.7 11.2 0.98 1.00 1.0051.5 10.7 13.8 11.3 10.3 13.7 11.2 0.98 1.00 1.0052.0 10.7 13.8 11.3 10.3 13.7 11.2 0.98 1.00 1.0052.5 10.7 13.8 11.3 10.3 13.7 11.2 0.98 0.99 1.00



205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)


TimeMin Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 4



53.0 10.7 13.8 11.2 10.3 13.7 11.2 0.98 0.99 1.0053.5 13.8 11.2 13.7 11.1 0.99 1.0054.0 13.8 11.2 13.7 11.1 0.99 1.0054.5 13.8 13.7 11.2 0.99 0.9855.0 13.8 13.7 11.1 0.99 0.9855.5 13.8 13.7 0.9956.0 13.8 13.7 0.9956.5 13.8 13.7 0.9957.0 13.8 13.7 0.9957.5 13.8 13.7 0.9958.0 13.8 13.7 0.9958.5 13.8 13.7 0.9959.0 13.8 13.7 0.9959.5 13.8 13.7 0.9960.0 13.8 13.7 0.9960.5 13.8 13.7 0.9961.0 13.8 13.7 0.9961.5 13.8 13.7 0.9962.0 13.8 13.7 0.9962.5 13.8 13.7 0.9963.0 13.8 13.7 0.9963.5 13.8 13.7 0.9964.0 13.8 13.7 0.9964.5 13.8 13.7 0.9965.0 13.8 13.7 0.9965.5 13.8 13.7 0.9966.0 13.8 13.7 0.9966.5 13.8 13.7 0.9967.0 13.8 13.7 0.9967.5 13.8 13.7 0.9968.0 13.8 13.7 0.9968.5 13.8 13.7 0.99



RH start 49%RH end 53%101 (C)

102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

TimeMin. Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Min. Cyl 1 Cyl 2 Cyl 3 Cyl 4

0.0 60.3 60.3 60.1 60.2 61.3 61.2 61.3 61.5 60.5 0.0 95.7 94.9 96.7 95.40.5 60.1 60.0 60.0 60.1 59.2 59.4 60.5 60.0 60.5 0.5 88.9 87.5 90.1 87.51.0 59.7 59.6 58.8 59.8 57.4 57.8 59.3 58.5 60.5 1.0 86.4 85.3 89.2 84.41.5 59.1 59.2 58.2 59.1 56.2 56.6 58.2 57.4 60.5 1.5 84.7 83.8 88.4 82.42.0 58.8 58.9 57.6 58.5 55.4 55.9 57.4 56.5 60.5 2.0 83.5 82.7 87.5 80.92.5 58.1 58.3 57.0 57.8 54.7 55.1 56.6 55.9 60.4 2.5 82.5 81.7 86.8 79.63.0 57.5 57.9 56.6 57.1 54.1 54.6 56.0 55.3 60.6 3.0 81.4 80.9 85.9 79.73.5 54.7 57.1 55.8 56.3 53.6 54.1 55.3 54.6 60.5 3.5 83.1 80.1 85.1 78.84.0 54.7 56.7 55.6 55.6 53.1 53.6 54.8 54.2 60.5 4.0 82.8 80.5 84.3 77.84.5 54.2 55.9 54.9 55.0 52.6 53.1 54.2 53.8 60.4 4.5 82.0 80.2 83.6 76.75.0 53.4 55.6 54.4 54.2 52.3 52.8 54.0 53.5 60.4 5.0 81.1 79.5 82.8 75.65.5 52.8 54.9 53.9 53.5 51.9 52.3 53.5 53.1 60.2 5.5 80.2 78.7 82.0 74.66.0 52.3 54.5 53.3 52.7 51.7 52.1 53.3 52.9 60.4 6.0 79.4 77.8 81.3 73.66.5 51.8 53.9 52.8 52.0 51.4 51.8 52.9 52.5 60.3 6.5 78.5 77.0 80.5 72.67.0 51.3 53.4 52.2 51.3 51.1 51.7 52.6 52.5 60.3 7.0 77.7 76.3 79.8 71.67.5 50.4 52.7 51.6 50.6 50.8 51.3 52.2 52.1 60.3 7.5 76.8 75.6 79.0 70.58.0 50.1 52.3 51.0 49.9 50.7 51.2 52.0 52.0 60.3 8.0 76.0 74.8 78.2 69.58.5 49.3 51.8 50.5 49.1 50.5 51.0 51.7 51.8 60.2 8.5 75.1 74.1 77.5 68.59.0 48.7 51.3 49.8 48.4 50.5 50.9 51.5 51.7 60.2 9.0 74.2 73.4 76.8 67.69.5 48.3 50.9 49.3 47.7 50.4 50.7 51.3 51.6 60.2 9.5 73.5 72.7 76.1 66.610.0 47.5 50.0 48.5 46.8 50.2 50.8 51.2 51.5 60.1 10.0 72.6 72.0 75.2 65.610.5 47.0 49.8 48.2 46.2 50.2 50.7 51.1 51.5 60.1 10.5 71.8 71.3 74.5 64.611.0 46.3 49.1 47.5 45.3 50.2 50.5 51.0 51.4 60.1 11.0 71.0 70.6 73.7 64.311.5 45.6 48.6 46.9 44.5 50.1 50.4 50.8 51.5 60.1 11.5 70.2 69.9 72.9 64.012.0 45.1 48.1 46.4 43.7 50.1 50.5 50.8 51.5 60.1 12.0 69.4 69.1 72.1 63.212.5 44.1 47.3 45.7 42.7 50.1 50.5 50.6 51.5 60.2 12.5 68.5 68.1 71.4 62.413.0 43.8 47.2 45.3 42.1 50.3 50.5 50.7 51.6 60.3 13.0 67.7 67.3 70.6 61.613.5 43.1 46.4 44.7 41.3 50.2 50.6 50.6 51.6 60.2 13.5 67.0 67.0 69.9 60.914.0 42.6 46.0 44.1 40.6 50.3 50.6 50.6 51.7 60.2 14.0 66.1 66.1 69.1 60.014.5 41.9 45.2 43.5 39.6 50.4 50.7 50.6 51.8 60.4 14.5 65.3 65.3 68.3 59.515.0 41.3 44.9 42.9 38.7 50.5 50.8 50.6 51.9 60.5 15.0 64.5 64.6 67.6 58.815.5 40.7 44.5 42.5 38.0 50.6 50.9 50.7 52.1 60.6 15.5 63.7 63.9 66.8 58.016.0 40.1 44.1 41.7 37.1 50.8 51.0 50.7 52.1 60.5 16.0 63.0 63.2 66.0 57.316.5 39.5 43.3 41.3 36.3 50.8 51.1 50.8 52.2 60.5 16.5 62.2 62.5 65.3 56.517.0 39.0 42.8 40.7 35.5 50.9 51.2 51.0 52.3 60.7 17.0 61.4 61.8 64.5 55.817.5 38.3 42.2 40.0 34.6 51.1 51.2 51.0 52.4 60.6 17.5 60.6 61.3 63.8 54.918.0 37.7 41.7 39.5 33.9 51.3 51.4 51.2 52.5 60.8 18.0 59.9 60.6 63.0 54.218.5 37.1 41.3 38.9 32.9 51.4 51.5 51.3 52.6 60.8 18.5 59.1 60.0 62.3 53.319.0 36.4 40.7 38.2 32.0 51.5 51.5 51.4 52.8 60.8 19.0 58.4 59.4 61.6 52.519.5 35.8 40.3 37.8 31.3 51.7 51.7 51.5 52.9 60.9 19.5 57.6 58.7 60.8 51.620.0 35.2 39.6 37.1 30.5 51.8 51.8 51.6 53.0 60.9 20.0 56.9 58.1 60.1 50.920.5 34.8 39.3 36.6 29.7 52.0 52.0 51.7 53.2 61.0 20.5 56.2 57.5 59.3 50.121.0 34.0 38.4 35.9 28.7 52.0 52.1 51.8 53.4 61.0 21.0 55.4 56.9 58.6 49.221.5 33.5 38.1 35.4 28.0 52.3 52.3 52.0 53.5 61.1 21.5 54.7 56.3 57.8 48.422.0 32.9 37.5 34.8 27.1 52.4 52.4 52.1 53.6 61.1 22.0 54.0 55.7 57.1 47.622.5 32.2 36.8 34.1 26.3 52.5 52.4 52.3 53.7 61.2 22.5 53.2 55.0 56.4 46.7

Cylinder Pressure, PSIGTemperature, Degrees Fahrenheit

Appendix H-2 60 F 050927.xls Temperature and Cylinder Pressure Data



102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)



23.0 31.7 36.5 33.7 25.5 52.7 52.7 52.5 54.0 61.2 23.0 52.5 54.4 55.7 45.823.5 31.1 36.0 32.9 24.5 52.9 52.8 52.5 54.1 61.2 23.5 51.8 53.8 55.0 44.924.0 30.4 35.6 32.4 23.8 53.0 52.9 52.8 54.3 61.3 24.0 51.0 53.1 54.3 44.124.5 29.8 34.7 31.8 22.8 53.2 53.1 52.9 54.4 61.3 24.5 50.4 52.5 53.5 43.125.0 29.3 34.3 31.3 22.1 53.3 53.3 53.1 54.6 61.4 25.0 49.6 51.9 52.8 42.225.5 28.6 33.8 30.5 21.0 53.4 53.3 53.2 54.8 61.4 25.5 49.0 51.4 52.1 41.426.0 28.2 33.2 30.1 20.3 53.7 53.6 53.4 54.9 61.5 26.0 48.3 50.8 51.4 40.526.5 27.5 32.5 29.4 19.4 53.8 53.6 53.5 55.1 61.5 26.5 47.6 50.2 50.6 39.627.0 26.9 32.2 28.7 18.5 53.9 53.8 53.7 55.3 61.6 27.0 46.9 49.6 49.8 38.727.5 26.1 31.8 28.2 17.6 54.1 53.9 53.8 55.4 61.5 27.5 46.3 49.0 49.2 37.928.0 25.4 31.0 27.5 16.7 54.2 54.0 53.9 55.6 61.6 28.0 45.6 48.4 48.5 37.028.5 25.0 30.8 27.0 15.9 54.5 54.2 54.1 55.8 61.6 28.5 44.9 47.9 47.8 36.229.0 24.2 29.9 26.3 15.0 54.5 54.3 54.2 55.9 61.7 29.0 44.2 47.3 47.1 35.329.5 23.7 29.4 25.8 14.0 54.8 54.4 54.4 56.1 61.7 29.5 43.5 46.8 46.4 34.530.0 22.9 29.0 25.1 13.1 54.8 54.6 54.6 56.2 61.6 30.0 42.9 46.2 45.7 33.630.5 22.4 28.5 24.4 12.2 55.1 54.7 54.7 56.5 61.8 30.5 42.2 45.7 45.0 32.831.0 21.7 27.7 23.7 11.2 55.3 54.9 54.9 56.6 61.8 31.0 41.6 45.1 44.4 32.031.5 21.1 27.6 23.3 13.0 55.6 55.2 55.1 56.9 61.8 31.5 40.9 44.6 43.7 31.232.0 20.3 27.1 22.5 9.7 55.7 55.3 55.2 57.0 61.7 32.0 40.3 44.1 43.0 30.432.5 19.8 26.7 21.9 8.6 55.9 55.5 55.5 57.2 61.8 32.5 39.7 43.5 42.3 29.733.0 19.2 26.0 21.3 7.5 56.0 55.5 55.6 57.4 61.7 33.0 39.1 42.9 41.6 28.833.5 18.6 25.4 20.7 6.5 56.3 55.8 55.8 57.5 61.6 33.5 38.5 42.4 41.0 28.134.0 17.8 24.9 19.8 5.6 56.2 55.7 55.8 57.6 61.6 34.0 37.8 41.9 40.3 27.234.5 17.2 24.7 19.2 4.8 56.4 55.8 56.0 57.7 61.5 34.5 37.1 41.4 39.7 26.535.0 16.6 23.9 18.6 3.7 56.4 55.9 56.0 57.8 61.4 35.0 36.5 40.9 39.1 25.735.5 16.0 23.1 17.9 2.7 56.5 55.9 56.1 57.9 61.3 35.5 35.9 40.4 38.5 25.036.0 15.4 22.9 17.2 1.9 56.5 56.0 56.2 57.9 61.2 36.0 35.3 39.9 37.8 24.236.5 14.7 22.4 16.4 0.8 56.5 56.0 56.2 57.9 61.0 36.5 34.7 39.4 37.2 23.437.0 14.2 21.8 15.8 -0.1 56.7 56.0 56.3 58.0 60.9 37.0 34.1 38.8 36.6 22.737.5 13.4 21.4 15.1 -1.3 56.5 56.0 56.2 58.1 60.8 37.5 33.5 38.3 35.9 21.938.0 12.9 20.9 14.5 -2.1 56.7 56.0 56.4 58.2 60.7 38.0 32.9 37.8 35.3 21.238.5 12.2 20.1 13.8 -3.3 56.6 56.0 56.4 58.2 60.6 38.5 32.3 37.3 34.6 20.439.0 11.8 19.7 13.2 -4.1 56.7 56.1 56.6 58.3 60.5 39.0 31.7 36.8 34.0 19.739.5 11.0 19.5 12.4 -5.2 56.7 56.1 56.5 58.2 60.3 39.5 31.1 36.3 33.3 19.040.0 10.2 18.8 11.7 -6.3 56.7 56.0 56.5 58.4 60.3 40.0 30.5 35.8 32.7 18.340.5 9.7 18.5 11.0 -7.2 56.8 56.1 56.6 58.4 60.1 40.5 29.9 35.4 32.0 17.641.0 8.9 17.9 10.3 -8.4 56.7 56.1 56.6 58.4 59.9 41.0 29.3 34.9 31.4 16.941.5 8.4 17.3 9.7 -9.3 56.8 56.1 56.6 58.5 60.0 41.5 28.7 34.4 30.7 16.242.0 7.8 16.8 9.0 -10.4 56.8 56.2 56.7 58.5 59.7 42.0 28.2 33.9 30.1 15.542.5 6.9 16.1 8.2 -11.5 56.7 56.2 56.7 58.6 59.6 42.5 27.6 33.4 29.4 14.843.0 6.5 15.8 7.4 -11.9 56.8 56.1 56.7 58.6 59.5 43.0 27.1 33.0 28.843.5 5.7 15.4 6.8 -11.4 56.8 56.1 56.8 58.7 59.4 43.5 26.5 32.5 28.244.0 4.8 14.4 6.5 -11.1 56.8 56.1 56.8 58.7 59.3 44.0 25.9 32.1 28.244.5 4.2 13.7 5.2 -10.7 56.7 56.0 56.8 58.7 59.1 44.5 25.4 31.6 27.345.0 3.9 13.7 4.6 -10.5 56.9 56.2 56.9 58.9 59.0 45.0 24.8 31.2 26.645.5 3.0 13.1 3.8 -10.4 56.9 56.2 56.9 58.9 58.9 45.5 24.3 30.7 26.0




102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C)

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)



46.0 2.3 12.6 3.1 -10.2 56.8 56.1 56.9 58.9 58.8 46.0 23.7 30.3 25.446.5 1.6 12.0 2.3 -9.8 56.9 56.1 56.9 58.9 58.7 46.5 23.2 29.9 24.847.0 0.9 11.3 1.6 -9.5 56.9 56.2 57.0 59.1 58.7 47.0 22.6 29.4 24.247.5 0.3 10.7 0.8 -9.4 56.8 56.1 57.1 59.0 58.5 47.5 22.1 29.0 23.648.0 -0.4 10.2 0.1 -9.3 56.9 56.1 57.1 59.0 58.5 48.0 21.6 28.6 23.048.5 -0.9 9.8 -0.5 -8.9 57.0 56.2 57.1 59.2 58.4 48.5 21.1 28.1 22.449.0 -1.8 9.3 -1.4 -8.8 56.9 56.2 57.2 59.2 58.4 49.0 20.6 27.7 21.749.5 -2.5 8.7 -2.2 -8.7 57.0 56.2 57.2 59.2 58.3 49.5 20.1 27.3 21.250.0 -3.3 8.0 -2.9 -8.6 57.0 56.1 57.1 59.1 58.4 50.0 19.6 26.9 20.650.5 -4.0 7.5 -3.7 -8.4 57.0 56.1 57.2 59.2 58.4 50.5 19.0 26.5 20.051.0 -4.7 7.0 -4.3 -8.3 57.1 56.2 57.3 59.3 58.3 51.0 18.5 26.1 19.451.5 -5.4 6.5 -5.2 -8.2 57.1 56.2 57.3 59.3 58.3 51.5 18.0 25.7 18.852.0 -6.0 6.1 -6.0 -7.9 57.1 56.2 57.3 59.2 58.3 52.0 17.5 25.3 18.252.5 -6.8 5.6 -6.8 -7.9 57.1 56.2 57.4 59.2 58.2 52.5 17.1 24.9 17.753.0 -7.6 5.2 -7.5 -7.8 57.1 56.1 57.3 59.2 58.2 53.0 16.5 24.5 17.153.5 -8.3 4.5 -8.4 -7.6 57.0 56.2 57.4 59.2 58.3 53.5 16.0 24.1 16.554.0 -8.8 4.4 -9.1 -7.4 57.2 56.3 57.5 59.3 58.3 54.0 15.5 23.7 16.054.5 -9.4 3.8 -9.9 -7.2 57.2 56.3 57.5 59.3 58.3 54.5 15.1 23.3 15.555.0 -10.3 3.2 -10.6 -7.1 57.1 56.3 57.5 59.3 58.1 55.0 14.6 22.9 15.055.5 -10.1 2.9 -10.9 -7.0 57.2 56.3 57.5 59.3 58.2 55.5 22.556.0 -9.6 2.2 -10.5 -6.8 57.3 56.3 57.5 59.2 58.2 56.0 22.156.5 -9.2 2.0 -10.3 -6.7 57.3 56.3 57.5 59.2 59.2 56.5 21.857.0 -8.8 1.3 -10.2 -6.5 57.3 56.3 57.6 59.2 60.4 57.0 21.457.5 -8.5 0.6 -10.2 -6.5 57.4 56.4 57.6 59.2 60.3 57.5 21.058.0 -7.9 0.2 -9.9 -6.2 57.5 56.4 57.6 59.3 60.1 58.0 20.758.5 -7.5 -0.3 -9.7 -6.0 57.7 56.5 57.7 59.2 60.0 58.5 20.359.0 -7.2 -0.7 -9.6 -5.9 57.7 56.6 57.7 59.3 59.8 59.0 20.059.5 -6.8 -1.5 -9.5 -5.8 57.7 56.6 57.7 59.2 59.6 59.5 19.660.0 -6.7 -2.1 -9.4 -5.7 57.8 56.7 57.8 59.3 59.6 60.0 19.360.5 -6.3 -2.8 -9.3 -5.6 57.8 56.9 57.8 59.4 59.4 60.5 19.061.0 -5.9 -3.4 -9.2 -5.5 57.9 57.0 57.9 59.2 59.3 61.0 18.761.5 -5.6 -3.9 -9.0 -5.3 57.9 57.1 57.8 59.3 59.3 61.5 18.362.0 -5.3 -4.3 -9.0 -5.2 57.9 57.2 57.9 59.3 59.2 62.0 18.062.5 -4.9 -4.8 -8.9 -5.1 58.1 57.2 57.9 59.4 59.0 62.5 17.763.0 -4.5 -5.0 -8.6 -4.9 58.2 57.5 58.0 59.4 59.1 63.0 17.463.5 -4.2 -5.6 -8.5 -4.7 58.3 57.6 58.2 59.5 59.0 63.5 17.164.0 -3.9 -5.9 -8.4 -4.5 58.4 57.7 58.2 59.5 59.1 64.0 16.864.5 -3.5 -6.5 -8.4 -4.4 58.4 57.9 58.3 59.6 59.0 64.5 16.565.0 -3.1 -6.6 -8.3 -4.4 58.5 58.0 58.3 59.6 59.0 65.0 16.265.5 -2.8 -7.3 -8.2 -4.2 58.6 58.1 58.4 59.6 58.9 65.5 15.966.0 -2.4 -7.8 -8.0 -4.0 58.6 58.2 58.4 59.7 58.9 66.0 15.666.5 -2.1 -8.3 -8.0 -3.8 58.8 58.4 58.4 59.8 58.9 66.5 15.467.0 -1.7 -8.6 -7.7 -3.7 58.9 58.6 58.5 59.9 59.0 67.0 15.1



205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)

212 (INW)

TimeMin. Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 4 Orf 1 Orf 2 Orf 3 Orf 4

0.0 0.0 0.0 0.0 0.0 0.0 -0.1 0.0 0.00.5 11.0 14.3 11.6 14.1 10.5 14.2 11.5 14.0 0.99 1.00 1.01 1.011.0 10.9 14.2 11.5 14.1 10.5 14.1 11.4 13.9 0.99 1.00 1.01 1.011.5 10.9 14.1 11.5 14.0 10.4 14.0 11.4 13.9 0.99 1.01 1.01 1.012.0 10.9 14.1 11.5 14.0 10.4 14.0 11.3 13.9 0.99 1.01 1.01 1.012.5 10.8 14.1 11.4 14.0 10.4 14.0 11.3 13.8 0.99 1.01 1.01 1.013.0 10.8 14.0 11.4 14.0 10.4 14.0 11.3 13.8 0.99 1.01 1.01 1.013.5 10.8 14.0 11.4 14.0 10.4 14.0 11.3 13.8 1.00 1.01 1.01 1.014.0 10.8 14.0 11.4 14.0 10.4 14.0 11.3 13.8 1.00 1.01 1.01 1.014.5 10.8 14.0 11.4 14.0 10.4 13.9 11.3 13.8 1.00 1.01 1.01 1.015.0 10.8 14.0 11.4 14.0 10.4 13.9 11.3 13.8 1.00 1.01 1.01 1.015.5 10.8 14.0 11.4 14.0 10.4 13.9 11.3 13.8 1.00 1.01 1.01 1.016.0 10.8 14.0 11.4 14.0 10.4 13.9 11.3 13.8 1.00 1.01 1.01 1.016.5 10.8 14.0 11.4 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.017.0 10.8 14.0 11.3 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.017.5 10.8 14.0 11.3 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.018.0 10.8 14.0 11.3 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.018.5 10.8 13.9 11.3 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.019.0 10.8 13.9 11.3 13.9 10.3 13.8 11.2 13.8 1.00 1.01 1.01 1.019.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.8 1.00 1.01 1.01 1.0110.0 10.7 13.9 11.3 13.9 10.3 13.9 11.2 13.8 1.00 1.01 1.01 1.0110.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.8 1.00 1.01 1.01 1.0111.0 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.8 1.00 1.01 1.01 1.0211.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0112.0 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0112.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0113.0 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0113.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0114.0 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0114.5 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0115.0 10.7 13.9 11.3 13.9 10.3 13.8 11.2 13.7 1.00 1.01 1.01 1.0115.5 10.7 13.9 11.3 13.9 10.3 13.8 11.1 13.7 1.00 1.01 1.01 1.0116.0 10.7 13.9 11.3 13.9 10.3 13.8 11.1 13.8 1.00 1.01 1.01 1.0116.5 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 1.00 1.01 1.01 1.0117.0 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0117.5 10.7 13.9 11.2 13.9 10.3 13.7 11.1 13.7 0.99 1.00 1.01 1.0118.0 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0118.5 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0119.0 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0119.5 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0120.0 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0120.5 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.01 1.01 1.0121.0 10.7 13.9 11.2 13.8 10.3 13.8 11.1 13.7 0.99 1.00 1.01 1.0121.5 10.7 13.9 11.2 13.9 10.3 13.8 11.1 13.7 0.99 1.00 1.01 1.0122.0 10.7 13.8 11.2 13.8 10.3 13.8 11.1 13.7 0.99 1.00 1.01 1.0122.5 10.7 13.8 11.2 13.8 10.2 13.8 11.1 13.7 0.99 1.00 1.01 1.0123.0 10.7 13.8 11.2 13.8 10.3 13.8 11.1 13.7 0.99 1.00 1.01 1.0123.5 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.01 1.0124.0 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.01 1.0124.5 10.7 13.8 11.2 13.8 10.2 13.8 11.1 13.7 0.99 1.00 1.00 1.0125.0 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.0025.5 10.7 13.8 11.2 13.8 10.2 13.8 11.1 13.7 0.99 1.00 1.00 1.0126.0 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.00

Flow deviation (1.00=target); f(P, T)Regulator Pressure, IN. WC Orifice Differential Pressure, IN. WC



205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)

212 (INW)



26.5 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.0027.0 10.7 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.0027.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.0028.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.99 1.00 1.00 1.0028.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.99 1.00 1.00 1.0029.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.99 1.00 1.00 1.0029.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0030.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.7 0.98 1.00 1.00 1.0030.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0031.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0031.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0032.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0032.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0033.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0033.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0034.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0034.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0035.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0035.5 10.6 13.7 11.2 13.8 10.2 13.7 11.1 13.6 0.98 1.00 1.00 1.0036.0 10.6 13.8 11.1 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0036.5 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0037.0 10.6 13.8 11.2 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0037.5 10.6 13.8 11.1 13.8 10.2 13.7 11.1 13.6 0.98 0.99 1.00 1.0038.0 10.6 13.8 11.2 13.8 10.2 13.7 11.0 13.6 0.98 0.99 1.00 1.0038.5 10.6 13.8 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 1.00 1.0039.0 10.6 13.8 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 1.00 1.0039.5 10.6 13.8 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 1.00 1.0040.0 10.6 13.8 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 0.99 0.9940.5 10.6 13.8 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 0.99 0.9941.0 10.6 13.7 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 1.00 1.0041.5 10.6 13.7 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 0.99 0.9942.0 10.6 13.7 11.1 13.8 10.2 13.7 11.0 13.6 0.98 0.99 0.99 0.9942.5 10.6 13.7 11.1 13.7 10.2 13.7 11.0 13.6 0.98 0.99 0.99 0.9943.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9943.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9944.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9944.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9945.0 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9945.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9946.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9946.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9947.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9947.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9948.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9948.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9949.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9949.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9950.0 10.6 13.8 11.1 10.2 13.7 11.0 0.98 0.99 0.9950.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9951.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9951.5 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9952.0 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9952.5 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.99



205 (INW)

206 (INW)

207 (INW)

208 (INW)

209 (INW)

210 (INW)

211 (INW)

212 (INW)



53.0 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9953.5 10.6 13.7 11.1 10.2 13.7 11.0 0.98 0.99 0.9954.0 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9954.5 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9955.0 10.6 13.7 11.1 10.2 13.6 11.0 0.98 0.99 0.9955.5 13.7 13.6 0.9956.0 13.7 13.6 0.9956.5 13.7 13.6 0.9957.0 13.7 13.6 0.9957.5 13.7 13.6 0.9958.0 13.7 13.6 0.9958.5 13.7 13.6 0.9959.0 13.7 13.6 0.9959.5 13.7 13.6 0.9960.0 13.7 13.6 0.9960.5 13.7 13.6 0.9961.0 13.7 13.6 0.9961.5 13.7 13.6 0.9962.0 13.7 13.6 0.9962.5 13.7 13.6 0.9963.0 13.7 13.6 0.9963.5 13.7 13.6 0.9964.0 13.7 13.6 0.9964.5 13.6 13.6 0.9965.0 13.7 13.6 0.9965.5 13.7 13.6 0.9966.0 13.7 13.6 0.9966.5 13.7 13.6 0.9967.0 13.7 13.6 0.99


The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill CylindersRH 32% Start

29% EndTime Time

Min.101 (C)

102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C) Min.

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1Reg 2Reg 3Reg 4 Amb. Cyl 1 Cyl 2 Cyl 3 Cyl 40.0 28.9 28.9 30.3 29.6 59.9 60.7 61.5 61.7 32.1 0.0 55.3 53.2 56.6 55.80.5 29.1 28.8 30.2 29.3 59.8 60.5 61.1 60.9 32.0 0.5 51.5 49.2 52.8 51.81.0 29.0 28.4 30.1 29.1 59.5 59.9 60.9 60.0 32.1 1.0 49.1 48.8 51.6 50.11.5 28.3 28.1 29.6 28.6 59.2 59.7 60.6 59.4 32.1 1.5 48.3 48.1 51.3 48.92.0 27.5 27.6 28.9 27.7 58.8 59.4 60.3 59.1 32.1 2.0 47.8 47.5 51.1 47.72.5 26.8 26.9 28.3 27.1 58.5 59.1 59.9 58.8 32.0 2.5 46.7 46.9 50.5 46.53.0 26.2 26.3 27.8 25.9 58.2 58.7 59.6 58.6 32.0 3.0 46.2 46.3 49.6 45.33.5 25.3 25.7 27.1 24.8 57.9 58.4 59.2 58.5 32.0 3.5 45.4 45.7 49.1 44.74.0 24.8 25.1 26.4 24.0 57.6 58.1 59.1 58.4 31.9 4.0 44.7 44.9 48.5 43.54.5 24.1 24.6 25.8 23.3 57.2 57.7 58.8 58.3 31.9 4.5 43.9 44.3 47.8 43.05.0 23.4 24.0 25.2 22.6 57.0 57.5 58.6 58.3 31.9 5.0 43.2 43.6 47.1 42.25.5 22.7 23.2 24.6 21.8 56.6 57.2 58.3 58.3 31.9 5.5 42.5 43.0 46.4 41.36.0 21.9 22.9 23.9 20.9 56.4 56.9 58.0 58.3 31.9 6.0 41.7 42.6 45.8 40.56.5 21.3 22.2 23.3 20.1 56.2 56.6 57.8 58.2 31.9 6.5 41.0 42.0 45.0 39.87.0 20.7 21.6 22.6 19.2 56.1 56.6 57.7 58.1 31.9 7.0 40.3 41.3 44.3 39.07.5 20.0 21.1 22.1 56.1 56.6 57.5 58.0 32.0 7.5 39.6 40.8 43.6 38.28.0 19.2 20.4 21.5 18.0 56.1 56.5 57.4 57.8 32.0 8.0 38.9 40.3 43.0 37.38.5 18.5 19.9 20.9 16.6 56.1 56.5 57.3 57.7 32.0 8.5 38.2 39.5 42.3 36.79.0 17.8 19.3 20.3 15.8 56.2 56.5 57.2 57.6 32.0 9.0 37.6 39.0 41.6 35.89.5 17.2 18.6 19.5 14.8 56.2 56.5 57.2 57.3 32.0 9.5 37.1 38.3 41.1 35.010.0 16.4 18.1 19.0 14.0 56.2 56.5 57.2 57.3 32.0 10.0 36.5 37.7 40.5 34.310.5 15.8 17.6 18.3 13.1 56.3 56.6 56.9 57.1 31.9 10.5 35.8 37.2 39.9 33.611.0 15.1 16.9 17.7 12.3 56.4 56.6 57.1 57.2 31.8 11.0 35.1 36.6 39.2 32.911.5 14.2 16.3 17.0 11.4 56.4 56.6 57.1 57.2 31.8 11.5 34.5 36.1 38.6 32.112.0 13.5 15.6 16.4 10.5 56.4 56.7 57.1 57.3 31.8 12.0 33.8 35.5 38.0 31.312.5 12.8 15.1 15.7 9.8 56.5 56.7 57.0 57.3 31.8 12.5 33.2 34.9 37.3 30.513.0 12.1 14.6 15.1 8.8 56.7 56.9 57.1 57.4 31.9 13.0 32.5 34.4 36.7 29.813.5 11.5 14.1 14.5 8.0 57.0 57.0 57.3 57.5 31.9 13.5 31.9 33.8 36.1 29.114.0 11.1 13.5 13.9 7.0 57.3 57.3 57.4 57.5 31.9 14.0 31.2 33.4 35.5 28.314.5 10.4 12.9 13.4 6.1 57.6 57.5 57.6 57.6 31.9 14.5 30.6 32.7 34.9 27.615.0 9.7 12.4 12.7 5.3 57.7 57.7 57.7 57.7 32.0 15.0 30.0 32.2 34.2 26.815.5 9.0 11.8 12.2 4.4 57.8 57.7 57.8 57.8 32.0 15.5 29.3 31.7 33.6 26.216.0 8.3 11.3 11.5 3.5 57.8 57.8 57.8 57.9 31.9 16.0 28.7 31.2 33.0 25.516.5 7.7 10.6 10.9 2.5 57.8 57.8 57.8 58.0 31.9 16.5 28.1 30.8 32.4 24.817.0 6.9 10.0 10.2 1.7 57.7 57.6 57.8 58.1 31.8 17.0 27.5 30.3 31.8 24.117.5 6.2 9.5 9.5 0.7 57.6 57.6 57.8 58.2 31.8 17.5 26.9 29.8 31.3 23.418.0 5.6 8.9 8.8 -0.1 57.5 57.4 57.7 58.5 31.7 18.0 26.3 29.3 30.7 22.818.5 4.8 8.2 8.1 -0.9 57.3 57.3 57.7 58.7 31.6 18.5 25.7 28.8 30.6 22.219.0 4.2 7.6 -1.8 57.2 57.2 57.6 58.8 31.7 19.0 25.1 28.3 29.6 21.519.5 3.5 7.0 6.8 -2.7 57.0 57.0 57.5 59.0 31.6 19.5 24.5 27.8 29.0 20.920.0 2.9 6.4 6.0 -3.6 56.9 57.0 57.5 59.0 31.6 20.0 23.9 27.4 28.5 20.220.5 2.1 5.9 5.4 -4.6 56.9 56.9 57.5 59.1 31.7 20.5 23.4 26.8 27.9 19.521.0 1.6 5.6 4.5 -5.6 57.0 57.0 57.5 59.1 31.7 21.0 22.8 26.4 27.3 18.921.5 0.9 4.7 4.0 -6.6 57.0 57.1 57.5 59.0 31.7 21.5 22.2 25.9 26.8 18.322.0 0.1 4.1 3.3 -7.6 56.9 57.1 57.7 59.0 31.6 22.0 21.7 25.4 26.2 17.622.5 -0.5 3.5 2.8 -8.5 56.9 57.0 57.6 58.9 31.6 22.5 21.1 25.0 25.7 17.023.0 -1.2 2.9 2.1 -9.4 56.9 57.0 57.6 58.9 31.6 23.0 20.5 24.5 24.8 16.323.5 -1.9 2.4 1.4 -10.5 56.9 56.9 57.5 58.8 31.5 23.5 19.6 24.0 24.1 15.7



The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill CylindersRH 32% Start

29% EndTime Time

Min.101 (C)

102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C) Min.

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1Reg 2Reg 3Reg 4 Amb. Cyl 1 Cyl 2 Cyl 3 Cyl 4Temperature, Degrees Fahrenheit Cylinder Pressure, PSIG

24.0 -2.5 1.9 0.7 -11.4 56.8 56.8 57.5 58.8 31.4 24.0 18.8 23.6 23.9 15.124.5 -3.1 1.2 0.1 -12.4 56.8 56.8 57.5 58.8 31.4 24.5 18.2 23.1 23.4 14.625.0 -3.7 0.6 -0.7 -12.6 57.0 56.7 57.5 59.0 31.3 25.0 17.7 22.7 22.825.5 -4.3 0.1 -1.5 -12.3 56.9 56.8 57.5 59.0 31.2 25.5 17.2 22.3 22.226.0 -5.1 -0.5 -2.0 -12.1 57.2 56.8 57.6 59.0 31.2 26.0 16.7 21.9 21.726.5 -5.8 -1.0 -2.8 -12.0 57.1 56.9 57.5 59.2 31.2 26.5 16.2 21.4 21.227.0 -6.5 -1.6 -3.4 -11.8 57.4 57.2 57.6 59.2 31.2 27.0 15.7 21.0 20.727.5 -7.4 -2.2 -4.0 -11.8 57.7 57.3 57.8 59.2 31.2 27.5 15.1 20.6 20.128.0 -8.2 -2.6 -4.7 -11.7 58.0 57.6 57.9 59.3 31.1 28.0 14.6 20.2 19.628.5 -9.1 -3.2 -5.3 -11.6 58.3 57.8 58.1 59.4 31.1 28.5 19.8 19.029.0 -9.2 -3.9 -6.1 -11.4 58.3 58.0 58.2 59.4 31.1 29.0 19.2 18.629.5 -9.0 -4.3 -6.7 -11.3 58.4 58.2 58.4 59.4 31.0 29.5 18.8 18.230.0 -8.9 -4.9 -7.5 -11.3 58.4 58.5 58.7 59.6 30.9 30.0 18.3 17.730.5 -8.8 -5.6 -8.0 -11.1 58.5 58.6 58.7 59.5 30.8 30.5 17.9 17.231.0 -8.6 -6.1 -8.9 -11.0 58.6 58.8 58.8 59.5 30.7 31.0 17.6 16.731.5 -8.4 -6.7 -9.6 -10.9 58.8 58.9 59.0 59.6 30.7 31.5 17.2 16.232.0 -8.2 -7.3 -10.4 -10.9 58.9 59.0 59.1 59.6 30.6 32.0 16.8 15.632.5 -8.1 -7.9 -11.0 -10.7 58.9 59.3 59.2 59.6 30.6 32.5 16.4 15.233.0 -8.1 -8.5 -11.8 -10.6 59.0 59.3 59.4 59.8 30.6 33.0 16.0 14.733.5 -7.9 -9.0 -12.6 -10.5 59.2 59.5 59.5 59.8 30.5 33.5 15.734.0 -7.7 -9.7 -12.9 -10.4 59.3 59.7 59.5 59.8 30.5 34.0 15.334.5 -7.7 -10.3 -12.9 -10.3 59.5 59.9 59.5 59.9 30.5 34.5 14.935.0 -7.5 -10.7 -12.8 -10.3 59.5 60.0 59.5 60.0 30.5 35.0



Time

Min.205

(INW)206

(INW)207

(INW)208

(INW)209

(INW)210

(INW)211

(INW)212

(INW) Orf 1 Orf 2 Orf 3 Orf 4

Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 40.0 -0.7 -0.8 -0.9 0.0 -0.8 -0.9 -0.9 0.10.5 10.9 13.1 10.5 13.3 10.4 13.0 10.4 13.1 0.98 0.96 0.95 0.971.0 10.9 13.1 10.5 13.5 10.4 13.0 10.4 13.3 0.98 0.96 0.95 0.981.5 10.9 13.1 10.6 13.5 10.4 13.0 10.4 13.3 0.98 0.96 0.95 0.992.0 10.9 13.8 10.5 13.5 10.4 13.7 10.5 13.4 0.98 0.99 0.95 0.992.5 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.4 0.99 0.99 0.99 0.993.0 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.4 0.99 0.99 0.99 0.993.5 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.4 0.99 0.99 0.99 0.994.0 10.9 13.9 11.3 13.6 10.4 13.7 11.2 13.4 0.99 0.99 0.99 0.994.5 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.5 0.99 0.99 0.99 1.005.0 10.9 13.8 11.3 13.7 10.4 13.7 11.2 13.6 0.99 0.99 0.99 1.005.5 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.5 0.99 0.99 0.99 1.006.0 10.9 13.8 11.3 13.6 10.4 13.8 11.2 13.5 0.99 0.99 0.99 1.006.5 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.5 0.99 0.99 0.99 1.007.0 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.5 0.99 0.99 0.99 1.007.5 10.9 13.8 11.4 13.6 10.4 13.7 11.3 13.5 0.99 0.99 0.99 1.008.0 10.9 13.8 11.3 13.6 10.4 13.7 11.2 13.5 0.99 0.99 0.99 1.008.5 10.9 13.8 11.3 13.7 10.4 13.8 11.2 13.5 0.99 1.00 0.99 1.009.0 10.9 13.9 11.3 13.6 10.4 13.8 11.1 13.5 0.99 1.00 0.99 1.009.5 10.9 13.9 11.3 13.6 10.4 13.8 11.2 13.5 0.99 1.00 0.99 1.0010.0 10.9 13.9 11.3 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0010.5 10.9 13.9 11.3 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0011.0 10.9 13.9 11.3 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0011.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0012.0 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0012.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0013.0 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 1.0013.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 0.99 0.99 1.0014.0 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.99 1.0014.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.99 1.0015.0 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 1.0015.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 1.0016.0 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 1.0016.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.99 0.9917.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9917.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9918.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9918.5 10.9 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9919.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.99 0.9919.5 10.9 13.8 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.99 0.9920.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.98 0.9920.5 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.99 0.99 0.98 0.9921.0 10.8 13.8 11.2 13.6 10.3 13.7 11.1 13.5 0.98 0.99 0.98 0.9921.5 10.8 13.8 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9922.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9922.5 10.8 13.8 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9923.0 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 0.99 0.98 0.9923.5 10.8 13.9 11.2 13.6 10.3 13.7 11.1 13.5 0.98 0.99 0.98 0.9924.0 10.8 13.8 11.2 13.6 10.3 13.8 11.1 13.5 0.99 1.00 0.98 0.9924.5 10.8 13.9 11.2 13.6 10.3 13.8 11.1 13.5 0.98 1.00 0.98 0.9925.0 10.8 13.9 11.2 10.3 13.8 11.1 0.98 1.00 0.98


Regulator Pressure, IN. WC Orifice Differential Pressure, IN. WC



Time

Min.205

(INW)206

(INW)207

(INW)208

(INW)209

(INW)210

(INW)211

(INW)212


Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 4



25.5 10.8 13.8 11.2 10.3 13.7 11.1 0.98 0.99 0.9826.0 10.8 13.8 11.2 10.3 13.7 11.1 0.98 0.99 0.9826.5 10.8 13.8 11.2 10.3 13.7 11.1 0.98 0.99 0.9827.0 10.8 13.9 11.2 10.3 13.8 11.1 0.98 0.99 0.9827.5 10.8 13.8 11.2 10.3 13.7 11.1 0.98 0.99 0.9828.0 10.8 13.8 11.2 10.3 13.7 11.1 0.98 0.99 0.9828.5 13.8 11.2 13.7 11.1 0.99 0.9829.0 13.8 11.2 13.7 11.1 0.99 0.9829.5 13.8 11.2 13.7 11.1 0.99 0.9830.0 13.8 11.2 13.7 11.1 0.99 0.9830.5 13.8 11.2 13.7 11.1 0.99 0.9831.0 13.8 11.2 13.7 11.1 0.99 0.9831.5 13.8 11.2 13.7 11.1 0.99 0.9832.0 13.8 11.2 13.7 11.1 0.99 0.9832.5 13.8 11.2 13.7 11.1 0.99 0.9833.0 13.8 11.2 13.7 11.1 0.99 0.9833.5 13.8 11.2 13.7 11.1 0.99 0.9834.0 13.8 13.7 0.9934.5 13.8 13.7 0.9935.0 13.8 13.7 0.99


The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill CylindersRH start 28%RH end 32%

Min.101 (C)

102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C) Min.

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Cyl 1 Cyl 2 Cyl 3 Cyl 40.0 28.6 28.6 30.1 29.6 58.7 59.6 60.2 60.4 29.8 0.0 55.5 53.0 57.1 56.40.5 28.5 28.5 30.1 29.4 58.5 59.1 59.9 59.9 29.9 0.5 49.6 48.1 51.4 49.81.0 27.9 27.6 29.7 28.9 58.3 58.8 59.6 59.4 30.0 1.0 47.1 47.8 50.5 47.21.5 27.1 26.8 28.5 27.7 58.2 58.8 59.3 59.1 30.0 1.5 45.3 47.1 49.7 46.72.0 26.6 26.2 27.8 27.0 58.0 58.6 59.2 58.9 29.9 2.0 44.0 46.5 48.9 45.52.5 26.0 25.5 27.3 26.0 58.0 58.4 58.9 58.8 29.9 2.5 43.0 45.8 48.2 44.63.0 25.3 25.0 26.5 25.2 57.8 58.1 58.8 58.6 29.9 3.0 42.3 45.2 47.5 43.73.5 24.7 24.4 25.9 24.4 57.6 58.0 58.6 58.4 29.9 3.5 41.5 44.5 46.8 42.94.0 24.1 23.8 25.5 23.7 57.6 57.7 58.5 58.3 30.0 4.0 40.8 43.9 46.1 42.14.5 23.5 23.3 24.8 23.1 57.2 57.5 58.4 58.2 30.1 4.5 40.1 43.3 45.4 41.25.0 22.7 22.8 24.1 22.1 57.1 57.4 58.1 58.0 30.1 5.0 39.4 42.7 44.5 40.45.5 22.2 22.1 23.5 21.4 56.9 57.1 57.9 57.9 30.5 5.5 38.7 42.0 43.8 39.66.0 21.5 21.5 23.0 20.4 56.7 56.9 57.8 57.8 30.1 6.0 38.1 41.5 43.3 39.06.5 20.7 20.9 22.4 19.7 56.5 56.8 57.6 57.6 30.2 6.5 37.4 40.9 42.6 38.47.0 20.1 20.3 21.7 20.5 56.5 56.6 57.4 57.4 30.2 7.0 36.8 40.4 41.8 37.87.5 19.2 19.6 21.1 18.2 56.4 56.7 57.4 57.5 30.2 7.5 36.1 39.8 41.1 37.38.0 18.6 19.0 20.5 17.2 56.3 56.7 57.4 57.5 30.1 8.0 35.5 39.2 40.5 36.48.5 18.0 18.5 19.9 16.5 56.4 56.7 57.4 57.5 30.1 8.5 34.8 38.6 39.9 35.79.0 17.4 20.4 19.3 15.4 56.4 56.6 57.4 57.6 30.2 9.0 34.1 38.2 39.2 34.89.5 16.5 17.4 18.6 14.7 56.3 56.5 57.3 57.6 30.0 9.5 33.5 37.4 38.6 34.1

10.0 16.0 16.7 18.0 13.9 56.3 56.5 57.3 57.5 30.0 10.0 32.8 36.9 38.0 33.310.5 15.1 16.1 17.4 12.9 56.2 56.4 57.2 57.4 30.0 10.5 32.3 36.4 37.4 32.511.0 14.5 15.5 16.8 12.2 56.0 56.2 57.1 57.4 29.9 11.0 31.6 35.7 36.7 31.811.5 13.6 14.9 16.1 11.1 56.0 56.1 57.0 57.2 30.0 11.5 31.0 35.1 36.1 31.112.0 13.2 14.6 15.3 10.1 55.9 55.9 57.0 57.2 30.0 12.0 30.4 34.6 35.5 30.512.5 12.5 13.8 14.8 9.6 55.8 55.9 56.8 57.1 29.9 12.5 29.8 34.0 34.9 29.713.0 11.7 13.2 14.1 8.5 55.7 55.9 56.8 56.9 29.9 13.0 29.2 33.5 34.3 29.013.5 11.1 12.7 13.5 7.9 55.5 55.7 56.7 56.9 30.0 13.5 28.7 32.9 33.7 28.314.0 10.4 12.2 12.9 6.8 55.7 55.8 56.6 57.1 30.0 14.0 28.0 32.4 33.1 27.614.5 9.8 11.5 12.2 6.2 55.8 55.9 56.7 57.1 29.9 14.5 27.5 32.0 32.5 26.915.0 9.2 10.9 11.6 5.3 56.1 56.0 56.7 57.2 30.0 15.0 26.9 31.5 31.9 26.215.5 8.2 10.4 10.9 4.5 56.2 56.1 56.8 57.3 29.9 15.5 26.3 30.9 31.3 25.516.0 7.8 9.8 10.2 3.7 56.4 56.3 56.9 57.5 29.8 16.0 25.8 30.3 30.7 24.716.5 7.0 9.2 9.6 2.8 56.6 56.4 57.0 57.6 29.7 16.5 25.1 29.9 30.1 24.117.0 6.3 8.7 9.0 1.8 56.8 56.7 57.1 58.0 29.6 17.0 24.7 29.4 29.5 23.417.5 5.5 8.1 8.3 1.0 57.1 56.7 57.2 58.0 29.6 17.5 24.1 28.8 29.0 22.718.0 5.0 7.5 7.6 0.1 57.2 57.0 57.4 58.1 29.7 18.0 23.6 28.3 29.3 22.018.5 4.3 6.9 6.6 -0.9 57.4 57.1 57.5 58.3 29.6 18.5 23.1 27.8 28.6 21.419.0 3.3 6.3 6.0 -1.7 57.5 57.3 57.7 58.5 29.6 19.0 22.5 27.3 28.1 20.719.5 2.8 5.7 5.2 -2.7 57.8 57.5 57.7 58.6 29.5 19.5 22.0 26.9 27.5 20.120.0 2.4 5.2 4.7 -3.6 57.9 57.5 57.9 58.8 29.5 20.0 21.5 26.4 26.9 19.520.5 1.4 4.4 3.9 -4.5 58.0 57.7 58.0 59.0 29.5 20.5 21.0 25.9 26.3 18.821.0 0.2 3.9 3.1 -5.4 58.2 58.0 58.0 59.3 29.5 21.0 20.5 25.4 25.7 18.221.5 0.1 3.4 2.5 -6.2 58.5 58.3 58.3 59.4 29.4 21.5 19.9 25.0 25.2 17.622.0 -0.7 2.8 1.8 -7.3 59.0 58.3 58.4 59.6 29.8 22.0 19.6 24.6 24.5 17.022.5 -1.4 2.2 1.3 -8.3 59.1 58.6 58.7 59.8 29.4 22.5 19.0 24.1 24.0 16.423.0 -2.1 1.7 0.7 -9.2 59.3 58.9 58.9 60.0 29.4 23.0 18.5 23.6 23.4 15.823.5 -2.9 1.1 -0.1 -10.1 59.4 59.0 59.0 60.2 29.2 23.5 18.0 23.2 22.9 15.2


Appendix H-4 30 F 051019.xls Temperature and Cylinder Data

The Comparative Vaporization Rates of Composite, Steel, and Aluminum Grill CylindersRH start 28%RH end 32%

Min.101 (C)

102 (C)

103 (C)

104 (C)

105 (C)

106 (C)

107 (C)

108 (C)

109 (C) Min.

201 (PSI)

202 (PSI)

203 (PSI)

204 (PSI)

Cyl 1 Cyl 2 Cyl 3 Cyl 4 Reg 1 Reg 2 Reg 3 Reg 4 Amb. Cyl 1 Cyl 2 Cyl 3 Cyl 4Temperature, Degrees Fahrenheit Cylinder Pressure, PSIG

24.0 -3.5 0.6 -0.9 -11.1 59.5 59.0 59.2 60.2 29.1 24.0 17.6 22.8 22.3 14.624.5 -4.5 -0.2 -1.6 -11.6 59.5 59.0 59.2 60.3 29.2 24.5 17.1 22.5 21.825.0 -5.0 -0.8 -2.2 -11.4 59.6 58.8 59.3 60.3 28.9 25.0 16.6 22.0 21.425.5 -5.8 -1.3 -2.9 -11.3 59.4 59.0 59.3 60.2 29.1 25.5 16.2 21.6 20.726.0 -6.5 -1.9 -3.5 -11.0 59.3 59.0 59.5 60.3 29.0 26.0 15.7 21.2 20.226.5 -7.3 -2.4 -4.2 -10.8 59.2 58.9 59.4 60.4 29.0 26.5 15.2 20.8 19.727.0 -7.7 -2.9 -4.7 -10.8 59.1 58.8 59.3 60.4 29.0 27.0 14.8 20.3 19.127.5 -8.1 -3.6 -5.4 -10.7 59.2 58.7 59.2 60.4 29.0 27.5 19.9 18.628.0 -8.1 -4.2 -6.2 -10.6 59.2 58.7 59.1 60.4 29.0 28.0 19.5 18.128.5 -8.2 -4.7 -6.9 -10.5 59.2 58.4 59.1 60.4 29.0 28.5 19.1 17.629.0 -7.9 -5.3 -7.7 -10.3 59.2 58.4 59.1 60.3 29.1 29.0 18.7 17.129.5 -7.8 -5.9 -8.4 -10.1 59.1 58.3 59.1 60.4 29.4 29.5 18.3 16.630.0 -7.6 -6.4 -9.1 -10.0 59.1 58.5 59.2 60.4 29.5 30.0 17.9 16.130.5 -7.4 -7.1 -9.8 -10.0 59.1 58.6 59.2 60.4 29.6 30.5 17.6 15.731.0 -7.1 -7.6 -10.5 -9.9 59.2 58.6 59.4 60.5 29.7 31.0 17.2 15.331.5 -7.1 -8.2 -11.3 -9.9 59.1 58.5 59.3 60.5 29.7 31.5 16.8 14.832.0 -7.0 -8.8 -11.5 -9.8 59.2 58.4 59.3 60.5 29.8 32.0 16.432.5 -7.0 -9.3 -11.5 -9.7 59.1 58.3 59.3 60.5 29.8 32.5 16.033.0 -6.8 -9.9 -11.5 -9.7 59.1 58.2 59.3 60.5 29.7 33.0 15.733.5 -6.4 -10.4 -11.3 -9.5 59.1 58.2 59.3 60.5 29.7 33.5 15.334.0 -6.2 -11.0 -11.2 -9.3 59.0 58.2 59.4 60.5 29.7 34.0 14.9

Appendix H-4 30 F 051019.xls Temperature and Cylinder Data


Min.205

(INW)206

(INW)207

(INW)208

(INW)209

(INW)210

(INW)211

(INW)212


Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 40.0 0.0 0.0 0.0 0.0 0.0 -0.1 0.0 0.10.5 11.0 14.3 11.6 13.7 10.6 14.2 11.4 13.6 1.00 1.01 1.00 1.001.0 11.0 14.3 11.5 13.6 10.5 14.2 11.4 13.5 0.99 1.01 0.99 0.991.5 10.8 14.1 11.4 13.6 10.4 14.0 11.3 13.5 0.99 1.00 0.99 0.992.0 10.8 14.1 11.4 13.6 10.4 14.0 11.3 13.5 0.99 1.00 0.99 0.992.5 10.8 14.1 11.4 13.6 10.4 14.0 11.3 13.5 0.99 1.00 0.99 0.993.0 10.8 14.1 11.4 13.6 10.4 14.0 11.3 13.5 0.99 1.00 0.99 0.993.5 10.8 14.1 11.4 13.5 10.4 14.0 11.3 13.4 0.99 1.00 0.99 0.994.0 10.8 14.1 11.4 13.5 10.4 14.0 11.2 13.4 0.99 1.00 0.99 0.994.5 10.8 14.1 11.4 13.5 10.4 14.0 11.2 13.4 0.99 1.00 0.99 0.995.0 10.8 14.1 11.3 13.5 10.4 14.0 11.2 13.4 0.99 1.00 0.99 0.995.5 10.8 14.1 11.3 13.5 10.4 14.0 11.2 13.4 0.99 1.00 0.99 0.996.0 10.8 14.0 11.3 13.5 10.4 13.9 11.2 13.4 0.99 1.00 0.99 0.996.5 10.8 14.0 11.3 13.6 10.3 13.9 11.2 13.5 0.99 1.00 0.99 0.997.0 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.997.5 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.998.0 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.998.5 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.999.0 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.999.5 10.8 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9910.0 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9910.5 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9911.0 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9911.5 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9912.0 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9912.5 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9913.0 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9913.5 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9914.0 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9914.5 10.7 14.0 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9915.0 10.7 13.9 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9915.5 10.7 13.9 11.3 13.5 10.3 13.8 11.2 13.4 0.99 1.00 0.99 0.9916.0 10.7 13.9 11.3 13.5 10.3 13.9 11.2 13.4 0.99 1.00 0.99 0.9916.5 10.7 13.9 11.3 13.5 10.3 13.9 11.1 13.4 0.98 1.00 0.99 0.9917.0 10.7 13.9 11.3 13.5 10.3 13.8 11.2 13.4 0.98 1.00 0.99 0.9917.5 10.7 13.9 11.3 13.5 10.3 13.8 11.1 13.4 0.98 1.00 0.99 0.9918.0 10.7 13.9 11.3 13.5 10.3 13.8 11.1 13.3 0.98 1.00 0.99 0.9918.5 10.7 13.9 11.3 13.5 10.3 13.8 11.1 13.4 0.98 1.00 0.99 0.9919.0 10.7 13.9 11.2 13.5 10.3 13.8 11.1 13.4 0.98 1.00 0.99 0.9919.5 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 1.00 0.99 0.9920.0 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 1.00 0.99 0.9920.5 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 1.00 0.99 0.9921.0 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.99 0.9921.5 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9922.0 10.7 13.9 11.2 13.5 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9922.5 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9823.0 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9823.5 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9824.0 10.7 13.9 11.2 13.4 10.3 13.8 11.1 13.3 0.98 0.99 0.98 0.9824.5 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.9825.0 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.9825.5 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.98





Min.205

(INW)206

(INW)207

(INW)208

(INW)209

(INW)210

(INW)211

(INW)212


Reg 1 Reg 2 Reg 3 Reg 4 Orf 1 Orf 2 Orf 3 Orf 4



26.0 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.9826.5 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.9827.0 10.7 13.9 11.2 10.0 13.8 11.1 0.96 0.99 0.9827.5 13.9 11.2 13.8 11.1 0.99 0.9828.0 13.9 11.2 13.8 11.1 0.99 0.9828.5 13.9 11.2 13.8 11.1 0.99 0.9829.0 13.9 11.2 13.8 11.1 0.99 0.9829.5 13.9 11.2 13.8 11.1 0.99 0.9830.0 13.9 11.2 13.8 11.1 0.99 0.9830.5 13.9 11.2 13.8 11.1 0.99 0.9831.0 13.9 11.2 13.8 11.1 0.99 0.9831.5 13.9 11.2 13.8 11.1 0.99 0.9832.0 13.9 13.8 0.9932.5 13.9 13.8 0.9933.0 13.9 13.8 0.9933.5 13.9 13.8 0.9934.0 13.9 13.8 0.99


Vaporization Study

Cylinders charged with 20% of WC, in a 60F environment, 80 KBTUH draw.RH start 49% Normalized:RH end 52% Minutes

WT % WT % withdrawal25-Sep-05 Temp Press. Gr Wt. TW Temp Press. Wt. TW D'Chgd D'Chgd ∆TW 10# chargeSteel; 9.5 lb Charge 60.9 95.7 27.48 18.04 66.6 106.3 23.98 18.04 53.0 3.50 19.4% 0.0% 56Aluminum; 9.5 Lb. Charge 60.2 95.4 24.24 13.68 67.0 105.5 20.04 13.68 68.5 4.20 30.7% 0.0% 65Lined Composite; 10.6 Lb. Charge 60.8 95.8 23.20 12.66 66.1 107.1 19.88 12.68 54.0 3.32 26.2% 0.2% 51Linerless Composite; 9.1 Lb. Charge 61.0 97.9 21.84 12.78 66.6 106.2 19.02 12.80 43.0 2.82 22.1% 0.2% 47

RH start 49% Normalized:RH end 53% Minutes

WT % WT % withdrawal27-Sep-05 Temp Press. Gr Wt. TW Temp Press. Wt. TW D'Chgd D'Chgd ∆TW 10# chargeSteel; 9.5 lb Charge 60.3 95.7 27.48 18.04 69.2 106.2 24.20 18.04 55.0 3.28 18.2% 0.0% 58Aluminum; 9.5 Lb. Charge 60.3 94.9 24.34 13.68 69.3 106.4 20.18 13.68 67.0 4.16 30.4% 0.0% 63Lined Composite; 10.6 Lb. Charge 60.1 96.7 23.24 12.68 69.4 110.0 19.96 12.68 55.0 3.28 25.9% 0.0% 52Linerless Composite; 9.1 Lb. Charge 60.2 95.4 21.94 12.80 69.4 109.0 19.06 12.80 42.5 2.88 22.5% 0.0% 46

Cylinders charged with 20% of WC, in a 30F environment, 80 KBTUH draw.RH start 32% Normalized:RH end 28% Minutes

WT % WT % withdrawal17-Oct-05 Temp Press. Gr Wt. TW Temp Press. Wt. TW D'Chgd D'Chgd ∆TW 10# chargeSteel; 9.5 lb Charge 28.9 55.3 27.48 18.04 56.4 91.0 25.88 18.04 28.0 1.60 8.9% 0.0% 30Aluminum; 9.5 Lb. Charge 28.9 53.2 24.24 13.68 57.0 91.7 22.18 13.68 34.5 2.06 15.1% 0.0% 33Lined Composite; 10.6 Lb. Charge 30.3 56.6 23.20 12.66 52.8 90.0 21.48 12.68 33.0 1.72 13.6% 0.0% 31Linerless Composite; 9.1 Lb. Charge 29.6 55.8 21.84 12.78 53.4 89.1 20.22 12.80 24.5 1.62 12.7% 0.0% 27

RH start 28% Normalized:RH end 32% Minutes

WT % WT % withdrawal19-Oct-05 Temp Press. Gr Wt. TW Temp Press. Wt. TW D'Chgd D'Chgd ∆TW 10# chargeSteel; 9.5 lb Charge 28.6 55.5 27.48 18.04 58.8 92.6 25.84 18.04 27.0 1.64 9.1% 0.0% 29Aluminum; 9.5 Lb. Charge 28.6 53.0 24.24 13.68 59 91.3 22.16 13.68 34.0 2.08 15.2% 0.0% 32Lined Composite; 10.6 Lb. Charge 30.1 57.1 23.20 12.68 57.1 92.1 21.36 12.68 31.5 1.84 14.5% 0.0% 30Linerless Composite; 9.1 Lb. Charge 29.6 56.4 21.84 12.80 58.3 91.7 20.34 12.80 24.0 1.50 11.7% 0.0% 27

Start End Min to 15 PSIG




Appendix I Test Summary

Appendix J 30 F 051017.xls Pressure

Vaporization Study: 30F, 80 KBTUH Draw, 20% Charge

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0 5 10 15 20 25 30 35

Time, Min

Pres

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Steel Aluminum Lined Composite Linerless Composite



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Vaporization Study: 60F, 80 KBTUH, 20% Charge

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0 10 20 30 40 50 60 70

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Appendix K 30 F 051017.xls Temperature


-20

-10

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, F

Steel Aluminum Lined Composite Linerless Composite Ambient



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Appendix K 60 F 050925.xls Temp

Vaporization Study: 60F, 80 KBTUH, 20% Charge

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, F




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