FC1500/SF2600: EPA 2016 Certification Report

REPORT NUMBER: 102527563MID-001b REPORT DATE: November 10, 2016

EVALUATION CENTER Intertek Testing Services NA Inc.

8431 Murphy Drive Middleton, WI 53562

RENDERED TO HY-C Company, LLC 10950 Linpage Place St. Louis, MO 63132

PRODUCT EVALUATED: MODEL FC1500 WOOD FORCED-AIR FURNACE

Report of Testing Model FC1500 Wood Forced-Air Furnace for compliance as an “Affected Wood Heater” with the applicable requirements of the following criteria: CAN/CSA B415.1-2010 Performance Testing of Solid- Fuel-Burning Heating Appliances, ASTM E2515-11 Determination of Particulate Matter Emissions Collected by a Dilution Tunnel, and EPA 40 CFR Part 60 “Standards of Performance for New Residential Wood Heaters, New Residential Hydronic Heaters and Forced-Air Furnaces”, March 16, 2015.

This report is for the exclusive use of Intertek's Client and is provided pursuant to the agreement between Intertek and its Client. Intertek's responsibility and liability are limited to the terms and conditions of the agreement. Intertek assumes no liability to any party, other than to the Client in accordance with the agreement, for any loss, expense or damage occasioned by the use of this report. Only the Client is authorized to copy or distribute this report and then only in its entirety. Any use of the Intertek name or one of its marks for the sale or advertisement of the tested material, product or service must first be approved in writing by Intertek. The observations and test results in this report are relevant only to the sample tested. This report by itself does not imply that the material, product, or service is or has ever been under an Intertek certification program.

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Contents I.

INTRODUCTION................................................................................................................ 4 I.A PURPOSE OF TEST ............................................................................................................................ 4 I.B LABORATORY .................................................................................................................................... 4 I.C DESCRIPTION OF UNIT ..................................................................................................................... 4 I.D REPORT ORGANIZATION .................................................................................................................. 5 II. SUMMARY......................................................................................................................... 5 II.A PRETEST INFORMATION ................................................................................................................ 5 II.B INFORMATION LOG ....................................................................................................................... 6

II.B(1) TEST STANDARD........................................................................................................................ 6

II.B(2)

Deviation from Standard Method......................................................................................... 6

II.C SUMMARY OF TEST RESULTS ........................................................................................................ 6 II.D DESCRIPTION OF TEST RUNS ......................................................................................................... 6 II.D SUMMARY OF OTHER DATA .......................................................................................................... 7

TABLE 1. – DATA SUMMARY PART A.................................................................................................... 7

TABLE 3. – WEIGHTED AVERAGE.......................................................................................................... 8

TABLE 5. - GENERAL SUMMARY OF RESULTS ....................................................................................... 8 III. PROCESS DESCRIPTION ................................................................................................ 9 III.A TEST SET-UP DESCRIPTON ............................................................................................................. 9 III.B AIR SUPPLY SYSTEM ...................................................................................................................... 9 III.C TEST FUEL PROPERTIES ................................................................................................................. 9 IV. SAMPLING SYSTEMS....................................................................................................... 9 IV.A. SAMPLING LOCATIONS .................................................................................................................. 9 IV.A.(1) DILUTION TUNNEL ................................................................................................................ 10 IV.B. OPERATIONAL DRAWINGS .......................................................................................................... 11

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Project No. G102527563 Page 3 of 15 IV.B.(1) STACK GAS SAMPLE TRAIN .................................................................................................... 11 IV.B.(2). DILUTION TUNNEL SAMPLE SYSTEMS ............................................................................... 12 V. SAMPLING METHODS ........................................................................................................12 V.A. PARTICULATE SAMPLING ............................................................................................................... 13 VI. QUALITY ASSURANCE ......................................................................................................13 VI.A. INSTRUMENT CALIBRATION ........................................................................................................... 13 VI.A. (1). DRY GAS METERS ............................................................................................................ 13 VI.A.(2). STACK SAMPLE ROTAMETER ........................................................................................... 14 VI.A.(3). GAS ANALYZERS .............................................................................................................. 14 VI.B. TEST METHOD PROCEDURES ...................................................................................................... 14 VI.B.(1). LEAK CHECK PROCEDURES .............................................................................................. 14 VI.B.(2). TUNNEL VELOCITY/FLOW MEASUREMENT ..................................................................... 15 VI.B.(3). PM SAMPLING PROPORTIONALITY....................................................................................... 15 VII. CONCLUSION ..................................................................................................................15

REVISION SUMMARY DATE

SUMMARY

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INTRODUCTION

Intertek Testing Services NA (Intertek) has conducted testing for HY-C Company, LLC, on model FC1500 Wood Air Furnace to evaluate all applicable performance requirements included in “Determination of particulate matter emissions from wood forced-air furnaces.” I.A PURPOSE OF TEST The test was conducted to determine if the unit is in accordance with U.S EPA requirements under EPA 40 CFR Part 60 “Standards of Performance for New Residential Wood Heaters, New Residential Hydronic Heaters and Forced-Air Furnaces”. This evaluation was started on June 6, 2016 and completed on June 9, 2016. The following test methods were applicable: ASTM E2515-11- Standard Test Method for Determination of Particulate Matter Emissions Collected by a Dilution Tunnel CSA B415.1-10 - Performance Testing of Solid-Fuel-Burning Heating Appliances I.B LABORATORY The tests on the model FC1500 Wood Forced-Air Furnace were conducted at the Intertek testing Services Laboratory located at 8431 Murphy Drive, Middleton, WI, 53562. The laboratory is accredited by the U.S. EPA, Certificate Number 3. The test was conducted by Ken Slater and observed by Dan Haynes of HY-C Company, LLC. I.C DESCRIPTION OF UNIT The model FC1500 Wood Forced-Air Furnace is constructed of sheet steel. The outer dimensions are 44-inches deep, 50.5-inches high, and 25.5-inches wide. The unit has a fueling door located on the front. (See product drawings.)

Proprietary drawings and manufacturing methods are on file at Intertek in (Intertek location)

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I.D

REPORT ORGANIZATION

This report includes summaries of all data necessary to determine compliance with the regulations. Raw data, calibration records, intermediate calculations, drawings, specifications and other supporting information are contained in appendices to this report.

II. SUMMARY II.A PRETEST INFORMATION

A sample was submitted to Intertek directly from the client. The sample was not independently selected for testing. The test unit was received at Intertek in Middleton, WI on June 6, 2016 and was shipped via the client. The unit was inspected upon receipt and found to be in good condition. The unit was set up following the manufacturer's instructions without difficulty. Following assembly, the unit was placed on the test stand. Prior to beginning the emissions tests, the unit was operated for a minimum of 10 hours at high-to-medium burn rates to condition the heater. This conditioning burn was performed by HY-C and the documents are included in the final report. The unit was found to be operating satisfactory during this break-in. The 10 plus hours of pre-burning were conducted from May 26, 2016 to May 28, 2016. The fuel used for the break-in process was cordwood. Following the pre-burn break-in process the unit was allowed to cool and ash and residue was removed from the firebox. The unit's chimney system and laboratory dilution tunnels were cleaned using standard wire brush chimney cleaning equipment. On June 6, 2016 the unit was set-up for testing.

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II.B INFORMATION LOG II.B(1) TEST STANDARD

From June 6, 2016 through June 9, 2016, the unit was tested for EPA emissions. For Wood Forced-Air Furnaces, the test was conducted in accordance with CSA B415.1- 2010. The fuel used for the test run was Oak cordwood. The applicable EPA regulatory limits are: Step 1 – 2016 – 0.93 lbs/MMBtu Output (0.4 g/MJ) – For furnaces rated less than 65,000 Btu/hr Step 1 – 2017 – 0.93 0.93 lbs/MMBtu Output (0.4 g/MJ) – For furnaces rated more than 65,000 Btu/hr Step 2 – 2020 – 0.15 lbs/MMBtu Output (0.026 g/MJ) II.B(2) DEVIATION FROM STANDARD METHOD No deviations from the standards were performed, however, only the applicable sections from each standard were used during all testing. II.C SUMMARY OF TEST RESULTS

The appliance tests resulted in the following performance:

Particulate Emissions: 0.368 lbs/MMBtu Output (0.159 g/MJ) Carbon Monoxide Emissions: 279.23 g/hr Heating Efficiency: 49.5% (Higher Heating Value Basis)

II.D DESCRIPTION OF TEST RUNS

RUN #1 June 6, 2016. The furnace was set to draw a category 3 draw rate. The combustion blower was turned on and off to maintain the desired heat rate. The Test Load weighed 32.63 lbs. and utilized an 8.1 lb. coal bed. The average Btu/hr output was 57,561. Burn time was 1.98 hours. The kg/hr burn rate was 5.90.

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Page 7 of 15 RUN #2 June 7, 2016. The furnace was set to draw a category 1 draw rate. The combustion blower was turned on and off to maintain the desired heat rate. The Test Load weighed 38.55 lbs. and utilized a 3.9 lb. coal bed. The average Btu/hr output was 23,905. Burn time was 5.95 hours. The kg/hr burn rate was 2.33. RUN #3 June 8, 2016. The furnace was set to draw a category 4 draw rate. The combustion blower was turned on to maintain the desired heat rate. The Test Load weighed 37.54 lbs. and utilized a 7.6 lb. coal bed. The average Btu/hr output was 68,541. Burn time was 1.45 hours. The kg/hr burn rate was 9.29. RUN #4 June 8, 2016. The furnace was set to draw a category 2 draw rate. The convection blower was turned on and off to maintain the desired heat rate. The Test Load weighed 38.37 lbs. and utilized a 5.1 lb. coal bed. The average Btu/hr output was 26,730. Burn time was 4.88 hours. The kg/hr burn rate was 2.84. RUN #5 June 9, 2016. The furnace was set to draw a category 4 draw rate. The combustion blower was turned on to maintain the desired heat rate. The Test Load weighed 37.85 lbs. and utilized an 8.6 lb. coal bed. The average Btu/hr output was 79,814. Burn time was 1.35 hours. The kg/hr burn rate was 10.031. *Client felt that the output for the first category 4 test was too low, so a second test was performed and the combined average of the two tests are used in the final results.

II.D SUMMARY OF OTHER DATA TABLE 1. – DATA SUMMARY PART A

W fuel

MC ave

Q in

Q out

Wood Weight as-fired

Run No.

Load % Capacity

Target Load Btu/hr 26,600

Actual Load Btu/hr 23,905

Test Duration

Wood Moisture

Heat Input

Heat Output

Category

E g/MJ,i x F i

E lb/mmbtu,i x F i

E g/hr,i x F i

CO g/hr,i x F i

2 4 1

0.250 0.250 0.250 0.250 1.000

0.137 0.126 0.130 0.102 0.495

0.017 0.016 0.041 0.085 0.159

0.039 0.036 0.095 0.198 0.368

0.427 0.439 2.468 6.493 9.827

39.980 42.615 154.020 42.615 279.230

III IV

3 & 5

Totals

TABLE 5. - GENERAL SUMMARY OF RESULTS

1 st Hour Emissions (g/hr)

Burn Rate (kg/hr)(Dry)

Run Time (min)

Run No.

2 4 1

2.33 2.84 5.90 9.66

12.6

357 293 119

7.6

12.1 33.7

3 & 5

TABLE 6. – CSA B415.1 RESULTS

CO Emissions (g/hr)

Heating Efficiency (% HHV)

Heat Output (Btu/hr)

Run No.

2 4 1

159.92 170.46 616.08 1473.88

67.2 66.8 61.0 58.2

29,281 35,573 67,106 103,916

3 & 5

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III. PROCESS DESCRIPTION

III.A TEST SET-UP DESCRIPTON

A standard 6” diameter vertical single wall pipe and insulated chimney system was installed to 15’ above floor level. The singe wall pipe extended to 8 feet above the floor and insulated chimney extended the remaining height. III.B AIR SUPPLY SYSTEM Combustion air enters a combustion blower located on the back of the heater, which is directed to the firebox. All gases exit through the 6” flue also located at the top back of the heater. The exhaust gases are assisted by a combustion blower. III.C TEST FUEL PROPERTIES

Wood used for the testing is split and seasoned oak cordwood. Oak has a default heating value of 8550 Btu/hr (19887 kJ/kg) and a moisture content between 18% and 28% on a dry basis.

IV.

SAMPLING SYSTEMS

IV.A. SAMPLING LOCATIONS

Particulate samples are collected from the dilution tunnel at a point 20 feet from the tunnel entrance. The tunnel has two elbows and two mixing baffles in the system ahead of the sampling section. (See Figure 3.) The sampling section is a continuous 13 foot section of 6 inch diameter pipe straight over its entire length. Tunnel velocity pressure is determined by a standard Pitot tube located 60 inches from the beginning of the sampling section. The dry bulb thermocouple is located six inches downstream from the Pitot tube. Tunnel samplers are located 60 inches downstream of the Pitot tube and 36 inches upstream from the end of this section. (See Figure 1.) Stack gas samples are collected from the steel chimney section 8 feet ± 6 inches above the scale platform. (See Figure 2.)

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IV.A.(1)

DILUTION TUNNEL

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IV.B. OPERATIONAL DRAWINGS

IV.B.(1) STACK GAS SAMPLE TRAIN

IV.B.

OPERATIONAL DRAWINGS

IV.B.(1). STACK GAS SAMPLE TRAI

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IV.B.(2). DILUTION TUNNEL SAMPLE SYSTEMS

Figure 3

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V. SAMPLING METHODS

V.A. PARTICULATE SAMPLING

Particulates were sampled in strict accordance with ASTM E2515-2011. This method uses two identical sampling systems with Gelman A/E 61631 binder free, 47-mm diameter filters. The dryers used in the sample systems are filled with “Drierite” before each test run. In order to measure first-hour emissions rates the a third filter set is prepared at one hour into the test run, the filter sets are changed in one of the two sample trains. The two filter sets used for this train are analyzed individually to determine the first hour and total emissions rate.

VI. QUALITY ASSURANCE

VI.A. INSTRUMENT CALIBRATION

VI.A. (1).

DRY GAS METERS

At the conclusion of each test program the dry gas meters are checked against our standard dry gas meter. Three runs are made on each dry gas meter used during the test program. The average calibration factors obtained are then compared with the six-month calibration factor and, if within 5%, the six-month factor is used to calculate standard volumes. Results of this calibration are contained in Appendix D.

An integral part of the post test calibration procedure is a leak check of the pressure side by plugging the system exhaust and pressurizing the system to 10” W.C. The system is judged to be leak free if it retains the pressure for at least 10 minutes.

The standard dry gas meter is calibrated every 6 months using a Spirometer designed by the EPA Emissions Measurement Branch. The process involves sampling the train operation for 1 cubic foot of volume. With readings made to .001 ft 3 , the resolution is .1%, giving an accuracy higher than the ±2% required by the standard.

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VI.A.(2).

STACK SAMPLE ROTAMETER

The stack sample rotometer is checked by running three tests at each flow rate used during the test program. The flow rate is checked by running the rotometer in series with one of the dry gas meters for 10 minutes with the rotometer at a constant setting. The dry gas meter volume measured is then corrected to standard temperature and pressure conditions. The flow rate determined is then used to calculate actual sampled volumes.

VI.A.(3).

GAS ANALYZERS

The continuous analyzers are zeroed and spanned before each test with appropriate gases. A mid-scale multi-component calibration gas is then analyzed (values are recorded). At the conclusion of a test, the instruments are checked again with zero, span and calibration gases (values are recorded only). The drift in each meter is then calculated and must not exceed 5% of the scale used for the test. At the conclusion of each unit test program, a three-point calibration check is made. This calibration check must meet accuracy requirements of the applicable standards. Consistent deviations between analyzer readings and calibration gas concentrations are used to correct data before computer processing. Data is also corrected for inter- ferences as prescribed by the instrument manufacturer’s instructions.

VI.B. TEST METHOD PROCEDURES

VI.B.(1).

LEAK CHECK PROCEDURES

Before and after each test, each sample train is tested for leaks. Leakage rates are measured and must not exceed 0.02 CFM or 4% of the sampling rate. Leak checks are performed checking the entire sampling train, not just the dry gas meters. Pre- test and post-test leak checks are conducted with a vacuum of 10 inches of mercury. Vacuum is monitored during each test and the highest vacuum reached is then used for the post test vacuum value. If leakage limits are not met, the test run is rejected. During, these tests the vacuum was typically less than 2 inches of mercury. Thus, leakage rates reported are expected to be much higher than actual leakage during the tests.

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VI.B.(2).

TUNNEL VELOCITY/FLOW MEASUREMENT

The tunnel velocity is calculated from a center point Pitot tube signal multiplied by an adjustment factor. This factor is determined by a traverse of the tunnel as prescribed in EPA Method 1. Final tunnel velocities and flow rates are calculated from EPA Method 2, Equation 6.9 and 6.10. (Tunnel cross sectional area is the average from both lines of traverse.) Pitot tubes are cleaned before each test and leak checks are conducted after each test.

VI.B.(3). PM SAMPLING PROPORTIONALITY

Proportionality was calculated in accordance with ASTM E2515-11. The data and results are included in Appendix C.

VII. CONCLUSION

This test demonstrates that this unit is an affected facility under the definition given in the regulation. The emission rate of 0.368 g/hr meets the EPA requirements for the Step 1 limits. Model FC1500 was tested as a representative sample of similar model SF2600. SF2600 is identical to the FC1500, with the only difference being the color. SF Series is sold under the Shelter Furnace name and the FC Series is sold under the Fire Chief Industries name. INTERTEK TESTING SERVICES NA

Evaluated by:

Ken Slater Associate Engineer - Hearth

Reviewed by:

Brian Ziegler Technical Team Lead - Hearth

Certificate of Conformity

Emissions – Wood Burning Forced Air Furnace EPA 40 CFR Part 60, Subpart QQQQ, CSA B415.1-2010 Certificate number: WHI15 – 10583801

Organization: Company Name: HY-C Company, LLC Address: 10950 Linpage Place City, State: St. Louis, MO Zip Code: 63132 Country: USA

This is a certificate of conformity to certify that the bearer has successfully completed the requirements of the above scheme which include the testing of products, the initial assessment, and are subject to continuing annual assessments of their compliance and testing of samples of products taken from production (as applicable to the scheme) and has been registered within the scheme for the products detailed.

Product: Model FC1500 and SF2600 Manufacturer’s Rated Output: 75,000 Btu/hour

Weighted Average Emissions: 0.34 lb/million Btu/hour Weighted Average Annual Delivered Efficiency: 50% Test Fuel Type: Cordwood Compliance: Certified to comply with 2017 particulate emissions standard. Report Number: 102527563MID-001b

Certification body: Intertek Testing Services NA, Inc. Initial registration: November 11, 2016 Date of expiry: May 16, 2020 Issue status: 1

Dustin Behling Certification Coordination Manager

11/11/2016

Name

Signature

Date

www.intertek.com The certificate and schedule are held in force by regular annual surveillance visits by Intertek Testing Services NA, Inc. and the reader or user should contact Intertek to validate its status. This certificate remains the property of Intertek Testing Services NA, Inc. and must be returned to them on demand. This Certificate is for the exclusive use of Intertek's Client and is provided pursuant to the Certification agreement between Intertek and its Client. Intertek's responsibility and liability are limited to the terms and conditions of the agreement. Intertek assumes no liability to any party, other than to the Client in accordance with the agreement, for any loss, expense or damage occasioned by the use of this certificate. Only the Client is authorized to permit copying or distribution of this certificate and then only in its entirety. Use of Intertek’s Certification mark is restricted to the conditions laid out in the agreement. Any further use of the Intertek name for the sale or advertisement of the tested material, product or service must first be approved in writing by Intertek. Initial Factory Assessments and Follow up Services are for the purpose of assuring appropriate usage of the Certification mark in accordance with the agreement, they are not for the purposes of production quality control and do not relieve the Client of their obligations in this respect. Registered address: Intertek Testing Services NA, Inc. 545 E. Algonquin Rd. Arlington Heights, IL 60005 USA

INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 1 INTRODUCTION This document provides a systematic guide for the technician conducting tests to CAN/CSA B415.1-2010 Performance Testing of Solid-Fuel-Burning Heating Appliances. This guide cannot cover every possible contingency that may develop during a particular test program. Many questions that may arise can be answered by a complete understanding of the test protocol and its intent. When in doubt on any detail check with the laboratory manager and be sure you understand the procedures involved. The primary measurements to be obtained are particulate emission data and efficiency data. The technician's duties include the following steps. It is critical that all spaces on the data forms be properly filled in. Each test must be represented by

a complete record of what was done and when. I. APPLIANCE INSPECTION AND SET-UP A. Incoming Inspection B. Unit Set-Up II. SAMPLING SYSTEMS - SET-UP A. Gas Analysis B. Dilution Tunnel III. TEST CONDUCT A. Pre-Test Fuel Load

B. Test Fuel Load C. Unit Start - up D. Test Run

IV.

POST TEST PROCEDURE A. Leak Checks B. Particulate Sample Recovery

TEST EQUIPMENT AND FIGURES

VI.

FUEL HANDLING AND STORAGE The technician running this test must be familiar with the following documents that are to be kept in the laboratory at all times. 1. ASTM E2515 2. CSA B415.1

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INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 2

I. APPLIANCE INSPECTION AND SET-UP A. Incoming Inspection

1. Check for completeness of unit including parts, accessories, installation and operating instructions, drawings and specifications, etc. Note any discrepancies or missing parts. 2. Check for shipping damage. If damage has occurred, notify the laboratory manager. In some cases repairs may be made, provided the manufacturer and laboratory manager concur that repairs will not affect the unit’s performance. If damage is irreparable, a new unit will need to be obtained. 3. Note whether unit is catalytic or non-catalytic. 4. Mark unit with manufacturer's name, model number, work order number, and date received. 5. If unit is safety listed, note label data including listing agency and serial number. B. Unit Set-Up 1. Prior to placing unit on scale, the scale must be turned on and allowed to warm up for 1-hour minimum. 2. Place unit on scale and align so chimney will be centered in hood. Record the weight of the unit and all accessories. (Do not weigh with chimney attached.) 3. Chimney and connector should be cleaned with a wire brush prior to mounting. Attach chimney and connector then seal all joints. Be sure the single wall stove pipe terminates and insulated pipe starts at proper level above scale platform. Chimney must be supported from scale so that it does not touch test enclosure or hood walls. 5. Measure firebox dimensions and record on appropriate data form. Make a three dimensional sketch of the firebox including firebrick, baffles, and obstructions. Calculate load area volume in cubic feet. See Section 8.2 of the CAN/CSA B415.1-2010 Performance Testing of Solid-Fuel-Burning Heating Appliances for details. 7. Plug thermocouples into data acquisition system jacks and verify that all instrumentation is working properly. 8. Dilution tunnel must be cleaned prior to each certification test series, and at anytime a higher burn rate follows a lower burn rate. 9. Install outlet air duct in accordance with the manufacturer’s requirements and section 5.3.2 of CAN/CSA B415.1-2010 Performance Testing of Solid-Fuel-Burning Heating Appliances. 10. Set duct static pressure to 0.2 in/wc or to the manufacturer’s specifications by reducing the duct outlet size uniformly.

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INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 3

II.

SAMPLING SYSTEMS SET-UP A. Gas Analysis 1. All instruments should be turned on and allowed to warm up for 1-hour minimum. 2. Prior to calibrating, make sure that the outlet pressure on each calibration gas bottle reads 10 PSI. Adjust flow meters at each gas analyzer to required flow. All gas analyzers (CO 2 , CO, O 2 ) are zeroed on nitrogen. The O 2 analyzer is spanned on air and set for 20.93%. CO 2 and CO analyzers are spanned with their respective gases. Calibrate analyzers as follows: a. With calibration switch at "SPAN", adjust all span controls to values specified on span gas label. b. Switch to "ZERO" and adjust zero controls to provide 0.00 readout on all analyzers. c. Repeat a. and b. until no further adjustment is required. d. Record these values on the appropriate data sheet. e. Switch to "CAL." and record all analyzer values. 3. Response time synchronization check. a. With switch at "SAMPLE" and no fire in unit, allow readings to stabilize (O 2 analyzer should read 20.93, CO and CO 2 should read 0.00). b. Switch to "CAL" setting and start the stopwatch. Note the time required for each unit to reach the calibration gas bottle value. If all three analyzers reach this value within 5 seconds of each other, synchronization is adequate. If not, contact the laboratory manager. Synchronization is adjusted by either internal instrument setting or adjustment of sample line length. c. Use section 8 of ASTM E2515 for procedures to check calibration of instruments. 4. Sample clean-up train. a. Load a new filter in 4-inch glass filter holder. b. Load four Impingers as follows:

#1: 100 ml. distilled or de-ionized water #2: 100 ml. distilled or de-ionized water #3: Empty #4: 200-300 grams Drierite.

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INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 4

c. Place Impingers in container and connect with greased "U TUBES". (Grease carefully on bottom half of ball joint so that grease will not get into tubes.) d. Connect filter to impinger #1 and sample line to impinger #4.

e. Connect stack probe to filter. f. Leak check system as follows: 1) Plug probe. 2)

Turn on sample system and increase flow rate slowly. Set vacuum-adjust valve to obtain a vacuum of 10 inches mercury.

4) If sapphire float in rotometer does not stabilize below 10 on scale, system must be resealed. 5) Repeat leak-check procedure until satisfactory results are obtained. 6) Unplug probe slowly, then decrease flow rate slowly before shutting off system. g. Just prior to starting test, fill impinger container with ice. B. Dilution Tunnel Sample Train Set-Up: 1. Filters and holders. a. Clean probes and filter holder front housings carefully and desiccate to a constant weight prior to use. b. Filters and filter probe combinations should be numbered and labeled prior to use. c. Weigh desiccated filters and probe filter units on analytical balance. Record the weights on the appropriate form. Note that the probe and front half of the front filter holder is to be weighed as a unit. d. Carefully assemble the filter holder units and connect to sampling systems. 2. Leak checking. a. Each sample system is to be checked for leakage prior to inserting probes in tunnel. b. Plug probes and start the samplers. Adjust pump bypass valve to produce a vacuum reading of 10 inches mercury. NOTE: During test, highest vacuum recorded is required for posttest leak check. c. Allow vacuum indication to stabilize at 10" mercury, record dry gas meter readings, (DGM 1 , DGM 2 ). At a convenient DGM value start stopwatch. Time for 1 minute then stop vacuum pumps. Record dry gas meter readings again, (DGM 3 , DGM 4 ). NOTE: If rotometer ball is floating above the 5-mm mark, system is leaking too much and all seals should be checked.

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INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 5

d. Calculate leakage rate as follows. System 1: DGM3-DGM 1 = CFM 1 System 2: DGM4-DGM 2 = CFM 2

If CFM 1 or CFM 2 is greater than 0.02 cfm, or 1 S greater than 0.04 x Sample Rate, leakage is unacceptable and system must be resealed. For most tests the sample rate will be 0.25 cfm, thus leakage rates in excess of 0.04 x 0.25 = 0.010 cfm are not acceptable. e. To prevent contamination, do not insert probes in tunnel until the start of the test run. TEST CONDUCT A. Pre-Test Fuel Load 1. Using oak wood, operate normally until the unit is heated and has cycled at least 2 times. Then remove all contents and zero scale 2. Reload with oak wood (pieces approximately 2” thick) and allow to burn down to specified coal bed weight. B. Test Fuel Load 1. Determine optimum load weight by multiplying loading area volume (ft 3 ) by 10lbs/ft 3 . This is the ideal load weight. 2. Test load fuel shall be red or white oak cordwood with a dimension of 20- inches (± 4”). Moisture content of each piece needs to be within 18-28%, with the overall average to be between 18-28%. 3. Weigh out test load and adjust weight by shortening or lengthening all pieces equally if necessary. 4. Measure and record moisture content of each fuel piece (using five total measurements). Determine if fuel load moisture content is within required range (18-28%). If not, construct new fuel pieces using wood with required moisture content. Contact laboratory manager if you cannot find suitable pieces. C. Unit Start-Up 1. With all doors and air controls closed, zero draft magnehelic using screw located at bottom of meter. 2. Before lighting a fire turn on dilution tunnel and set flow rate to 60 scfm. 3. Check draft imposed on cold stove. All inlets must be closed and a draft gauge in the chimney. If draft is greater than 0.005 inches water column, adjust tunnel to stack gap until draft is less than 0.005 inches water column.

III.

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INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 6

4. With hot wire anemometer check for ambient airflow around unit (must be less than 50 ft/min). 5. Zero scale and start fire with newspaper and kindling. (Make sure stack sample probe is on the unit.) 6. Once kindling is burning well, add preload fuel. Operate at high fire for sufficient time to get fuel load burning well. Then adjust settings to intended test run levels. 7. Perform the dilution tunnel traverse as prescribed in ASTM #2515, Section 9.3. (Pitot tube should be carefully cleaned prior to each test.) 8. Pretest load must burn until the unit has cycled at least 2 times. 9. Stir fire often during preburn (after a reading) to get a good coal bed. Fire can only be raked once (door open 1 minute or less) during the 15 minutes prior to the start of the test. 10.Traverse the outlet duct velocity with a vane anemometer and enter into the spreadsheet. D. Test Run 1. Stack gas analyzers should be on and in the sample mode. 2. When the fuel bed is between 10-20% of the test load weight the test is to be started. a. Insert the sample probes into the tunnel being careful not to hit sides of tunnel with probe tip. b. Check tunnel Pitot tube for proper position. c. Record initial readings. d. Turn on probe sample systems and start timing test. e. Tare platform scale. f. Open stove doors and load stove. Close door or follow manufacturer's start-up procedures. Five minutes is the maximum time before all doors and controls must be set to final positions for duration of test. g. Record length of time door and bypass are open, include any air control setting adjustments. h. Every 10 minutes or less record the following: 1) Dry gas meter readings. 2) Weight remaining. 4) Tunnel Pitot tube reading. 5) Draft reading. 6) Rotometer readings. i. Every 1 minute record the following: 1) All temperature points 2) Water meter 3) Delta T thermopile

G:\Hearth\EE - Emissions and Efficiencey\Furnace solid fuel\Lab Procedures for EPA Air Furnaces 11.11.16.doc

INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 7

j. Filter temperatures shall not exceed 90ºF anytime during the test. If the filters are approaching 90ºF turn on cooling pump. Filters must be kept above the dilution tunnel wet bulb temperature in order to prevent condensation. k. Regularly check impinger train for ice level during test. l. After 30 seconds of 0.00 lbs. weight, and on the minute, shut off

sample trains and record last reading. m. Record final dry gas meter values.

IV. POST TEST PROCEDURES A. Leak Checks 1. Dilution Tunnel

a. Remove both sample probes from tunnel and plug with rubber stopper. b. Turn on sample system and set vacuum to 10" mercury or to the highest value reached during the test. c. At a convenient value start stopwatch and record the DGM starting value. d. After 1 minute stop sample system and record ending DGM value. e. Calculate leakage rate per pre-test description (see II.B.2.c.). 2. Gas Analyzers a. Set stack sample flow to about 75 mm on the rotometer. b. Plug with rubber stopper. c. Adjust vacuum to 10" mercury. d. Let system stabilize then record rotometer readings. e. If the rotometer readings do not equal zero, check with the laboratory manager. f. SLOWLY unplug probe and decrease flow rate to zero. g. Turn off stack sampling system. h. Zero, span and calibrate the analyzers (see Gas Analysis). RECORD ONLY these meter values. B. Particulate Sample Recovery 1. Disassemble filter holder and scrape gasket with scalpel. Collect all loose material on filters. 2. Weigh and record probes and filters for each train. NOTE: 24 hours of desiccation must pass before final "no change" weight values can be recorded. 3. Weigh and record probes and fillers at 6-hour intervals until weight change between weighing is less than 0.2 mg.

G:\Hearth\EE - Emissions and Efficiencey\Furnace solid fuel\Lab Procedures for EPA Air Furnaces 11.11.16.doc

INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 8

TEST EQUIPMENT AND FIGURES Figure 1 – Dilution Tunnel

∆ T

Figure 2 – Flue Gas Sample Train

G:\Hearth\EE - Emissions and Efficiencey\Furnace solid fuel\Lab Procedures for EPA Air Furnaces 11.11.16.doc

INTERTEK/WARNOCK HERSEY AIR FURANCE EMISSIONS AND EFFICIENCY TESTING LABORATORY OPERATING PROCEDURES pg. 9

Figure 4 – Dilution Tunnel Sample System

VI. FUEL HANDLING AND STORAGE Test fuel is purchased at various sources and once received; the moisture is checked by the Intertek staff. The fuel is then placed in a sealed room with the humidity and temperature maintained at a desired level to equilibrate and maintain the moisture content of the fuel. The room is only opened as necessary to retrieve the fuel for preparation prior to the test.

G:\Hearth\EE - Emissions and Efficiencey\Furnace solid fuel\Lab Procedures for EPA Air Furnaces 11.11.16.doc

CLIENT: HY-C

PERFORMED BY: REVIEWED BY: MODEL: DATE: LOCATION: CALIBRATION DUE: CALIBRATION DUE: CALIBRATION DUE:

Ken Slater

PROJECT #: G102527563

Brian Ziegler

FC1500 6/6/2016

PRODUCT:

SAMPLE ID #:

STANDARD(S): CSA B415.1

MID

EQUIPMENT

See Appenix C in final report

ASSET # - DESCRIPTION:

ASSET # - DESCRIPTION: See Appenix C in final report ASSET # - DESCRIPTION: See Appenix C in final report

CONDITIONING SAMPLE CONDITIONING (IF APPLICABLE): NA

AMBIENT TEMPERATURE: NA

Run:

Test Duration: Output Category:

119

Test Results in Accordance with CSA B415.1-09

HHV Basis

LHV Basis

Overall Efficiency

61.0% 92.4%

65.7% 92.4% 71.2%

Combustion Efficiency Heat Transfer Efficiency

66%

Output Rate (kJ/h) Burn Rate (kg/h)

(Btu/h) (lb/h) (Btu/h)

70,741

67,106 12.84 109,936

5.83

Input (kJ/h)

115,892

Test Load Weight (dry kg)

dry lb

11.56 20.99 26.57 19.58 1,222

25.47

MC wet (%) MC dry (%)

Particulate (g )

CO (g)

Test Duration (h)

1.98

Emissions Particulate

g/MJ Output g/kg Dry Fuel

0.14 1.69 9.87 0.32

8.71

105.72 616.08 20.24

g/h

lb/MM Btu Output

Air/Fuel Ratio (A/F)

9.87

1 Minutes

6.996917

0.036931

Reading Interval

1 2

Elapsed

Flue

Room Tunnel

DGM 1 DGM 1 Filter 1 DGM 2 DGM 2 Filter 2 DGM 3 Filter 3 Meter 1 Meter 2 Draft

Tunnel

Duct

Tunnel

Draft

Sys 1 Sys 2

Degrees F

Time temp 1 temp 2 dry bulb 3Outlet air Inlet Air

Out

Pitot

CO CO2

scale

Pitot

pitot

Pitot Correction Cu Ft

Cu Ft

0 929.0 79.1 167.7 136.7 76.1 80.62086 79.46604 -64.3017 81.5733 79.12464 138.40 78.29 138.60 0.02 1 995.5 79.4 184.5 146.8 76.7 80.21478 79.27772 -73.8761 81.16428 78.97082 136.99 78.01 136.83 0.02 2 1046.4 79.0 197.0 156.6 76.0 80.29775 79.26831 -3.54138 81.60515 78.87584 141.59 78.15 138.06 0.02

0.02 1.2447 1.2026 0.787218 5.58989 14.59851 34.14334 1.137267 0.034317 0.050655 0.061175 0.001 0.001 0.02 1.2454 1.1770 0.787121 5.58989 14.62106 32.93879 1.141266 0.035316 0.044258 0.061342 0.001 0.001 0.02 1.2481 1.1813 0.787279 5.590713 14.62841 31.75008 1.165552 0.041388 0.045331 0.062028 0.001 0.001

3 1073.7 78.7 206.0 165.0 75.8 80.42956 79.34073 -48.5607 81.59294 78.98393 138.23 78.19 138.02 0.02 0.02 4 1083.1 78.9 211.4 173.2 75.7 80.5655 79.47006 -53.9815 81.6153 78.97313 138.31 77.80 136.38 0.02 0.02 5 1090.1 78.5 214.2 181.2 75.7 80.61886 79.64221 -15.0831 81.65725 79.08931 140.57 78.09 138.14 0.02 0.02 6 1107.8 78.8 218.2 188.9 75.9 80.52724 79.70237 -7.25183 81.6744 79.00631 140.10 78.09 136.66 0.02 0.02 7 1125.4 79.0 220.8 195.9 75.6 80.5518 79.56853 -33.4654 81.87086 79.22469 139.03 77.96 136.56 0.02 0.02 8 850.3 79.0 175.3 197.6 75.9 80.59462 79.4134 -14.058 81.68803 79.12052 140.86 78.15 138.25 0.02 0.02 9 802.6 78.2 158.7 196.9 75.4 80.52354 79.68547 -56.548 81.85845 79.09258 141.95 78.24 139.20 0.02 0.02 10 781.6 78.0 150.5 195.9 75.7 80.71395 79.48653 -38.58 81.55883 78.8891 139.17 77.93 138.36 0.02 0.02 11 764.1 78.8 145.7 195.3 75.4 80.67471 79.68486 -11.4166 81.74419 78.99679 139.87 77.99 136.84 0.02 0.02 13 753.5 78.1 141.7 195.0 75.7 80.55604 79.33522 -12.6504 81.73125 78.93681 141.26 78.05 138.28 0.02 0.02 14 858.4 78.3 148.9 195.4 75.7 80.61687 79.66002 -8.58039 81.42617 78.60062 140.51 77.82 138.40 0.02 0.02 15 813.6 78.4 150.9 198.8 75.8 80.47837 79.33675 -10.054 81.59207 78.82242 141.54 78.03 139.19 0.02 0.02 16 783.3 78.8 143.0 200.3 76.2 80.43353 79.35789 -35.6523 81.6919 78.77644 140.43 78.08 137.05 0.02 0.02 17 779.0 78.1 140.2 201.2 75.5 80.18968 79.27242 -70.452 81.66885 78.7999 137.84 77.90 137.21 0.02 0.02 18 777.1 77.5 138.8 202.7 75.7 80.40636 79.40991 -31.6857 81.62549 78.82285 139.87 78.15 138.02 0.02 0.02 19 777.8 78.3 138.2 203.5 76.1 80.44829 79.41884 -53.2634 81.58922 78.99355 137.83 78.22 138.16 0.02 0.02 20 775.2 77.9 137.1 204.3 75.3 80.34117 79.27873 -54.2454 81.56037 79.05129 140.92 78.04 137.85 0.02 0.02 12 760.5 78.4 143.2 195.0 76.0 80.692 79.60976 -44.9166 81.76936 79.18917 141.89 78.07 139.52 0.02 21 774.7 77.7 137.1 205.5 75.6 80.29657 79.12144 -13.6892 81.45975 78.77523 141.68 78.20 141.17 0.02 0.02 22 774.3 77.7 136.1 206.6 75.7 80.46095 79.35892 -61.7623 81.78421 78.93028 139.13 78.54 140.80 0.02 0.02 23 772.2 78.1 135.9 207.6 75.5 80.27148 79.29483 -72.4423 81.52205 79.0325 138.52 78.22 139.24 0.02 0.02 24 767.0 78.6 135.4 208.4 76.1 80.35197 79.32253 -17.9672 81.65276 79.0446 138.65 78.27 138.10 0.02 0.02 25 760.5 78.4 135.5 209.3 76.1 80.54349 79.36887 -66.1622 81.5687 78.93926 139.84 78.38 138.88 0.02 0.02 26 758.3 78.3 135.0 210.1 75.9 80.7253 79.4781 -21.5065 81.77199 78.83758 142.66 78.24 139.65 0.02 0.02 27 865.4 78.4 147.1 210.8 76.2 80.57182 79.3972 -41.3313 81.68867 78.94048 137.39 78.08 136.58 0.02 0.02 28 839.7 79.0 154.8 215.3 76.7 80.73986 79.66422 2.628293 82.07005 79.23251 136.88 78.28 135.99 0.02 0.02 29 726.2 79.0 136.4 215.9 76.2 80.74374 79.52953 -52.6694 81.77461 79.16804 137.55 78.10 138.65 0.02 0.02 30 684.9 78.3 129.0 215.7 76.1 80.99589 79.56391 -9.79716 81.71494 79.18755 138.14 78.20 139.52 0.02 0.02 31 669.0 79.2 124.1 213.9 76.4 81.18044 79.91343 -7.81604 81.97551 79.32934 139.43 78.39 136.78 0.02 0.02 32 657.3 78.7 121.4 213.4 76.8 81.03721 79.55904 -7.86331 81.7715 79.17812 139.20 78.23 137.06 0.02 0.02 33 651.3 79.6 119.6 212.6 77.1 81.09957 79.66759 -69.0236 81.84284 79.48703 138.33 78.32 138.98 0.02 0.02 34 644.7 79.0 118.3 211.5 76.1 80.90082 79.56123 -73.9692 81.80675 79.18698 139.50 78.12 140.06 0.02 0.02 35 660.5 78.6 118.7 210.2 77.0 80.93616 79.54377 -3.4868 81.80299 79.05642 137.56 78.29 136.68 0.02 0.02 36 726.9 78.8 139.2 209.8 77.8 80.95071 79.83547 -2.14565 81.95293 79.30676 139.52 78.31 137.74 0.02 0.02 37 686.1 78.8 136.0 207.0 76.6 81.04675 79.68076 -21.6815 81.78066 79.21368 141.70 78.32 139.36 0.02 0.02 38 638.3 78.8 121.3 206.0 76.6 80.84692 79.87026 -5.48595 81.8894 79.22344 141.26 78.29 138.59 0.02 0.02 39 599.7 77.9 116.2 203.6 76.0 80.80177 79.65354 77.04359 81.82433 79.15838 763.73 78.31 133.09 0.02 0.02 40 575.8 78.8 112.7 201.0 76.4 80.92252 79.66212 78.05622 81.64611 79.23751 150.28 78.38 138.95 0.02 0.02 41 550.8 78.1 110.5 197.9 76.3 80.8979 79.67049 78.96156 81.85927 79.27249 77.57 78.48 140.51 0.02 0.02 42 536.5 78.4 109.7 194.5 76.4 81.09905 79.95742 79.21825 81.91351 79.34653 78.88 78.29 137.55 0.02 0.02 43 523.7 77.8 107.9 191.9 76.3 80.86745 79.79842 79.25061 81.82796 79.24117 79.45 78.31 143.10 0.02 0.02 44 608.6 77.8 118.7 189.3 76.0 80.85121 79.73598 79.51814 82.00367 79.2849 79.63 78.36 78.22 0.02 0.02 45 645.4 78.0 120.6 190.7 75.9 80.85389 79.63968 79.23705 81.83954 79.25936 79.73 78.38 78.32 0.02 0.02 46 661.0 78.0 121.8 192.6 76.5 81.06255 79.91433 79.52491 82.02579 79.51819 80.18 78.86 78.83 0.02 0.02 47 700.1 78.4 123.8 195.6 76.4 80.94527 79.64526 79.40762 81.95646 79.2245 79.83 78.47 78.58 0.02 0.02 48 770.0 78.7 145.3 198.2 77.4 81.19811 79.63416 79.39651 81.62402 79.3474 79.73 78.47 78.70 0.02 0.02 49 724.4 79.7 131.8 200.6 77.3 81.04176 79.66917 79.19396 81.67826 79.32246 79.98 78.56 78.78 0.02 0.02 50 719.8 79.2 128.7 202.9 76.9 81.19229 79.64812 79.31149 81.72945 79.23505 79.91 78.49 78.66 0.02 0.02 51 719.3 78.9 126.9 203.9 76.6 81.07872 79.8447 79.58727 81.90547 79.39789 79.86 78.39 78.52 0.02 0.02 52 711.1 79.2 125.5 204.2 76.8 81.18571 80.08368 79.58208 82.03773 79.60273 80.34 78.56 78.70 0.02 0.02 53 701.6 79.0 124.4 204.6 76.5 81.09274 79.85872 79.65408 82.05189 79.69607 80.01 78.45 78.75 0.02 0.02 54 687.7 78.7 123.2 203.9 76.6 81.03316 80.22147 79.87825 82.18193 79.2784 80.07 78.46 78.71 0.02 0.02 55 674.8 78.7 122.1 203.5 76.6 81.08368 80.02784 79.64502 81.90866 79.46706 80.18 78.52 78.63 0.02 0.02 56 656.4 78.4 120.9 201.8 76.4 80.93337 79.77855 80.12163 81.79266 79.27847 80.17 78.38 79.30 0.02 0.02 57 642.5 78.2 119.6 199.9 76.6 80.93964 79.90359 80.62942 81.82594 79.35794 80.69 78.51 79.67 0.02 0.02 58 632.1 78.7 118.4 197.9 76.6 81.39983 80.245 80.79926 82.08282 79.45646 80.96 78.60 79.65 0.02 0.02 59 622.1 79.2 117.3 196.1 76.3 81.31718 80.07657 80.90797 82.10999 79.72119 81.00 78.62 79.50 0.02 0.02 60 606.8 79.1 117.0 193.7 76.7 81.25571 80.12729 80.70133 82.11941 79.41386 80.99 78.61 79.61 0.02 0.02

1.25 1.1832 0.787352 5.591048 14.62874 30.43458 1.155677 0.038919 0.0458 0.062184 0.001 0.001 1.25 1.1901 0.787352 5.591292 14.64365 29.22392 1.143851 0.035963 0.047516 0.062031 0.001 0.001 1.25 1.2093 0.784109 5.5905 14.66648 27.94012 1.137291 0.034323 0.052335 0.062391 0.001 0.001 1.25 1.2009 0.784195 5.590865 14.71174 26.63315 1.153836 0.038459 0.050235 0.062622 0.001 0.001 1.25 1.1601 0.784048 5.590043 14.7795 25.43835 1.146374 0.036594 0.040015 0.061833 0.001 0.001 1.21 1.1724 0.784121 5.590835 14.88441 24.33376 1.156762 0.03919 0.04309 0.053488 0.001 0.001 1.21 1.1587 0.784195 5.590804 14.99029 23.54373 1.163662 0.040916 0.03968 0.052293 0.001 0.001 1.21 1.1706 0.781208 5.590804 15.07308 22.82075 1.150617 0.037654 0.042651 0.051964 0.001 0.001 1.21 1.1917 0.781342 5.591597 15.12663 22.03194 1.142327 0.035582 0.047937 0.051409 0.001 0.001 1.20 1.1726 0.781049 5.590744 15.22484 20.52136 1.149252 0.037313 0.043151 0.050784 0.001 0.001 1.25 1.2052 0.77833 5.591444 15.26144 23.38767 1.163918 0.04098 0.051311 0.062284 0.001 0.001 1.21 1.1699 0.778379 5.583519 15.29198 19.0303 1.136182 0.034045 0.042475 0.051781 0.001 0.001 1.21 1.1621 0.778245 5.583093 15.32197 18.32927 1.131634 0.032909 0.040518 0.051305 0.001 0.001 1.20 1.1824 0.775185 5.583215 15.35325 17.72943 1.155738 0.038934 0.045599 0.051156 0.001 0.001 1.21 1.2225 0.77527 5.583489 15.37473 17.12959 1.136267 0.034067 0.055614 0.05215 0.001 0.001 1.21 1.1828 0.775197 5.583946 15.38177 16.52487 1.15781 0.039453 0.045705 0.051601 0.001 0.001 1.21 1.1937 0.772149 5.583672 15.40604 15.92747 1.158481 0.03962 0.048418 0.0519 0.001 0.001 1.21 1.1912 0.77193 5.575473 15.41384 15.43126 1.146094 0.036523 0.047809 0.051772 0.001 0.001 1.21 1.1527 0.772307 5.576357 15.42838 14.82288 1.143521 0.03588 0.038186 0.051388 0.001 0.001 1.21 1.1820 0.772161 5.575656 15.44408 14.31692 1.126428 0.031607 0.045492 0.051942 0.001 0.001 1.21 1.2236 0.769284 5.576143 15.45048 13.81705 1.156749 0.039187 0.055907 0.05204 0.001 0.001 1.21 1.1904 0.769089 5.575625 15.45907 13.21843 1.148362 0.03709 0.047589 0.051851 0.001 0.001 1.21 1.1483 0.769101 5.568737 15.45773 12.71125 1.140278 0.03507 0.037077 0.051421 0.001 0.001 1.25 1.1888 0.766187 5.568523 15.46654 16.21519 1.142644 0.035661 0.047205 0.063485 0.001 0.001 1.21 1.1859 0.766285 5.569834 15.4659 11.50547 1.134439 0.03361 0.046467 0.051875 0.001 0.001 1.20 1.1882 0.766138 5.560477 15.46566 11.00073 1.157359 0.03934 0.04704 0.049955 0.001 0.001 1.19 1.1787 0.748033 5.454103 14.27362 10.61425 1.155945 0.038986 0.044672 0.048577 0.001 0.001 1.19 1.1652 0.747741 5.453585 14.27405 10.2046 1.173001 0.04325 0.041295 0.047029 0.001 0.001 1.19 1.1863 0.748411 5.455017 14.29658 9.898583 1.157944 0.039486 0.046586 0.047267 0.001 0.001 1.19 1.1932 0.747948 5.454042 14.31169 9.605978 1.160139 0.040035 0.04829 0.046685 0.001 0.001 1.19 1.1812 0.748058 5.447306 14.31956 9.203647 1.132183 0.033046 0.045306 0.046642 0.001 0.001 1.19 1.1904 0.748009 5.45453 14.35619 8.904945 1.151641 0.03791 0.047601 0.046846 0.001 0.001 1.22 1.1680 0.718395 5.50095 14.33501 14.01212 1.129403 0.032351 0.041999 0.053966 0.001 0.001 1.19 1.1969 0.202202 2.153789 18.22215 8.306324 1.149886 0.037471 0.049235 0.046892 0.001 0.001 1.18 1.1865 0.271635 6.702888 13.084 8.097844 1.153763 0.038441 0.046632 0.044606 0.001 0.001 1.18 1.2136 0.940824 10.40718 8.579951 7.900335 1.159078 0.03977 0.053408 0.043804 0.001 0.001 1.17 1.2181 0.6791 12.29869 7.048101 7.711361 1.166978 0.041745 0.054529 0.043128 0.001 0.001 1.16 1.2032 0.34714 11.51615 8.254123 7.595538 1.139474 0.034868 0.050799 0.04089 0.001 0.001 1.17 1.2105 0.202117 10.80101 9.183449 7.501661 1.15319 0.038297 0.052621 0.041293 0.001 0.001 1.16 1.1749 0.175015 10.26658 9.830869 7.306591 1.1607 0.040175 0.04373 0.039552 0.001 0.001 1.19 1.2335 0.171674 9.994576 10.10275 11.81637 1.15069 0.037673 0.058373 0.047026 0.001 0.001 1.19 1.2355 0.115506 9.452433 10.67857 11.22384 1.127514 0.031878 0.058873 0.047197 0.001 0.001 1.19 1.2011 8.865015 24.56093 21.87658 10.70812 1.152373 0.038093 0.050265 0.047791 0.001 0.001 1.22 1.2225 0.024554 4.876908 9.952179 11.30674 1.128976 0.032244 0.05563 0.055606 0.001 0.001 1.20 1.1746 0.014277 4.835913 9.941754 9.796171 1.160785 0.040196 0.043648 0.04972 0.001 0.001 1.20 1.1860 0.016605 4.836004 4.661539 9.413346 1.118638 0.029659 0.046507 0.048788 0.001 0.001 1.20 1.2124 0.016898 4.846886 4.691652 9.006138 1.157774 0.039443 0.053094 0.049224 0.001 0.001 1.19 1.1865 0.013813 4.855176 4.713568 8.692807 1.136389 0.034097 0.046623 0.048492 0.001 0.001 1.19 1.1929 0.016691 4.862522 4.752276 8.403859 1.1518 0.03795 0.048235 0.04802 0.001 0.001 1.19 1.2200 0.016861 4.871178 4.789493 8.190501 1.135609 0.033902 0.055011 0.04791 0.001 0.001 1.19 1.1865 0.016959 4.879773 4.834877 7.900335 1.135328 0.033832 0.04662 0.04741 0.001 0.001 1.18 1.2132 0.016886 4.894861 4.872641 7.704046 1.143107 0.035777 0.053295 0.046154 0.001 0.001 1.18 1.2008 0.016971 4.902115 4.92531 7.493126 1.138888 0.034722 0.050198 0.045706 0.001 0.001 1.19 1.2002 0.016788 4.910253 4.978375 7.39803 1.148398 0.0371 0.050055 0.04648 0.001 0.001 1.18 1.1837 0.016788 4.91769 5.02318 7.205399 1.148447 0.037112 0.045916 0.04592 0.001 0.001 1.18 1.1930 0.159653 7.481218 11.09614 7.107863 1.154994 0.038748 0.04826 0.044716 0.001 0.001 1.17 1.2172 3.011226 12.7116 6.483616 6.996917 1.143302 0.035825 0.054304 0.043426 0.001 0.001

0.02 1.21 1.2262 0.781086 5.590652 15.18189 21.337 1.155091 0.038773 0.056556 0.051659 0.001 0.001

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