FC1000E/SF1000E/X1020/L1020: EPA 2020 Certification Report

Certificate of Conformity Emissions – Wood Burning Forced Air Furnace EPA 40 CFR Part 60, Subpart QQQQ, ASTM E2515 ‐ 2011, CSA B415.1 ‐ 2010 (R2015), ALT ‐ 134 ‐ 2019 Certificate number: WHI18 – 10583804

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 FC1000E, SF1000E, L1020, X1020 Manufacturer’s Rated Output: 46,435 Btu/hour Weighted Average Emissions: 0.142 lb/million Btu/hour Weighted Average Annual Delivered Efficiency: 40.3% Average Stack Loss Efficiency: 69.57% Test Fuel Type: Cordwood Compliance: Certified to comply with 2020 particulate emissions standard. Report Number: 104415176MID ‐ 002A Revised Report Number: 104415176MID ‐ 002AR2

Certification body: Intertek Testing Services NA, Inc. Initial registration: October 30, 2018 Reissue Date: November 17, 2020 Revised Report Date: November 9, 2021 Date of expiry: December 3, 2026 Issue status: 4

Jean ‐ Philippe Kayl Vice President ‐ Global Certification

12/03/2021

Name

Signature

Date

Registered address: Intertek Testing Services NA, Inc. 545 E. Algonquin Rd. Arlington Heights, IL 60005 USA

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. Page 1 of 2

HY-C COMPANY, LLC TEST REPORT

SCOPE OF WORK EPA EMISSIONS TESTING FOR MODEL SF1000E REPORT NUMBER 104415176MID-002AR2 TEST DATE(S) 09/15/20 - 09/19/20 ISSUE DATE REVISED DATE 10/06/20 11/09/21 RECORD RETENTION END DATE 11/09/31 PAGES 25

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

REPORT ISSUED TO HY-C COMPANY, LLC 10950 Linpage Place St Louis, MO 63132 SECTION 1 SCOPE

Intertek Building & Construction (B&C) was contracted by HY-C Company, LLC to perform testing in accordance with EPA 40 CFR Part 60, “Standards of Performance for New Residential Wood Heaters, New Residential Hydronic Heaters and Forced-Air Furnaces,” 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", and ALT-134 EPA Alternate Test Method Letter, issued by the U.S. EPA on August 19, 2019. Results obtained are tested values and were secured by using the designated test method(s). Testing was conducted at Intertek test facility in Middleton, WI. This report does not constitute certification of this product nor an opinion or endorsement by this laboratory. SECTION 2 SUMMARY OF TEST RESULTS The appliance tests resulted in the following performance: Particulate Emissions: 0.14 lb/MMBtu Output Carbon Monoxide Emissions: 1.73 g/min

Heating Efficiency: 40.27% (Higher Heating Value Basis – Direct Output) Heating Efficiency: 69.57% (Higher Heating Value Basis – Stack Loss)

For INTERTEK B&C: COMPLETED BY: Ken Slater

REVIEWED BY: Brian Ziegler

Associate Engineer - Hearth

Technical Team Leader - Hearth

TITLE:

SIGNATURE:

DATE:

11/09/21

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 permit copying or distribution of 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(s) 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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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

SECTION 3 TEST METHOD(S) The specimen was evaluated in accordance with the following: EPA 40 CFR Part 60-2015 , Standards of Performance for New Residential Wood Heaters, New Residential Hydronic Heaters and Forced-Air Furnaces ASTM E2515-11 , Standard Test Method for Determination of Particulate Matter Emissions Collected by a Dilution Tunnel CSA B415.1-10 (R2015), Performance Testing of Solid-Fuel-Burning Heating Appliances ALT-134 EPA Alternate Test Method Letter , issued by the U.S. EPA on August 19, 2019. See Appendix A for a copy.

SECTION 4 MATERIAL SOURCE

A sample was submitted to Intertek directly from the client. The sample is the test sample used for the original testing performed in October 2018. The test unit was received at Intertek in Middleton, WI on September 9, 2020 and was shipped via the client. The sample was unsealed per the following requirements outlined by the U.S. EPA. In General: 1. Manufacturers are never allowed to unseal a heater. 2. Manufacturers must not involve themselves in the conduct of the test after the pretest burn has begun. 3. All communications must be included in the test documentation required to be submitted pursuant to § 60.533(b)(5) and must be consistent with instructions provided in the owner’s manual required under § 60.536(g), except to the extent that they address details of the certification tests that would not be relevant to owners or regulators. 4. Communications between the manufacturer and laboratory or third-party certifier personnel regarding operation of the wood heater must be limited to written communications transmitted prior to the first pretest burn of the certification test series. Specifics: 5. Take color photographs of the unsealed heater. Photos must include the front, top, and side views and must be date stamped. 6. Describe the tasks, tests, or procedures to be performed on the unsealed. Any modification to the heater will require prior EPA approval. 7. The results of the new certification test will supersede results obtained during the initial certification testing for the above-referenced heater.

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

8. Upon completion of the new test series, the heater must be re-sealed with a lab-specific seal in accordance with the 2015 Standards. (60.535(a)(2)(vii)). 9. Provide color photographs of the front, top, and side views of the resealed heater. Photos must be date stamped. 10. Submit the above documentation along with your new performance data, i.e., test report within 60 days after completion of the test(s). 11. The test report must include the EPA request to perform new tests on the heater, request to unseal the heater and EPA response granting the unsealing of the heater. 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. Because this is the original test sample used for EPA emissions testing, no additional conditioning was required. The unit's chimney system and laboratory dilution tunnels were cleaned using standard wire brush chimney cleaning equipment. On September 15, 2020 the unit was set-up for testing. SECTION 5 EQUIPMENT

EQUIPMENT Data Logger

INV NUMBER

CALIBRATION DUE

10/7/2020 4/7/2021 4/7/2021 1/24/2021 1/24/2021 1/13/2021 1/13/2021 12/9/2020 10/7/2020 10/7/2020 10/13/2020 5/13/2021

0.06°F 0.7 sec 0.7 sec

986

Timer Timer

1213 1212 1413 1414 1406 1407 1538

Flow Meter Flow Meter

0.020 slpm 0.020 slpm

Pressure Transducer Pressure Transducer

0.00007 inH2O 0.00007 inH2O

Hygrometer

0.74 %RH, 0.05°C

Balance

0.00023 g

713

Scale Scale

0.081 lb

.118 lb 22 fpm

1134 1457

Anemometer

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8431 Murphy Drive Middleton, WI 53562

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

SECTION 6 LIST OF OFFICIAL OBSERVERS

NAME

COMPANY

Danny Hanes

HY-C Company, LLC

Ken Slater

Intertek B&C Intertek B&C

Brian Ziegler

SECTION 7 TEST PROCEDURE

From September 16, 2020 to September 19, 2020, the unit was tested for EPA emissions. For 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 lb/MMBtu Output (0.4g/MJ) – For furnaces rated less than 65,000 Btu/hr Step 1 – 2017 – 0.93 lb/MMBtu Output (0.4g/MJ) – For furnaces rated more than 65,000 Btu/hr Step 2 – 2020 – 0.15 lb/MMBtu Output (0.026 g/MJ) TEST SET-UP DESCRIPTION A 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. AIR SUPPLY SYSTEM

Combustion air enters an inlet pipe 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 of the heater. The exhaust gases are assisted by a combustion blower. TEST FUEL PROPERTIES

Wood used for the testing is split and seasoned oak cordwood. Oak has a default heating value of 8595 Btu/hr (19973 kJ/kg) and a moisture content between 18% and 28% on a dry basis.

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

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.) FIGURE 1 – DILUTION TUNNEL

FIGURE 2 – STACK GAS SAMPLE TRAIN

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

FIGURE 3 – DILUTION TUNNEL SAMPLE SYSTEMS

Figure 3

SAMPLING METHODS 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. INSTRUMENT CALIBRATION 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.

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

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. 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. 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 interferences as prescribed by the instrument manufacturer’s instructions.

TEST METHOD PROCEDURES

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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8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

TUNNEL VELOCITY/FLOWMEASUREMENT 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.

PM SAMPLING PROPORTIONALITY Proportionality was calculated in accordance with ASTM E2515. The data and results are included in Appendix C.

DEVIATIONS FROM STANDARD METHOD: Use of ALT-134 for output rate categories. SECTION 8 TEST CALCULATIONS NOMENCLATURE FOR ASTM E2515: A

= Cross-sectional area of tunnel m2 (ft2).

B ws = Water vapor in the gas stream, proportion by volume (assumed to be 0.02 (2.0 %)). C p = Pitot tube coefficient, dimensionless (assigned a value of 0.99). c r = Concentration of particulate matter room air, dry basis, corrected to standard conditions, g/dscm (gr/ dscf) (mg/dscf). c s = Concentration of particulate matter in tunnel gas, dry basis, corrected to standard conditions, g/dscm (gr/dscf) (mg/dscf). E T = Total particulate emissions, g. F p = Adjustment factor for center of tunnel pitot tube placement. F p = V strav /V scent K P = Pitot Tube Constant, 34.97 s 𝑚𝑚 ec [ � 𝑔𝑔 𝑔𝑔 ∎𝑚𝑚𝑚𝑚𝑚𝑚𝑚𝑚� ( 𝑚𝑚𝑚𝑚 𝐻𝐻𝐻𝐻 ) ( 𝐾𝐾 )( 𝑚𝑚𝑚𝑚 𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤 ) ] 1 2 or = Pitot Tube Constant, 85.49 s 𝑓𝑓 e 𝑓𝑓 c [ � 𝑙𝑙 𝑙𝑙 𝑙𝑙 𝑙𝑙 −𝑚𝑚𝑚𝑚𝑚𝑚𝑚𝑚� ( 𝑖𝑖𝑖𝑖 𝐻𝐻𝐻𝐻 ) ( 𝑅𝑅 )( 𝑖𝑖𝑖𝑖 𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤𝑤 ) ] 1 2 L a = Maximum acceptable leakage rate for either a pretest or post-test leak- check, equal to 0.0003 m3/min (0.010 cfm) or 4 % of the average sampling rate, whichever is less. L p = Leakage rate observed during the post-test leak-check, m3/min (cfm). m p = mass of particulate from probe, mg. m f = mass of particulate from filters, mg. m g = mass of particulate from filter gaskets, mg.

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8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

m r = mass of particulate from the filter, filter gasket, and probe assembly from the room air blank filter holder assembly, mg. m n = Total amount of particulate matter collected, mg. M s = the dilution tunnel dry gas molecular weight (may be assumed to be 29 g/g mole (lb/lb mole). P bar = Barometric pressure at the sampling site, mm Hg (in. Hg). P g = Static Pressure in the tunnel (in. water). P R = Percent of proportional sampling rate. P s = Absolute average gas static pressure in dilution tunnel, mm Hg (in. Hg). P std = Standard absolute pressure, 760 mm Hg (29.92 in. Hg). Q std = Average gas flow rate in dilution tunnel. Q std = 60 (1 - B ws ) V s A [T std P s /T s P std ] dscm/min (dscf/min). T m = Absolute average dry gas meter temperature, K (R). T mi = Absolute average dry gas meter temperature during each 10-min interval, i , of the test run. T mi = (T mi(b) + T mi(e) )/2 where: T mi(b) = Absolute dry gas meter temperature at the beginning of each 10-min test interval, i, of the test run, K (R), and T mi(e) = Absolute dry gas meter temperature at the end of each 10-min test interval, i, of the test run, K (R). Ts = Absolute average gas temperature in the dilution tunnel, K (R). Tsi = Absolute average gas temperature in the dilution tunnel during each 10-min interval, i, of the test run, K (R). T si = (T si(b) + T m=si(e) )/2 where: T si(b) = Absolute gas temperature in the dilution tunnel at the beginning of each 10-min test interval, i, of the test run, K (R), and T si(e) = Absolute gas temperature in the dilution tunnel at the end of each 10-min test interval, i, of the test run, K (R). V m = Volume of gas sample as measured by dry gas meter, dcm (dcf). V mc = Volume of gas sampled corrected for the post test leak rate, dcm (dcf). V mi = Volume of gas sample as measured by dry gas meter during each 10-min interval, i, of the test run, dcm. V m(std) = Volume of gas sample measured by the dry gas meter, corrected to standard conditions. V m(std) = K 1 V m Y [(P bar + (ΔH/13.6))/T m ] where: K 1 = 0.3855 K/mm Hg for SI units and = 17.64 R/in. Hg for inch-pound units. V m(std) = K 1 V mc Y [(P bar + (ΔH/13.6))/T m ] where:

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

V mc V mr

= Vm– (Lp– La)u

= Volume of room air sample as measured by dry gas meter, dcm (dcf), and V mr(std) = Volume of room air sample measured by the dry gas meter, corrected to standard conditions. V m(std) = K 1 V mr Y [(P bar + (ΔH/13.6))/T m ] Where: K 1 = 0.3855 K/mm Hg for SI units and = 17.64 R/in. Hg for inch-pound units, and

V s

= Average gas velocity in the dilution tunnel. V s = F p K p C p (√ΔP avg )(√(T s /P s M s ))

V si = Average gas velocity in dilution tunnel during each 10-min interval, i, of the test run. V si = F p K p C p (√ΔP i )(√(T si /P s M s )) V scent = Average gas velocity at the center of the dilution tunnel calculated after the Pitot tube traverse. V strav = Average gas velocity calculated after the multipoint Pitot traverse. Y = Dry gas meter calibration factor. Δ H = Average pressure at the outlet of the dry gas meter or the average differential pressure across the orifice meter, if used, mm water (in. water). Δ P avg = Average velocity pressure in the dilution tunnel, mm water (in. water). Δ P i = Velocity pressure in the dilution tunnel as measured with the Pitot tube during each 10-min interval, i, of the test run. ΔP i = (ΔP i(b) + ΔP i(e) )/2 where: ΔP i(b) = Velocity pressure in the dilution tunnel as measured with the Pitot tube at the beginning of each 10-min interval, i, of the test run, mm water (in. water), and ΔP i(e) = Velocity pressure in the dilution tunnel as measured with the Pitot tube at the end of each 10-min interval, i, of the test run, mm water (in. water). θ = Total sampling time, min. 10 = ten min, length of first sampling period. 13.6 = Specific gravity of mercury. 100 = Conversion to percent. TOTAL PARTICULATE WEIGHT – ASTM E2515 M n = m p + m f + m g PARTICULATE CONCENTRATION – ASTM E2515 C s = K 2 (m n /V m(std) ) g/dscm (g/dscf) where: K 2 = 0.001 g/mg TOTAL PARTICULATE EMISSIONS (g) – ASTM E2515

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

E T = (C s – C r )Q std θ

PROPORTIONAL RATE VARIATION (%) – ASTM E2515 PR = [θ(V mi V s T m T si )/(10(V m V si T s T mi )] x 100 MEASUREMENT OF UNCERTAINTY – ASTM E2515 MU weighing = √ 0.1 2 • X GENERAL FORMULA – ASTM E2515 uY = √((δY/δx 1 ) x u 1 ) 2 + … + ((δY/δx n ) x u n ) 2 Where: δ Y/ δ x i = Partial derivative of the combining formula with respect to individual measurement xi, u i = is the uncertainty associated with that measurement. TOTAL PARTICULATE EMISSIONS – ASTM E2515 E T = (c s – c r ) Q std θ where: c s = sample filter catch/(sample flow rate x test duration), g/dscf, c r = room background filter catch/(sample flow x sampling time), g/dscf, Q std = average dilution tunnel flow rate, dscf/min, and θ = sampling time, minutes. MU OF c s c s = F c /(Q sample x θ) = 0.025/(0.25 x 180) = 0.0005555 δc s /δF c = 1/Q sample • Θ = 1/0.25 • 180 = 0.0222 δc s /δQ sample = -F c /Q 2 sample • Θ = -0.025/0.25 2 • 180 = -0.00222 δc s /δΘ = -F c /Q sample • Θ 2 = -0.025/0.25 • 180 2 = -0.000003 MUc s = √(0.00027 • 0.0222) 2 + (0.0025 • - 0.00222) 2 √ + (0.1 • - 0.000003) 2 = 0.0000091g Thus, c s would be 0.555 mg/dscf ± 0.0081 mg/dscf at 95% confidence level. MU OF c r

c r = BG c /(QBG x θ) = 0.002/(0.15 x 180) = 0.000074 δc r /δBG c = 1/Q BG • Θ = 1/0.15 • 180 = 0.03704 δc r /δQ BG = -BG c /Q 2 BG • Θ = -0.002/0.15

2 • 180 = -0.0004938

δc r /δΘ = -BG c /Q BG • Θ

2 = -0.002/0.15 • 180 2 = -0.0000004

MUc r = √(0.00027 • 0.03704)

2 + (0.0015 • - 0.0004938) 2

√ + (0.1 • - 0.0000004) 2 = 0.00001g Thus, c r would be 0.074 mg/dscf ± 0.01 mg/dscf at 95% confidence level.

E T AND MU ET

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TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

E T = (c s – c r ) Q sd θ = (0.000555 - 0.000074) x 150 x 180 = 13.00g δE T /δc s = Q std • Θ = 150 • 180 = 27,000 δE T /δc r = Q std • Θ = 150 • 180 = 27,000 δE T /δQ std = c s • Θ – c r • Θ = 0.000555 • 180 – 0.000074 • 180 = 0.08667 δE T /δΘ = c s • Q std – c r • Q std = 0.000555 • 180 – 0.000074 • 180 = 0.07222 MU ET = √(27,000 • 0.0000081) 2 + (27,000 • 0.00001) 2 (0.08667 • 3) 2 √ + (0.07222 • 0.1) 2 = 0.436

Thus the result in this example would be: ET = 13.00g ± 0.44 g at a 95% confidence level. EFFICIENCY – CSA B415.1 The change in enthalpy of the circulating air shall be calculated using the moisture content and temperature rise of the circulating air, as follows:

Δ h = Δ t (1.006 + 1.84x)

Where: Δ h

= change in enthalpy, kJ/kg

Δ t = temperature rise, °C 1.006 = specific heat of air, kJ/kg °C 1.84

= specific heat of water vapor, kJ/kg °C

= humidity ratio, kg/kg

The equivalent duct diameter shall be calculated as follows:

ED = 2HW/H+W

Where: ED

= equivalent duct diameter

= duct height, m = duct width, m

The air flow velocity shall be calculated as follows:

V = F p x C p x 34.97 x √T/28.56(P baro + P s )

where V

= velocity, m/s

F P = Pitot tube calibration factor determined from vane anemometer measurements C P = Pitot factor = 0.99 for a standard Pitot tube or as determined by calibration for a Type S Pitot tube 34.97 = Pitot tube constant Note: The Pitot tube constant is determined on the basis of the following units:

Version: 03/13/18

Page 13 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

m/s[g/g mole (mm Hg)/(K)(mm H 2 O)] 0.5

Δ P

= velocity pressure, mm H2O

T = temperature, K 28.56 = molecular weight of air P Baro

= barometric pressure, mm Hg = duct static pressure, mm Hg

P s

The mass flow rate shall be calculated as follows:

m = 3600VAp

where: m

= mass flow rate, kg/h

V = air flow velocity, m/s 3600 = number of seconds per hour A = duct cross-sectional area, m2 p

= density of air at standard temperature and pressure (use 1.204 kg/m3) The rate of heat release into the circulating air shall be calculated using the air flow and change in enthalpy, as follows:

Δ e = Δ h × m

Where: Δ e

= rate of heat release into the circulating air, kJ/h = change in enthalpy of the circulating air, kJ/kg

Δ h

= mass air flow rate, kg/h

The heat output over any time interval shall be calculated as the sum of the heat released over each measurement time interval, as follows:

E t = ∑ ( Δ e × i) for i= t 1 to t 2

Where: Et

= delivered heat output over any time interval t 2 –t 1 , kJ

= time interval for each measurement, h

The average heat output rate over any time interval shall be calculated as follows:

e t = E t /t

where e t

= average heat output, kJ/h

= time interval over which the average output is desired, h

Version: 03/13/18

Page 14 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

The total heat output during the burn shall be calculated as the sum of all the heat outputs over each time interval, as follows:

E d = ∑ (E t ) for t = t 0 to t final

Where: E d

= heat output over a burn, kJ/h (Btu/h)

E t

= heat output during each time interval, kJ/h (Btu/h)

The efficiency shall be calculated as the total heat output divided by the total energy input, expressed as a percentage as follows:

Efficiency, % = 100 × E d /I

Where: E d

= total heat output of the appliance over the test period, kJ/kg

I = input energy (fuel calorific value as-fired times weight of fuel charge), kJ/kg (Btu/lb) SECTION 9 TEST SPECIMEN DESCRIPTION The model SF1000E Solid Fuel Air Furnace is constructed of sheet steel. The outer dimensions are 50.5-inches deep, 42-inches high, and 25.5-inches wide. The unit has a fueling door located on the front. SECTION 10 TEST RESULTS DESCRIPTION OF TEST RUNS: RUN #1 (9/16/20): The furnace was set to draw a category 4 output rate. The test load weighed 30.61 lb. and utilized a 7.5 lb. coal bed. The average Btu/hr. output was 46,435. Burn time was 2.93 hours. The kg/hr. burn rate was 3.94. RUN #2 (9/17/20): The furnace was set to draw a category 2 output rate. The test load weighed 35.58 lb. and utilized a 6.6 lb. coal bed. The average Btu/hr. output was 21,540. Burn time was 5.82 hours. The kg/hr. burn rate was 2.31. RUN #3 (9/18/20): The furnace was set to draw a category 1 output rate. The test load weighed 37.19 lb. and utilized a 5.3 lb. coal bed. The average Btu/hr. output was 15,727. Burn time was 6.57 hours. The kg/hr. burn rate was 2.11.

Version: 03/13/18

Page 15 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

RUN #4 (9/19/20): The furnace was set to draw a category 3 output rate. The test load weighed 32.35 lb. and utilized a 7.0 lb. coal bed. The average Btu/hr. output was 24,739. Burn time was 3.73 hours. The kg/hr. burn rate was 3.19. TABLE 1 – DATA SUMMARY PART A Θ W fuel MC ave Q in

Q out

Wood Weight as- fired

Run No.

Load % Capacity <35% of Max 36-53% of Max 53-76% of Max Max capacity

Target Load Btu/hr 16,252

Actual Load Btu/hr 15,727

Actual Load

Test Duration

Wood Moisture

Heat Input

Heat Output

Cat

% of Max

hrs

% DB 21.97

Btu

33.87

6.57

37.19

262,070

103,277

24,610

21,540

46.39

5.82

35.58

19.92

255,004

125,290

34,826

24,739

53.28

3.73

32.35

21.55

225,737

92,358

46,435

100.00

2.93

30.61

20.27

218,757

136,210

TABLE 2. – DATA SUMMARY PART B E T E

E g/hr

 del

 SLM

PM Output Based

Load % Capacity

Total PM Emissions

PM Output Based lb/mmBtu Out

1 st Hour Emissions

1 st Hour Emissions Lb/mmBtu Out

Delivered Efficiency

Stack Loss Efficiency

Category

Run No.

0.946

37.280

0.059

65.856

0.137

0.976

0.404

0.061

3.005

0.004

4.290

0.009

0.085

0.669

0.048

1.931

0.002

3.298

0.005

0.053

0.210

0.012

0.773

0.001

0.831

0.001

0.028

0.448

Totals

1.055

40.267

0.065

69.572

0.142

1.070

1.731

TABLE 4 - CSA B415.1 STACK LOSS RESULTS

RUN NO.

CO EMISSIONS (g/min)

HEATING EFFICIENCY (% HHV)

HEAT OUTPUT (Btu/hr)

3 2 4 1

1.62 2.68 0.84 1.79

69.60 70.10 69.00 67.00

27,524 30,288 41,565 48,998

SECTION 11 CONCLUSION

This test demonstrates that this unit is an affected facility under the definition given in the regulation. The emission rate of 0.142 lb/MMBtu Output meets the EPA requirements for the Step 2 limits. The models FC1000E, X1020, and L1020 are identical to the tested model SF1000E with the only differences being the exterior color and the name casted into the fuel door.

Version: 03/13/18

Page 17 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

SECTION 12 REVISION LOG

REVISION #

DATE

PAGES

REVISION

0 1

10/06/20 11/17/20

N/A

Original Report Issue

Updated report to HY-C Alt Test Method Updated report back to ALT-134 Alternate Test Method Added correct dilution tunnel information to Figure 1. Removed HY-C Alt Test Method and added ALT- 134 Alt Test Method

2, 3, 9

11/9/21

19-21

Version: 03/13/18

Page 18 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21 SECTION 13 APPENDIX U.S. EPA Alternate Test Method Letter

Version: 03/13/18

Page 19 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 20 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 21 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 22 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 23 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 24 of 25

RT-L-AMER-Test-3778

8431 Murphy Drive Middleton, WI 53562

Telephone: 608-836-4400 Facsimile: 608-831-9279 www.intertek.com/building

TEST REPORT FOR HY-C COMPANY, LLC Report No.: 104415176MID-002AR2 Date: 11/09/21

Version: 03/13/18

Page 25 of 25

RT-L-AMER-Test-3778

5/9/2018 6/8/2020 1

Approved By Issue Date Revision Date Revision Level

Brian Ziegler

Middleton Laboratory Local Operating Procedure

This Calibration procedure applies to all Dry Gas Meters in Middleton, Wisconsin Laboratory.

Equipment used: Spirometer

Using the Spirometer: The Spirometer consists of two tanks. The green tank has a U-tube on it to show any pressure (either positive or negative) in the green tank. The sight glass vial with the ruler near it tells what the level of water is in the green tank. The controls at the Spirometer consist of a water valve and a clamp for the hose. The valve controls the flow of water between the tanks. The clamp controls the up and down movement of the red tank. NEVER STAND UNDER THE RED TANK WHEN IT IS ELEVATED!!

When the Spirometer is not in use most of the water is stored in the red tank on the floor.

1. Connect hoses to Dry Gas Meter (DGM) and manometer as shown in figure 1 for leak test.

Figure 1

2. With spirometer clamped off pressurize the system by blowing into the hose, which is attached to the inlet port of the DGM. When there is 6 to 8 inches of pressure, clamp off the hose you just blew into. The manometer liquid will rise until pressure is equal in the system then stop. If the manometer does not stop rising there is a leak. Repair the leak as necessary and recheck. 3. Connect as in figure 2 for calibration of the meter. In this case, the manometer is used to monitor the pressure at the DGM. A reading of 2.0 in H2O with the system operating indicates a flow restriction that must be remedied before continuing the calibration.

Figure 2

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7. Perform 5 runs to determine an average. Pass/fail criteria is ±1.0% for the measurement of uncertainty. If not passing, adjust and repeat the test. After adjusting the pressure in the green tank to zero using the water valve, measure the amount of water in the green tank with the ruler. (Typically around 22 inches ± 1 inch) Interpolate this measurement to the nearest 1/32 of an inch and convert to decimal. This figure is used in the Spirometer Calibration program found where these instructions were located. Enter this number into the spreadsheet and the final DGM number after the run. 5. Plug the manometer hose on the green tank. Turn the water valve on (to start water flowing into the green tank). (The sample rate is usually set on a "set up" run, as the first run will not be used in the calibrations.) Enter the initial DGM reading into the spreadsheet. Sample 1 cubic foot as near as possible then pinch off hose leading from the Spirometer (this prevents the DGM from being driven backwards) and quickly go out to the Spirometer and close the water valve. While sampling, include the barometric pressure, Spirometer temperature, meter temperature and meter pressure (from the manometer) into the spreadsheet. 6. Without removing the hose clamp at the meter, lower the red tank and adjust the water in the green tank using the water valve so there is no pressure in the green tank. This requires you to unplug the left manometer hose. Do this with care, as there might be enough pressure to either blow the fluid out of the hose or draw it into the green tank. Adjust the pressure in the constant volume tank (green) using the water valve. Normally you have to add water to the constant volume tank to equalize the pressure but if you go too far, it will be necessary to lower the red tank and allow some water out of the green tank. This takes some practice. 4. Raise the red tank above the green tank. Plug the manometer on the green tank. (Plugging the manometer hose when transferring water in either direction keeps the fluid in the manometer from being forced either out of the hose or into the green tank.) Using the water valve adjust the water in the green tank just enough to be able to adjust the ruler up or down to zero the ruler with the water level. Set the ruler bottom at the top of the meniscus. Unplug manometer slowly on green tank and using the water valve, toggle on and off until the manometer on the green tank shows no pressure at all. The fluid in the two tubes will be level when there is no pressure in the green tank. Leave the clamp open and reset the ruler if necessary. At this point, clamp open, water off, manometer levels the same and the ruler at the top of the meniscus in the water level vial, you are ready to start sampling.

Following the successful calibration of this piece of equipment a calibration sticker shall be attached to the instrument.

Measurement Uncertainty is calculated using the following formula: O.M.U. = k*((A.D.)2 + (S.D.)2 + (R.M.U.)2)1/2 O.M.U. = Overall Measurement Uncertainty A.D. = Average Deviation of the percent difference of all measured results compared to the reference value. S.D. = Standard Deviation of the percent difference of all measured results compared to the reference value. k = Confidence Factor (2 for 95% confidence) R.M.U. = Standard Measurement Uncertainty of Reference Measurement Equipment. R.M.U. is considered as the measurement uncertainty as stated on calibration certificates of equipment, or the tolerance listed in the calibration standard of the test equipment

LMS-AMER-MID-WI-13

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8431 Murphy Drive Middleton, WI 53562

Calibration Certificate Number Issue Date

6/8/2020 1210-MID-05-08-20

Middleton Laboratory Local Calibration Certificate

1210 Rockwell 974270 See Procedure Tab

Dry Gas Meter DGM-110

Serial Number Manufacturer Asset Number

Calibration Date Calibration Due Date Asset Description Model Number As Found Condition As Left Condition Calibration Location

11/8/2020 5/8/2020

Procedure

Relative Humidity (%) QA's Name Ambient Temperature ( o F)

67.4 30

Middleton Lab In Tolerance In Tolerance

Quality Supervisor Christine Schultze

QA's Title

QA's Signature

Calibration Data Summary

Measurement of Uncertainty (MU)

Adjusted? No

Maximum As Found As Left 0.0100 0.0062 0.0062

The above results relate only to the equipment calibrated. This Calibration Certificate shall not be reproduced except in full, without written approval of the laboratory.

End of Calibration Certificate

LMS-AMER-MID-WI-13

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Calibration Certificate Number

1210-MID-05-08-20

Issue Date

6/8/2020

Middleton Laboratory Local Calibration Data

1210

Asset Number Calibration Date Calibration Due

Asset Description

Dry Gas Meter Ken Slater Brian Ziegler

5/8/2020 11/5/2020

Peformed By Reviewed By

Reference Equipment

Asset Description - Asset Number Spirometer - #51

Calibration Due Calibration Due Calibration Due Calibration Due

4/8/2021 12/9/2020 1/9/2021 5/8/2021

Asset Description - Asset Number Starrett Tape Measure - #1470 Asset Description - Asset Number Hygrometer - #1538 Asset Description - Asset Number Temp reader - #1312

Ambient Temp ( o F)

Barometric Pressure (in Hg)

67.4

Relative Humidity (%)

29.08

As Found Data

Spirometer Temp ( o F)

Meter Temp ( o F)

Run Number

Meter Initial

Barometric Pressure (in Hg)

Vapor Pressure of H2O (Hg)

Meter Pressure (in Hg)

Measurement (in)

Spirometer Volume

Meter Final

29.08 29.08 29.08 29.08 29.08

68.1 68.3 68.3 68.3 68.1

0.6909 0.6909 0.6863 0.6863 0.6909

1 2 3 4 5

228.024 229.038 230.046 231.05 232.053

68.8 68.8 68.7 68.9 68.8

4 4 4 4 4

22.375

1.0170 229.038 0.98063 1.0114 230.046 0.98043 1.0057 231.05 0.97862 1.0114 232.053 0.9855 1.0028 233.056 0.97754 1.0097 Ave 0.98054 0.0055 Std Dev 0.00305 M of U 0.00621

22.25

22.125

22.25

22.0625

Pass

As Left Data

Spirometer Temp ( o F)

Meter Temp ( o F)

Run Number

Meter Initial

Barometric Pressure (in Hg)

Vapor Pressure of H2O (Hg)

Meter Pressure (in Hg)

Measurement (in)

Spirometer Volume

Meter Final

29.08 29.08 29.08 29.08 29.08

68.1 68.3 68.3 68.3 68.1

0.6909 0.6909 0.6909 0.6863 0.6863

1 2 3 4 5

228.024 229.038 230.046 231.05 232.053

68.8 68.8 68.7 68.9 68.8

4 4 4 4 4

22.375

1.0170 229.038 0.98063 1.0114 230.046 0.98043 1.0057 231.05 0.97862 1.0114 232.053 0.9855 1.0028 233.056 0.97754 1.0097 Ave 0.98054 0.0055 Std Dev 0.00305 M of U 0.00621

22.25

22.125

22.25

22.0625

Pass

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33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81

0.187 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.195 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.203 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.211 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.219 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.228 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.237 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.247 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.256 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.266 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.277 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.287 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.298 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.310 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.322 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.334 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.347 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.387 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.402 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.417 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.432 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.448 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.465 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.482 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.499 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.517 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.536 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.555 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.575 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.595 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.616 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.638 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.661 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.684 0.6863 0.6909 0.6909 0.6909 0.6863 0.6863 0.707 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.732 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.757 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.783 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.810 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.838 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.866 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.896 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.926 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.957 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.989 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 1.022 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 1.056 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.6909 0.6863 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000

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