HY-C Company, LLC
Date: November 10, 2016
Project No. G102523311
Page 9 of 16
TABLE 5. - GENERAL SUMMARY OF RESULTS
1 st Hour Emissions (g/hr)
Burn Rate (kg/hr)(Dry)
Run Time (min)
Run No.
7 2 1 3 4
2.30 2.41 3.89 5.63 5.91
15.29 11.91 10.51 8.89 4.09
414 405 214 150 154
TABLE 6. – CSA B415.1 RESULTS Run No.
CO Emissions (g/hr)
Heating Efficiency (% HHV)
Heat Output (Btu/hr)
7 2 1 3 4
153.46 123.38 157.53 312.05 289.21
68.8 67.8 67.0 48.4 61.1
29,718 30,678 48,188 50,944 67,064
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 8500 Btu/hr (19752 kJ/kg) and a moisture content between 18% and 28% on a dry basis.
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