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World Leader in Biogas Treatment Phone (360) 668-6021 Fax (360) 668-7017 Project: St. Petersburg Revision Date: 10/8/2008 Analytical Results ppbv TMS, Others 161 MM, MDM, D3 444 MDDM, D4 1,500 D5, D6 1,250 Total 3,355 μg/m3 598 Gas Constituents, VOCs Date Sulfur Species Date Inorganics Date Biogas Characteristics GAS STREAM CONDITIONS: Gas Avg. Molecular Weight: 25.4 Gas Density, lb/ft3: 0.49 ACF/lb.-Mole: 52.0 Total Moles/Hr.: 32.4 Total Relative Density: 0.87 Total Flow in SCFM: Pressure, psig: Temperature in Deg. F.: Total mJ/m3: 194 90 77 25.06 (± 20%) Total Flow in ACFM: Total Pressure (psia)*: Temperature in Deg. C.: 28 104.73 25.0 Silicon Source Pounds per Year % of Total Silicates μg Silicon per SCF μg Silicon per BTU 1Others: See Organosilicons Report D3 to D6 232.6 98.6% 668.0 1.014 MDM+MDDM MM 0.3 0.2 0.1% 0.1% 0.0 0.1 0.000 0.000 TMS, Others 2.7 Total 235.9 100% 676.1 < 0.01 - 0.09 + 2 5 - 5 0% 0.10 - 0.19 0.20 - 0.49 0.50 - 0.99 1.00 - 2.00 + > 4 0 0% Design Flow ACFM Model SAGTM SAGTM media Velocity ft3 FPM Resistance in. w.c.(1.5mm)* media (1.5mm) 4,021 18,185 18,945 41,749 9/14/2007 9/14/2007 9/14/2007 Other --- 9/14/2007 NIOSH Ash --- --- Silicon Species Contribution to Silicate Production (as SiO2) Potential Damage from Silicon μg Silicon per BTU Siloxane Removal Media Life Days to Breakthrough if H2S is 5 ppmv or lower Siloxanes and Organosilicons Major Gas Components TVOCS Organosilicons TVOCs Scan Inorganic Sulfur Organic Sulfur 9/14/2007 9/14/2007 Applied Filter Technology 1.2% 7.94 0.012 Potential Contribution to O&M Costs 19524 75th Avenue S.E. Snohomish, WA 98296 Siloxane Removal System Design Parameters D5 28 24D 12 38 9.0 9.0 1,125 48 42 41 36 32 D4 D3 MDM 28 24D 16 50 9.0 12.1 1,500 64 56 55 48 42 Depth ft. MM, TMS 28 18D 12 21 15.9 28 18D 16 28 15.9 20.5 625 27 23 23 20 18 27.3 825 35 31 30 26 23 1Assumes water has been removed from the gas stream and that the sulfur species and organics will not interfere with siloxane removal. Assumes that the temperature of the gas stream is 77 oF (25 oC). If water has not been removed to below 45% RH equivalent, the life of the media could be reduced by 50% or more. Media life calculations assume 2 beds in series. *Resistance based on 1.5 mm media. Hydrogen sulfide must be reduced to below 5 ppmv to protect SAGTM media. At constant operation, this gas will produce up to 235.9 lb. of silicates (as SiO2) per year upon combustion. NOTE: Breakthrough order is approximate. Actual field results may vary. To determine precise system performance, a pilot study is recommended. This page, this page format, these data and these calculation methods are the property of Applied Filter Technology, Inc. 19524 75th Ave. S.E., Snohomish, WA 98296 (360) 668-6021 and may not reproduced in any manner mechanically or manually, or divulged to any third parties without the express written consent of Applied Filter Technology, Inc. 1.03 + 5 0 - 1 0 0% + 1 0 0 - 2 0 0% + 2 0 0 - 4 0 0% lb. SAG *(psig + 14.7)PDF Image | ST PETERSBURG TABLE OF CONTENTS
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