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HomeMy WebLinkAboutDEQ-CFW_000861729 2008 Air Emissions Inventory Supporting Documentation • Emission Source ID No.: WTS-A Emission Source Description: Central Wastewater Treatment Plant Process and Emission Description: The Wastewater Treatment Plant (WWTP) consists of the biological treatment of process and sanitary wastewater utilizing extended aeration. The WWTP is comprised of an open equalization basin and open -top tanks and clarifiers. The basin is mixed using floating mixers and the tanks are aerated primarily with diffused air. Emissions from the WWTP result from the volatilization of solubilized compounds which are air stripped via the aeration of the wastewater. The extent of the volatilization is a function of the specific compound's solubility in water and its vapor pressure, typically expressed as the compound's Henrys Law Constant. Also, the volatilization of an organic compound is dependent on its rate of biodegradability. For example, methanol which is a Hazardous Air Pollutant (HAP), is highly biodegradable, and as such its biodegradation rate is much faster than its volatilazation rate, thereby limiting the air emissions of methanol from the WWTP. Basis and Assumptions: The emissions of methanol and dimethylformamide from the WWTP were determined using the EPA WATER8 model. This modeling takes into account the specific operational units of the WWTP to predict the ultimate fate of specific compounds. Two major compounds that are treated in the WWTP are ethylene glycol and butyraldehyde. The Henry's Law Constant for ethylene glycol is 6.0 x 10e-08 atm-m3/mole which is very similar to the Henry's Law Constant for dimethylformamide of 7.4 x 10e-08 atm-m3/mole. Not surprisingly, ethylene glycol and dimethylformamide are both exempt from the wastewater control requirements of 40 CFR 63 Subpart G as both are excluded from Table 9 of that subpart. Because of the above, it will be assumed that the WWTP unit operation's emission factors for ethylene glycol are the same as those for dimethylformamide. However, the biodegradation rate of ethylene glycol will be assumed to be the same as that of methanol, since the technical literature found in the Handbook of Environmental Data on Organic Chemicals indicates that for an acclimated system, ethylene glycol is biodegraded at twice the rate of methanol. To be conservative, the slower methanol rate will be used. DEQ-CFW 00086172 • The Henry's Law Constant for butyraldehyde is 1.15 x 10e-04 atm-m3/mole which is higher than the Henry's Law Constant for methanol of 4.55 x 10e-06 atm-m3/mole, meaning the quantity that is air stripped from the wastewater would be expected to be higher than that for methanol. According to the Handbook of Environmental Data on Organic Chemicals, butyraldehyde is biodegraded at the same rate of methanol in an acclimated system. Because of the above, it will be assumed that the WWTP unit operation's emission factors for butyraldehyde are twice as those for methanol. To be conservative, the biodegradation rate of butyraldehyde will be assumed to be the same as that of the slower dimethylformamide rate. Information Inputs and Source of Inputs: Information Inputs Source of Inputs Estimated quantity of compounds entering the WWTP for the year SARA 313 Report and other Air Emission Inventory inputs Fugitive Emissions Determination: All air emissions from the Wastewater Treatment Plant are fugitive. Estimates of the emission for individual components are given in the following pages. DEQ-CFW 00086173 • 2008 Emissions from Wastewater Treatment Plant (WTS-A) BA DMF EtGly McOH To WWTP from Butacite (lb) 106,800 13,902 7,126 129,300 To WWTP from Nafion (lb) - - - 49,283 To WWTP from PMDF (lb) - - - - To WWTP from SentryGlas (lb) - - - To WWTP from Other Sources (lb) - - - - Total to WWTP (lb) 106,800 13,902 7,1261 178,583 Quantity entering EQB (lb) 106,800 13,902 7,126 178,583 Percent of compound volatilized 23.42% 0.29% 0.29% 11.71 % Quantity volatilized from EQB (lb) 25,013 40 21 20,912 Quantity leaving EQB (lb) 81,787 13,862 7,105 157,671 Quantity entering Predigester (lb) 81,787 13,862 7,105 157,671 Percent of compound volatilized 8.30% 0.10% 0.10% 4.15% Quantity volatilized from Predigester (lb) 6,788 14 7 6,543 Quantity leaving Predigester (lb) 74,999 13,848 7,098 151,128 Quantity entering Aeration Tank (lb) 74,999 13,848 7,098 151,128 Percent of compound volatilized 0.16% 0.002% 0.002% 0.08% Quantity volatilized from Aeration Tank (lb) 120 0 0 121 Percent of compound biodegraded 94.40% 94.40% 99.74% 99.7406 Quantity biodegraded in Aeration Tank (lb) 70,799 13,072 7,080 150,735 Quantity leaving to Cape Fear River (lb) 4,080 775 18 272 Butacite Quantity to Cape Fear River (lb) 4,080 775.19252 18 197 Nafion Quantity to Cape Fear River (lb) - - - 75 PMDF Quantity to Cape Fear River (lb) SentryGlas Quantity to Cape Fear River (lb) Nafion Quantity to Cape Fear River (lb) Total Quantity to Cape Fear River (lb) 4,080 775 18 272 Butacite Fraction Volatilized to Air (lb) 31,921 54 28 19,966 Nafion Fraction Volatilized to Air (lb) - - - 7,610 PMDF Fraction Volatilized to Air (lb) - - - - SentryGlas Fraction Volatilized to Air (lb) - - - - Nafion Fraction Volatilized to Air (lb) - - - - Total Volatilized to Air (lb) 1 31,921 1 541 28 1 27,576 * Source of Reduction Factors: EPA WATER8 computer model BA = Butyraldehyde DMF = Dimethylformamide EtGly = Ethylene Glycol McOH = Methanol DEQ-CFW 00086174 9 2008 Air Emissions Summary WTS-A Central Wastewater Treatment Plant A. VOC Compound Summary Compound CAS Chemical Name CAS No. Emission (lb.) BA Butyraldehyde 123-72-8 31,921 DMF Dimethylformamide 68-12-2 54 EtGly Ethylene Glycol 107-21-1 28 McOH Methanol 67-56-1 27,576 Total VOC Emissions (Ib.) 59,580 Total VOC Emissions (tons) 29.8 B. Hazardous Air Pollutant Summary Compound CAS Chemical Name CAS No. Emission (lbs) DMF Dimethylformamide 68-12-2 54 EtGly Ethylene Glycol 107-21-1 28 McOH Methanol 67-56-1 27,576 r� DEQ-CFW 00086175