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HomeMy WebLinkAboutWQ0039473_Correspondence_20190423Soil, Water, & Environment Group, PLLC .3216 Layers Drive, Suite B Raleigh, NC 27607 Ph# (919) 831-1234 • Faxr {919) 899-9100 - htipalwnlv.swegrp.com Soil, Water, & Environment — Group April 23, 2019 Mr. Tom McKinney Department of Environmental Quality Division of Water Resources Non -Discharge Permitting Unit 1617 Mail Service Center Raleigh, NC 27699-1617 Re: WQ0039473, Atkinson Milling Company WWTF Wastewater Irrigation System Johnston County Dear Mr. McKinney, Please find enclosed our official updated notificaiton to DEQ regarding Permit No WQ0039473, Atkinson Milling Company WWTF, Wastewater Irrigation System, Johnston County, NC. 1. Wastewater parameters (pH, BOD and TSS): As we have reported, the laboratory analysis of the wastewater taken November 28, 2018 showed both BOD and TSS were out of compliance with the permit conditions. The wastewater sample taken on April 2, 2019 shows progress in bringing the parameters into compliance. Through the addition of magnesium hydroxide and/or calcium hydroxide, the pH appears to be settling out around 6.0, up from the pH of 4.4 noted in December 2018. This indicates good progress with pH adjustments. TSS is down from 138 ppm in December to 83 ppm in the last sample. Not unexpectedly, considering that the anaerobic upflow reactors have not been re- seeded, the BOD has not exhibited any significant reduction, from a level of 2580 ppm in December down to 2330 ppm. 2. Structural Compromise of the Settling Tank: The compromised settling tank has been removed from the system as of December 21, 2018. There was no visually apparent evidence of leakage when the tank was removed. No further structural modifications to the system should be necessary. 3. Progress in the Corrective Action Plan: The proposed corrective action plan was to replace the plastic settling tank with a reinforced concrete tank. The reinforced concrete tank was placed on December 21, 2018. The concrete tank appears to be functioning properly at this time. Over the period since the last update, the switch of the hushpuppy production line to the "new" unit has been completed. As was expected, there has been a corresponding drop in the overall wastewater production in the system due to the improved production process. At this time, the flows have been averaging in the range of 6,000 gallons per week, down from approximately 10,000 gallons per week previously. Flow reduction obviously is a benefit, as it provides additional storage time in the system for pollutant attenuation and reduces the effective hydraulic and process load onto the land application area. As noted previously, we are continuing to evaluate pH stabilization measures. Ideally, a pH between 6.5 and 7.0 is preferred, but the anaerobic decomposition should be acceptable at a pH in excess of 6.0. The initial use of calcium hydroxide has been hampered by the apparent need for aggressive agitation, which is mostly available in the latter portions of the system. Ideally, we want to be able to adjust pH from an initial point in the system, such as the floor drain in the processing area. The addition of magnesium hydroxide shows some promise and benefits over the calcium hydroxide in this case, including ease of handling, introduction at a more advantageous point, and possibly a flocculation effect that could improve the effectiveness of the settling tank and solids recovery components. There is apparently some additional flocculation effect present, as the TSS has been reduced by approximately 40%. At the point the pH is stabilized, it is proposed that the reactors be "spiked" with material from another treatment works to "jump start" the bacteria population's recovery in the reactor cell. It would be counterproductive to spike the reactor, merely to re -introduce low pH material that detrimentally affects the bacteria population. We are continuing to monitor the progress of the pH regulation within the system. We anticipate once the anaerobic upflow reactors have a re- introduced and stable bacteria population, we will see much better results on BOD reduction. At this point, the relatively small reduction (approximately 10%) is probably attributable to the overall reduction in solid materials as opposed to any improvement in biological treatment. We have identified a good potential source for suitable, biologically active "spike" material in the near vicinity, and will keep you informed as to progress. Because both the pH attenuation chemicals currently under evaluation contain either calcium or magnesium, we also propose to recalculate the Sodium Adsorption Ratio (SAR). Either chemical is required in fairly moderate amounts, so no ill effect to the land application area is anticipated, but verification by analysis is needed. We appreciate your assistance in this matter. We have replaced the structurally compromised components and actively working to bring the chemical and biological treatment components of the system back into compliance. We look forward to any comments you have on the progress of the corrective action plan and remediation as related to the permit for the Atkinson Milling Facility. Thank you. Sincerely, A.R. Rubin, PhD Stephen L. Crawford, PE Scott J. Frederick, NCLSS, El r—� Soil, Water, & Environment Group Enclosures: nla