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. 4 <br /> WASTE DISCHARGE RC:QUCREMENTS ORDERNO RS 200b 0088 =3 <br /> LANCE'TWINS FAMILY LIMITED dba t <br /> 4 . <br /> 7AH 4T Wf ODS-CELLARS ' <br /> SAN'JOAQUIN'COUNTY <br /> WASTEWATER TREATMENT-SYSTEM <br /> 9 Wastewater generate0om winery processing f�g activities(process/equipment cleaning,wash down <br /> ,operations; and bottling)'is collectedrin oor drains, screened,•pH adjusted,flow metered; <br /> ,,. <br /> :biologically treated m ponds;stared in a storage pond, aril'then and applied: Each of the <br /> `processes is'fi,6 described below <br /> 10 :'Screened grates will be installed on drains collecting wastewater at the crushing, bottling and barrel <br /> cleaning areas bf:the'winery',Wastevtiia'ter will be conveyedthiough piping Iiy;gravity"to a lift <br /> station that will pump water through a fine•screen. The fine.'screen will remove solids 1,Arker than <br /> 0.02 inch.' . <br /> I 1 Amin m,hydroxlde will 1}e-used for pH adjustment`and will be fed into the waste stream using <br /> an automati77 <br /> c sensor, iriaiiitarnirig the'pH influent t0 the treatment ponds betweenr6 and 7 ` <br /> i2 * Biological treatment for removal of Biochemical Oxygen DemandBOD Twill occur in they <br /> t '. Y .r �f�4n <br /> treatment ponds Two ponds withya�tcitai capacity of 1,3O,U00 gallonskw�ll b�scotst{ructcdtiThe <br /> ponds vurll be double lined with vzny. r egdivalenf liners equipped with leak detection system <br /> �< r>The treatment Pon_ ds will be eq rpped*'Mth up to 40 horsepower of floAting me h rca aerators.to <br /> provide surface aeration for o'rygeri errand and odor control Waste%' te, rrinstttuent <br /> _ -s+ ¢'ern r.r r fry' y <br /> TM r.concentratlons after biological treatment in;the ponds is presented below P T <br /> µ fReclaimed Water aReclatme;d Nater71 <br /> Compound rUnits -, Concentration Rafige Concentration Range g <br /> i <br /> r <br /> min-max avers e <br /> pH a x _pH.units 6:5`—9 5.' <br /> j X7:9 <br /> Dissolved Oxygen. i mg/L; 1-10 6 , <br /> $ Biocheiriical Oxygen Demand TO=160U k <br /> . 'her ical Oxygen°Demand tig/L' "NR ' "90Y <br /> lease m NR fl:2 F <br /> Settleable Solids ,k � g� NR x A 0 2 <br /> SNonfilterable ResiduejYz <br /> `volatile Suspended Solids in' NR �` 1$ r { <br /> t ' - �'' _ , { ��� <br /> otal Dissolved Solids rrig/L Y . 8-.150 0 <br /> �, d z' �r io-f�s r 1 <br /> I�iitrogen mgfi, <br /> 5 0 1=40 g ;, l » a <br /> orate (as Nitrate)' g <br /> g yL z <br /> �hi�s�horou m <br /> itrn e t t h ` �5 �jr3 [\ 0 vnq <br /> - ! 3 r u 4 `, h�7 L < <br /> lkalintty (CaCO3} rnglL NR <br /> << 5 x <br /> Chia ide tr�g�L f 2 5-"'2'1 0 -f r <br /> L ,. s l e Y -.v -.25 <br /> g NP, <br /> Sulfatm IT. <br /> , <br /> wasi%' a er concentrations and calculated values from Table 3, Report of'waste Qischarge Lange Twins' , <br /> Winery,'Wallace Group, !�`February 2006'': <br />