Laserfiche WebLink
RECEIVE <br /> MAY 14 1993 <br /> CALIFORNIA REGIONAL WATER QUALITY CONTROL BOARP4VIRC)NWNTAL HEALTH <br /> ORDER NO. PERMIT/kRvicE <br /> WASTE DISCHARGE REQUIREMENTS <br /> FOR <br /> SIMPSON INVESTMENT COMPANY AND <br /> SIMPSON PAPER COMPANY <br /> RIPON MILL <br /> SAN JOAQUIN COUNTY <br /> The California Regional Water Quality Control Board, Central Valley Region, <br /> (hereafter Board) finds that: N <br /> anP y p n Paper Company, Ripon M�111 . Simpson Investment Com and Sim so <br /> (hereafter Discharger) submitted a Report of Waste Discharge, dated <br /> 31 July 1987, to discharge waste under the National Pollutant Discharge <br /> Elimination System. The Discharger has not discharged any wastewater to <br /> the Stanislaus River in the past seventeen years and no longer proposes <br /> to discharge to the Stanislaus River in the future. Therefore, NPDES <br /> Permit No. CA0004006, which expired on 1 February 1988, will not be <br /> renewed. The Discharger proposes the continued discharge of wastewater <br /> to on-site ponds and adjacent percolation fields. <br /> 2. The Discharger operates a paper mill in Section 29, T2S, R8E, MDB&M (see <br /> Attachment A which is hereby made part of this Order) . The Discharger <br /> discharges a maximum 1.8 mgd (6,817,000 liters/day) of combined treated A <br /> industrial wastewater and stormwater runoff to 90 of 228 acres owned by <br /> Simpson Paper Company (APN No. 259-340-01 and 259-340-02) for disposal <br /> by percolation and nonagricultural irrigation. Domestic waste is <br /> sewered to the City of Ripon wastewater treatment facilities. <br /> 3. The Discharger manufactures several grades of fine papers from purchased <br /> pulps which includes virgin bleached pulp, deinked post-consumer waste, <br /> and waste paper (secondary fiber) . The mills maximum daily production <br /> rate is 280,000 lbs of paper. Process water is added to bales of pulp <br /> to make a pulp slurry wh ch is made into paper. Dyes , starches, <br /> inorganic fillers, such as clay and titanium dioxide rosin and alum, are <br /> also added to the slurry during the papermaking process. The water that <br /> drains from the paper ("white water") , is recycled to be used in the <br /> makeup of additional pulp slurry. The "white water" holding tank and <br /> stock chests are dumped when colors are changed which may be as often as <br /> 2 to 3 times per day. Periodically, (once a month) the entire paper <br /> machine system is cleaned ("boiled out") with a caustic solution. The /] <br /> spent caustic is commingled with other mill effluent and discharged to \\// <br /> the clarifier. Wastewater effluent to the clarifier from the V <br /> papermaking process averages 1.0 - 1.2 mgd. <br /> 4. Regeneration brine from the cogeneration plant water softeners and the <br /> mill effluent are collected in a sump and discharged into a circular <br /> primary clarifier. The clarifier effluent is discharged into two <br /> aeration stabilization basins (ASB) in series (see Attachment B which is <br /> hereby made part of this Order) . The first ASB #1 is a 14-foot deep <br /> lined basin converted from an abandoned sludge pit. The second ASB #2 <br /> is an unlined 5-foot deep basin. Effluent from ASB #2 is disposed of <br />