Laserfiche WebLink
GEORGE DEUKMFJ'AN, C'O'"7'0' <br /> -HEALTH AND WELFARE AGENCY <br /> STATE OF CALIFORNIA - <br /> DEPARTMENT OF HEALTH SERVICES I <br /> TOXIC SUBSTANCES DIVISION A - <br /> NORTHERN CALIFORNIA SECTION STATEMENT OF FACTS <br /> 4250 POWER INN ROAD <br /> SACRAMENTO,CA 95826 <br /> (916)739-3145 Proposed Resource Recovery Permit <br /> for <br /> Falcon Energy Associate <br /> 6540 South Austin Road <br /> Stockton, CA 95205 <br /> �- has <br /> Falcon Energy Associate (hereafter ,the facility" ) <br /> rvices <br /> applied to the California ment for aartment of Health Series "A" ResourceeRecovery <br /> (hereafter "Department" ) <br /> Facility Permit for the operation of a hazardous waste <br /> recycling facility located540 south Stockton.Austin Road in <br /> San Joaquin County near the city <br /> The facility will operate a used oil recycling plant that <br /> employs physical separation processes to recycle used oil <br /> into fuel oil products. I <br /> Hazardous waste operations start when the facility <br /> accepts used oil from local generators. Each incoming <br /> used oil load will be analyzed for Polychlorinated <br /> specific gravity, ater conten't�, <br /> total halogens , <br /> result O'f <br /> biphenyls (PCB) cont nt, a the f l f aci l ityashoint. ki lla determine <br /> the sampling analysis, <br /> whether or not the incoming materials can be processed at <br /> the plant. <br /> When the incoming used oil load is accepted, the waste <br /> will be discharged into one of the three which oncluden <br /> ister filter unit ( <br /> storage .tanks via a canthe used <br /> eight mesh filter media) . In the storage tanks , <br /> oil will be heated to improve flow characteristics he <br /> decrease the oil density for oil/water separation. - <br /> heated oil will then be discharged to thefirst% <br /> andeea <br /> ehea <br /> 8 ,000 gallon settling tanks via a pr <br /> canister filter ter densityhincludes 11 lubricants will tolthe <br /> esh <br /> media) . The light <br /> top of the settling tank and will be decanted to one o <br /> the other two settling tanks. The total residence time <br /> for the series of three settling tank decanting processes <br /> will be approximately 40 hours. <br /> Wastewater and other sediments will also be extra ed <br /> from the cone-shaped bottom of each of the settling tanks <br /> to a wastewater coalesced separator which w l Pemove <br /> umped <br /> more lubricants. The separated lubricants will <br /> will <br /> back to one of the storage tanks , <br /> � • � the wastewater <br /> be tested 'for hazardous cons-hues„s. If f low to a <br /> is determined dryer e systemZforoevaporation us , It 1 If , on he <br /> biomass rotary <br /> other hand, the wastewater is determined to be hazardous , <br />