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i <br /> Z T -W <br /> ON 9, 'NT MV�JO <br /> A <br /> A <br /> UNLOADING FILTER USED LUBRICANT SETTLING EVAPORATOR WATER F F <br /> PREHEATER FEEDSTOCK ATMOSPHERIC FINISHED OIL VEL FUEL OIL <br /> PUMP STORAGE TANKS TANKS FEED PUMP PUMP HEATER EVAPORATOR STORAGE TANKS BLENDING STORAGE <br /> FEED TANK TANK <br /> PUMP HOLDING <br /> RECTRC FINISHED FUEL 0 <br /> OLDING OIL MIXING FUEL IL <br /> TANK PUMP TRANSFER PUMP PUMP PUMP TRANSFER <br /> PUMP <br /> VENT i4 <br /> VENT <br /> VENT 1 TOT( PNORAL ) <br /> 2 k 1 VE <br /> NT <br /> { TOTAL FOR 3 } 1 <br /> 1 VENT 7 i OVERFEED <br /> ( TOTAL FOR 3 ) 1L � � ( ( TYPICAL <br /> A 1� 8 ) I OF 3 ) <br /> ( G-- 10 ) STEAM COILS <br /> _ VENT A <br /> ( TOTAL FOR 3 ) - <br /> J 3 6 I VENT <br /> I <br /> FI ' D I 11 i I <br /> UNLOADING <br /> f ! i C <br /> ( NOTE <br /> 10 2 ) ' <br /> STEAM <br /> E 9 <br /> 5 r_ <br /> 4 <br /> DRYER FEED F <br /> CONVEYOR <br /> - <br /> CONVEYOR - ( F-8 ) g DRYER BURNER <br /> ( M-- 1 1 , X-X ) �.� ( M- 1 1 , B-4 ) <br /> S <br /> ( TYPICAL FOR 2 ) <br /> — -----�- MIXING CONVEYOR <br /> UNLOAD ( M- 11 , E-7 ) <br /> 1 2 3 4 5 6 7 8 9 10 11 1.2 13 14 15 16 17 Ie 19 20 21 22 23 24 2S 26 27 28 29 <br /> ,NOPE 2 <br /> _ NOTE 3 <br /> USED LUBRICANT ( GPH ) 6o°.oa 600 600 566 566 566 0 I �� <br /> ------�• -----�.-�--- STEAM <br /> F._ SEPARATED WATER ( GPH ) �34 3� _ __-__ __ __- - <br /> _ ,000 _�_�_ _ - �-._ GENERATOR T T <br /> STEAM ( lb/hr ) 150 200 500 216 --- _.._.�.. - ... -_ .� <br /> 150 <br /> WELL WATER ( GPH ) <br /> I 120 <br /> FINISHED OIL ( GPH ) <br /> 540 s4o sus Boz 0 <br /> t'000 ,000 ,000 <br /> DISTILLATE ( GPH ) i oz ( C-3 ) <br /> BLENDED FUEL v ( GPH ) BURNER E <br /> { C-3 ) <br /> i 100 0 4 ( D-S ) B <br /> TEMPERATURE ( `F ) 60 100 250 100 340 160 160 160 i60 AMB 160000 340 300 30Q 30Q 300 100 100 100 60 � 60 60 60 60 <br /> 250 <br /> PRESSURE ( PSI ) Is 100 100 AMB I <br /> 1Q0 OVERFEED DRYER BURNERS <br /> RETURN <br /> sox ( ibs/dy ) i ATOMIZING STEAM <br /> 0*3 ( M�- 1 1 , B--4 ) <br /> NOx ( 1 bs/dy ) <br /> 806 NOTES t I - ALL FIGURES ARE ESTIMATED AVERAGES EXCEPT AVE/MAX WHERE <br /> INDICATED* <br /> ROC ( lbs/dy ) 0*06 0*08 0106 0*04 0* 04 0 2 <br /> 2* WATER DISPOSAL IS A BATCH OPERATION* <br /> TSP ( lbs/dy ) i 3* RECIRCULATION i Ods ION RATE CAN BE SET BETWEEN 0 AND 100 PERCENT , <br /> CO ( Ibsldy ) , 4o TO BE DETERMINED BASED ON AGGLOMERATION PROPERTIES AND <br /> 0*6 BUYERS REQUIREMENTS* <br /> w <br /> 5o BLENDING MIX IS DETERMINED BASED ON HEATING VALUE OF <br /> FINISHED OIL MAXIMUM DISTILLATE REQUIREMENT IS <br /> ANTICIPATED TO BE SO% * <br /> SCALE : o <br /> oSo <br /> - PROCESS <br /> LOW DIAGRAM <br /> B NO, 4490-009 <br /> -.. <br /> __. ._._ <br /> - - - <br /> RESOURCE RECOVERY +�R �w ' r'r� �.�r� <br /> SYSTEM <br /> ------ <br /> M- 12 0 <br /> �� ii rr oI r f - — _ SSU <br /> J !I j C7;G� r�i.Y� � r� .l.•R�_.r F? / _ .. -^-f"� _ <br /> t�f 1t G f l w_ - IE <br /> SB <br /> SEDGRARH/ ^ �. ., - <br /> 2811/SB 11 <br />