silo 3 - U.S. Department of Energy

+
I I 2 I 3 I 4 I 5 I 6 I 7 I a
STREAM DESCRPTION
TOTAL FLOW
TO PROCESS
EXHWST FANS
TOT& FLOW
FROM PROCESS
EXHAVST FMIS
PROCESS
BVlLOlNG
EXHAUST
SILO 3 - MATERIAL BALANCE TABLE
TOT* EXHAUST
oncHmcx OF
FROU STACK EXCAVATOR ROOU
PND EXCAVATOR
SERVICE ROOM
SWAP PVUPS
oncnmx OF
WASTEWATER
PUUPS ---
PHASE 2 bPPLLS TO EXCAVATION OF SLO 3 UATERIAL.
3. UWOR OlSCREP/WCIES IN UASS BALANCE t4J.f THE RESULT OF
, EITHER ROUNDOFF OR TRUNCATIOII.
1. ESTIUATEO
TOT& OUANTITY TO BE OF 5088 SLO yoa. 3 UATERIAL TO BE REUOMO IS
6. OENSlTY OF 42.4 LBlFT J WAS USE0 FOR SLO 3 UATERIAL
FROU lQSTORC& DATA LNO CHmRLETERIZAWJN. TREATLBILITY
#MI COUPACTION STVDY.
7.mo 3 UATEWAL n 5.2% WATER BY WEIGHT FROM
STABelZATlON WORK PLAN 40430-WP-ooO2.
NOTES: 506.9
1. DURWG PHASE 2. PIR WILL BE REUOVED USING STREW 6.
2. DCRlNG PHASE 1. AIR CbN BE REUOVEO USING STREW 6
WRtNC SPOOL PIECE ADOITION TO PNELIUATIC VACWM WAND
ASSEMEiY.
3.STREAMS 18 AND 19 ARE OPERATED lNOlVlOUALLY
MATERIAL
7.BASED ON 5% BY WEIGHT OF SILO 3 MATERIAL IN THE
WASTEWATER STREAU.
3.THE FLW RATES SHOWN ARE INSTANTANEOUS.
REF OWG NO. DRAW niLE
PFO-WTWLL RETRIEVAL *H) FEE0 SYSTEUS
FUEC FROU PVS DISCHARGE
WASTEWATER OF VACUUM NTERYITTENT EXHWST
13 FEES
PFD-PROCESS VENT AND PAWXNC SlSTEUS
COLLECTION S W PUUP FROU FEES
ENS AhB
COLLECTION
PFD-LWITIYE M@ WASTEWATER SYSTEUS
SYSTEY BWS
m2qEENG
10004 I H V L NR FLOW DUCRW
8 STREAM NUMBER
* STREAM DESCRIPTION
SoMuLl FERROUS SULFATE CXLUTION WATER WED ADolTlVE )roxED ADDITIVE YXEO MOlTlVE NOZZLE FLUSH NOZZLE FLUSH SILO 3 MATERIAL
LIOIK)SUFONATE TO MOlTNE MX TO AOOlTNE TO CHARGE TO PACK= TO PACKPGE
TO LDMTNE UIX T M MX T M TANKSAMIOB LONJNG
TPNK STAN0 A STMIO e Lome
STMiO A
LOmNG
STAN0 B
2.PHpsE IbPPLlES TO REUUATK: REUOVU Of YLO 3 UATERIAL.
5. A PHASE OESlGNATION NOICATES USAGE OUN4TITY OUR!NG
THE W1CATEO PHASE ONLY. NO PHASE OESWATIOW INDICATES
USffiE OUANTITY IS THE W E OURP4C BOTH PHASES OF
0PERATK)FI.
S.STREAM 14 WILL BE IN OPERATION OURING PHASE 1 AND
SILO 1 INTRUSION ACTIVITIES (CUTTING OF THE CONCRETE
I4LL ).
6.STREAH 9 OPERATES OWING PHASE 1 TO PROVIDE A SLIGHT
VACUUM ON FEED CONVEYOR (FOR-10-5102).
8.STREANS 13A AN0 138 ARE NOT ACTIVE AT THE SAUE TIME.
10.RADON FLOW RATES ARE IN THE RANGE OF 1 X 10-6 CilHR,
WHICH IS CONSIOEREO TO BE NEGLIGIBLE.
I.RAOON CONCENTRATIONS ARE CONSIDERED TO BE NEGLIGIBLE~
il3.ONLY ONE OF THE SUU? P W S WILL OPERATE AT A TIME. :
\14.STREAU 18 IS SILO 3 MATERIAL PLUS ADDITIVES AN0 WATER :
1 REMSED PER CCN 40430-EG-035
0 SlEDTOCO)(STRVETDN m N m m m
II. .o
a m - m - -
.DI .nw I
lMulDDuL
UNITED STATES
DEPARTMENT OF ENERGY
FERNALD MVWoHlDlTAL NANAGEMENT PROJEC1
lI6-mmEl
FLOW MAGRALlS
PROCESS FLOW DIAGRAkl