Document pprvRKgK1y5Mgn4ZQKvedbYJj

f T--r ~ir n progress report 1.8, vnwwiaiCM HAMT jO . I 913VO: 3^57 ftf0T *0. I1 bATC 10 b /5 v.C. K MU wee AlCM IAMT CCMCBAL OM'CI m.C. caeca V ' COa-a,,.aTO. ^3 T.w. eat.Tea Qa.C. aciuca Q.*, * 3 a. a. aatbick Q CL leeca .3 R.M. Scott 13 J.A.Hellala ^TJ 0. , j 4 ) 13 L.H.Horcher Q .w. te**ao* 13 H.J. Horner 1 ., MOMU 13 H.F.JCellerman Q CeCe ANA0tOlt0tQUbll g (take MIMCSWKII a T.L.Ross {Ji-L m.kCaooai 13 J.R.McClain Qia. abcw DC J.H.Nichols OR.E. soden OTCft let. rtuiiHCC* Qj.lwti * Q .. CtLLOCe 13UC. rvalaauiTCB Qa. CkkiMCea G Anniston 13 W. Voss 2 z . J. Ceers Q titui: Mercury Recovery - DeNora Chlorine Cells c**o*.cu: c. E. Woodward (J. R. Savage) o*lc>*: To dstemi.-.e r.ercury loss sources in the WGX DeNora Chlorine Facility and to prepare a mercury material balance around the cell house. Q Inventory measurements of mercury for 1964 and the first half of 1565 show loss .of mercury at the rate of 0.4 pound mercury per ton of chlorine produced. The material balance determined acaaints for 0.37 pound mercury per ton of chlorine. Mercury price fluctuations ' have been between $5 and 59 a pound. Expenses of adding make up r.ercury average at around 5110,000 a year (mercury cost at $7 a pound). It is now felt that significant reductions can be made in usages. Major mercury lasses which were Identified are listed below with the appropriate mercury value - mercury cost at 57 a pound. Loss Source With NaOH from Decomposers (13 ceils) With XOH from Decomposers (9 cells) ' With Sewer .a ter With Vented Hydrogen Result of "Load Dumps" Mercury Loss Rate,lb/year 2240 2180 3700 3700 4Q0Q 15,820 Cost of Loss Source, S/year 15,660 15,260 25.900 25.900 23,000 $109,640* J' WGK * CONFIDENTIAL INFORMATION TV* UI *** < HaaiMiw CtmiMf w<ucw ait *< IA* rtcuifftl t( Im tti (tkt(*tA| it Meemernti ^eiteat *W wtA*futtie*. CiMtr w lilts er ttttr?, itt # - 263S517 U CM*U( tritMul ptm+m* *On Hs H tn ri o 5?. -- -- r. 0n *>r ~ h S5: Xc sn ?t H2 Sn S> H" --H >* s p; Ul o CD CD --1 WATER_PCB-SD0000006188 81370:3*57(1} 1' PS. 2 October 8, 1965 Future Work 1} Develop mercury recovery method for pump tank cover water. 2) Develop mercury recovery method for caustic and potaah filter backwashes. 3) observe performance of replacement hydrogen line coolers. . /jd C. E. Woodward __ Technical Services Dept. c 2- H [n H cn * n 0S1 SS5 *X r c s * >cw*. 8"- eg W jnr H HO wV) hn sn rn> Q* > -4 a |CQ 1 WCH 28333 IS i WATER_PCB-SD0000006189