|
FAX Transmittal Memo No of PCs-Is a today s im•
<br /> e From
<br /> carnpany campany
<br /> FAX Y oc�an
<br /> cammrnts i
<br /> SYSTEMS MONITORING DATA y
<br /> Date: -'I —1 ¢ Location cle-r0-j �41`2 �F eld Technician (z �'-
<br /> 6fttt.2Station No 1414 , Job No- LQ!Ein Initial System StatusDown. System Type C+7/W
<br /> Tot. Hrs: 10294, I H0 K�0•�_7 Full, 4 fi of Full Drums, Propane
<br /> z
<br /> ,gyp M. current sTareo Pipe Size 1 D "
<br /> BEFORE ANY ADJUSTMENT:
<br /> INITIAL Dilution Valve Positron: open, r.Iosed or cracked Flow Meter scfm
<br /> INITIAL Vac 6vO " Op _off" H2O, dp " H2O, Ccic scfm, Calc scfm
<br /> l+7 C., before duut after dllut T`KHA. etore ailut c-Fer T7ut
<br /> INITIAL- lnfl ppm,flnfl- .-opm, Effl• m 0 pprn, tc-, ' 0�4%, Motor Amps.
<br /> before drlut 0
<br /> a:kU �,� 7 t7 Inrticl Rectrculat�on r
<br /> FINAL Dilution Valve Position: open. closed or cracked Flow Meter: scfm
<br /> FINAL Vac: 60 _" Hg, L.1p O r " H2O, Ap " H2O, Ccic scfm, Calc scfrn
<br /> be ore arlut crier Arlo ba,are cit t. aT•er c+iu1
<br /> FINAL: Infl- pprr, Infl-+d / ppm, Eff1 0 O PPm, CO2/.d,P�1 7� L7, Mctor Amps-
<br /> before ddut. after3 ifs �v b5 Final RecireulCTron oen� out. ,sect
<br /> Set Pt- Chcrnber Temp- fExit Terno =Motor Amo Rating-
<br /> STACK.
<br /> ating-
<br /> STACK. Temperature: F, Magnzhelic- Calc scfn, H2O: %
<br /> Field Instrument Lcst Monitoring ;� S her `-�rL ?4 'rG� A" S�F
<br /> Mani-fold Box Number ,/ Man[f olc Box Number. y
<br /> Well , � Vec. OZ CO2 ppmlValve Well r� Vac 02 1 CO2 I ppm Valy?
<br /> Vw-IA -76 1°1
<br /> 2.0 51 �, o � l a o P-i "11v I �! 1 0 01 ? 0 IC c l
<br /> Vw-2A 1 `� a 19,5 1 y , o f Ll!DO v o �'-1 1 15 1 Zi 1 0. 0 1 o
<br /> vt„/_zri 50 1 LD' S 1 1 ZZ boo C- c
<br /> v�-j-3Ar 1 -79 I Z I 10- 2 1 9 �
<br /> \i vi- 3 -3o TT—il v, Z 1 rj L) c7 I u �-
<br /> 1 v,., -7 5 1 1 -7 1 �,� 1 10 a
<br /> w -
<br /> -70 L o 1 0. 5 � (D � P-g I i l� 1 Z I 1 0' a � -
<br /> r-�w- I -78 Z 1 0.5 1 c.R rz
<br /> P_a, 1 �1 5 1 2- 0 0 1 10 o G 4
<br /> r-I w-z _74o Z o I C] 1 3 1 G c I 1 1
<br /> p.qw-3 -7 ) Z 1 1 5 GR c, _'-2!I 7,9 1 v:
<br /> -] 7 Z)
<br /> Mme_,k � e Zt 2.
<br /> I I I 1 !
<br /> • Otte DetI Y I Dcte Det j
<br /> Influent Effluent 1AnalyZed1Um1t1Lcb Factor InFlue^r _fluent Analv_ed Lirnttl Lcb lFac'J
<br /> Benzene I CH4 I I T
<br /> Tr Hg 11 C3 5— L
<br /> - ,Mvr_.,ac-E,,--- T�,c�,, wr � ,LJ �a Z
<br />
|