october 2000 monthly progress report pol sites
october 2000 monthly progress report pol sites
october 2000 monthly progress report pol sites
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Cumulative Mass of Vo, Hydrocarbons Discharged<br />
r Extraction System<br />
MCB Camp1 Lejeune - Hadnot Point Fuel Farm, North West<br />
SVE Stack<br />
Commehts<br />
01/12/00 11:30 6460<br />
01/21/W 1242 8665<br />
02/01/w 13:46 6744<br />
02/07/W 13:46 6744<br />
02/16/W lo:47 6808<br />
02/25/W 12:38 7014<br />
03/16/W 13:30 7429<br />
03/21/W IO:06 7529<br />
03/28/W 10:00 7610<br />
04/05/w 13:30 7774<br />
04/11/w 930 7915<br />
04/18/W 9:35 8040<br />
04/27/W 10:30 8161<br />
05/03/w 730 8305<br />
05/09/w lo:00 8391<br />
05/15/00 14:30 8536<br />
05/24/W 8:15 8745<br />
06/01/W Ml5 8819<br />
06/06/W 1430 8928<br />
06/15/w 15:50 9146<br />
06/23/W 14:20 9338<br />
07/06/W 13:12 9638<br />
07/13/w 13:31 9806<br />
07/20/W 13:16 9974<br />
07/28/W 11:41 10148<br />
08/l l/W II:02 10392<br />
06/15/w 10:12 10428<br />
08/23/w 7:35 10511<br />
08/29100 7:45 10628<br />
09/13/w 8:05 10854<br />
09/22/w 1319 11010<br />
10/06/W 13:56 11134<br />
10/12/w 13156 11220<br />
10/18/W lo:02 11359<br />
10/25/W 13:25 11530<br />
10/31/w 13:25 11674<br />
9<br />
94<br />
355.5<br />
36.9<br />
16.4<br />
46.4<br />
51.4<br />
112<br />
84<br />
187<br />
42<br />
16<br />
120<br />
35<br />
8<br />
13<br />
64<br />
66<br />
24<br />
36<br />
32<br />
24<br />
16<br />
26<br />
22<br />
22<br />
6300<br />
6900<br />
3800<br />
7300<br />
7700<br />
6652<br />
6758<br />
6980<br />
3588<br />
6891<br />
3500<br />
3500<br />
3500<br />
8100<br />
6000<br />
7100<br />
1200<br />
600<br />
7800<br />
7900<br />
5700<br />
7600<br />
7000<br />
7800<br />
7700<br />
7800<br />
8200<br />
8100<br />
8400<br />
8800<br />
9700<br />
7900<br />
8200<br />
7900<br />
8425<br />
568<br />
549<br />
548<br />
460<br />
558<br />
565<br />
571<br />
559<br />
584<br />
570<br />
565<br />
560<br />
562<br />
562<br />
578<br />
574<br />
583<br />
591<br />
582<br />
589<br />
594<br />
587<br />
586<br />
595<br />
579<br />
587<br />
584<br />
570<br />
569<br />
573<br />
579<br />
587<br />
574<br />
566<br />
574<br />
575<br />
603<br />
684<br />
379<br />
714<br />
710<br />
602<br />
632<br />
609<br />
297<br />
566<br />
290<br />
325<br />
325<br />
548<br />
545<br />
634<br />
110<br />
56<br />
870<br />
724<br />
528<br />
656<br />
595<br />
702<br />
683<br />
727<br />
783<br />
774<br />
798<br />
827<br />
861<br />
749<br />
788<br />
749<br />
789<br />
0.25<br />
0.29<br />
0.20<br />
0.05<br />
0.50<br />
13.50<br />
17.90<br />
6.67<br />
3.06<br />
26.91<br />
1.89 50.20<br />
0.20 9.95<br />
0.10 2.85<br />
0.25 12.11<br />
0.27 13.33<br />
0.60 33.82<br />
0.45 4.42<br />
0.99 4.99<br />
0.22 14.46<br />
0.09 4.02<br />
0.64 37.45<br />
0.19 9.91<br />
0.04 2.67<br />
0.07 4.23<br />
0.34 22.13<br />
0.35 24.58<br />
0.13 8.85<br />
0.19 13.87<br />
0.17 12.59<br />
0.13 9.83<br />
0.09 5.70<br />
0.14 9.75<br />
0.12 7.84<br />
0.12 8.26<br />
7592.87<br />
7726.96<br />
7787.39<br />
7767.39<br />
7771.47<br />
7784.60<br />
8017.30<br />
8073.37<br />
8073.37<br />
8244.88<br />
8421.56<br />
8447.46<br />
8454.64<br />
8463.19<br />
8484.88<br />
8561.73<br />
8767.08<br />
8826.01<br />
8847.38<br />
8870.05<br />
8927.30<br />
9043.61<br />
9188.78<br />
9354.55<br />
9400.18<br />
9435.24<br />
9455.01<br />
9535.79<br />
9617.28<br />
9723.28<br />
9808.62<br />
9866.55<br />
9894.39<br />
9939.15<br />
10001.82<br />
10050.12<br />
System down for repairs to Separate<br />
Extra<strong>pol</strong>ated<br />
Da<br />
Notes:<br />
C = (PPM-,& Y K x (M&J I1000<br />
C: vspar concentration (mgfl)<br />
PPMww: FID reading (PPM)<br />
K: numberofmrbon atoms in calibration gas<br />
(1 in methane)<br />
TH: total hydrocarbons calculated ss gasoline<br />
GRO)<br />
percent water vapor by volume 0.003<br />
SVE Stack pipe diameter 4<br />
Q=(l-B)xVxAx(P/P~)xCTsmlT)<br />
(1: vsporflowale (SCFM)<br />
8: percent vaster vspor in flowstream<br />
V: vapor velocity (ftlmin)<br />
A: cross-sectional area (sq. fl)<br />
P: absolute pressure offlowstrsam (” Hg)<br />
Pm standard pressure (29.92” Hg)<br />
r: absolute temperature of Rowstream (degrees Rankine)<br />
T*. standard lempsmture (528 degrees Rankine)<br />
at 68 degrees F (from Peny’s handbook)<br />
* Estimated value due to malfunctionng instrument<br />
M=QxCx0.0895<br />
M: hydrocarbon recovery rate (lb/day)<br />
CM = [delta (blower meter houn)/24) * [(Mprevious + Mwrrent)/Z) + CMprevious<br />
Assumptions:<br />
Mg = 128 mgimg-mole<br />
Kg = 24.07 dsm”3/l(r6 gm -mole<br />
B = 0.003 from Perry’s Chemical Handbook<br />
A = 0.0873 sq. ft<br />
Hpff-nw Updated: 1 l/10/00 Page 2 of 2
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