Exhibit EMT-101 in Trans Alaska Pipeline System's et al proceeding under OR89-2 et al: Economies of Scales Analysis (2000 $).

Jnofflclal FERC-Generated PDF of 20040907-0512 Received by FERC OSEC 11/21/2002 in D o c k e t # : OR89-2-017 4~ Exhibit EMT- 61 Economies of Scale Ar~lysis ( 20O0 $} Unit SMM SMM Size (000) USGC USWC Coker Naphtha HT 6.5 8.4 10.8 CoVer Distillate HT 6.3 12.9 16.8 Coker Gas Oil HT 12.0 16.3 20.8 Sulfur Plant (TPD) 100.0 19.0 24.7 Tota/Coker UnNs 56.6 73.0 V)l~n Feed Unh Coker Naphtha HT 40 23.4 30.2 Coker Distillate HT 26 26.0 38.8 Coker Gas Oil HT 80 55.7 71.0 Sulfur Plant (TPD) 500 67.8 88.1 Total W t ~ Feed Unite 1~8 223.0 MbcedFeed Urd~ Coker Naphtha HT 46.5 33.3 43.0 Coker Distillate HT 36.3 38.2 47.1 Coker Gas Oil HT 92.0 67.8 86.4 Sulfur Plant (TPD) 600.0 78.3 101.8 qw Total Mixed Feed 21,5.7 278.2 Total Set~l~te Units (6 hvtlto~eters} Coker Naphtha HT 31.8 41.0 Coker DLsti]lete HT 38.9 50.5 Coker Gas O~ HT 72.0 01.8 Sulfur Plant (TPD) 86.7 112.8 Tota/Separate 229.4 296.1 4ira Econom/es of Sce/e. Sm4nos tLo~) Coker Naphtha liT -1.5 -2.0 Coker D~Jlbde liT 2.6 3.4 lie Coker Gas Oil HT 4.1 5.4 S u ~ r P/am (TPD) 6.5 11.0 Total Economies of Scale, ISBL 13.7 17.9 ISBL & OSBL 20.3 26.4 I With IDC and OwneFs Costs, $ MM 23.3 30.3 rJ~Jl~, |]i];~t! AJ~tJJ,A:~I,T0OM]IIIM810I 4gw 4m l)m ~ms~ed. d ~ T / : ~ : ~ R ~ . JJ...~.. P.""