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The vessel length is, therefore, where Ltb ta,g (1.23) ta,g = access/gas distribution allowance = 2 to 6 feet (depending on vertical vessel diameter) Finally, use the following equation to calculate the surface area of either a horizontal or vertical vessel: S D(L D / 2) Similar equations can be developed for other vessel shapes, configurations, etc. Based on vendor data, we developed a correlation between adsorber vessel cost and surface area: [10] (1.24) (1.25) where C 271F S0.778 vm vessel cost (fall 1999 $), F.O.B. vender7 adjustment factor for fabrication material (from Table 1.3) surface area of the vessels (ft2) Cv = Fm = S = Table 1.3: Adjustment Factors to Obtain Costs for Fabricated Material Material Fm Factor Reference(s) Stainless steel, 304 Stainless steel, 316 Carpenter 20 CB-3 Monel-400 Nickel-200 Titanium 1.0 [10] 1.3 [9,10,11] 1.9 [11] 2.3 [9,11] 3.2 [11] 4.5 [11] Equation 1.25 is valid for carbon adsorption vessels with surface areas (S) within the following range: 97 S 2110 ft 2 7 Two vendors provided information for the 1999 updates, neither felt that modifications to the capital costs of adsorber system between 1989 and 1999 were appropriate. The major change for 1999 was a decrease in the price of carbon.[4, 5] 1-23PDF Image | Carbon Adsorbers
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