Carbon Adsorbers

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Carbon Adsorbers ( carbon-adsorbers )

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(NA ND) 1.9.2 Cost Estimate Example Q 10,000acfm Q'N  2 5,000acfm/bed A M ' Mc c 10,800lbs 3,600lbs/bed (21) Once the carbon adsorption system is sized, the total cost of the system can be estimated as the sum of the total capital investment (TCI) and the total annual costs. Total Capital Investment: The total capital investment (TCI) costs are estimated as 𝑇𝐶𝐼 = ∑ 𝐷𝑖𝑟𝑒𝑐𝑡 𝐶𝑎𝑝𝑖𝑡𝑎𝑙 𝐶𝑜𝑠𝑡𝑠 + ∑ 𝐼𝑛𝑑𝑖𝑟𝑒𝑐𝑡 𝐶𝑎𝑝𝑖𝑡𝑎𝑙 𝐶𝑜𝑠𝑡𝑠 Table 1.7 shows the direct and indirect capital costs for the carbon adsorption system based on the factors provided in Section 1.8. Adsorber Equipment Cost (including costs for carbon and instrumentation): The equipment cost is comprised of the adsorber vessels, carbon, and the condenser, decanter, fan, pumps and other equipment usually included in the adsorber price. The costs of the latter items are based on the combined cost of the vessels and carbon. Combining Equations 1.26 and 1.27, we have: CA 5.82Q0.133Cc NA NDCv (1.43) Because S falls between 97 and 2,110 ft2, equation 1.25 can be used to calculate the cost per vessel, Cv. Additionally, since each vessel will be constructed from 304 stainless steel, the adjustment factor for fabrication material (Fm) in Equation 1.25 is 1, and the cost per vessel is calculated as follows: C  271 F S 0.778  (271)(1)(283)0.778  $21,900 / vessel vm The cost per vessel, Cv, is then converted to the current year dollars using the Chemical Engineering Plant Cost Index (CEPCI). In this example, the scaling factor for 2017 dollars was 567.5/390.6). Hence, Cv is $31,834 in 2017 dollars. The total cost of the carbon required for the adsorber (Cc) is calculated using equation 1.16 as follows: Cc CCMc $4.210,800lbs$45,360 lb Substituting the values for Cv and Cc into equation 1.43 yields: 𝐶 =(5.82)(10,000)−0.133[45,360+(2+1)(31,834)]=$240,800 𝐴 1-37

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