capital costs v1

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Different version of Capital Cost Estimates

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Sheet1Heat Exchangers (U-tube shell and tube)Size (area in m^2)75647312018a2800028000280002800028000b5454545454n1.21.21.21.21.2Ce37604.334469606235939.803029739537297.82123550544881.508628838829732.689589143F3.53.53.54.55.5Ci131615.170643622125789.310604088130542.374324267201966.788829775163529.792740286Pump (single stage centri)This is only for carbon steel, changing materials = f in Table 7.6Size (flow in L/s)5.28Ctotal29973120.5887267a8000b240n0.9Ce9072.9556523861F4Ci36291.8226095445Reactor (pressure vessel, vertical, cs)Size (shell mass in kg)1428622235327554302.5a11600116001160011600b34343434n0.850.850.850.85Ce127251.951646561180045.914005837245734.21320156953300.5385882561F4567Ci509007.806586244900229.5700291871474405.27920942373103.770117792Distillation Columns (Packing+Tray+Pressure Vessel)Pressure VesselSize (shell mass in kg)1010a11600b34n0.85Ce23766.1196908589Tray (bubble cap?)Size (diameter in m)1.22a340b640n1.9N20Ce25476.4206897191F4Ci196970.161522312Compressor (Centrifugal)Driver Power, kW30000a580000b20000n0.6Ce10291867.4966041F2.5Ci25729668.7415102