Petroleum Refining Design and Applications Handbook. A. Kayode Coker

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СКАЧАТЬ 0.3 L/D 5 2 Towers Pressure (bar) 400 Vacuum Normal Limits Diameter L/D Temperature (°C) 400^b −200 0.5 3.0–40^c Height (m) 50 2 1.0 2.5–30^c Diameter (m) 4 0.3 2.0 1.6–23^c L/D 30 2 4.0 1.8–13^c Pumps Reciprocating Power^d (kW) 250 <0.1 Pressure (bar) 1000 Rotary and positive Power^d (kW) 150 <0.1 Displacement Pressure (bar) 300 Centrifugal Power^d (kW) 250 <0.1 Pressure (bar) 300 Compressors Axial, Centrifugal + Recipr. Power^d (kW) 8000 50 Rotary Power^d (kW) 1000 50 Drives for compressor Electric Power^e (kW) 15,000 <1 Steam turbine Power^e (kW) 15,000 100 Gas turbine Power^e (kW) 15,000 10 Internal combustion eng. Power^e (kW) 15,000 10 Process heaters Duty (MJ/h) 500,000 10,000 Duties different for reactive heaters/furnaces Heat exchangers Area (m²) 1000 10 For Area <10 m² use Tube Dia. (m) 0.0254 0.019 double-pipe exchanger Length (m) 6.5 2.5 Pressure (bar) 150 Vacuum For 150 < P < 400 bar Temperature (°C) 400^b −200 need special design

      ^aMost of the limits for equipment sizes shown here correspond to the limits used in the costing program (CAPCOST.BAS).

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