The purchased cost of a shell and tube heat exchanger, carbon shell, stainless steel tubes, heat transfer area 500 m^{2}, was £7600 in January 1998; estimate the cost in January 2006. Use the Process Engineering plant index.
The purchased cost of a shell and tube heat exchanger, carbon shell, stainless steel tubes, heat transfer area 500 m^{2}, was £7600 in January 1998; estimate the cost in January 2006. Use the Process Engineering plant index.
From Figure 6.1:
Index in 1998 = 106
2000 = 108, 100 (change of base)
2004 = 111
\text { So, estimated cost in January } 2000=7600 \times 108 / 106=£ 7743 \text {, }
\text { and in } 2004=7743 \times 111 / 100=£ 8595
From Figure 6.1, the average increase in costs is about 2.5 per cent per year. Use this value to predict the exchanger cost in 2006.
\text { Cost in } 2006=8595 \times(1.025)^{2}=£ 9030
\text { Say } £ 9000