Question 1 A small expansion to an existing chemical facility is being investigated, and a preliminary Process Flow Diagram (PFD) of the process is shown in Figure Q1. E-101 T-101 V-101 P.101AB E-103 E-102 Figure Q1. PFD for the expansion The expansion involves the installation of a new distillation column with a reboiler, condenser, pumps. and other associated equipment. A list of the equipment, sizes, materials of construction, and operating pressures is given in Table Q1. (a) Calculate the Purchase Cost, Cp. and the Bare Module Cost. Com of: (0) the overhead condenser E-101 [8 marks] (ii) the reboiler E-102 (8 marks] (ili) the product cooler E-103 18 marks (iv) the reflux pumps P-101 A/B (8 marks] (v) the aromatics column T-101 (8 marks] (vi) the reflux drum V-101 18 marks] NOTE: . All the data for the purchased cost of equipment were obtained from a survey of equipment manufacturers during the period May to September of 2019. so an average value of the Chemical Engineering Plant Cost Index (CEPCI) of 607.6 over this period should be used when accounting for inflation. atle Q1 Information on Equipement Required for the Plant Expansion Material of Operating Pressure Equipment No. Capacity / Size / Type Construction (barg) E-101 Area = 170 m Tube - OS Tube = 8.0 Overhead condenser Shell and tube (floating- Shell - CS Shell = 8.0 head) E-102 Area = 205 m Tube - SS Tube = 18.0 Reboiler Shell and tube (fioating- Shell - CS Shell = 6.0 head) E-103 Area = 10 m AICS construction Inner 5.0 Product cooler Double pipe Ouner = 5.0 P-101A/B Power = 5 kW CS Discharge = 5.0 Reflux pumps Centrifugal T-101 Diameter = 2.1 m Vessel - CS Column=7.0 Aromatics column Height = 23 m 32 sieve trays Trays - SS V-101 Diameter = 1.8 m Vessel - CS Vessel = 3.0 Reflux drum Length = 6 m Horizontal