Preliminary Design Proposal CHEN 4887 Date
Document Title Author
Table of Contents
Summary
Financial Summary Fixed Capital Investment Working Capital
$ $
Primary Product Enter primary product By-Products List by-products Raw Materials List raw materials
Utilities High Pressure Steam, MJ/hr Medium Pressure Steam, MJ/hr Low Pressure Steam, MJ/hr Boiler Feedwater, tonne/hr Cooling Water, tonne/hr Electricity, MJ/hr Other (list) Operating Labor, $/year Revenue, $/year Utilities, $/year Waste Treatment, $/year Cost of Manufacturing, $/year Interest Rate, % Net Present Value, $
Hourly Production/usage Rate (units/hr)
Annual Production/usage Rate (units/year)
Price ($/unit)
Process Description
Process Flow Diagram
Stream Summary Table Stream ID
â °
Temperature, C Pressure, kPa Vapor Fraction
1
2
25.0 200.0 0.0
Mass Flow, tonne/hr
10.0
Mole Flow, kmole/hr
500.0
Component Flowrates (kmole/hr)
100.0
Material 1
300.0
Material 2
150.0
Material 3
50.0
Other Properties
3
4
5
6
7
8
Equipment Summary Table Heat Exchangers Type Area, m2
E-101 Vaporizer 25.2
Shell Temperature, ⁰C
125.0
Shell Pressure, kPa
300.0
Shell MOC
Stain. Steel
Tube Temperature, ⁰C
185.0
Tube Pressure, kPa
600.0
Tube MOC Duty, MJ/hr Bare Module Cost
Carbon Steel 450.0
Vessels/Towers/ Reactors
T-101
Temperature, â °C
120.0
Pressure, kPa
110.0
Orientation MOC Height/Length, m Diameter, m Internals
Vertical Stain. Steel 25.0 1.2 65 valve trays Stain. Steel
Total Module Cost
Pumps
P-101
Flow, kg/hr
500.0
Outlet Pressure, kPa
440.0
Temperature, ⁰C
110.0
∆ P, kPa Driver Type Shaft Power, kW MOC Total Module Cost
300.0 Electric 300.0 Carbon Steel
Compressors
C-101
Flow, kg/hr
500.0
Outlet Pressure, kPa
220.0
Temperature, ⁰C
110.0
∆ P, kPa Driver Type Shaft Power, kW MOC Total Module Cost
300.0 Electric 300.0 Carbon Steel
Fired Heaters
H-101
Tube Pressure, kPA
500.0
Tube Temperature, â °C
500.0
Duty, MJ/hr
110.0
Fuel MOC Total Module Cost
300 Carbon Steel
Safety Considerations
Recommendations