Chemical Process Design Wiki: Difference between revisions
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= Chemical Process Design Theory and Method = | = Chemical Process Design Theory and Method = | ||
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== | ==Design Basis== | ||
# | # Set design specifications | ||
# | # Preliminary site selection and market analysis | ||
# Block flow diagram | |||
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==Process Flow Diagram== | |||
# Literature review | |||
# Process alternatives and technology options | |||
# Define the major unit operations | |||
# Process flow diagram | |||
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==Process simulation== | |||
# Reactors | |||
# Separation processes | |||
# Heat Exchangers | |||
# Storage vessels | |||
# Other vessels | |||
# Pumps | |||
# HYSYS | |||
# Aspen Plus | |||
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==Economic analysis== | |||
# Estimation of capital | |||
# Estimation of production cost | |||
# Estimation of revenue | |||
# Profitability measures | |||
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==Other process design considerations== | |||
# Safety analysis | |||
# Environmental concerns | |||
# Controls and P&ID | |||
# Sensitivity analysis | |||
# Process Optimization | |||
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|} <!-- End Process Design child table --> | |} <!-- End Process Design child table --> | ||
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=Chemical Process Design Projects= | =Chemical Process Design Projects= | ||
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== | == Example == | ||
# | # Sugar Cane Ethanol Plant (2011) | ||
# | # Other examples | ||
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==Glycerol to propylene glycol== | |||
== | # Design 1 | ||
# | # Design 2 | ||
# | # Design 3 | ||
# | |- | ||
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# | ==3-Hydroxypropionic acid to 1,3-propanediol== | ||
# Design 1 | |||
# Design 2 | |||
# Design 3 | |||
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==Succinic acid to 1,4-butanediol== | |||
# Design 1 | |||
# Design 2 | |||
# Design 3 | |||
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Revision as of 01:00, 21 December 2013
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