Keyphrases
Control Structure
100%
Reactive Distillation Column
95%
Reactive Distillation
49%
Temperature Control
46%
Two-temperature
37%
Distillation Column
37%
Methanol
32%
Biobutanol
27%
Relative Volatility
25%
Side Reactor
25%
Flowsheet
25%
Process Configuration
24%
Optimum Design
22%
Pressure-swing Distillation
22%
Temperature Controller
22%
Reactor
21%
Steady State
20%
Dynamic Controllability
20%
Product Type
19%
Purification Process
19%
Bioethanol Purification
19%
Fermentation Broth
19%
Chemical Equilibrium Constant
18%
Total Annual Cost
18%
Energy Efficient
18%
Azeotropic Mixture
17%
Multi-unit
17%
Separation Process
16%
Triple Columns
16%
Process Intensification
16%
Dimethyl Carbonate
16%
Inferential Control
15%
Plant-wide Control
15%
Acetone
15%
Acetone-butanol-ethanol Fermentation
15%
Distillation Process
14%
Bioethanol
14%
Steady-state Economy
14%
Extractive Distillation Process
14%
Alternative Process
14%
Cost of Capital
13%
Temperature Range
12%
Azeotrope
12%
Ethanol Fermentation
12%
Acetone-butanol-ethanol
12%
Reactor Processes
12%
Hexane
12%
Temperature-based Method
12%
Ternary System
12%
Reversible Reaction
12%
Engineering
Reactive Distillation
84%
Distillation Column
80%
Control Structure
61%
Bioethanol
19%
Relative Volatility
18%
Controllability
17%
Extractive Distillation
16%
Reactant
15%
Ternary System
14%
Fresh Feed
12%
Pressure Swing Distillation
12%
Operating Pressure
11%
Quaternary System
9%
Reversible Reaction
8%
Feed Stream
8%
Temperature Controller
7%
Azeotrope
7%
Fermentation Broth
6%
Equilibrium Constant
6%
Product Type
6%
Regulatory Control
5%
Atmospheric Pressure
5%
Optimum Design
5%
Feed Composition
5%
