Q.1
14 MarksDiscuss in brief for design opportunities and general steps in product and process design.
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Discuss in brief for design opportunities and general steps in product and process design.
Calculate the number of possible sequences of ordinary distillation column for 5 number of product and draw the sequences.
Discuss the procedure for reactor network design using concept of attainable region.
For ΔTmin = 20°C, find out pinch point and construct the Hohmann composite curve (HCC). Find out sink (Qhmin) and source (Qcmin). Stream Tin (°C) Tout (°C) mCp (kW/°C) H1 180 40 2 H2 150 40 4 C1 60 180 3 C2 30 105 2.6
Explain the concept of threshold approach temperature and optimum approach temperature.
For stream matching to be feasible at pinch, justify that Ch ≥ Cc must be satisfied on cold side of pinch.
Explain Heuristics for determining favorable sequences of ordinary distillation column.
For the process fluids as shown in the table, find minimum utility requirements and pinch temperature using temperature-interval method. Consider ΔTmin = 10°C. Stream Ts (oC) Tt (oC) mCp (kW/oC) H1 180 40 20 H2 160 40 40 C1 220 600 30 C2 180 300 22
Explain energy saving in multi-effect distillation compared to the conventional distillation using TQ diagram.
Given the processing times for two products A and B, determine make span and cycle time for manufacturing two batch of A and two batch of B using
Compare forward heat integration and reverse heat integration in distillation with necessary
Determine make span and cycle time for processing times of two product plants are as given below:
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BE Chemical
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Official Gujarat Technological University (GTU) examination paper for Computer Aided Process Synthesis (Summer 2026, B.E. · Chemical Engineering, Sem 7). Features complete 70-mark regular & remedial examination pattern, official marking distribution across all 5 questions, and direct 1-click official PDF download.
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3170507 Computer Aided Process Synthesis
Official GTU PDF · Summer 2026
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