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Constrained Optimization MCP Server

flowsheet_data.csvโ€ข980 B
stream_id,stream_name,component_A_flowrate,component_B_flowrate,temperature,pressure,unit_from,unit_to,description S1,Feed Stream,100.0,60.0,80.0,1.5,FEED,DISTILLATION_COL,Raw binary feed to distillation column S2,Distillate,95.0,2.0,65.0,1.2,DISTILLATION_COL,CONDENSER,Top product from column (A-rich) S3,Bottoms,5.0,58.0,120.0,1.6,DISTILLATION_COL,REBOILER,Bottom product from column (B-rich) S4,Reflux,47.5,1.0,40.0,1.2,CONDENSER,DISTILLATION_COL,Reflux back to column S5,Net Distillate,47.5,1.0,40.0,1.2,CONDENSER,PRODUCT_TANK_1,Final distillate product (A-rich) S6,Reboiler Vapor,5.0,58.0,120.0,1.6,REBOILER,DISTILLATION_COL,Vapor back to column S7,Final Bottoms,5.0,58.0,110.0,1.4,REBOILER,PRODUCT_TANK_2,Final bottom product (B-rich) S8,Steam,0.0,0.0,150.0,3.0,STEAM_GENERATOR,REBOILER,Heating steam S9,Cooling Water In,0.0,0.0,25.0,2.0,COOLING_TOWER,CONDENSER,Cooling water supply S10,Cooling Water Out,0.0,0.0,40.0,1.8,CONDENSER,COOLING_TOWER,Heated cooling water return

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