Assembly of Database Propane to Acrylic Acid design plant proses

19 Table 4.1: Overall Process Stream Summary. This table provides temperature, pressure, vapor fraction, and component flow rates for all streams in the process flowsheet. Stream S‐ AIR O2 PRODUCT PROPANE PURGE S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ Temperature °F 225 75 75 100 75 85 ‐ 6 230 406 24 230 228 740 780 280 85 82 85 85 Pressure psia 54 14.6959 500 75 150 25 60 55 54 60 55 54 49 45 40 35 30 25 25 Vapor Fraction 1 1 1 1 1 1 1 0.2 1 1 1 1 1 0.92 0.92 1 1 Total Flow lbhr 554490 12636 23839 25314 23616 17149 23839 23839 12636 23616 23616 620230 620230 620230 620230 620230 620230 571630 554490 Component Flows lbhr Propane 153820 23616 4757 23616 23616 180250 180250 162230 162230 162230 162230 158570 153820 Oxygen 2427 2943 23839 75 23839 23839 2943 29212 29212 2505 2505 2505 2505 2502 2427 Propylene 19146 592 19451 19451 20119 20119 20119 20119 19739 19146 Acrylic Acid 1791 25286 55 1901 1901 28548 28548 28548 28548 1846 1791 Water 5713 25 177 7547 7547 22309 22309 22309 22309 5890 5713 Nitrogen 313410 9693 9693 9693 323240 323240 323240 323240 323240 323240 323110 313410 Acetic Acid 379 2.5 12 537 537 1393 1393 1393 1393 390 379 Carbon Dioxide 57798 1788 58094 58094 59894 59894 59894 59894 59585 57798 Dowtherm Stream S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ S‐ WASTE Temperature °F 225 85 86 86 400 418 318 317 295 307 374 371 415 100 298 287 265 264 236 Pressure psia 59 25 150 130 125 98 95 90 70 73 68 68 68 63 65 67 65 60 25 Vapor Fraction 1 1 1 1 1 1 1 1 1 1 0.3 Total Flow lbhr 554490 48596 48596 48596 48596 23846 24750 24750 19472 5278 5278 1469 25314 25314 3809 13819 5653 5653 17628 Component Flows lbhr Propane 153820 3651 3651 3651 3651 3651 3651 3651 834 2817 2817 834 Oxygen 2427 3 3 3 3 3 3 3 3 3 Propylene 19146 380 380 380 380 380 380 380 75 305 305 75 Acrylic Acid 1791 26702 26702 26702 26702 23844 2858 2858 1024 1834 1834 1443 25286 25286 392 913 110 110 1305 Water 5713 16419 16419 16419 16419 16419 16419 13036 3383 3383 25 25 25 3358 11202 1834 1834 14560 Nitrogen 313410 130 130 130 130 130 130 130 130 130 Acetic Acid 379 1003 1003 1003 1003 1 1001 1001 941 60 60 1 3 3 59 783 158 158 842 Carbon Dioxide 57798 308 308 308 308 308 308 308 12 296 296 12 Dowtherm Stream DOWTHERM‐1 DOWTHERM‐2 DOWTHERM‐3 DOWTHERM‐4 DOWTHERM‐5 DOWTHERM‐6 Temperature °F 198 738 458 299 203 198 Pressure psia 40 35 30 25 20 15 Vapor Fraction Total Flow lbhr 385000 385000 385000 385000 385000 385000 Component Flows lbhr Dowtherm 385000 385000 385000 385000 385000 385000 20

4.2 Mixing Section

Figure 4.2: Mixing Section Process Diagram. This shows the flowsheet for the mixing section of the process. 21 Table 4.2: Mixing Section Stream Summary. This table provides temperature, pressure, vapor fraction, and component flow rates for all streams in the mixing section of the process flowsheet. Stream S ‐114 S ‐115 S ‐133 O2 S ‐101 S ‐102 AIR S ‐103 PROPANE S ‐104 S ‐105 S ‐132 S ‐106 Temperature °F 85 225 225 75 ‐106 230 75 406 75 24 230 264 228 Pressure psia 25 59 54 500 60 55 14.6959 54 150 60 55 60 54 Vapor Fraction 1 1 1 1 1 1 1 1 0.2 1 1 1 Total Flow lbhr 554490 554490 554490 23839 23839 23839 12636 12636 23616 23616 23616 5653 620230 Component Flows lbhr Propane 153820 153820 153820 23616 23616 23616 2817 180250 Oxygen 2427 2427 2427 23839 23839 23839 2943 2943 3 29212 Propylene 19146 19146 19146 305 19451 Acrylic Acid 1791 1791 1791 110 1901 Water 5713 5713 5713 1834 7547 Nitrogen 313410 313410 313410 9693 9693 130 323240 Acetic Acid 379 379 379 158 537 Carbon Dioxide 57798 57798 57798 296 58094 Dowtherm