TE RO TE01 WOOOO TK ( 1 ) Product w Red ) RO PAN 100 E- VI 1 OG UU Hint of assignment: next page Stream data Control system in V-101 is using ratio control for each flow rate plus feed back control for level. Output from V-101 should be control by split range control. Meanwhile, R-101/2/3/4 required control for level. There is temperature sensor for main process through E-101/2/3 and flow control for stream of steam for heat exchanger. Flow control also required before entering D-101. Draw P&ID from this PFD. Follow the guideline. You may try separate your drawing into a few sheets of P&ID to make it more clear (if required). 100 100 2001 E 10 11 STREAM DRZATS MEER LOREM 100 10 BATE 20 11 10 2005 1024 330 3700 2300 20 33 BONTE BORE 48761 461 300 Total 192 1 358001 1 130 120 130 DC STAY HT OPERATINI Te IC MO Thr Total Coll 501 304 100 300 A LAM 121 BATCH 20 el 1011 13 249834 4916692 1918 24584 1011 249234 1.4773 al 101 6.000 1 2001 30 1752.731 173272 273273 20434 TE RO TE01 WOOOO TK ( 1 ) Product w Red ) RO PAN 100 E- VI 1 OG UU Hint of assignment: next page Stream data Control system in V-101 is using ratio control for each flow rate plus feed back control for level. Output from V-101 should be control by split range control. Meanwhile, R-101/2/3/4 required control for level. There is temperature sensor for main process through E-101/2/3 and flow control for stream of steam for heat exchanger. Flow control also required before entering D-101. Draw P&ID from this PFD. Follow the guideline. You may try separate your drawing into a few sheets of P&ID to make it more clear (if required). 100 100 2001 E 10 11 STREAM DRZATS MEER LOREM 100 10 BATE 20 11 10 2005 1024 330 3700 2300 20 33 BONTE BORE 48761 461 300 Total 192 1 358001 1 130 120 130 DC STAY HT OPERATINI Te IC MO Thr Total Coll 501 304 100 300 A LAM 121 BATCH 20 el 1011 13 249834 4916692 1918 24584 1011 249234 1.4773 al 101 6.000 1 2001 30 1752.731 173272 273273 20434