歯국문-Heatran소개자료1111.PDF

Heat Transfer Technology

HEATRAN Heat Transfer Technology 1. 회사개요

Heat Transfer Technology

12-EA-201 Heavy Cycle Oil Product Cooler AIR-COOLED HEAT EXCHANGER 1 2.7 9.4 450,000 531 m² 47.2 98.59 8.60 9.33 96.8 105.0 PERFORMANCE DATA - TUBE SIDE Heavy Cycle Oil 826.8 979.6 4,700 0.387 6.274 0.0802 0.1071 4,700 239 4,700 239 0.5468 0.3635 0.0006 0.21 0.20 268.0 60.0 4.8 0.5 PERFORMANCE DATA - AIR SIDE 33.0 51.5 0.0004 100,200 726 18.0 17.8 3.22 13.0 DESIGN, MATERIALS AND CONSTRUCTION 9.5 300 TUBE BUNDLE HEADER PLUG TUBE 822 mm 9,144 mm A516 Gr.70 A214 1 6 A105 Soft Iron 25.40 9,144 1 1 6 3.0 2.77 Hot Dip Galvanized 11 / 11 / 11 / 11 / 11 / 11 66 None --- 60.33 O 30 NOZZLES FIN Embedded(G-fin) 1 2 150# RF Aluminium LOUVER 1 2 150# RF 57.15 196.9 STEAM COIL 2 1 150# RF 0.4 300 VIBRATION SWITCH 1 1 150# RF AIR RECIRCULATION NOISE LIMIT 85 None API 661, 4th ed., 1997 MECHANICAL EQUIPMENT DRIVER FAN SPEED REDUCER O kw φ kw CONTROL Action on Air Failure ESTIMATION 6,170 REMARKS 1. Minimum design metal temperature is 18.0. 2. This Item is common bay with 12-EA-202. See 12-EA-202 data sheet for mechanical equipment data 3. Tube to tube sheet joint : Expanded with groove and seal weld.

AIR-COOLED HEAT EXCHANGER 12-EA-201 Heavy Cycle Oil Product Cooler 2750 (APP.) 822 1848 2743 12-EA-201 12-EA-202 9400 (APP.) 9144 2750(APP.) 12-EA -202 12-EA -201 2743 2743 2743

12-EA-202 Light Cycle Oil Product Cooler 1 2.7 9.4 1,080,000 1,888 m² 80.1 53.42 10.71 12.36 252.3 291.2 PERFORMANCE DATA - TUBE SIDE Light Cycle Oil 832.5 933.6 19,361 0.487 2.641 0.0914 0.1092 19,361 185 19,361 185 0.4929 0.3699 0.0004 0.21 0.21 176.0 47.0 5.5 0.7 PERFORMANCE DATA - AIR SIDE 33.0 51.7 0.0004 240,000 1,737 18.0 17.8 3.43 13.0 DESIGN, MATERIALS AND CONSTRUCTION 55.0 205 205 TUBE BUNDLE HEADER PLUG TUBE 1,848 mm 9,144 mm A516 Gr.70 A214 1 4 A105 Soft Iron 25.40 9,144 1 1 4 3.0 2.77 Hot Dip Galvanized 28 / 28 / 28 / 28 112 None --- 60.33 O 30 NOZZLES FIN Embedded(G-fin) 1 3 600# RF Aluminium LOUVER 1 3 600# RF 57.15 433.1 STEAM COIL 2 1 600# RF 0.4 205 VIBRATION SWITCH 1 1 600# RF AIR RECIRCULATION NOISE LIMIT 85 None API 661, 4th ed., 1997 MECHANICAL EQUIPMENT DRIVER ELECTRIC MOTOR FAN MOORE SPEED REDUCER V-Belt 40 VT Manual 2 2 395 O 9.4 2 3.696 kw 15.0 4 2,743 1.4 1,460 100 0 T.E.F.C None Aluminum Cast Alum. 380 3 φ 50 kw 12.6 13.3 CONTROL Action on Air Failure ESTIMATION 2.7 X 9.4 10,000 25,000 26,300 REMARKS 1. Minimum design metal temperature is 18.0. 2. This Item is common bay with 12-EA-201. The mechanical equipment data specified is for common bay fan. 3. Tube to tube sheet joint : Expanded with groove and seal weld. AIR-COOLED HEAT EXCHANGER

AIR-COOLED HEAT EXCHANGER 12-EA-202 Light Cycle Oil Product Cooler 2750 (APP.) 822 1848 2743 12-EA-201 12-EA-202 9400 (APP.) 9144 2750(APP.) 12-EA -202 12-EA -201 2743 2743 2743

12-EA-203 Main Column Condenser 5 3.8 9.6 13,190,000 29,858 m² 1,285.0 27.27 16.20 20.22 376.4 469.9 PERFORMANCE DATA - TUBE SIDE AIR-COOLED HEAT EXCHANGER HCBN,WATER & HYDROGEN 2.844 772.4 2.731 786.1 116,333 0.011 0.39 0.01 0.468 73,361 28,210 0.0243 0.1003 0.0255 0.2537 29,423 123 74,577 102 0.4518 0.4821 0.4293 0.5336 12,389 807 100 0.0004 11,589 0.11 1,160 30.9 1,150 30.9 0.05 104.0 47.0 0.9 15.3 PERFORMANCE DATA - AIR SIDE 33.0 53.8 0.0004 2,637,000 3,817 18.0 31.8 3.68 13.0 DESIGN, MATERIALS AND CONSTRUCTION 3.5 135 TUBE BUNDLE HEADER PLUG TUBE 3,779 mm 9,144 mm A516 Gr.70 (Killed) A214 (Killed) 1 6 A105 Soft Iron 25.40 9,144 1 1 1 5.0 2.77 Hot Dip Galvanized 360 360 None 10.0 60.33 O 30 NOZZLES FIN Knurled (KL) 2 10 150# RF Aluminium LOUVER 2 8 150# RF 57.15 433.1 STEAM COIL 1 1 150# RF 0.4 135 VIBRATION SWITCH 1 1 150# RF AIR RECIRCULATION NOISE LIMIT 85 Wet H2S Service (UOP Spec. 4-13, Sec. 4.2) API 661, 4th ed., 1997 MECHANICAL EQUIPMENT DRIVER ELECTRIC MOTOR FAN MOORE SPEED REDUCER HTD-Belt 60 VT 2 2 282 O 12.0 2 5.177 kw 37.0 10 3,048 1.8 1,460 50 50 T.E.F.C None Aluminum Cast Alum. 380 3 φ 50 kw 31.3 32.9 CONTROL Action on Air Failure ESTIMATION 19.1 X 9.6 27,000 41,000 215,000 REMARKS 1. Minimum design metal temperature is 18.0. 2. Design for wet H2S service per UOP Standard Specification 4-13, Section 4.2. 3. Provide post-weld heat treat. 4. Tube to tube sheet joint : Strength Weld.

12-EA-203 Main Column Condenser AIR-COOLED HEAT EXCHANGER 19100(APP.) 3779 3048 9600 (APP.) 9140 3779 19100 (APP.) 3048 3048 3048 3048

FEED WATER HEATER POWER PLANT No.3 HP Heater 0 2000-04-22 1,240 OD x 8,860 TL 3-zone, U-tube 709.8 1 1 HORIZONTAL PERFORMANCE OF ONE SHELL 3,289.2 860.8 744.0 758.2 843.2 414.5 195.0 173.2 178.8 1,402 196.1 20,400 1 2 15.0 0.04 0.81 1.91 95 15.4 0 32.9 60.3 0.00006 *1) 0.00004 *1) 3,126.6 65.2 84.13 639.8 597.5 D-Seg, 400 TTD - 0.96 15,178.1 556.6 7.17 4,808.5 3,865.2 Supp, 785 DCA 5.71 2,727.7 88.1 11.31 4,727.5 3,102.9 Seg, 230 1,900 23,000 220 460 220 672 U-tubes 19.05 1.83 *5) 8,860 1,240 23.81 30(Triangle) 8,830 r 12,510 5,922 A556-C2, CS CS CS CS CS CS CS WELDED 3.0 3.0 S1 S7 S2 1 1 1 200 200 150 T1 T2 1 1 300 300 S3 1 40 connected to restriction orifice S4 S5 S6 25,176 ASME SEC. VIII, DIV. 1, HEI 113,634 1 150 T3 1 20 2 25 2 50 T4 1 400 Strength weld with rolled expanding 1. The values of fouling resistance are based on the HEI recommended. 2. Channel shall be of hemisphere head type. 3. Channel ID: 1,048 mm 4. The pipe of DN80 for operation air venting shall be installed in the shell. 5. Tube thickness of inner 3 rows in U-bend should be min. 2.11mm(BWG 14). 6. Each inlet tube end shall be provided with a stainless steel insert to protect tube end from inlet attack. 759,626

FEED WATER HEATER 0 2000-04-22 POWER PLANT No.3 HP Heater APP. 10,600 APP. 9,200 60 @785 x 8 = 6,280 540 1,620 S1 T2 OD 1,240 ID 1,048 S2 T1 2,200

FEED WATER HEATER POWER PLANT No.6 LP Heater 0 2000-04-22 1,090 ID x 10,620 TL 2-ZONE, U-tube 863.3 ONE ONE HORIZONTAL 250 150 670 U-tubes 19.05 1.245 18 10,620 1,090 23.81 Triangle 30 10,765 r 4,445 2,078 SUS 304 CS CS WELDED 3.0 3.0 2883.0 553.1 398.6 207.5 128.7 95.1 259.9 ONE 0.60 0.29 NIL. 11.3 0.00006 *1) 300 / FV 2,100 24,575 783.5 2,331.8 79.8 CS CS PERFORMANCE OF ONE SHELL 37,091 22,165 11.44 16.65 3,206.0 2,459.1 S1 2 300 T1 S2 1 125 S3 1 125 T2 S4 2 40 Connected to restriction orifice 375.6 529.9 89.5 125.9 16,150 2 1.27 110 36.1 0.00004 *1) 2,714.8 Supp, 750 1,946.3 SEG, 155 1 1 622,011 250 250 TTD = 2.8 DCA = 5.6 150 T3 25 50 1. The values of fouling resistance are based on the HEI recommended. 2. Channel shall be of full access type. 3. Channel ID: 1020 mm 4. The pipe of DN100 for operation air venting shall be installed in the shell. 5. It mounted in condenser neck and is twin (duplex) type with N0.7 LP Heater. S4 S5 S6 1 2 2 ASME SEC. VIII, DIV. 1, HEI 1 20 Heavy Expanded(Roller)

FEED WATER HEATER POWER PLANT No.6 LP Heater 0 2000-04-22 APP. 12,690 APP. 11,210 50 @750 X 13 = 9,750 700 S2 S1 T2 ID 1,090 1020 2,000 S3 T1

FEED WATER HEATER POWER PLANT No.7 LP Heater 0 2000-04-22 1,080 ID x 6,100 TL 1-ZONE, U-tube 486.5 ONE ONE HORIZONTAL 120 120 650 U-tubes 19.05 1.245 18 6,100 1,080 23.81 Triangle 30 6,253 r 1,607 1,157 SUS 304 SUS 304 CS CS WELDED 3.0 3.0 2667.8 388.1 92.7 92.7 92.7 77.57 ONE 18.7 2.77 0.00006 *1) 50 / FV 2,100 28,299 486.5 CS CS S1 PERFORMANCE OF ONE SHELL 43,316 169.1 372.6 40.2 88.8 1,700 4 2.25 120 94.1 0.00004 *1) 17.50 4,030.2 3,386.8 Supp. 650 4 400 S2 1 125 T2 S3 2 65 Connected to restriction orifice T1 1 1 499,617 250 250 TTD = 3.9 S4 1 200 T3 1 20 ASME SEC. VIII, DIV. 1, HEI 1. The values of fouling resistance are based on the HEI recommended. 2. Channel shall be of full access type. 3. Channel ID: 1080 mm 4. The pipe of DN100 for operation air venting shall be installed in the shell. 5. It mounted in condenser neck and is twin (duplex) type with N0.6 LP Heater. Heavy Expanded(Roller)

FEED WATER HEATER 0 2000-04-22 POWER PLANT No.7 LP Heater APP. 7,740 APP. 6,600 50 @650 X 8 = 5,200 750 S1 S1 S1 S1 T2 ID 1,080 ID 1,080 S2 T1

WASTE HEAT BOILER WASTE HEAT BOILER 0 99-12-30 1 3,000 2,500 2,180 21,882,800 917.9 202.5 367.28 61.26 69.22 277.6 313.7 PERFORMANCE OF ONE BATTERY (CASE A-2) 125,323 *3) 463,561 125,323 125,323 46,356 463,561 417,205 945.9 310 194.1 194.1 170 13 0.3163 0.6561 874.6 6.9335 0.0427 0.0274 0.1378 0.0166 0.0661 0.0368 0.5683 0.0309 0.2953 0.2524 1.0648 0.6605 463.29 194.1 194.1 19.8 1.65 110 T-SIPHON 0.5 0.0006 0.0002 75.4 8,487 CONSTRUCTION CROSS FLOW ONE *4) T1 1 12 T2 1 24 T5 1 3/4 WASTE GAS WATER/STEAM Min. 2740 24 20 (Odd Row), 19 3,000 *4) 122.5 90 STAGGERED CS HFW 177 10.1 1.25 1. Design basis: (A)- 2. Case Case 1 Case 2 Case 3 Case 4 Case 5 Case Steam generated, kg/h 20,120 46,356 16,372 16,106 31,862 10,240 Gas pre.drop., mmaq 100 100 61 58 63 7 Gas outlet temp, 260 310 242 241 280 23 3. 1501.7 N/min: 7.93% O2, 17.54% CO2, 74.53% N2 4. Bare tube: SS321, 78 ea, 60.3mmOD(2" pipe), 3.91t Fin tube: CS, 390 ea, 48.26mmOD(1.5" pipe) x 3.68t x 3000mmL, Fin: 10.1mm height, 1.25t, 177 fins/m.

GAS COOLER HE-100 4 1,353 710 2,000 11,158,900 588.8 27.8 60.0 32.80 41.93 694.8 859.9 PERFORMANCE OF ONE BATTERY HN GAS WATER 43,420 (Note 1) 116,000 43,420 24.9 43,420 24.9 116,000 116,000 150 50 30 40 460 5 0.7491 0.9768 994.3 990.5 0.0227 0.0185 0.807 0.6632 0.0384 0.0311 0.541 0.5457 0.2811 0.2793 0.9998 0.9984 9.21 1.69 86 47.0 0.43 0.28 0.0001 0.0002 57.15 6,192 CONSTRUCTION CROSS FLOW 4 20 10 (Odd Row), 10 2,000 SUS 304 134.3 33.3 STAGGERED ALUMINUM L-FOOT 10 15.875 0.432 T1 1 6 T2 1 6 T5 1 3/4 T3 1 200 25.4 1.65 16 Min. 1740 6 CROSSOVER PIPE T4 1 6 CROSSOVER PIPE 0 ECONOMIZER 1. VOLUME FLOW RATE = 58,000 M3/Hr at 150 deg.c, 460 mmaq H2 : 12% / N2 : 88% (Vol.%) 2. CASING MATERIAL : SUS 304 or EQUIV. 3. The vent (coupling with plug) should be provide on the top of the cross-over line (6") from 2nd and 3rd pass, for start-up vent. 4. Lane of 10mm between fin tips is for cleaning. 99-11-26

歯국문-Heatran소개자료1111.PDF