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1 Heat Transfer Technology

2 Heat Transfer Technology

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4 HEATRAN Heat Transfer Technology 1. ํšŒ์‚ฌ๊ฐœ์š”

5 Heat Transfer Technology

6 Heat Transfer Technology

7 Heat Transfer Technology

8 Heat Transfer Technology

9 Heat Transfer Technology

10 Heat Transfer Technology

11 Heat Transfer Technology

12 Heat Transfer Technology

13 Heat Transfer Technology

14 Heat Transfer Technology

15 Heat Transfer Technology

16 Heat Transfer Technology

17 Heat Transfer Technology

18 Heat Transfer Technology

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30 12-EA-201 Heavy Cycle Oil Product Cooler AIR-COOLED HEAT EXCHANGER , m² PERFORMANCE DATA - TUBE SIDE Heavy Cycle Oil , , , PERFORMANCE DATA - AIR SIDE , DESIGN, MATERIALS AND CONSTRUCTION TUBE BUNDLE HEADER PLUG TUBE 822 mm 9,144 mm A516 Gr.70 A A105 Soft Iron , Hot Dip Galvanized 11 / 11 / 11 / 11 / 11 / None O 30 NOZZLES FIN Embedded(G-fin) # RF Aluminium LOUVER # RF STEAM COIL # RF VIBRATION SWITCH # 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 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.

31 AIR-COOLED HEAT EXCHANGER 12-EA-201 Heavy Cycle Oil Product Cooler 2750 (APP.) EA EA (APP.) (APP.) 12-EA EA

32 12-EA-202 Light Cycle Oil Product Cooler ,080,000 1,888 m² PERFORMANCE DATA - TUBE SIDE Light Cycle Oil , , , PERFORMANCE DATA - AIR SIDE ,000 1, DESIGN, MATERIALS AND CONSTRUCTION TUBE BUNDLE HEADER PLUG TUBE 1,848 mm 9,144 mm A516 Gr.70 A A105 Soft Iron , Hot Dip Galvanized 28 / 28 / 28 / None O 30 NOZZLES FIN Embedded(G-fin) # RF Aluminium LOUVER # RF STEAM COIL # RF VIBRATION SWITCH # 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 O kw , , T.E.F.C None Aluminum Cast Alum φ 50 kw CONTROL Action on Air Failure ESTIMATION 2.7 X ,000 25,000 26,300 REMARKS 1. Minimum design metal temperature is 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

33 AIR-COOLED HEAT EXCHANGER 12-EA-202 Light Cycle Oil Product Cooler 2750 (APP.) EA EA (APP.) (APP.) 12-EA EA

34 12-EA-203 Main Column Condenser ,190,000 29,858 m² 1, PERFORMANCE DATA - TUBE SIDE AIR-COOLED HEAT EXCHANGER HCBN,WATER & HYDROGEN , ,361 28, , , , , , , PERFORMANCE DATA - AIR SIDE ,637,000 3, DESIGN, MATERIALS AND CONSTRUCTION TUBE BUNDLE HEADER PLUG TUBE 3,779 mm 9,144 mm A516 Gr.70 (Killed) A214 (Killed) 1 6 A105 Soft Iron , Hot Dip Galvanized None O 30 NOZZLES FIN Knurled (KL) # RF Aluminium LOUVER # RF STEAM COIL # RF VIBRATION SWITCH # 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 O kw , , T.E.F.C None Aluminum Cast Alum φ 50 kw CONTROL Action on Air Failure ESTIMATION 19.1 X ,000 41, ,000 REMARKS 1. Minimum design metal temperature is Design for wet H2S service per UOP Standard Specification 4-13, Section Provide post-weld heat treat. 4. Tube to tube sheet joint : Strength Weld.

35 12-EA-203 Main Column Condenser AIR-COOLED HEAT EXCHANGER 19100(APP.) (APP.) (APP.)

36 FEED WATER HEATER POWER PLANT No.3 HP Heater ,240 OD x 8,860 TL 3-zone, U-tube HORIZONTAL PERFORMANCE OF ONE SHELL 3, , , *1) *1) 3, D-Seg, 400 TTD , , ,865.2 Supp, 785 DCA , , ,102.9 Seg, 230 1,900 23, U-tubes *5) 8,860 1, (Triangle) 8,830 r 12,510 5,922 A556-C2, CS CS CS CS CS CS CS WELDED S1 S7 S T1 T S connected to restriction orifice S4 S5 S6 25,176 ASME SEC. VIII, DIV. 1, HEI 113, T T 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

37 FEED WATER HEATER POWER PLANT No.3 HP Heater APP. 10,600 APP. 9,200 x 8 = 6, ,620 S1 T2 OD 1,240 ID 1,048 S2 T1 2,200

38 FEED WATER HEATER POWER PLANT No.6 LP Heater ,090 ID x 10,620 TL 2-ZONE, U-tube ONE ONE HORIZONTAL U-tubes ,620 1, Triangle 30 10,765 r 4,445 2,078 SUS 304 CS CS WELDED ONE NIL *1) 300 / FV 2,100 24, , CS CS PERFORMANCE OF ONE SHELL 37,091 22, , ,459.1 S T1 S S T2 S Connected to restriction orifice , *1) 2,714.8 Supp, 750 1,946.3 SEG, , TTD = 2.8 DCA = T 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 S ASME SEC. VIII, DIV. 1, HEI 1 20 Heavy Expanded(Roller)

39 FEED WATER HEATER POWER PLANT No.6 LP Heater APP. 12,690 APP. 11,210 X 13 = 9, S2 S1 T2 ID 1, ,000 S3 T1

40 FEED WATER HEATER POWER PLANT No.7 LP Heater ,080 ID x 6,100 TL 1-ZONE, U-tube ONE ONE HORIZONTAL U-tubes ,100 1, Triangle 30 6,253 r 1,607 1,157 SUS 304 SUS 304 CS CS WELDED ONE *1) 50 / FV 2,100 28, CS CS S1 PERFORMANCE OF ONE SHELL 43, , *1) , ,386.8 Supp S T2 S Connected to restriction orifice T , TTD = 3.9 S T 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)

41 FEED WATER HEATER POWER PLANT No.7 LP Heater APP. 7,740 APP. 6,600 X 8 = 5, S1 S1 S1 S1 T2 ID 1,080 ID 1,080 S2 T1

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53 WASTE HEAT BOILER WASTE HEAT BOILER ,000 2,500 2,180 21,882, PERFORMANCE OF ONE BATTERY (CASE A-2) 125,323 *3) 463, , ,323 46, , , T-SIPHON ,487 CONSTRUCTION CROSS FLOW ONE *4) T T T5 1 3/4 WASTE GAS WATER/STEAM Min (Odd Row), 19 3,000 *4) STAGGERED CS HFW 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 Gas outlet temp, 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.

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57 GAS COOLER HE , ,000 11,158, PERFORMANCE OF ONE BATTERY HN GAS WATER 43,420 (Note 1) 116,000 43, , , , ,192 CONSTRUCTION CROSS FLOW (Odd Row), 10 2,000 SUS STAGGERED ALUMINUM L-FOOT T1 1 6 T2 1 6 T5 1 3/4 T Min 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

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........(2006)-01 ํ”Œ๋Ÿฌ๊ทธ U-ํŒจํ‚น ์„ธ๋ฉด๊ธฐ(๋„๊ธฐ) ์‚ผ๊ฐํŒจํ‚น ์™€์ƒค ํ”„๋ Œ์ง€ ๋„ˆํŠธ ๊ณ ์ •๋„ˆํŠธ ์„ธ๋ฉด๊ธฐ(๋„๊ธฐ) ํ”„๋ Œ์ง€ ๋„ˆํŠธ ์™€์ƒค ๊ณ ์ •๋„ˆํŠธ ๋ชธํ†ต ํŒŒ์ดํ”„ ์—ฐ๊ฒฐ๋„ˆํŠธ ๊ฐ€๋กœ๋Œ€ ์—ฐ๊ฒฐ๋Œ€ ์Šคํฌ๋ฅ˜ ํฝ์—…๋กœ๋“œ 5mm ๋…ธ๋ธŒ ๋ฌผ๋งˆ๊ฐœ ํ”Œ๋Ÿฌ๊ทธ ์‚ผ๊ฐํŒจํ‚น U-ํŒจํ‚น U-ํด๋ฆฝ ์„ธ๋ฉด๊ธฐ(๋„๊ธฐ) ํ”„๋ Œ์ง€ ๋„ˆํŠธ ๊ณ ์ •๋„ˆํŠธ ๋ชธํ†ต ํŒŒ์ดํ”„ ์—ฐ๊ฒฐ๋„ˆํŠธ ๊ฐ€๋กœ๋Œ€ ํฝ์—…๋กœ๋“œ 5mm ๋…ธ๋ธŒ ๋ฌผ๋งˆ๊ฐœ ํ”Œ๋Ÿฌ๊ทธ ์‚ผ๊ฐํŒจํ‚น U-ํŒจํ‚น U-ํด๋ฆฝ ์™€์ƒค ๋ฒฝ๋ฉด ๋ฒฝ๋ฉด ร˜6

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2) Available Sizes ๊ณต๊ธ‰ ๊ฐ€๋Šฅ (1) A์—ด์—ฐ 1 30Kg๊ธ‰ 900 1300 < 40 2 40Kg๊ธ‰ 900 1300 < 40 3 50Kg๊ธ‰ 900 1000 1100 ์‚ฌ์ „ํ˜‘์˜ ํ•„์š” (Please consult us in advance) < 1.6 < 1.9

2) Available Sizes ๊ณต๊ธ‰ ๊ฐ€๋Šฅ (1) A์—ด์—ฐ 1 30Kg๊ธ‰ 900 1300 < 40 2 40Kg๊ธ‰ 900 1300 < 40 3 50Kg๊ธ‰ 900 1000 1100 ์‚ฌ์ „ํ˜‘์˜ ํ•„์š” (Please consult us in advance) < 1.6 < 1.9 1) Standard & Applications ์ œํ’ˆ ๋ฐ ์šฉ๋„ ์šฉ๋„ Applications ์—ด๊ฐ„์••์—ฐ ์—ฐ๊ฐ•์žฌ Hot Rolled Mild Steel Plate, Sheet ๋ƒ‰์—ฐ์šฉ ํƒ„์†Œ๊ฐ•์žฌ Reduced Carbon Steel for Cold Rolled Steel ์ผ๋ฐ˜๊ตฌ์กฐ์šฉ Rolled Steel for General Structure ์šฉ์ ‘๊ตฌ์กฐ์šฉ Rolled

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(2) : :, ฮฑ. ฮฑ (3)., (3). ฮฑ ฮฑ (4) (4). (3). (1) (2) Antoine. (5) (6) 80, ฮฑ =181.08kPa, =47.38kPa.. Figure 1.

(2) : :, ฮฑ. ฮฑ (3)., (3). ฮฑ ฮฑ (4) (4). (3). (1) (2) Antoine. (5) (6) 80, ฮฑ =181.08kPa, =47.38kPa.. Figure 1. Continuous Distillation Column Design Jungho Cho Department of chemical engineering, Dongyang university 1. ( ).... 2. McCabe-Thiele Method K-value. (1) : :, K-value. (2) : :, ฮฑ. ฮฑ (3)., (3). ฮฑ ฮฑ (4) (4).

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