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Indirect and Direct Bath Heaters
Raj Dewangan
Emp Id: 203481
Dept: PSS (STF)
Process Flow Diagram
HX-3
HX-2
HX-1
IDBH
Wet crude tank
DBH
EET
Dry crude
Tank
DCO inlet header
WCO inlet header
DCO outlet header
WCO outlet header
CoCP
CoDP
8’’
12’’
Out
to
CTF
NHK
Indirect bath heater
• IDBH is used to heat the crude to maintain its flowability
• Following properties need to be maintained:
• Bath temperature = 85 ℃
• Crude outlet temperature = 43.2 ℃
• Flow rate= 5000kLPD * 2 (capacity 6500*2)
• Inlet temperature (>29)
• Inlet pressure: 4 < P < 6.2 kg/cm2g
• IDBH consist
• shell
• Firetubes & chimney
• heater coils: 8 passes
• expansion tank: 120mm level
• burner
IDBH Schematic
IDBH P&ID
IDBH Control philosophy
1. Wet crude inlet temperature (TT5601 > 44 ℃)
2. High Bath temperature (TT 5603 > 85 ℃)
3. Expansion tank level (L < 120mm)
4. NG line pressure P>1.4kg or P<0.1kg
5. Flame failure
In above cases close SDV,SV and open XV (BH tripped manual reset required)
Crude Inlet and Outlet
Expansion tank
Bath temperature sensors
Chimney
Natural gas supply line
Safeties and limits
1. Heating medium temperature is below set point(H-44,L-29 )
• TT5603 & 5604 = 85 ℃
2. Water level is at normal condition
• LG 5602, LT 5601
3. Pressure Transmitter high and low set point is at healthy condition
• PT 5605
4. Stack temperature of chimney is below set point
5. No flame in fire tube
Unit can be operated only when all safeties are in good condition
Burner and BMS
Spark ignition (for
10sec)
Pilot SV open
Flame relay
energised
Flame sense by UV
Ignition transformer
cutoff
Flame relay de-
energised
SDV Open, main
burner on
Ignition transformer
cutoff
Burner trip,
Mannual reset
required
Flame stablished No Flame
safety check
IDBH Control philosophy
1. Wet crude inlet temperature (TT5601) (H-44,L-29 )
• T > 44 ℃ , close SDV 5601&2, (main burner off) no need to heat through IDBH
2. Bath temperature (TT 5603) (SP = 85)
• T = 82-86 ℃, TCV 5601 operate on High fire (82-84 ℃) or Low fire (85-86 ℃)
• T = 88 ℃, close SDV 5601&2 (main burner off)
• T= 90 ℃, close SDV, SV and open XV (BH tripped manual reset required)
3. Expansion tank level
• L >= 120mm, close FLV
• 100 mm < L < 120mm, open FLV
• L < 90mm, close SDV,SV and open XV (BH tripped manual reset required)
4. NG line pressure P>1.4kg or P<0.1kg
• P>1.4kg or P<0.1kg , close SDV,SV and open XV (BH tripped manual reset required)
5. Flame failure: close SDV,SV and open XV (BH tripped manual reset required)
Direct bath heater
• DBH is used to heat the crude before processing in EET, inlet of crude is from HX-1 and
outlet to EET
• Following properties need to be maintained:
• operating temperature = 90 ℃
• Operating pressure = 7kg/cm2g
• Crude inlet temperature = 55.5 ℃
• Flow rate= 2500kLPD * 4
• Interface level = 450mm
• IDBH consist of
• Shell : filled with crude
• Firetubes & chimney
• Burner assembly
• XV at crude inlet (5706),
crude outlet (5707)
water outlet (5703)
out
inlet
Ew outlet
out
inlet
Ew outlet
DBH Schematic
DBH P&ID
Crude Inlet and Outlet
Bath Temperature sensors and pressure guage
Level guages
Water Outlet
Gas outlet
DBH Control philosophy
1. Bath temperature (TT 5705) (SP = 90 )
• T = 82-86 ℃, TCV 5701 operate on High fire(T<87 ℃) or Low fire (T<89 ℃)
• T = 91-92 ℃, close SDV 5701&2 (main burner off)
• T>= 92.5 ℃, close SDV, SV and open XV (BH tripped manual reset required)
2. Bath heater level (LS 5701)
• L < 3500mm, close SDV,SV and open XV of NG line(BH tripped manual reset required), close
XV (5703/06/07)
3. Interface Level (ILT 5701/02 = 450mm)
• ILT 5701 L > 450mm, open LCV 5702 for EW outlet, low alarm at 300mm
• ILT 5702 L< 300mm, close XV 5703 for EW outlet
4. NG line pressure P>1.4kg or P<0.1kg
• P>1.4kg or P<0.1kg , close SDV,SV and open XV (BH tripped manual reset required)
5. Flame failure: close SDV,SV and open XV (BH tripped manual reset required)
Fire safety arrangements
Thank you

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IDBH & DBH.pptx

  • 1. Indirect and Direct Bath Heaters Raj Dewangan Emp Id: 203481 Dept: PSS (STF)
  • 2. Process Flow Diagram HX-3 HX-2 HX-1 IDBH Wet crude tank DBH EET Dry crude Tank DCO inlet header WCO inlet header DCO outlet header WCO outlet header CoCP CoDP 8’’ 12’’ Out to CTF NHK
  • 3. Indirect bath heater • IDBH is used to heat the crude to maintain its flowability • Following properties need to be maintained: • Bath temperature = 85 ℃ • Crude outlet temperature = 43.2 ℃ • Flow rate= 5000kLPD * 2 (capacity 6500*2) • Inlet temperature (>29) • Inlet pressure: 4 < P < 6.2 kg/cm2g • IDBH consist • shell • Firetubes & chimney • heater coils: 8 passes • expansion tank: 120mm level • burner
  • 6. IDBH Control philosophy 1. Wet crude inlet temperature (TT5601 > 44 ℃) 2. High Bath temperature (TT 5603 > 85 ℃) 3. Expansion tank level (L < 120mm) 4. NG line pressure P>1.4kg or P<0.1kg 5. Flame failure In above cases close SDV,SV and open XV (BH tripped manual reset required)
  • 12. Safeties and limits 1. Heating medium temperature is below set point(H-44,L-29 ) • TT5603 & 5604 = 85 ℃ 2. Water level is at normal condition • LG 5602, LT 5601 3. Pressure Transmitter high and low set point is at healthy condition • PT 5605 4. Stack temperature of chimney is below set point 5. No flame in fire tube Unit can be operated only when all safeties are in good condition
  • 13. Burner and BMS Spark ignition (for 10sec) Pilot SV open Flame relay energised Flame sense by UV Ignition transformer cutoff Flame relay de- energised SDV Open, main burner on Ignition transformer cutoff Burner trip, Mannual reset required Flame stablished No Flame safety check
  • 14. IDBH Control philosophy 1. Wet crude inlet temperature (TT5601) (H-44,L-29 ) • T > 44 ℃ , close SDV 5601&2, (main burner off) no need to heat through IDBH 2. Bath temperature (TT 5603) (SP = 85) • T = 82-86 ℃, TCV 5601 operate on High fire (82-84 ℃) or Low fire (85-86 ℃) • T = 88 ℃, close SDV 5601&2 (main burner off) • T= 90 ℃, close SDV, SV and open XV (BH tripped manual reset required) 3. Expansion tank level • L >= 120mm, close FLV • 100 mm < L < 120mm, open FLV • L < 90mm, close SDV,SV and open XV (BH tripped manual reset required) 4. NG line pressure P>1.4kg or P<0.1kg • P>1.4kg or P<0.1kg , close SDV,SV and open XV (BH tripped manual reset required) 5. Flame failure: close SDV,SV and open XV (BH tripped manual reset required)
  • 15. Direct bath heater • DBH is used to heat the crude before processing in EET, inlet of crude is from HX-1 and outlet to EET • Following properties need to be maintained: • operating temperature = 90 ℃ • Operating pressure = 7kg/cm2g • Crude inlet temperature = 55.5 ℃ • Flow rate= 2500kLPD * 4 • Interface level = 450mm • IDBH consist of • Shell : filled with crude • Firetubes & chimney • Burner assembly • XV at crude inlet (5706), crude outlet (5707) water outlet (5703) out inlet Ew outlet
  • 18. Crude Inlet and Outlet
  • 19. Bath Temperature sensors and pressure guage
  • 23. DBH Control philosophy 1. Bath temperature (TT 5705) (SP = 90 ) • T = 82-86 ℃, TCV 5701 operate on High fire(T<87 ℃) or Low fire (T<89 ℃) • T = 91-92 ℃, close SDV 5701&2 (main burner off) • T>= 92.5 ℃, close SDV, SV and open XV (BH tripped manual reset required) 2. Bath heater level (LS 5701) • L < 3500mm, close SDV,SV and open XV of NG line(BH tripped manual reset required), close XV (5703/06/07) 3. Interface Level (ILT 5701/02 = 450mm) • ILT 5701 L > 450mm, open LCV 5702 for EW outlet, low alarm at 300mm • ILT 5702 L< 300mm, close XV 5703 for EW outlet 4. NG line pressure P>1.4kg or P<0.1kg • P>1.4kg or P<0.1kg , close SDV,SV and open XV (BH tripped manual reset required) 5. Flame failure: close SDV,SV and open XV (BH tripped manual reset required)

Editor's Notes

  1. The supply line is divided to a 3’’ main burner line and ¾’’ pilot line PRV reduces supply pressure (of 2-2.5kg) to 1.1kg for main burner line and 0.6kg for pilot line SDV is shut down valve to close main burner supply and SV is solenoid valve to close pilot gas supply TCV controls flow of NG in burner to maintain the temperature XV is on/off valve to vent the NG