Fired Heater Design & Performance Calculations

Simulation Results

Technical Summary

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

ENERGY PERFORMACE
Total Absorbed Duty	MW	59.993
Total Heat Release	MW	68.701
Total Efficiency	%	87.324

PROCESS
Process Name		Crude Oil 1
Heat Duty	MW	59.993
Flow rate (sec)	kg/s	200
INLET CONDITIONS
Inlet Temperature	°C	100
Inlet Pressure	kPa a	750.1
OUTLET CONDITIONS
Outlet Temperature	°C	484.6
Outlet Pressure	kPa a	-58043.828

AIR
Air Flow	kg/s	14.025	14.342
Air Temp.	°C	15.5	15.5
Excess Air	%	20	20

FUEL
Fuel Flow	kg/s	0.679	0.694
Fuel LHV	kJ/kg	50015	50015
Fuel Mol. Wt.		16	16

STACK
Flue Gas Flow	kg/s	29.74
Flue Gas Temp.	°C	233
CO2	mol%	8.06
H2O	mol%	16.06
N2	mol%	72.67
O2	mol%	3.21
SO2	mol%	0

CONVECTION
Convection Sect. No.		1
Heat Duty	MW	21.024
Flue Gas Flow	kg/s	29.74
Max Tube Temp.	°C	251
Total Press. Loss (inc. gain)	mmH2O	-0.96

RADIANT SECTION
Radiant Cell		1	2
Heat Duty	MW	19.484	19.484
Heat Release	MW	33.967	34.734
Arch Temp.	°C	785.1	785.1
Max Tube Temp.	°C	496.1	496.1
Average Flux	W/m²	34292	34292
Maximum Flux	W/m²	57388	57694
No. of Burners		8	8
Arch Pressure	mmH2O	-2.582	-2.582
Floor Pressure	mmH2O	-17.497	-17.497

Carbon Emissions

ENVIRONMENTAL IMPACT
Energy Efficiency	%	87.324
Daily CO2 Emissions	kg	327586

Commercial

BID / PROJECT VALUE

Total:	£ 1,781,252

Total:	£ 1,781,252

Total:

£ 1,781,252

SAFETY AND COMPLIANCE

Radiant cell no. 1: The burners to tube distance seems OK (API 560)

Radiant cell no. 2: The burners to tube distance seems OK (API 560)

Radiant cell no. 1: The burners to wall clearance seems OK (API 560)

Radiant cell no. 2: The burners to wall clearance seems OK (API 560)

Radiant cell no. 1: Burner Vertical Clearance seems OK (API 560)

Radiant cell no. 2: Burner Vertical Clearance seems OK (API 560)

Flame-tube impingment risk not identified

Radiant cell no. 1: API 560 Radiant height to width seems OK

Radiant cell no. 2: API 560 Radiant height to width seems OK

Radiant cell no. 1: Single lane of burners considered

Radiant cell no. 2: Single lane of burners considered

Stack No. 1: Auto Stack calc. has converged OK

Radiant section 1,Coil sect. no. 1, complies with API 530#Radiant section 2,Coil sect. no. 1, complies with API 530

Convection section 1,Coil sect. no. 1, complies with API 530

Convection section 1,Coil sect. no. 2, complies with API 530

Convection section 1,Coil sect. no. 3, complies with API 530

COIL ARRANGEMENT
Heater Section		RADIANT 1	RADIANT 2	CONVECTION 1	CONVECTION 1	CONVECTION 1
Orientation		Vertical	Vertical	Horizontal	Horizontal	Horizontal
Tube OD	mm	141.3	141.3	141.3	141.3	141.3
Tube Material		Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel
Tube Wall Thk	mm	Sch 40	Sch 40	Sch 40	Sch 40	Sch 40
Max Tube Temperature	°C	496.1	496.1	238.3	251	195.8
No. Tubes		80	80	36	24	36
Effective Length	m	16	16	15	15	15
Straight Length	m	15.5	15.5	15.4	15.4	15.4

Commercial

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Materials & Equipment Supply Steelwork & Fabrication Painting, Refractory & Anchors Ladders & Platforms, Tubes & Fittings Finning, Tube Supports Coil Fabrication (inc. Radiography) BMS, Instrumentation & Fuel Skid Burners	Detail Engineering Process & Thermal Design, Mechanical Design Piping Stress Analysis, Stuctural Design 3D Modelling, Detailed Design Drawings Fabrication, Shipping & Transport Drawings
Shipping & Delivery 1. Radiant Section - fully modulurised 2. Convection Section - fully modulurised 3. Stack - fully modulurised sections 4. Fuel Skid - fully modulurised	Terms 1. Delivery: 54 weeks (28 weeks Detailed Eng. only) 2. Validity: 14 days 3. Warranty: 3 years

Our Partners & Vendors

Heater companies:
Birwelco
FEI
GasTech
KT-Technology
Thermax

Burner Vendors:
Callidus (UOP)
Greens Combustion
ICE
John Zink Hamworthy
Zeeco

Fabricators:
Vatana Phisal (VPE)
Vipco
Steelcon Malaysia
AD Demirel
Polimex

Refractory:
Morgan
Linco Baxo
Insulcon B.V.
Zibo Luzhong

Summary

Main items
Material & Equipment Supply	£ 1,469,350
Option items
Detail Engineering (by HeaterSIM)	£ 220,402
Performance Guarantee	£35000
Third Party Design Check	£29500
Burner Performance Test	£27000
Total	£1,781,252

1. Fuel Temperature as per project specifications. This value is not reported here.
2. Fuel Pressure typically ~2 barg (29 psig) at maximum burner heat release. This value is not reported here.

Process Flow Diagram (PFD) Summary

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

STREAM NO.		1	2	3	3	4	5	5	6	6
Fluid Name		Crude Oil 1	Crude Oil 1	Radiant 1 Flue Gas	Radiant 2 Flue Gas	Stack 1 Flue Gas	Fuel No. 1	Fuel No. 1	Combustion Air	Combustion Air
Flow (sec)	kg/s	200	200	14.704	15.036	29.74	0.679	0.694	14.025	14.342
Flow (hr)	kg/hr	720000	720000	52935	54130	107066	2445	2500	50490	51630
Temperature	°C	100	484.6	785.1	785.1	233	Note 1	Note 1	15.5	15.5
Pressure	kPa a	750.1	-58043.828	-2.582	-2.582	-1.597	Note 2	Note 2	101.32	101.32

1. Fuel Temperature as per project specifications. This value is not reported here.
2. Fuel Pressure typically ~2 barg (29 psig) at maximum burner heat release. This value is not reported here.

GA Drawing

Stack Top Platform

Online API Fired Heater Software

Top of Stack Top of Transition Top of Conbox Top of Radiant Step off platform Hearth Grade Stack Dia Conbox eff Conbox IS Width I/S wall TCD No. Burners

COIL ARRANGEMENT
Heater Section		RADIANT 1	RADIANT 2	CONVECTION 1	CONVECTION 1	CONVECTION 1
Design Code		API 530	API 530		API 530	API 530
Orientation		Vertical	Vertical	Horizontal	Horizontal	Horizontal
Tube OD	mm	141.3	141.3	141.3	141.3	141.3
Tube Material		Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel
Tube Wall Thk	mm	Sch 40	Sch 40	Sch 40	Sch 40	Sch 40
Tube Spacing	mm	254	254	254	254	254
Vert. Row Spacing (Vert)	mm	N/A	N/A	220.1	220.1	220.1
No. Tubes		80	80	36	24	36
Effective Length	m	16	16	15	15	15
Straight Length	m	15.5	15.5	15.4	15.4	15.4

Notes

1. DIMENSIONS TO BE CONFIRMED DURING DETAILED ENGINEERING PHASE

2. LADDERS AND PLATFORMS SHALL BE IN ACCORDANCE WITH API 56O REQUIREMENTS MINIMUM AND PROJECT SPECIFICATIONS

3. THIS PROPOSAL DRAWING SHOULD BE CONSIDERED AS A SKETCH AND MAY NOT BE ENTIRELY DRAWN TO SCALE

4. REFRACTORY MATERIAL AND THICKNESSES SHALL BE AS PER PROJECT HEATER DATASHEET

5. PLEASE REFER TO COIL CONFIGURATION AND MATERIAL WITHIN THE TABLE BELOW

6. DOORS SHALL BE PROVIDED IN ACCORDANCE WITH PROJECT HEATER DATASHEET

REV	DATE	DRAWING DESCRIPTION	BY	CHK

GENERAL ARRANGEMENT DRAWING
API 560 FIRED HEATER PROPOSAL

TAG NO. / PROJECT REF. HS

PROJECT TITLE

CLIENT

PROJECT LOCATION

EmissionsLow NOx burners

Carbon Dioxide
Sulphur Dioxide
Carbon Monoxide	<100 ppm
N2 Oxides (NOx)	<150 ppm

NOTE

The ability to view full results and modify the model is not availble on the screen size that you're currently using

Process Conditions

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Process Name		Crude Oil 1
Heat Duty	MW	59.993
Flow rate (sec)	kg/s	200
Flow rate (hr)	kg/hr	720000
Pressure drop	kPa	58793.93
Max. Film Temp. Calculated	°C	488.2
Max. Film Temp. Allowed	°C	350
Max Tube Average Flux Calculated (1)	W/m²	38153
Average Flux Allowed	W/m²	31500
INLET CONDITIONS
Inlet Temperature	°C	100
Inlet Pressure	kPa a	750.1
Inlet Vapour Fraction		0
Inlet Enthalpy	kJ/kg	135
OUTLET CONDITIONS
Outlet Temperature	°C	484.6
Outlet Pressure	kPa a	-58043.828
Outlet Vapour Fraction		1
Outlet Enthalpy	kJ/kg	435

Crude Oil 1: Calculated outlet pressure is excessively below atmospheric pressure

If the specified or calculated fluid temperature(s) and pressure(s) are outside of the defined property grid the program will use extrapolation. Significant extrapolation may introduce inaccuracies.

1) The max flux calculated on a individual tube basis (see tube profile results data).

API 560 Fired Heater, API 560 Fired Heater P&ID, API 560 Fired Heater Control and Instrumentation, API 560 Fired Heater Instruments, API 560 Fired Heater Piping and Instrumentation Diagram

Typical Schematic

Radiant Section

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

API 560 Fired Heater, VC Fired Heater, API VC Fired Heater

Radiant Cell		1	2
Radiant Type
Heat Duty	MW	19.484	19.484
Heat Release	MW	33.967	34.734
Arch Temp.	°C	785.1	785.1
Max Tube Temp.	°C	496.1	496.1
Tube Cirle Diameter	m	N/A	N/A
Average Flux	W/m²	34292	34292
Maximum Flux	W/m²	57388	57694
Flue Flow	kg/s	14.704	15.036
Air Flow	kg/s	14.025	14.342
Fuel Flow	kg/s	0.679	0.694
Excess Air	%	20	20
Air Temp.	°C	15.5	15.5
Arch Pressure	mmH2O	-2.582	-2.582
Floor Pressure	mmH2O	-17.497	-17.497
Radiant Height	m	17	17
Radiant Width	m	7.08	7.08
Radiant Length	m	10.54	10.54
No. of Burners		8	8
Burner Cirle Diameter	m	N/A	N/A
Burner Design Firing	MW	4.67	4.78
Burner Normal Firing	MW	4.25	4.34
Burner Min Firing	MW	0.93	0.96
Burner-to-Tube Note		OK	OK
Burner-to-Wall Note		OK	OK
Burner-to-Roof Note		OK	OK
API Burner-to-Tube Dist.	m	1.668	1.71
API Burner-to-Wall Dist.	m	1.527	1.555
API Burner-to-Roof/Roof Dist	m	11.057	11.271
Floor Flux	W/m²	454989	465258

Flame-tube impingment risk not identified

Firing Notes
1. The Lower Heating Value (LHV) of the fuel efficiencies shall be used for efficiency calculations
2. Typical radiation heat loss value of 1.5% is used typically considered. However, in cases with a flue gas/air preheater, a value of 2.5% is normally considered.
3. Typical Excess Air values can be used as follows:
- Natural Draft - 15% excess air
- Forced Draft - 10% excess air
4. API 560 - Pressure at the Arch should be maintained at -2.5mmH2Og (-0.1inH2Og)

Tube Support Notes
1. Design temp. for tube supports should be Arch temp + 100 C (180 F) 2. No credit should be considered for shielding effect of tube supports by refractory 3. API 560 states if fuel the Vanadium + Sodium content in fuel exceeds 100ppm, supports to be either: - 50Cr-50Ni metallurgy, without any coating
- Covered with 50 mm (2 in) of castable refractory (see API 560)

Combustion

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Radiant Type
Flue Flow	kg/s	14.704	15.036
Air Flow	kg/s	14.025	14.342
Fuel Flow	kg/s	0.679	0.694
Fuel LHV	kJ/kg	50015	50015
Excess Air	%	20	20
Air Temp.	°C	15.5	15.5
CO2	mol%	8.06	8.06
H2O	mol%	16.06	16.06
N2	mol%	72.67	72.67
O2	mol%	3.21	3.21
SO2	mol%	0	0
Dew Point	°C	56	56
Fuel Mol. Wt.		16	16
Flue Mol. Wt.		27.812	27.812
Flame Temperature	°C	1805.6	1805.6
Flue Gas Emissivity		0.58	0.58

Process Burner, Combustion Burner, Burner Flame, Industrial Burner

Notes
1. One UV scanner per burner is recommended (if total no. burners < 20)
2. One Pilot per burner is recommended
3. Electric spark ignition is recommended for each pilot
4. Forced draft system

Notes
1. The Lower Heating Value (LHV) of the fuel efficiencies shall be used for efficiency calculations
2. Typical radiation heat loss value of 1.5% is used typically considered. However, in cases with a flue gas/air preheater, a value of 2.5% is normally considered.
3. Typical Excess Air values can be used as follows:
- Natural Draft - 15% excess air
- Forced Draft - 10% excess air
4. API 560 - Pressure at the Arch should be maintained at -2.5mmH2Og (-0.1inH2Og)

Convection Section

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

API 560 Fired Heater Process Flow, Fired Heater process coil, Fired Heater process design, furnace process layout, radiant and convection section process scheme

Convection Sect. No.		1
Heat Duty	MW	21.024
Max Tube Temp.	°C	251
Total Flue Press. Loss (ex. gain)	mmH2O	1.8
Total Press. Gain	mmH2O	2.76
Total Press. Loss (inc. gain)	mmH2O	-0.96
Convection Width	m	3.175
Effective Length	m	15
Convection Height	m	3.601
Total No. Rows		8
FLUE GAS DATA
Flue Gas Flow	kg/s	29.74
Flue Gas Inlet Temp.	°C	784.6
Flue Gas Outlet Temp.	°C	233
CO2	mol%	8.058337
H2O	mol%	16.05639
N2	mol%	72.674
O2	mol%	3.211277
SO2	mol%	0

Convection (Flue gas side)

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

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Conbox	Row	Coil Section	Duty	Temp Inlet	Temp Outlet	Enthalpy In	Enthalpy Out	Flue Density	Fin Type	Avg Flux	Max Flux	Tubes per Row	FG Mass Vel.	Flue P drop	Tube Material	Fin Material	Avg Fin Temp	Max Fin Temp
			MW	°C	°C	kJ/kg	kJ/kg	kg/m³		W/m²	W/m²		kg/s m²	mmH2Og			°C	°C
1	8	Coil Section 3	1.79	284.9	233	303.1	242.8	0.64	Solid	22439	26782	12	1.653	0.234	C.S.	C.S.	164.9	183.5
1	7	Coil Section 3	2.28	350	284.9	379.7	303.1	0.58	Solid	28538	33985	12	1.653	0.263	C.S.	C.S.	192.2	211.4
1	6	Coil Section 3	3.27	441.9	350	489.7	379.7	0.51	Solid	40958	48616	12	1.653	0.298	C.S.	C.S.	225.7	252.4
1	5	Coil Section 2	3.47	535.9	441.9	606.3	489.7	0.45	Solid	43387	52262	12	1.572	0.242	C.S.	C.S.	243.5	275.4
1	4	Coil Section 2	4.91	666.7	535.9	771.6	606.3	0.39	Solid	61538	75791	12	1.572	0.278	C.S.	C.S.	294.1	336.1
1	3	Coil Section 1	1.43	700.9	666.7	816.5	771.6	0.35	None	18970	33137	12	1.466	0.156	C.S.	None	0	0
1	2	Coil Section 1	1.69	738.8	700.9	865.6	816.5	0.34	None	23917	41778	12	1.466	0.162	C.S.	None	0	0
1	1	Coil Section 1	2.19	784.6	738.8	919.6	865.6	0.33	None	34768	60732	12	1.466	0.169	C.S.	None	0	0

Convection (Process Side)

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Conv. Box	Row	Coil Section	Duty	Flue Temp. IN	Flue Temp. OUT	Process	Flow	Bulk Temp. In	Bulk Temp. Out	Bulk Press. In	Bulk Press. Out	Vap. Fraction In	Vap. Fraction Out	Inlet Velocity	Outlet Velocity	Inlet Crit.Vel.	Outlet Crit.Vel.	Inlet M Vel.	Outlet M Vel.	Inlet Reynolds No.	Inlet Reynolds No.
			MW	°C	°C			°C	°C	kPa a	kPa a			m/s	m/s	m/s	m/s	kg/s m²	kg/s m²
1	8	Coil Section 3	1.79	284.9	233	Crude Oil 1	1	100	137.7	750	666	0	0	5.2	5.2	0	0	3874	3874	636645	649577
1	7	Coil Section 3	2.28	350	284.9	Crude Oil 1	2	137.7	147.4	666	581	0	0	5.2	5.2	0	0	3874	3874	649575	655234
1	6	Coil Section 3	3.27	441.9	350	Crude Oil 1	3	147.4	161.5	581	496	0	0	5.2	5.3	0	0	3874	3874	655235	663519
1	5	Coil Section 2	3.47	535.9	441.9	Crude Oil 1	4	161.5	176.3	496	411	0	0	5.3	5.3	0	0	3874	3874	663509	677412
1	4	Coil Section 2	4.91	666.7	535.9	Crude Oil 1	5	176.3	197.4	411	267	0	0.04	5.3	26	0	42	3874	3874	677397	719620
1	3	Coil Section 1	1.43	700.9	666.7	Crude Oil 1	6	197.3	206.7	267	-800	0.04	0.43	26	335	42	NaN	3874	3874	719596	49658332
1	2	Coil Section 1	1.69	738.8	700.9	Crude Oil 1	7	206.7	215.6	-800	-4061	0.43	1	335.1	774.7	NaN	NaN	3874	3874	49658332	49658332
1	1	Coil Section 1	2.19	784.6	738.8	Crude Oil 1	8	215.6	227.2	-4054	-15619	1	1	774.7	618.2	NaN	NaN	3874	3874	49658332	49658332

Conv. Box	Row	Coil Section	Duty	Flue Temp. IN	Flue Temp. OUT	Process	Flow	Bulk Temp. In	Bulk Temp. Out	Bulk Press. In	Bulk Press. Out	Vap. Fraction In	Vap. Fraction Out	Inlet Velocity	Outlet Velocity	Inlet Crit.Vel.	Outlet Crit.Vel.	Inlet M Vel.	Outlet M Vel.	Inlet Reynolds No.	Inlet Reynolds No.
			MW	°C	°C			°C	°C	kPa a	kPa a			m/s	m/s	m/s	m/s	kg/s m²	kg/s m²
1	8	Coil Section 3	1.79	284.9	233	Crude Oil 1	1	100	137.7	750	666	0	0	5.2	5.2	0	0	3874	3874	636645	649577
1	7	Coil Section 3	2.28	350	284.9	Crude Oil 1	2	137.7	147.4	666	581	0	0	5.2	5.2	0	0	3874	3874	649575	655234
1	6	Coil Section 3	3.27	441.9	350	Crude Oil 1	3	147.4	161.5	581	496	0	0	5.2	5.3	0	0	3874	3874	655235	663519
1	5	Coil Section 2	3.47	535.9	441.9	Crude Oil 1	4	161.5	176.3	496	411	0	0	5.3	5.3	0	0	3874	3874	663509	677412
1	4	Coil Section 2	4.91	666.7	535.9	Crude Oil 1	5	176.3	197.4	411	267	0	0.04	5.3	26	0	42	3874	3874	677397	719620
1	3	Coil Section 1	1.43	700.9	666.7	Crude Oil 1	6	197.3	206.7	267	-800	0.04	0.43	26	335	42	NaN	3874	3874	719596	49658332
1	2	Coil Section 1	1.69	738.8	700.9	Crude Oil 1	7	206.7	215.6	-800	-4061	0.43	1	335.1	774.7	NaN	NaN	3874	3874	49658332	49658332
1	1	Coil Section 1	2.19	784.6	738.8	Crude Oil 1	8	215.6	227.2	-4054	-15619	1	1	774.7	618.2	NaN	NaN	3874	3874	49658332	49658332

Radiant Tube Profile

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Tube No.	Loc.	Process	Bulk Temp In.	Bulk Temp Out.	Bulk Press In.	Bulk Press. Out	Enth. In	Enth. Out	Vapour Out	Tube OD	Velocity Out	Film Temp	Avg Tube Temp.	Max Tube Temp.	API Design Temp.	Avg HTC	Flow Regime	Tube Mat.	Avg Flux	Max Flux	Regime X	Regime Y
			°C	°C	kPa a	kPa a	kJ/kg	kJ/kg			m/s	°C	°C	°C	°C	W/m² °C			W/m²	W/m²
1	Wall	Crude Oil 1	227.2	232.4	-15618.8	-18789.9	240.1	244.9	1	141.3	542	237.7	239.8	247.1	262.1	13116.5	Turbulent		38153	63038	0	0
2	Wall	Crude Oil 1	232.4	237.6	-18789.9	-21596.8	244.9	249.8	1	141.3	483.8	242.8	244.9	252.2	267.2	13209.9	Turbulent		38007	62836	0	0
3	Wall	Crude Oil 1	237.6	242.8	-21596.8	-24120.1	249.8	254.7	1	141.3	437.7	247.9	250	257.3	272.3	13301.2	Turbulent		37860	62632	0	0
4	Wall	Crude Oil 1	242.8	247.9	-24120.1	-26416.4	254.7	259.5	1	141.3	400.4	253.1	255.2	262.4	277.4	13390.5	Turbulent		37712	62424	0	0
5	Wall	Crude Oil 1	247.9	253.1	-26416.4	-28524.6	259.5	264.4	1	141.3	367.4	258.2	260.3	267.5	282.5	13478.9	Turbulent		37561	62212	0	0
6	Wall	Crude Oil 1	253.1	258.3	-28524.6	-30459.9	264.4	269.3	1	141.3	338.7	263.3	265.4	272.6	287.6	13574.5	Turbulent		37409	61997	0	0
7	Wall	Crude Oil 1	258.3	263.4	-30459.9	-32251.2	269.3	274.2	1	141.3	314.6	268.4	270.5	277.7	292.7	13668.1	Turbulent		37254	61778	0	0
8	Wall	Crude Oil 1	263.4	268.6	-32251.2	-33920.7	274.2	279	1	141.3	294.1	273.6	275.6	282.9	297.9	13759.7	Turbulent		37098	61555	0	0
9	Wall	Crude Oil 1	268.6	273.8	-33920.7	-35485.8	279	283.9	1	141.3	276.5	278.7	280.7	288	303	13849.6	Turbulent		36940	61329	0	0
10	Wall	Crude Oil 1	273.8	279	-35485.8	-36960.5	283.9	288.8	1	141.3	261.1	283.8	285.8	293.1	308.1	13937.7	Turbulent		36780	61099	0	0
11	Wall	Crude Oil 1	279	285.4	-36960.5	-38343.3	288.8	293.6	1	141.3	242.9	290.2	291.6	299.5	314.5	14005.9	Turbulent		36597	60816	0	0
12	Wall	Crude Oil 1	285.4	292.2	-38343.3	-39630.5	293.6	298.5	1	141.3	226.5	297	298.2	306.2	321.2	14050.5	Turbulent		36385	60502	0	0
13	Wall	Crude Oil 1	292.2	299	-39630.5	-40834.5	298.5	303.4	1	141.3	212.5	303.7	304.9	312.9	327.9	14097.1	Turbulent		36163	60179	0	0
14	Wall	Crude Oil 1	299	305.8	-40834.5	-41967	303.4	308.3	1	141.3	200.3	310.5	311.7	319.7	334.7	14142.7	Turbulent		35939	59848	0	0
15	Wall	Crude Oil 1	305.8	312.6	-41967	-43037.2	308.3	313.1	1	141.3	189.4	317.2	318.4	326.4	341.4	14187.2	Turbulent		35710	59511	0	0
16	Wall	Crude Oil 1	312.6	319.4	-43037.2	-44048.2	313.1	318	1	141.3	179.2	324	325.2	333.1	348.1	14234.1	Turbulent		35478	59165	0	0
17	Wall	Crude Oil 1	319.4	326.2	-44048.2	-45006.8	318	322.9	1	141.3	170.2	330.8	331.9	339.9	354.9	14280.4	Turbulent		35241	58812	0	0
18	Wall	Crude Oil 1	326.2	333	-45006.8	-45919	322.9	327.7	1	141.3	162.2	337.5	338.6	346.6	361.6	14325.7	Turbulent		35000	58451	0	0
19	Wall	Crude Oil 1	333	339.8	-45919	-46789.9	327.7	332.6	1	141.3	155.1	344.3	345.4	353.3	368.3	14370.2	Turbulent		34755	58082	0	0
20	Wall	Crude Oil 1	339.8	346.7	-46789.9	-47612.6	332.6	337.5	1	141.3	144.8	351.1	352.2	360.1	375.1	14409.6	Turbulent		34504	57699	0	0
21	Wall	Crude Oil 1	346.7	353.6	-47612.6	-48382.1	337.5	342.4	1	141.3	135.8	358	359	366.9	381.9	14445	Turbulent		34247	57308	0	0
22	Wall	Crude Oil 1	353.6	360.5	-48382.1	-49105.7	342.4	347.2	1	141.3	128	364.8	365.8	373.8	388.8	14479.7	Turbulent		33985	56907	0	0
23	Wall	Crude Oil 1	360.5	367.4	-49105.7	-49789.3	347.2	352.1	1	141.3	121.2	371.7	372.7	380.6	395.6	14513.7	Turbulent		33718	56497	0	0
24	Wall	Crude Oil 1	367.4	374.3	-49789.3	-50437.7	352.1	357	1	141.3	115.1	378.5	379.5	387.4	402.4	14547.1	Turbulent		33447	56078	0	0
25	Wall	Crude Oil 1	374.3	381.2	-50437.7	-51054.9	357	361.8	1	141.3	109.8	385.4	386.4	394.2	409.2	14579.9	Turbulent		33170	55650	0	0
26	Wall	Crude Oil 1	381.2	388.1	-51054.9	-51644.4	361.8	366.7	1	141.3	105	392.3	393.2	401	416	14612.1	Turbulent		32889	55212	0	0
27	Wall	Crude Oil 1	388.1	395	-51644.4	-52208.8	366.7	371.6	1	141.3	100.7	399.1	400	407.8	422.8	14643.7	Turbulent		32602	54764	0	0
28	Wall	Crude Oil 1	395	401.9	-52208.8	-52750.7	371.6	376.5	1	141.3	96.8	406	406.8	414.6	429.6	14674.7	Turbulent		32310	54307	0	0
29	Wall	Crude Oil 1	401.9	408.8	-52750.7	-53272	376.5	381.3	1	141.3	93.2	412.8	413.7	421.4	436.4	14705.2	Turbulent		32013	53839	0	0
30	Wall	Crude Oil 1	408.8	415.7	-53272	-53774.7	381.3	386.2	1	141.3	89.9	419.7	420.5	428.2	443.2	14735.2	Turbulent		31711	53361	0	0
31	Wall	Crude Oil 1	415.7	422.6	-53774.7	-54260.3	386.2	391.1	1	141.3	87	426.5	427.3	435	450	14764.7	Turbulent		31403	52872	0	0
32	Wall	Crude Oil 1	422.6	429.5	-54260.3	-54730.1	391.1	395.9	1	141.3	84.2	433.4	434.2	441.8	456.8	14793.8	Turbulent		31089	52373	0	0
33	Wall	Crude Oil 1	429.5	436.4	-54730.1	-55185.4	395.9	400.8	1	141.3	81.7	440.2	441	448.6	463.6	14822.3	Turbulent		30770	51862	0	0
34	Wall	Crude Oil 1	436.4	443.3	-55185.4	-55627.3	400.8	405.7	1	141.3	79.3	447.1	447.8	455.4	470.4	14850.4	Turbulent		30445	51341	0	0
35	Wall	Crude Oil 1	443.3	450.2	-55627.3	-56056.7	405.7	410.6	1	141.3	77.1	453.9	454.6	462.2	477.2	14878.1	Turbulent		30113	50808	0	0
36	Wall	Crude Oil 1	450.2	457.1	-56056.7	-56474.5	410.6	415.4	1	141.3	75.1	460.8	461.4	469	484	14905.3	Turbulent		29776	50264	0	0
37	Wall	Crude Oil 1	457.1	464	-56474.5	-56881.4	415.4	420.3	1	141.3	73.2	467.6	468.2	475.8	490.8	14932.2	Turbulent		29433	49708	0	0
38	Wall	Crude Oil 1	464	470.9	-56881.4	-57278.2	420.3	425.2	1	141.3	71.4	474.5	475.1	482.5	497.5	14958.6	Turbulent		29083	49141	0	0
39	Wall	Crude Oil 1	470.9	477.8	-57278.2	-57665.5	425.2	430	1	141.3	69.7	481.3	481.9	489.3	504.3	14984.7	Turbulent		28727	48561	0	0
40	Wall	Crude Oil 1	477.8	484.6	-57665.5	-58043.8	430	434.9	1	141.3	68.1	488.2	488.7	496.1	511.1	15010.3	Turbulent		28365	47969	0	0
1	Wall	Crude Oil 1	227.2	232.4	-15618.8	-18789.9	240.1	244.9	1	141.3	542	237.7	239.8	247.1	262.1	13116.5	Turbulent		38153	63038	0	0
2	Wall	Crude Oil 1	232.4	237.6	-18789.9	-21596.8	244.9	249.8	1	141.3	483.8	242.8	244.9	252.2	267.2	13209.9	Turbulent		38007	62836	0	0
3	Wall	Crude Oil 1	237.6	242.8	-21596.8	-24120.1	249.8	254.7	1	141.3	437.7	247.9	250	257.3	272.3	13301.2	Turbulent		37860	62632	0	0
4	Wall	Crude Oil 1	242.8	247.9	-24120.1	-26416.4	254.7	259.5	1	141.3	400.4	253.1	255.2	262.4	277.4	13390.5	Turbulent		37712	62424	0	0
5	Wall	Crude Oil 1	247.9	253.1	-26416.4	-28524.6	259.5	264.4	1	141.3	367.4	258.2	260.3	267.5	282.5	13478.9	Turbulent		37561	62212	0	0
6	Wall	Crude Oil 1	253.1	258.3	-28524.6	-30459.9	264.4	269.3	1	141.3	338.7	263.3	265.4	272.6	287.6	13574.5	Turbulent		37409	61997	0	0
7	Wall	Crude Oil 1	258.3	263.4	-30459.9	-32251.2	269.3	274.2	1	141.3	314.6	268.4	270.5	277.7	292.7	13668.1	Turbulent		37254	61778	0	0
8	Wall	Crude Oil 1	263.4	268.6	-32251.2	-33920.7	274.2	279	1	141.3	294.1	273.6	275.6	282.9	297.9	13759.7	Turbulent		37098	61555	0	0
9	Wall	Crude Oil 1	268.6	273.8	-33920.7	-35485.8	279	283.9	1	141.3	276.5	278.7	280.7	288	303	13849.6	Turbulent		36940	61329	0	0
10	Wall	Crude Oil 1	273.8	279	-35485.8	-36960.5	283.9	288.8	1	141.3	261.1	283.8	285.8	293.1	308.1	13937.7	Turbulent		36780	61099	0	0
11	Wall	Crude Oil 1	279	285.4	-36960.5	-38343.3	288.8	293.6	1	141.3	242.9	290.2	291.6	299.5	314.5	14005.9	Turbulent		36597	60816	0	0
12	Wall	Crude Oil 1	285.4	292.2	-38343.3	-39630.5	293.6	298.5	1	141.3	226.5	297	298.2	306.2	321.2	14050.5	Turbulent		36385	60502	0	0
13	Wall	Crude Oil 1	292.2	299	-39630.5	-40834.5	298.5	303.4	1	141.3	212.5	303.7	304.9	312.9	327.9	14097.1	Turbulent		36163	60179	0	0
14	Wall	Crude Oil 1	299	305.8	-40834.5	-41967	303.4	308.3	1	141.3	200.3	310.5	311.7	319.7	334.7	14142.7	Turbulent		35939	59848	0	0
15	Wall	Crude Oil 1	305.8	312.6	-41967	-43037.2	308.3	313.1	1	141.3	189.4	317.2	318.4	326.4	341.4	14187.2	Turbulent		35710	59511	0	0
16	Wall	Crude Oil 1	312.6	319.4	-43037.2	-44048.2	313.1	318	1	141.3	179.2	324	325.2	333.1	348.1	14234.1	Turbulent		35478	59165	0	0
17	Wall	Crude Oil 1	319.4	326.2	-44048.2	-45006.8	318	322.9	1	141.3	170.2	330.8	331.9	339.9	354.9	14280.4	Turbulent		35241	58812	0	0
18	Wall	Crude Oil 1	326.2	333	-45006.8	-45919	322.9	327.7	1	141.3	162.2	337.5	338.6	346.6	361.6	14325.7	Turbulent		35000	58451	0	0
19	Wall	Crude Oil 1	333	339.8	-45919	-46789.9	327.7	332.6	1	141.3	155.1	344.3	345.4	353.3	368.3	14370.2	Turbulent		34755	58082	0	0
20	Wall	Crude Oil 1	339.8	346.7	-46789.9	-47612.6	332.6	337.5	1	141.3	144.8	351.1	352.2	360.1	375.1	14409.6	Turbulent		34504	57699	0	0
21	Wall	Crude Oil 1	346.7	353.6	-47612.6	-48382.1	337.5	342.4	1	141.3	135.8	358	359	366.9	381.9	14445	Turbulent		34247	57308	0	0
22	Wall	Crude Oil 1	353.6	360.5	-48382.1	-49105.7	342.4	347.2	1	141.3	128	364.8	365.8	373.8	388.8	14479.7	Turbulent		33985	56907	0	0
23	Wall	Crude Oil 1	360.5	367.4	-49105.7	-49789.3	347.2	352.1	1	141.3	121.2	371.7	372.7	380.6	395.6	14513.7	Turbulent		33718	56497	0	0
24	Wall	Crude Oil 1	367.4	374.3	-49789.3	-50437.7	352.1	357	1	141.3	115.1	378.5	379.5	387.4	402.4	14547.1	Turbulent		33447	56078	0	0
25	Wall	Crude Oil 1	374.3	381.2	-50437.7	-51054.9	357	361.8	1	141.3	109.8	385.4	386.4	394.2	409.2	14579.9	Turbulent		33170	55650	0	0
26	Wall	Crude Oil 1	381.2	388.1	-51054.9	-51644.4	361.8	366.7	1	141.3	105	392.3	393.2	401	416	14612.1	Turbulent		32889	55212	0	0
27	Wall	Crude Oil 1	388.1	395	-51644.4	-52208.8	366.7	371.6	1	141.3	100.7	399.1	400	407.8	422.8	14643.7	Turbulent		32602	54764	0	0
28	Wall	Crude Oil 1	395	401.9	-52208.8	-52750.7	371.6	376.5	1	141.3	96.8	406	406.8	414.6	429.6	14674.7	Turbulent		32310	54307	0	0
29	Wall	Crude Oil 1	401.9	408.8	-52750.7	-53272	376.5	381.3	1	141.3	93.2	412.8	413.7	421.4	436.4	14705.2	Turbulent		32013	53839	0	0
30	Wall	Crude Oil 1	408.8	415.7	-53272	-53774.7	381.3	386.2	1	141.3	89.9	419.7	420.5	428.2	443.2	14735.2	Turbulent		31711	53361	0	0
31	Wall	Crude Oil 1	415.7	422.6	-53774.7	-54260.3	386.2	391.1	1	141.3	87	426.5	427.3	435	450	14764.7	Turbulent		31403	52872	0	0
32	Wall	Crude Oil 1	422.6	429.5	-54260.3	-54730.1	391.1	395.9	1	141.3	84.2	433.4	434.2	441.8	456.8	14793.8	Turbulent		31089	52373	0	0
33	Wall	Crude Oil 1	429.5	436.4	-54730.1	-55185.4	395.9	400.8	1	141.3	81.7	440.2	441	448.6	463.6	14822.3	Turbulent		30770	51862	0	0
34	Wall	Crude Oil 1	436.4	443.3	-55185.4	-55627.3	400.8	405.7	1	141.3	79.3	447.1	447.8	455.4	470.4	14850.4	Turbulent		30445	51341	0	0
35	Wall	Crude Oil 1	443.3	450.2	-55627.3	-56056.7	405.7	410.6	1	141.3	77.1	453.9	454.6	462.2	477.2	14878.1	Turbulent		30113	50808	0	0
36	Wall	Crude Oil 1	450.2	457.1	-56056.7	-56474.5	410.6	415.4	1	141.3	75.1	460.8	461.4	469	484	14905.3	Turbulent		29776	50264	0	0
37	Wall	Crude Oil 1	457.1	464	-56474.5	-56881.4	415.4	420.3	1	141.3	73.2	467.6	468.2	475.8	490.8	14932.2	Turbulent		29433	49708	0	0
38	Wall	Crude Oil 1	464	470.9	-56881.4	-57278.2	420.3	425.2	1	141.3	71.4	474.5	475.1	482.5	497.5	14958.6	Turbulent		29083	49141	0	0
39	Wall	Crude Oil 1	470.9	477.8	-57278.2	-57665.5	425.2	430	1	141.3	69.7	481.3	481.9	489.3	504.3	14984.7	Turbulent		28727	48561	0	0
40	Wall	Crude Oil 1	477.8	484.6	-57665.5	-58043.8	430	434.9	1	141.3	68.1	488.2	488.7	496.1	511.1	15010.3	Turbulent		28365	47969	0	0

Flame-tube impingment risk not identified

Convection Tube Profile

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Conv. Box	Tube No.	Coil Sect.	Row	Process	Bulk Temp. In	Bulk Temp. Out	Press. In	Press. Out	Enth. In	Enth. Out	Vapour Fraction	Tube OD	Velocity	Film	Avg Tube Temp.	Max Tube Temp.	API Design Temp.	Avg HTC	Fin Type	Flow Regime	Tube Mat.	Avg Flux	Max Flux	Regime X	Regime Y
					°C	°C	kPa a	kPa a	kJ/kg	kJ/kg			m/s	°C	°C	°C	°C	W/m² °C				W/m²	W/m²
1	1	3	8	Crude Oil 1	100	112.6	750.1	722	135	138	0	141.3	5.2	128.9	125	133.7	148.7	2265.8	Solid	Turbulent	C.S.	24104	33541	0	0
1	2	3	8	Crude Oil 1	112.6	125.1	722	693.8	138	141	0	141.3	5.2	140	135.9	144.4	159.4	2274.6	Solid	Turbulent	C.S.	22056	30692	0	0
1	3	3	8	Crude Oil 1	125.1	137.7	693.8	665.7	141	144	0	141.3	5.2	151.1	146.8	155.1	170.1	2284	Solid	Turbulent	C.S.	20002	27833	0	0
1	4	3	7	Crude Oil 1	137.7	140.9	665.7	637.4	144	147.8	0	141.3	5.2	160.2	161.5	166.1	181.1	2295.5	Solid	Turbulent	C.S.	28953	40228	0	0
1	5	3	7	Crude Oil 1	140.9	144.2	637.4	609.2	147.8	151.6	0	141.3	5.2	163.1	164.3	168.8	183.8	2300.4	Solid	Turbulent	C.S.	28410	39474	0	0
1	6	3	7	Crude Oil 1	144.2	147.4	609.2	581	151.6	155.4	0	141.3	5.2	166	167.1	171.6	186.6	2305.2	Solid	Turbulent	C.S.	27867	38720	0	0
1	7	3	6	Crude Oil 1	147.4	152.1	581	552.7	155.4	160.8	0	141.3	5.3	179.6	181.4	188	203	2315.4	Solid	Turbulent	C.S.	41572	57640	0	0
1	8	3	6	Crude Oil 1	152.1	156.8	552.7	524.4	160.8	166.3	0	141.3	5.3	183.6	185.4	191.9	206.9	2321.9	Solid	Turbulent	C.S.	40762	56516	0	0
1	9	3	6	Crude Oil 1	156.8	161.5	524.4	496.1	166.3	171.7	0	141.3	5.3	187.7	189.4	195.8	210.8	2328.3	Solid	Turbulent	C.S.	39951	55392	0	0
1	10	2	5	Crude Oil 1	161.5	166.4	496.1	467.7	171.7	177.5	0	141.3	5.3	195.4	197.4	204.4	219.4	2336.7	Solid	Turbulent	C.S.	43941	61474	0	0
1	11	2	5	Crude Oil 1	166.4	171.4	467.7	439.4	177.5	183.2	0	141.3	5.3	199.8	201.8	208.7	223.7	2344.9	Solid	Turbulent	C.S.	43261	60523	0	0
1	12	2	5	Crude Oil 1	171.4	176.3	439.4	411	183.2	189	0	141.3	5.3	204.2	206.1	213	228	2352.8	Solid	Turbulent	C.S.	42581	59572	0	0
1	13	2	4	Crude Oil 1	176.3	183.3	411	382.6	189	197.2	0	141.3	5.3	224.6	227.7	237.8	252.8	2363	Solid	Turbulent	C.S.	62385	88556	0	0
1	14	2	4	Crude Oil 1	183.3	190.3	382.6	354.2	197.2	205.4	0	141.3	5.3	230.7	233.7	243.7	258.7	2374.7	Solid	Turbulent	C.S.	61327	87053	0	0
1	15	2	4	Crude Oil 1	190.3	197.4	354.2	266.8	205.4	213.6	0.0422	141.3	26	238.3	241.1	251	266	2305.3	Solid	Bubble	C.S.	60268	85551	15288.12	10870.17
1	16	1	3	Crude Oil 1	197.3	200.4	266.8	75	213.6	215.9	0.139	141.3	112.3	216.1	216.9	220.7	235.7	2205.6	None	Bubble	C.S.	17947	31349	15040.16	26910.24
1	17	1	3	Crude Oil 1	200.4	203.6	75	-444.4	215.9	218.3	0.305	141.3	239.9	218.9	219.7	223.5	238.5	2233.6	None	Mist	C.S.	17839	31160	13357.52	107073.8
1	18	1	3	Crude Oil 1	203.6	206.7	-444.4	-799.7	218.3	220.7	0.4286	141.3	335	213.4	214.2	218	233	5032.5	None	Mist	C.S.	17731	30972	10800.19	232530
1	19	1	2	Crude Oil 1	206.7	209.6	-800.1	-1386.2	220.7	223.5	0.629	141.3	489.2	215.8	217.1	221.3	236.3	6598.8	None	Mist	C.S.	21202	37036	8891.784	326055
1	20	1	2	Crude Oil 1	209.6	212.6	-1386.2	-2350.6	223.5	226.3	0.9552	141.3	740.3	217.2	218.4	222.6	237.6	8968.8	None	Mist	C.S.	21095	36848	5774.438	477563.1
1	21	1	2	Crude Oil 1	212.6	215.6	-2350.6	-4060.9	226.3	229.1	1	141.3	774.7	218.8	220.1	224.3	239.3	12532.8	None	Annular & Mist	C.S.	20988	36661	665.4189	724486.6
1	22	1	1	Crude Oil 1	215.6	219.5	-4053.8	-8191.2	229.1	232.8	1	141.3	774.7	223.6	225.2	230.7	245.7	12957.8	None	Turbulent	C.S.	27581	48178	0	0
1	23	1	1	Crude Oil 1	219.5	223.4	-8191.2	-12130.6	232.8	236.4	1	141.3	692.6	227.4	229	234.5	249.5	12985.4	None	Turbulent	C.S.	27437	47926	0	0
1	24	1	1	Crude Oil 1	223.4	227.2	-12130.6	-15618.8	236.4	240.1	1	141.3	618.2	231.3	232.9	238.3	253.3	13058.4	None	Turbulent	C.S.	27292	47673	0	0

Coil Configuration

HeaterSIM - Fired Heater Simulation Results

Online API Fired Heater Software

Upgrade Membership

Heater Section		RADIANT 1	RADIANT 2	CONVECTION 1	CONVECTION 1	CONVECTION 1
Coil Section		Coil Section 1	Coil Section 1	Coil Section 1	Coil Section 2	Coil Section 3
Process Name		Process 1: Crude Oil 1	Process 1: Crude Oil 1	Process 1: Crude Oil 1	Process 1: Crude Oil 1	Process 1: Crude Oil 1
Tube OD	mm	141.3	141.3	141.3	141.3	141.3
Tube Material		Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel
Tube Wall Thk	mm	Sch 40	Sch 40	Sch 40	Sch 40	Sch 40
Max Tube Temperature	°C	496.1	496.1	238.3	251	195.8
Tube Temperature Margin	°C	15	15	15	15	15
Design Tube Temperature	°C	511.1	511.1	253.3	266	210.8
Design Tube Pressure	kPa	2000.2	2000.2		2000.2	2000.2
Design Code		API 530	API 530		API 530	API 530
Tube Thk. Comment		Tube Thk. OK (API 530)	Tube Thk. OK (API 530)	Tube Thk. OK (API 530)	Tube Thk. OK (API 530)	Tube Thk. OK (API 530)
No. Tubes		80	80	36	24	36
No. Tubes Per Row				12	12	12
No. Passes		2	2	4	4	4
Effective Length	m	16	16	15	15	15
Straight Length	m	15.5	15.5	15.4	15.4	15.4
No. Rows				3	2	3
Tube Spacing	mm	254	254	254	254	254
Vert. Row Spacing (Vert)	mm	N/A	N/A	220.1	220.1	220.1
Coil Alignment				Staggered	Staggered	Staggered
Orientation		Vertical	Vertical	Horizontal	Horizontal	Horizontal
Tube Area	m²	568.2	568.2	239.59	1253.19	3091.42
Intermediate Supports		0 / 0	0 / 0	3 / 3	3 / 3	3 / 3
Corbel Width	m			1/2 Tube Space	1/2 Tube Space	1/2 Tube Space
Fin Type				None	Solid	Solid
Fin Material				None	Carbon Steel	Carbon Steel
Fin Height	mm				19.05	25.4
Fin Thickness	mm				1.27	1.27
Serrated Fin Wn
Fin Density	fins/m				157	197

Radiant section 1,Coil sect. no. 1, complies with API 530#Radiant section 2,Coil sect. no. 1, complies with API 530

Convection section 1,Coil sect. no. 1, complies with API 530

Convection section 1,Coil sect. no. 2, complies with API 530

Convection section 1,Coil sect. no. 3, complies with API 530

Notes
1. For vertical-tube, vertical-fired heaters, the maximum radiant straight tube length shall be 18,3 m (60 ft)
2. For horizontal heaters fired from both ends, the maximum radiant straight tube length shall be 12,2 m (40 ft)
3. API 560 - The tube-wall thickness should be in accordance with ISO 13704 (unless otherwise mutually agreed)
4. API 560 - Tube-wall thicknesses should include the minimum allowances for corrosion and/or erosion as follows:
- Carbon Steel Tubes - 3mm (0.125in)
- P Grade Tubes Tubes - 2mm (0.08in)
- Stainless Steel Tubes - 1mm (0.04in)
5. The unsupported length of horizontal tubes shall not exceed 35 times the outside diameter or 6 m (20 ft), whichever is less.

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API 530

Calculation of Heater-tube Thickness in Petroleum Refineries

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tblCalcType,calcref999	Calculation Ref Type		0
tblUnits,calcref999	Units selection		0
tblHeaterSection	Location		RADIANT	RADIANT	CONVECTION	CONVECTION	CONVECTION
tblCoilSectName	Coil/Piping Section		Coil Section 1	Coil Section 1	Coil Section 1	Coil Section 2	Coil Section 3
tblDesignPress,calcref0	Design Pressure	kPa g	2000.2	2000.2	2000.2	2000.2	2000.2
tblMaxOpPress,calcref0	Max Operating Pressure	kPa g	750.1	750.1	750.1	750.1	750.1
tblDesignTemp,calcref0	Design Temperature	°C	511.0971	511.0971	253.3483	266.0134	210.785
tblTubeMaterial	Tube Material		Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel	Carbon Steel
tblTubeOD	Tube Outside Diameter		141.3	141.3	141.3	141.3	141.3
tblTubeThk,calcref0,calcref2,calcref3	Tube Thickness	mm	6.55	6.55	6.55	6.55	6.55
tblCorrosionAllowance,calcref0	Corrosion Allowance	mm	3	3	3	3	3
tblDesignLifeHrs,calcref0	Design Life	hours	100000	100000	100000	100000	100000

ResultsMainTitle,resultref0	TUBE DESIGN RESULTS
UserSpecifiedThk,resultref0	Specified Tube Thickness	mm	6.55	6.55	6.55	6.55	6.55
ResultsElasticTitle,resultref0	ELASTIC DESIGN
AllowableElasticStress,resultref0	Elastic Allowable Stress	kPa	84244.3	84244.3	126439	124841.6	131807.3
ElasticStressThk,resultref0	Elastic Stress Thickness	mm	1.6578	1.6578	1.1089	1.123	1.0641
ElasticMinTubeThk,resultref0	Elastic Min. Tube Thickness	mm	4.66	4.66	4.11	4.12	4.06
ElasticAvgTubeThk,resultref0	Elastic Average Tube Thickness	mm	5.32	5.32	4.7	4.71	4.64
ElasticDesignCalcResultComment,resultref0	Elastic Design Comment		Thickness is OK	Thickness is OK	Thickness is OK	Thickness is OK	Thickness is OK
ResultsRuptureTitle,resultref0	RUPTURE DESIGN
RuptureStress,resultref0	Rupture Allowable Stress		31211.2	31211.2	0	0	0
RuptureNfactor,resultref0	Rupture n factor		4.520613	4.520613	0	0	0
RuptureStressThk,resultref0	Rupture Stress Thickness	mm	1.6778	1.6778	0	0	0
RuptureMinTubeThk,resultref0	Rupture Min. Tube Thickness	mm	4.68	4.68	0	0	0
RuptureAvgTubeThk,resultref0	Rupture Avg. Tube Thickness	mm	5.35	5.35	0	0	0
RuptureBfactor,resultref0	B factor		1.788087	1.788087	0	0	0
RuptureFcorrfactor,resultref0	Corrosion Factor Fcorr		1	1	0	0	0
RuptureDesignCalcResultComment,resultref0	Rupture Design Comment		Thickness is OK	Thickness is OK	Not applicable	Not applicable	Not applicable

btnRUN,calcref0,calcref1,calcref2,calcref3
btnRESET,resultref0,resultref1,resultref2,resultref3

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BPVC Section VIII Rules for Construction of Pressure Vessels

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Stack & Draft Summary

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Stack Height	m	16
Stack Diameter	m	3.15
Cone Diameter	m	3.052
Cone Height	m	0.5
Actual Exit Velocity	m/s	6.5
Design Exit Velocity	m/s	7.8
Flue Gas Temp.	°C	233
Flue Gas Flow	kg/s	29.74
Steel Area	m²	158.438
Stack Entry Pressure	mmH2O	-1.597
CO2	mol%	8.06
H2O	mol%	16.06
N2	mol%	72.67
O2	mol%	3.21
SO2	mol%	0

Draft at Stack Base	mmH2Og	-2.5
Draft at Arch	mmH2Og	-2.5
Draft at Floor	mmH2Og	0

Stack No. 1: Auto Stack calc. has converged OK

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		Hot-Face	Hot-Face	Hot-Face	Back-Up	Back-Up	Back-Up	Material
	Flue Temp.	Material	Thickness	Conductivity	Material	Thickness	Conductivity	Allowable Flux	Actual Flux	Design Temp.	Anchor Type	Casing Temp.	Comment
	°C		mm	W/mK		mm	W/mK	W/m²	W/m²	°C
RADIANT FLOOR 1	735.1	MW Castable	74.9	0.4	ULW Castable	150.1	0.14	732.5	503.9	1400	V Y Anchors	73.3	Refrac. thickness OK
RADIANT WALL 1	640.6	Fibre (High Density)	74.9	0.1	None	0	0	732.8	618.9	1260	Twistlock Pins	74.4	Refrac. thickness OK
RADIANT ARCH 1	785.1	Fibre (High Density)	87.6	0.1	None	0	0	824	800.8	1260	Twistlock Pins	80.6	Refrac. thickness OK

RADIANT FLOOR 2	735.1	MW Castable	74.9	0.4	ULW Castable	150.1	0.14	732.5	503.9	1400	V Y Anchors	73.3	Refrac. thickness OK
RADIANT WALL 2	640.6	Fibre (High Density)	74.9	0.1	None	0	0	732.8	618.9	1260	Twistlock Pins	74.4	Refrac. thickness OK
RADIANT ARCH 2	785.1	Fibre (High Density)	87.6	0.1	None	0	0	824	800.8	1260	Twistlock Pins	80.6	Refrac. thickness OK

CONVECTION SIDEWALL 1	508.8	LW Castable	74.9	0.3	ULW Castable	74.9	0.13	732.8	512.8	1100	V Y Anchors	68.1	Refrac. thickness OK

STACK 1	233	LW Castable	62.7	0.3	None	0	0	732.8	616.6	1100	V Y Anchors	74.4	Refrac. thickness OK

No thermal calc. carried out for Convection End Wall (Tubesheets) or Headerbox sections

Notes
1. Environmentally friendly body-soluble fibre is the recommended choice for fire insulation
2. HW and MW Castable is strong enough to be used on floor without a top brick layer
3. Ceramic fibre insulation are typically used in all areas except stack and ducting.
4. Ceramic fibre not suitable for convection sections with sootblowers or steam lances are used for cleaning.
5. Vapour barrier protective coating is required behind all areas lined with ceramic fibre
6. SS foil barrier is required for ceramic fibre lined areas if the sulphur content exceeds 500ppm by mass.

Process:	Crude Oil 1
Flow rate:	200 kg/s
Temperature:	100 °C
Pressure:	750.1 kPa a
Liquid Flow:	200 kg/s
Vapour Flow:	0 kg/s

Process:	Crude Oil 1
Flow rate:	200 kg/s
Temperature:	484.6 °C
Pressure:	-58043.8 kPa a
Liquid Flow:	0 kg/s
Vapour Flow:	200 kg/s

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