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vTHERMODYNE
Prepared By-Archana Prajapati
vTHERMODYNE
vTHERMODYNEWe Are Covering Today
Preparation of
Detail Drawing
Save Max
Boiler
Design
Design
Procedure
Development
of Tube Plate
Customer
Input
vTHERMODYNE
About Save Max Boiler Design
 Save Max Boiler: Boiler uses oil & gas as fuel in
arrangement to generate steam.
 This model is efficient , cause there is less fuel losses.
 The efficiency is 88% as we convert the maximum
percentage of fuel into heat.
vTHERMODYNE
Customer Inputs
v Capacity
v Pressure
v Type of Fuels(Oil & Gas)
Through Capacity , we decide how much Heat Surface Area we need
to give in design.
Heat Surface Area=HAS(Furnace +2nd pass tubes +3rd+pass tubes
+ Front Tube Plate +Rear Tube Plate
+Wrapper Drum+ Wrapper Drum Front
Tube Plate +Wrapper Drum Rear Tube Plate
+Access Ring)
1 TPH=27 TO 30 m^2 (For Light Density Oil)
vTHERMODYNE
Design Procedure
Determine the Heat Surface Area
Prepare the tube plate
Shell Dia Size Defined as per HSA
Shell Length defined by length of Tube available as per HSA
Calculate Mandatory IBR boiler Calculation
Mechanical Design-Place the Studs & Gussets
Place all Nozzles ,Circumferential Seam , Longitudinal Seam
Material Selection
vTHERMODYNE
Design Parameters
 Material Selection
vTHERMODYNE
Design Parameters
 Mandatory Calculation:
1. Pitch of Tubes as per IBR Regulation -580
Required Minimum Ligament : (D/8)+12.7 mm
D:Diameter of Tubes Holes
2. Thickness of Tubes, t=(PXDX1.6f)+C
D:OD of Tube in mm.
P:Working Pressure in Kg/cm^2
f:Allowable Stress,(Et/1.5)
E:Ultimate Tensile Strength
t:Working Metal Temperature
c:Corrosion Allowance(0.75mm)
vTHERMODYNE
Design Parameters
3.Plain Furnace & Wrapper Drum as per IBR Regulation-592(a)
We calculate the thickness of plate by two formulas:
v e=B/2[1+Sq.rt(1+0.12 dxu/B(1+d/0.3xL)}
Where , B=(PxdxS1)/{2XEXt(1+d/15xL)}
e:thickness of plate
P:Working Pressure
d:Mean Dia
E:Ultimate Tensile Strength(UTS)
S1:2.50(Factor of safety :For furnace in class 1 & class 2)
C=0.75mm(Corrosion Allowance)
u(Out of roundness):1.50(For Plain Furnace)
t:Working Metal Temperature
e=d^0.6(LxS2xP/1.73xE)^0.4+C
Where, e:thickness of plate
P:Working Pressure
d:Mean Dia
L:Distance between stiffners
C:0.75mm(Corrosion Allowance)
E:Young Modulus of elasticity.
We consider greater thickness in above two. Then compare the thickness with
standard size that available in market.
vTHERMODYNE
Design Parameters
4.Stayed Surface as per IBR Regulation-574
e=cxdxsq.rt(P/f1+e1)
We check the dia of free surface ,by putting the value of d in above
equation.
e:Thickness of end plates
c:0.40(Weld Factor Coefficient for stays bar )
d:Largest Circle dia
P:Working Pressure
f1:0.85xallowable stress
e1:( Additional Thickness : 0.75mm)
We use to give stayed surface in design in two places:
v Between Gusset , Shell ID & tube
v Between Shell ID , Furnace & Stay Tubes.
vTHERMODYNE
Design Parameters
 Stayed Surface in shell
vTHERMODYNE
Design Parameters
4.Shell Thickness as per IBR Regulation -270
W.P : {2XfxE(T-0.03)/D+(T-0.03)}
Where,
E: For Class 1 Boilers ,the weld factor shall be taken as 1.
W.P: Working Pressure
f:Permissible Working Stress
D:Inner Diameter of shell
Permissible Working Stress, f=(Et)/1.5
E:Ultimate Yield Strength
t:Working Metal Temperature
T:Thickness of shell plates.
vTHERMODYNE
Tube Plate Development
 Factors need to be consider Tube plate Development
a) Tubes OD
b) Pitch or Ligament
c) Heat Surface Area
d) Gusset Placement
vTHERMODYNE
Preparing Detail Drawing
 Now we are ready for preparing the detail drawing.
 The drawing is the way of communication from design to
production
vTHERMODYNE
Thank You

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Concept of save max boiler design (1)

  • 2. vTHERMODYNEWe Are Covering Today Preparation of Detail Drawing Save Max Boiler Design Design Procedure Development of Tube Plate Customer Input
  • 3. vTHERMODYNE About Save Max Boiler Design  Save Max Boiler: Boiler uses oil & gas as fuel in arrangement to generate steam.  This model is efficient , cause there is less fuel losses.  The efficiency is 88% as we convert the maximum percentage of fuel into heat.
  • 4. vTHERMODYNE Customer Inputs v Capacity v Pressure v Type of Fuels(Oil & Gas) Through Capacity , we decide how much Heat Surface Area we need to give in design. Heat Surface Area=HAS(Furnace +2nd pass tubes +3rd+pass tubes + Front Tube Plate +Rear Tube Plate +Wrapper Drum+ Wrapper Drum Front Tube Plate +Wrapper Drum Rear Tube Plate +Access Ring) 1 TPH=27 TO 30 m^2 (For Light Density Oil)
  • 5. vTHERMODYNE Design Procedure Determine the Heat Surface Area Prepare the tube plate Shell Dia Size Defined as per HSA Shell Length defined by length of Tube available as per HSA Calculate Mandatory IBR boiler Calculation Mechanical Design-Place the Studs & Gussets Place all Nozzles ,Circumferential Seam , Longitudinal Seam Material Selection
  • 7. vTHERMODYNE Design Parameters  Mandatory Calculation: 1. Pitch of Tubes as per IBR Regulation -580 Required Minimum Ligament : (D/8)+12.7 mm D:Diameter of Tubes Holes 2. Thickness of Tubes, t=(PXDX1.6f)+C D:OD of Tube in mm. P:Working Pressure in Kg/cm^2 f:Allowable Stress,(Et/1.5) E:Ultimate Tensile Strength t:Working Metal Temperature c:Corrosion Allowance(0.75mm)
  • 8. vTHERMODYNE Design Parameters 3.Plain Furnace & Wrapper Drum as per IBR Regulation-592(a) We calculate the thickness of plate by two formulas: v e=B/2[1+Sq.rt(1+0.12 dxu/B(1+d/0.3xL)} Where , B=(PxdxS1)/{2XEXt(1+d/15xL)} e:thickness of plate P:Working Pressure d:Mean Dia E:Ultimate Tensile Strength(UTS) S1:2.50(Factor of safety :For furnace in class 1 & class 2) C=0.75mm(Corrosion Allowance) u(Out of roundness):1.50(For Plain Furnace) t:Working Metal Temperature e=d^0.6(LxS2xP/1.73xE)^0.4+C Where, e:thickness of plate P:Working Pressure d:Mean Dia L:Distance between stiffners C:0.75mm(Corrosion Allowance) E:Young Modulus of elasticity. We consider greater thickness in above two. Then compare the thickness with standard size that available in market.
  • 9. vTHERMODYNE Design Parameters 4.Stayed Surface as per IBR Regulation-574 e=cxdxsq.rt(P/f1+e1) We check the dia of free surface ,by putting the value of d in above equation. e:Thickness of end plates c:0.40(Weld Factor Coefficient for stays bar ) d:Largest Circle dia P:Working Pressure f1:0.85xallowable stress e1:( Additional Thickness : 0.75mm) We use to give stayed surface in design in two places: v Between Gusset , Shell ID & tube v Between Shell ID , Furnace & Stay Tubes.
  • 11. vTHERMODYNE Design Parameters 4.Shell Thickness as per IBR Regulation -270 W.P : {2XfxE(T-0.03)/D+(T-0.03)} Where, E: For Class 1 Boilers ,the weld factor shall be taken as 1. W.P: Working Pressure f:Permissible Working Stress D:Inner Diameter of shell Permissible Working Stress, f=(Et)/1.5 E:Ultimate Yield Strength t:Working Metal Temperature T:Thickness of shell plates.
  • 12. vTHERMODYNE Tube Plate Development  Factors need to be consider Tube plate Development a) Tubes OD b) Pitch or Ligament c) Heat Surface Area d) Gusset Placement
  • 13. vTHERMODYNE Preparing Detail Drawing  Now we are ready for preparing the detail drawing.  The drawing is the way of communication from design to production