Pressure Vessles PPT 25.02.2020
Pressure Vessles PPT 25.02.2020
Pressure Vessles PPT 25.02.2020
Presentation on
PRESSURE VESSEL
By
Mrs. Sonali Mahajan
Thermax Ltd, Pune
CONTENTS
VESSEL REACTOR
COLUMN
REACTORS
SEPARATORS
RECEIVERS
DRUMS
HEAT EXCHANGERS
VI Recommended Rules for the Care and • Division 3 — Containment Systems for Transportation
Operation of Heating Boilers and Storage of Spent Nuclear Fuel and High-Level
X Fiber-Reinforced Plastic Pressure Vessels XII Rules for Construction and Continued Service of
Transport Tanks
PD-5500
FACTOR OF SAFETY
1) For Ferrous & Non-Ferrous alloys:
• 1.5 based on Sy Sy - Yield Stress
• 3.5 based on ST ST - Ultimate Tensile Stress
2) For Bolting materials (Ferrous & Non-Ferrous):
• 1.5 based on Sy
• 4.0 based on ST
3) For Bolting Materials (Ferrous & Non-ferrous Enhanced by HT/ Strain Hardening)
• 4.0 based on Sy
• 5.0 based on ST
LIMITATIONS
1) Minimum Internal Pressure (U-1(c)2) >= 15 psi (100 Kpa)
2) Maximum Internal Pressure (U-1(d)) <= 3000 psi (20 Mpa)
3) Minimum Inside Dim. (dia./width/length/diagonal) (U-1(c)2) >= 6 in (152 mm)
4) Cyclic loading not covered.
FACTOR OF SAFETY
1) For Ferrous & Non-ferrous Alloys:
1.5 based on Sy
2.4 based on ST
2) For Bolting Materials (Ferrous & Non-ferrous):
1.5 based on Sy
4.0 based on ST
3) For Bolting Materials (Ferrous & Non-ferrous Enhanced by HT/ Strain Hardening)
4.0 based on Sy
5.0 based on ST
3.0 based on ST ( For Table 4 i.e. Design as per part 5)
LIMITATIONS
1) Minimum Int./Ext. Op. Pressure (1.2.4.2 h) >= 15 psi (103 Kpa)
2) Maximum Pressure NO FIXED LIMITS
3) Minimum Inside Dim. (dia./width/length/diagonal) (1.2.4.2 i) >= 6 in (150 mm)
LIMITATIONS
WRC 297
FEA
PD-5500 (Annexure-G)
1) WIND LOADS
ASCE 7, 2018
2) SEISMIC LOADS
ASCE 7, 2018
but does not include a pressure vessel with less than 1.0 Kg/Cm2 design gauge pressure or in which water is
heated below 1000C.
Steam-pipe means any pipe through which steam passes from a boiler if the pressure exceeds 3.5 Kg/cm2above
atmospheric pressure; or if such pipe exceeds 254 mm in internal diameter and includes any connected fitting.
Feed-pipe means any pipe under pressure through which feed-water passes directly to a boiler. Every reference to
a steam-pipe shall be deemed to include also a feed-pipe.
◦ CCOE (Chief Controller of Explosive - Head of Petroleum & Explosive Safety organization ) : Rules related to
manufacture, import, export, transport, possession, sale & use of explosives, petroleum products & compressed
gas.
Piping Loads
Temperature
Platform & Other Loads
Corrosion Allowance
Material of Construction
Allowable stress
Loadings
Wind
Seismic
1.Cylindrical Shells
2. Spherical Shells
3. Heads
Ellipsoidal
Torispherical
Hemispherical
4. Transition Sections
Cones
Toricones
Scope
Sub section A
Sub section B
Sub section C
Mandatory Appendices
Non-Mandatory Appendices
In relation to the geometry of pressure containing parts, the scope of this Division shall include the
following:
U-1(e)(1)
Where external piping; other pressure vessels including heat exchangers; or mechanical devices such as
pumps, mixers, compressors, are to be connected to the vessel:
(a) the welding end connection for the first circumferential joint for welded connections
(c) the face of the first flange for bolted, flanged connections
U-1(e)(3) Pressure retaining covers for vessel openings such as manhole or handhole covers and bolted
covers with their attaching bolts and nuts
Based on the Committee’s consideration, the following transport of fluids from one location to another within a
classes of vessels are not included in the scope system of which it is an integral part, that is, piping
(-a) those within the scope of other Sections; (-e) piping components, such as pipe, flanges, bolting,
(-b) fired process tubular heaters; gaskets, valves, expansion joints, and fittings, and the
(-c) pressure containers which are integral parts pressure-containing parts of other components, such as
or components of rotating or reciprocating mechanical strainers and devices which serve such purposes as
mixing,
devices, such as pumps, compressors, turbines, generators,
separating, snubbing, distributing, and metering or
engines, and hydraulic or pneumatic cylinders where
controlling flow, provided that pressure-containing parts
the primary design considerations and/or stresses are
derived of such components are generally recognized as piping
(1) Unfired steam boilers shall be constructed in accordance with the rules of Section I.
(2) The following pressure vessels in which steam is generated shall not be considered as unfired steam boilers
,and shall be constructed in accordance with the rules of this Division:
exchangers;
of heat resulting from operation of a processing system containing a number of pressure vessels such as used in
the manufacture of chemical and petroleum products;
(-c) vessels in which steam is generated but not withdrawn for external use.
U-2 (g)
This Division of Section VIII does not contain rules to cover all details
of construction. Where complete details of construction are not given,
the Manufacturer, subject to the acceptance of the Authorized Inspector,
shall provide the appropriate details to be used.
PR PRo
t c t c
SE 0.6P SE 0.4P
P = Internal Pressure
R = Inside radius (corroded)
Ro = Outside radius
c = Corrosion Allowance
The above equation can be rewritten to calculate the maximum pressure when the thickness is known.
SE (t c) SE(t c)
P P
R 0.6(t c) Ro 0.4(t c)
Longitudinal Direction -
PR
t c When t < 0.5R or P < 1.25SE
2SE 0.4P
2SE(t c)
P
R 0.4(t c)
Note: Minimum required thickness = 1.5 mm + Corrosion Allowance (Ref. UG-16 b)
4B
P
3 Do t
2 AE
P
3 Do t
Is = [Do2 Ls (t + As/Ls) A] / 14
or
Where,
Is = Reqd. Moment Of Inertia of the Cross Section of the Ring about its Neutral Axis, in.4
Is’ = Reqd. Moment Of Inertia of the Cross Section of the Ring and Effective Shell about their
combined Neutral Axis, in4.
Ls = Half the distance from central line of the Stiffening Ring to the next Line of
Support on one side plus Half the distance from the central line of the Ring to
the next line of Support on the other Side.
A line of Support is
- A Stiffening Ring
- Jacket Bar
-Circumferential Line on a head at one third the depth of the Head
-Cone-to-Cylinder Junction
As = Area of the Stiffening Ring, in.2.
t = Minimum Required Thickness of the Shell, in.
ts = Nominal Thickness of the Shell, in.
Openings in cylindrical shells and formed heads are usually circular, elliptical or obround.
However, any other shape is also permitted, but there may be no method of analysis given in the Code.
Properly reinforced openings in cylindrical & conical shells are not limited to size except with the following
provisions for design.
Limitations: For openings in a cylindrical shell, the rules given in UG-36 through UG-43 are limited to the
following sizes:
For vessels 60 in. (1 520 mm) inside diameter and less, onehalf the vessel diameter, but not to exceed 20 in.
(510 mm).
For vessels over 60 in. (1 520 mm) inside diameter, one‐third the vessel diameter, but not to exceed 40 in. (1
020 mm).
5 March 2020 THERMAX LTD Slide 37
UG-36 Opening in Shell & heads
Finish opening diameter < 89 mm (3 ½ in.) [ in vessel shells or heads with required
minimum thickness < 10 mm ( 3/8 in.) ]
Finish opening diameter < 60 mm (2 3/8 in.) [ in vessel shells or heads with required
minimum thickness > 10 mm ( 3/8 in.) ]
Threaded, studded or expanded connections with opening diameter < 60 mm (2 3/8 in.)
Strength of reinforcement
NOMENCLATURE:
Nozzle Neck Thickness (UG-45)
tn - Min. wall thickness of nozzle neck
ta - Min. required neck thickness for internal
pressure (UG-27) & external pressure (UG-28)
tb1 - For vessel under internal pressure, min.
required thickness of vessel for internal
pressure (assuming joint efficiency = 1)
tb2 - For vessel under external pressure, min.
required thickness of vessel using the external
pressure as an equivalent internal design
pressure (assuming joint efficiency = 1)
tb3 - Minimum required thickness of nozzle neck (as
per table UG-45)
tug-45 - Minimum required wall thickness of nozzle
neck.
1) SUPPORTS 2) ATTATCHMENT
Supports –
PD 5500 gives good guidance for many calculations not given in ASME code,
including support calculations. Else use any design handbook. Saddle supports are
normally calculated by the Zick method. However, this method does not consider any
external load (e.g., wind, earthquake). Also, it is limited to 2 saddles
Note – worst condition for saddle supports may be a condition when vessel is full of
water with no pressure
As far as ASME code is concerned, the support itself is out of the code purview (but it
needs to be designed anyway)
Our interest is limited to stress in shell at the location of support
Allowable stresses must always be taken as per Div. 1
1) Carbon Steels
UG-5 Plates
UG-6 Forgings UG-7 Castings
UG-9 Welding
UG-8 Pipes & Tubes Materials UG-14 Rods & Bars.
5 March 2020 THERMAX LTD Slide 52
MATERIALS (UG-4 to UG-15)
ORDERING MATERIALS CORRECTLY
ASTM Materials
See Guideline on Acceptable ASTM Editions
NO.
NO.
NO.
NO.
NO.
(2507)
Maximum carbon content = 0.08% (for material UNS no. S30400, S31600, S32100 & S34700)
Maximum carbon content = 0.030% (for material UNS no. S30403 & S31603)
5 March 2020 THERMAX LTD Slide 58
MATERIALS (UG-4 to UG-15)
NO.
Ti-0.3Mo-0.8Ni (SB-265)
5 March 2020 THERMAX LTD Slide 59
MATERIALS (UG-4 to UG-15)
NO.
0.02 P
– 0.02 P
Lethal (UW-2(a))
Joint category
RT (UW-11)
RT1/RT2/RT3/RT4 (UG-116(e))
Efficiency (Table UW-12)
Part UW
UT (UW-53)
PT/MT (UG-103)
(1) Cold-formed and bent P-No. 1 pipe and tube material having a nominal thickness not greater than 3/4 in. (19
mm) does not require post-forming heat treatment.
(2) For P-No. 1, Group Nos. 1 and 2 materials other than those addressed by (1), post-forming heat treatment is
required when the extreme fiber elongation exceeds 40% or if the extreme fiber elongation exceeds 5% and any
of the following conditions exist:
(-a) The vessel will contain lethal liquid or gaseous substances (see UW-2).
(-b) The material is not exempt from impact testing by the rules of this Division, or impact testing is required
by the material specification.
(-c) The nominal thickness of the part before cold forming exceeds 5/8 in. (16 mm).
(-d) The reduction by cold forming from the nominal thickness is more than 10% at any location where the
extreme fiber elongation exceeds 5%.
(-e) The temperature of the material during forming is in the range of 250°F to 900°F (120°C to 480°C).
(3) Cold-formed or bent P‐Nos. 3 through 5C pipe and tube materials having an outside diameter not greater
than 41/2 in. (114 mm) and a nominal thickness not greater than 1/2 in. (13 mm) do not require a post-forming
heat treatment. The extreme fiber elongation shall be determined by the equations in Table UG-79-1.
UCS-66-
Unless exempted by the rules of UG-20(f) or other rules of this Division, Fig. UCS-66 shall be used to
establish impact testing exemptions for steels listed in Part UCS.
When Fig. UCS-66 is used, impact testing is required for a combination of minimum design metal
temperature and thickness which is below the curve assigned to the subject material.
If a minimum design metal temperature and thickness combination is on or above the curve, impact
testing is not required by the rules of this Division.
Components such as shells, heads, nozzles, manways, reinforcing pads, flanges, tube sheets, flat cover
plates, backing strips which remain in place and attachments which are essential to the structural
integrity of the vessel when welded to pressure retaining components, shall be treated as separate
components.
Each component shall be evaluated for impact test requirements based on its individual material
classification, thickness and minimum design metal temperature
Low temperature operation UCS-66
Governing Thickness
Conditions of service
Materials
Fabrication
Heat Treatment
(a) Before applying the detailed requirements and exemptions in these paragraphs, satisfactory
weld procedure qualifications of the procedures to be used shall be performed in accordance with
all the essential variables of Section IX including conditions of postweld heat treatment or lack of
postweld heat treatment and including other restrictions listed below. Welds in pressure vessels or
pressure vessel parts shall be given a postweld heat treatment at a temperature not less than
specified in Tables UHA-32-1 through UHA-32-7 when the nominal thickness, as defined in UW-
40(f), including corrosion allowance, exceeds the limits in the Notes to Tables UHA-32-1 through
UHA-32-7. The exemptions provided for in the Notes to Tables UHA-32-1 through UHA-32-7 are
not permitted when welding ferritic materials greater than 1/8 in. (3 mm) thick with the electron
beam welding process, or when welding P‐Nos. 6 and 7 (except for Type 405 and Type 410S)
materials of any thickness using the inertia and continuous drive friction welding processes. The
materials in Tables UHA-32-1 through UHA-32-are listed in accordance with the Section IX
P‐Number material groupings of Section IX, Table QW-432 and are also listed in Table UHA-23.
(c) Required Impact Testing When Thermal Treatments Are Performed. Impact tests are required at
the test temperature in accordance with (a) but not warmer than 70°F (20°C) whenever thermal
treatments79 within the temperature ranges listed for the following materials are applied:
(1) austenitic stainless steels thermally treated at temperatures between 900°F (480°C) and 1650°F
(900°C); however, Types 304, 304L, 316, and 316L that are thermally treated at temperatures
between 900°F (480°C) and 1,300°F (705°C) are exempt from impact testing provided the MDMT is
−20°F (−29°C) or warmer and vessel (production) impact tests of the thermally treated weld metal
are performed for Category A and B joints;
(2) austenitic‐ferritic duplex stainless steels thermally treated at temperatures between 600°F (315°C)
(3) ferritic chromium stainless steels thermally treated at temperatures between 800°F (425°C) and
1,350°F (730°C);
(4) martensitic chromium stainless steels thermally treated at temperatures between 800°F (425°C)
and 1,350°F (730°C).
Applicable for round & rectangular attachment (on Cylindrical & Spherical Shells)
Analysis is valid for orthogonal nozzles only. (Nozzle axis perpendicular to vessel axis)
Provides vessel stress summation (at pad edge & vessel to nozzle junction) & Nozzle stress
summation at vessel – nozzle junction, flexibility check