The document discusses the design of dimple jackets for vessels. Dimple jackets allow for construction from light gauge metals while maintaining strength for pressures. Their design begins with an assumed flow velocity between 2-5 ft/s. Dimple jackets are typically more economical than other choices when internal pressure is less than 1.67 times the jacket pressure. However, dimple jackets are not practical for vessels less than 10 gallons. The design of dimple jackets is governed by inspection standards and limited to a pressure of 300 psi and temperature of 700°F. Correlations and estimates are provided for heat transfer coefficients and pressure drop calculations for dimple jacket design.

1. Jacketed Vessel Design (design of dimple jackets)
Jacketed Vessel Design
(design of dimple jackets)
The design of dimple jackets permits construction from light gauge
metals without sacrificing
the strength required to withstand the specified pressure. This results
in considerable cost saving as compared to convention jackets. Design
calculation begin with an assumed flow velocity between 2 and 5 ft/s.
As a rule of thumb the jacket pressure will be governing when internal
pressure of vessel is less than 1.67 times the jacket pressure. At such
conditions, dimple jackets are typically more economical than other
choices. However in small vessels (less than 10 gallons) it is not
practical to apply dimple jackets.
The design of dimple jackets is governed by the National Board of
Boiler and Pressure Vessel Inspectors and can be stamped in
accordance with ASME Unfired Pressure Vessel Code. Dimple jackets
are limited to a pressure of 300 psi by Section VIII, Div.I of the ASME
Code. The design temperature is limited to 700 °F. At high
temperatures, it is mandatory that jacket be fabricated from a metal
having same thermal coefficient of expansion as that used in inner
vessel.
Heat Transfer Coefficients: Dimple Jackets

2. All other variables are as previously defined. Garvin (CEP Magazine,
April 2001) reports an average error of 9.8% with manufacturers data
for the above correlation and a maximum error of 30% over 116 data
points. This results in average deviations in the heat transfer
coefficient of 15-20% most of which was at velocities below 2 ft/s.
Good agreement with manufacturers data was found between 3 and 6
ft/s. A recommended excess area of 15% should be used in this
velocity range.
Note: The correlation above is for integrally welded jackets (ie.
jackets welded directly to the vessel). If a dimple jacket is clamped
onto an existing vessel and adhered with heat transfer mastic, the
overall heat transfer coefficient of the system will be very low. Mastic
is used to try to minimize air pocket resistances between the vessel
wall and the jacket. Historically, this arrangement results in poor heat
transfer. A recommended overall heat transfer coefficient of 10-15
Btu/h ft² °F should be used for such systems regardless of the utility
used.
Pressure Drop: Dimple Jackets
The pressure loss in a dimple jacket can be estimated from the
following for water or water-like fluids:
Pressure Loss in Jacket = (Total Lenght of Flow, ft) x ((0.40 x
Velocity, ft/s) - 0.35)
Pressure Loss Across Entire Jacket (including inlets and outlets) =
Pressure Loss in Jacket + (0.10)(Pressure Loss in Jacket)
The above estimates should be used for velocities ranging from 1.5 to
6 ft/s.
This method is based on a graph found on page 217 of the
Encyclopedia of Pharmaceutical Technology by James Swarbrick.
For detailed design, it is advisable to rely on manufacturer's data for

3. pressure drop calculations.
Heat Transfer Coefficients Inside Agitated Process Vessels
In order to complete the overall heat transfer coefficient calculation,
an estimate must also be made inside the process vessel. The
following estimate should yield reasonable results:
Calculating the Overall Heat Transfer Coefficient
When calculating the overall heat transfer coefficient for a system, the
vessel wall resistance and any jacket fouling must be taken into
account:
Notice that the thermal conducitivity of the vessel wall and the wall
thickness are included in the calculation. A typical jacket fouling factor
is around 0.001 h ft² °F/Btu. When calculating the overall heat
transfer coefficient, use a "common sense" analysis of the final value.
The table below will give some guidance to reasonable final values:
English Units

4. Metric Units

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Jacketed-Vessel-Design-(design-of-dimple-jackets)#ixzz1feaQaMgu