...the need to re-tube exchangers that have localized corrosion or damage. The cost savings
are  significant  as the exchanger does not have to be disassembled or shipped  to complete
the sleeving operation. Sleeves can be removed at a later date and new sleeves installed.
...service life,  some  sleeve  materials  can be easily inspected
under to allow for continued  inspection and  document  corro-
sion rates.   Sleeving can add additional  benefits such as, add
structural integrity to rolls and tubesheet joints, reduce “Cold”
zones where  increased corrosion can occur and tighten loose
packed tube joints.
...a common problem found in process exchangers due to entrained abrasive solids or turb-
ulent  flow conditions  (non-laminar conditions).  Header box and channel  designs can also
add to the turbulence that is  primary cause of erosion/corrosion to the tube ends.  Metallic
inserts  can shield and protect the tube ends from wear caused by these factors.  Selection
of proper sleeve material,  wall  thickness and length is required to provide complete cover-
age of corrosion zone.
...metallic  sleeving  inserts is a cost effective and quick repair  method that will return your
equipment  to reliable service.  Sleeve can be scheduled  during routine  maintenance sche-
dules to avoid last minute retubes or impacting plant operation.
View of Finfan being sleeved
due to severe inlet thinning
– Sleeve length 2’
...a protective sleeve into pre-existent equipment
is an accepted process to protect tubing from ac-
tive  corrosion and/or erosion mechanisms.  Thin
walled metal  inserts  can be hydraulically  expan-
ded into existing tubes to add additional years of
service to a process exchanger.
Heat Exchanger Tube Sleeving
FINFAN
Correct  design  information  is required to insure a high strength sleeve
to tube  joint by the use of  hydro-expansion  techniques.   The frictional
interference  fit  between  the  installed  sleeve  and the parent tube pro-
duced by hydro-expansion is governed by many variables.  These varia-
bles are listed below.

It should be noted that  specific tube  heats may vary the expansion to a
great degree. Calculated and actual expansion pressures might be diffe-
rent and the calculated pressure is meant as a guide line for installation.
Determination of the actual field installing pressure are to be determined
by calculated and field tuned pressures that yield the proper fit.

Sleeve  expansion  develops  interference  fit pressure that expands the
sleeve for its entire length within the parent tube. The appropriate calcu-
lation’s for specific material yields, material compatibility, and sleeve in-
stallation  pressure  are  reviewed  prior to sleeve  installation  to  insure
proper fit.    Expansions  of the sleeve  test  coupons are  shown to have
wall reductions of between 2% and 5%. These wall reductions are appro-
ximately 1/3rd to 1/2 of the wall reductions found in hard rolled tubes.
Load pressure – 2000 PSIG
Yield Pressure – Calculated and field tuned
(8000 PSIG - .750 X .030 wall – 316l Stainless Steel)
Interference fit pressure -  Yield pressure + 1000 PSIG
Tube O.D. – (Eg - . . 1” O.D. )
Tube I.D. -  (Eg. - .782 I.D.)
Tube wall Thickness – (Eg. - .109)
Tube Material – (Eg. – SA-178)
Sleeve O.D. – (Eg. - .593 “ O.D.)
Sleeve I.D. – (Eg. - .495” I.D.)
Sleeve wall thickness – (eg. - .049”)
Sleeve Material – 316 L Stainless steel)
View of process gas cooler
in sleeving process
– Sleeve length 3’
Thorough review of corrosion mechanism, location and extent allow for
the sleeving of tubular process equipment to be fully effective. The cor-
rect sleeve metallurgy being selected, the sleeve being positioned with-
in the corrosion area,  and  the correct  sleeve  length to cover the corro-
sion area must all be considered when planning a sleeve operation.
Conditional  analysis of heat  transfer  tubing is a major  concern  due  to
budgeted funding, repair,  retube, and or modification of your heat trans-
fer equipment to return it to 100 percent capacity. For this reason a com-
prehensive  Eddy Current inspection should be performed to allow your
plant personnel to make wise decision's concerning tubular equipment.
The installation of...
Inlet erosion is...
Tube sleeving by...
Sleeving reduces...
To extend the...
PROCEDURE FOR HYDRO-EXPANSION
SLEEVE INSTALLATION
NOMENCLATURE
Magnetec
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EXCHANGER TUBE
SLEEVING / FERRULES
Full length sleeve expansion
921 tubes completed in 27 hours
Tubes  should  be clean  from all debris and the tube ends free of  dings,
weld  spatter, ect.   The parent  tube is prepared  for sleeve installation –
measurements are  re-confirmed as correct on the parent  tube I.D.  sur-
face and sleeve.   A sleeve is  installed onto the  sleeving tube – Expan-
sion pressure is brought to 2000 PSIG to lock sleeve on installation tool-
ing.   The sleeve is installed into the  parent  tube section and set to the
predetermined position (Flush or protruded). The sleeve is raised to it’s
expansion/yield pressure where the stress pressure begins to yield the
tube and reacts in a fully elastic condition.   The sleeve is brought to it’s
interference  pressure (IP).   The sleeve is held  as it’s IP for a predeter-
mined time (Dwell Time)during which there is elastic material recovery
(Spring back). The pressures are released and installation tool removed.
The  flared  sleeve  end is rolled into  the  parent  tube  (Soft Roll).    The
straight sleeve end is expanded to the tube parent tube.
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