Eliminating Cool Hp Bloch

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    H P In ReliabilityHeinz P. Bloch, Reliability/Equipment Editor

    Eliminating cooling water from pumps

    HYDROCARBON PROCESSING / AUGUST 1996 17

    Extensive experimentation with removing

    cooling water from pumps and general-purpose

    turbine drivers in large petrochemical plants

    indicates that machinery reliabil-

    ity may increase. The obvious sav-

    ings in capital expenditures for

    piping and water-treatment facili-

    ties, and savings in operating cost

    alone, provide good incentives to

    take a closer look at this topic.

    Discontinue pedestal cooling. It has been shown

    conclusively over many years that pedestal cool-

    ing is not required for any centrifugal pump gen-

    erally found in pertochemical plants. Pumping

    services with fluid temperatures as high as 740F

    (393C) require nothing more than hot alignment

    verification between driver and pump. Risk of

    pump fires due to cooling water-induced corro-

    sion, and subsequent pedestal collapse has been

    eliminated by numerous companies that accepted

    this experience-based recommendation decades

    ago.

    Mechanical seal cooling alternatives. Pump

    stuffing-box jacket cooling, while reducing heat

    migration from the pump casing toward the bear-

    ing housing, will not lower the temperature in

    the seal environment. A changeover to high-tem-

    perature mechanical seals may be possible and is

    preferred by U.S. plants. If mechanical seals need

    cooling because the flush liquid has a low boiling

    point, the least troublesome way to control seal

    temperatures may be to circulate a coolant such

    a water, steam, or cool flushing oil through an

    external seal flush cooler. However, many hotservices may be ideally suited for a maintenance-

    free dead-ended flush arrangement. This option

    may become entirely feasible if narrow-face seals

    or suitable seal housing internal geometries are

    selected.

    Bearing cooling not usually needed. Cooling

    water can be deleted from many sleeve bearings

    on centrifugal pumps and on small turbine drivers

    after experimentally verifying that oil sump tem-

    peratures do not exceed 180F (82C). This limit

    was found to be extremely conservative from a

    bearing-life point of view. If it is exceeded by a

    few degrees, more frequent oil sampling or syn-

    thetic lubricants will help.

    Since most general-purpose machinery is

    equipped with antifriction bearings, significant

    gnitanimilemorftlusernacstidercecnanetniam

    cooling water from antifriction bearings on pumps

    and small steam turbines. Experience shows

    that equipment life can actually be extended by

    removing cooling water from bearings. Cooling

    bearing oil sumps invites moisture condensation,

    and bearings will fail much more readily if the oil

    is contaminated by water. Laboratory tests show

    that even trace amounts of water in the lube oil

    are highly detrimental.

    Hydrogen embrittlement on the steel granular

    structure can reduce expected bearing life to less

    than one-fifth normal or rated values. Another

    reason for not cooling the bearing housing of

    pumps and drivers is to maintain proper bear-

    ing internal clearances. Hot-service pump bear-

    ings have often failed immediately after startup

    when the bearing housings were cooled by water.When it was recognized that high temperature

    gradients were responsible for reducing bearing

    clearances to unacceptably low values, a heating

    medium was introduced into the bearing bracket

    to heat the housing. The problem was solved.

    Parameters influencing bearing cooling. Mini-

    mum permissible viscosity of ball-bearing lube

    oils at the bearing operating temperature is a

    function of bearing size and speed. As a rule of

    thumb and valid for most bearings operating in

    typical centrifugal pumps, rated bearing life will

    be obtained if metal temperatures of operatingbearings remain low enough to ensure minimum

    viscosities of 150 SUS (32.1cSt) for spherical

    roller bearings in thrust-loaded services, 100

    SUS (20.6 cSt) for radially loaded spherical roller

    bearings, and 70 SUS (13.1 cSt) for ball and

    cylindrical roller bearings. If the viscosities drop

    below the given values, the oil film may have

    insufficient adhesion or strength, and metal-to-

    metal contact could result.

    It is safe to assume that standard antifriction

    bearings will show no loss of life as long as

    metal temperatures do not exceed 250F (121C).

    eliminatingcoolhpbloch.pdf August '02 Rev. 0

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    H P In Reliability. . .

    Maintaining oil temperatures within given limits is thus

    aimed at satisfying only two requirements:

    1. Oil viscosities must remain sufciently high to ade-

    quately coat the rolling elements under the most adverse

    operating temperature.

    2. Oil additives, such as oxidation inhibitors, must not

    be boiled off, i.e., adequate service life of the lubricant

    must be maintained.

    A properly formulated diester or PAO-based synthetic

    lubricant would be ideally suited in this case.

    BIBLIOGRAPHY

    Excerpted from the authors text Improving Machinery Reliability, Second Edi-

    tion, Gulf Publishing Company, Houston, Texas, 1988.

    The author is a consulting engineer in Montgomery, Texas.

    He advises modern process plants worldwide on reliability

    improvement and maintenance cost reduction opportuni-

    ties.