RE: Pump selection [bcc][faked-from][mx][spf]

From: <Bruce>
Date: Fri Dec 03 2004 - 10:53:00 EST


I have used double-seal pumps with an external reservoir and seal-less (magnetic drive) centrifugals (such as by Crane)for similar service, with great success. The mag drive pumps are more cost to purchase to to operate, but maintenance is about nil.

                            ... Bruce D. Bullough ...
                            Sebesta Blomberg & Associates, Inc.
                            2381 Rosegate
                            Roseville, MN  55113       USA
                            + 651-634-7344
                            www.sebesta.com


-----Original Message-----
From: Jacques Chaurette [mailto:jchaurette@fluidedesign.com] Sent: Thursday, December 02, 2004 4:51 PM To: <a href="/group/PipingDesign/post?postID=NBzpFtJNPrUh4axAykul4y0jwlJ6A1LVe7jmQc0J4ersVG9zK4We03VSb3x71TCiB0ojQeVti7n8n6GXT7kRnvjwqYg">PipingDesign@yahoogroups.com</a> Subject: Re: [PipingDesign] Pump selection [bcc][faked-from][mx][spf]

Now that we have the vapor pressure sorted out this does not seem like too difficult an application. It seems to me that a self-priming centrifugal pump by Gorman-Rupp or Goulds will do the job, they don`t normally come with these types of seals but maybe they can be installed.

Jacques

   Yes, you are right. It is 2 psia. Not 2 psig.

     You said 2 psig at 80F, not the same.

     Jacques

       The liquid is a mixture of Benzene (80%), Xylene and Toulene. The stated boiling temperature of the mixture at 14.7 psia is 170 F. The vapor pressure of 2 psia at 80 F is only a derived number from a vendor. As a VOC the liquid is required to be stored under a nominal blanket of 5 in WC.

       Thank you for your interest.

         I think there is something missing here. Are you sure that the vapor pressure is 2 psig, this is extremely high, what kind of liquid is it, with a vapor pressure like that when the liquid is open to atmosphere then it will completely evaporate, there will be nothing left to pump. If the vapor pressure is correct, then you need to have this liquid under pressure which is a data that you have not given.

         Jacques

           I am trying to find a suitable pump for a rather complex
           application. The pump needs to be self priming as it has a
lift of
           14 feet. At 100 GPM I expect the total head to be 150 feet. It
needs
           to handle solids atleast 1/4 inch size, the vapor pressure of
the
           pump liquid is about 2 psig at 80 F which really cuts down on
the
           NPSH. And on top of it it would handle a VOC subject to NESHAP

           requirements- meaning sealless or double seal pumps. I have
already
           rejected diaphragm type pump because of pulsations.
           Any suggestions, generic or otherwise ?








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Yahoo! Groups Links Received on Fri Dec 03 10:53:00 2004

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