+ Reply to Thread
Page 1 of 2 12 LastLast
Results 1 to 20 of 25

Thread: Cvhve oil log ref??"??

  1. #1
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes

    Cvhve oil log ref??"??

    Opened up system to change oil and clean inside oil drum after oil analysis (found dirt),replaced rear bearings , cuz of hi brg temp, started system purged , added some refrigerant(123) got system down to 50degf but it refuses to go lower .
    Customer said they were losing oil before and added abt 27 gallons of oil because the oil level kept droping which was probably due to ejectors, so here r the temps n approaches.lwt51
    Retchw-59
    Ent con-94degf
    Levcon-104
    Evap-18hg
    Con press-14psi
    Condensin temp 116
    Condensin temp in 107

  2. #2
    Join Date
    Aug 2006
    Location
    Mixing oil and fire with a big spoon.
    Posts
    8,082
    Post Likes
    Quote Originally Posted by mr hottstepper View Post
    ...Customer said they were losing oil before and added abt 27 gallons of oil ...
    and the machine runs at all? get a chair, you are going to be there awhile. you will need to remove the refrigerant, distill, repair the oil eductors, evacuate and recharge with distilled refrigerant. good luck.
    "Right" is not the same as "Wise".

    Don't step on my favorite part of the Constitution just to point out your favorite part.

    Just because you can measure it, doesn't mean it is important. Just because you can't measure it, doesn't mean it isn't important.

  3. #3
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by jayguy View Post
    and the machine runs at all? get a chair, you are going to be there awhile. you will need to remove the refrigerant, distill, repair the oil eductors, evacuate and recharge with distilled refrigerant. good luck.
    Was kinda hoping I didn't hav to bring out the drier cores, taut It could hav been something else

  4. #4
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by jayguy View Post
    and the machine runs at all? get a chair, you are going to be there awhile. you will need to remove the refrigerant, distill, repair the oil eductors, evacuate and recharge with distilled refrigerant. good luck.
    Machine is running quiet no surging , jus temps are holding @ 50 , 100% loaded

  5. #5
    Join Date
    Aug 2006
    Location
    Mixing oil and fire with a big spoon.
    Posts
    8,082
    Post Likes
    Quote Originally Posted by mr hottstepper View Post
    Machine is running quiet no surging , jus temps are holding @ 50 , 100% loaded
    you may also be low on charge...if anyone pulls the charge and weighs it, 27 gallons of oil will weigh about 222# and takes up the same volume as 325# of R123 at 90F or 341# at 40F...so distillation is more critical than most people think.
    "Right" is not the same as "Wise".

    Don't step on my favorite part of the Constitution just to point out your favorite part.

    Just because you can measure it, doesn't mean it is important. Just because you can't measure it, doesn't mean it isn't important.

  6. #6
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by jayguy View Post
    you may also be low on charge...if anyone pulls the charge and weighs it, 27 gallons of oil will weigh about 222# and takes up the same volume as 325# of R123 at 90F or 341# at 40F...so distillation is more critical than most people think.
    So still either way I'd still hav to pull the charge ,but if it was low on charge and vanes fully open it should have surged ,and condensing press n saturation temp would have been lower? So I think I'm right back to where I feared. To go I can't afford to shut that machine down this building takes abt 5 days to recover

  7. #7
    Join Date
    Aug 2006
    Location
    Mixing oil and fire with a big spoon.
    Posts
    8,082
    Post Likes
    Quote Originally Posted by mr hottstepper View Post
    ...but if it was low on charge and vanes fully open it should have surged ,and condensing press n saturation temp would have been lower?...
    not necessarily. oil inhibits heat transfer which helps keep your condensing temperature and pressure high. i have yet to see a properly running machine with the vanes at 100% and fully loaded...it is possible i suppose, but i would be very suspect if the vanes needed to be that far open at full load.
    "Right" is not the same as "Wise".

    Don't step on my favorite part of the Constitution just to point out your favorite part.

    Just because you can measure it, doesn't mean it is important. Just because you can't measure it, doesn't mean it isn't important.

  8. #8
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by jayguy View Post
    not necessarily. oil inhibits heat transfer which helps keep your condensing temperature and pressure high. i have yet to see a properly running machine with the vanes at 100% and fully loaded...it is possible i suppose, but i would be very suspect if the vanes needed to be that far open at full load.
    Oil drum is filled way past sight glass , so I'm thinking if reduce the oil charge to a lower level not to low do you think the ejector/eductor will sip the oil that's in the evap and fill back the drum and give me a little more efficency?I'm at the job site now and this jus dawned on me what do u think?

  9. #9
    Join Date
    Jun 2010
    Location
    Tampa, FL
    Posts
    101
    Post Likes
    If you must keep the machine on line, drain oil to bottom of lower sight glass. Come back once a day and drain more oil until conditions improve and oil level is no longer rising. You need some vapor space in oil tank for system to work right. How did oil leave? Slow or fast. Some things to check: Eductor operation, oil tank vent line solenoid, restricted return line from suction cover,oil tank temp/heater, oil pressure, worn oil seals,refrigerant overcharge w/carryover. Why are cond temps so high? Get temps to about 85/95.

  10. #10
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by deltap10 View Post
    If you must keep the machine on line, drain oil to bottom of lower sight glass. Come back once a day and drain more oil until conditions improve and oil level is no longer rising. You need some vapor space in oil tank for system to work right. How did oil leave? Slow or fast. Some things to check: Eductor operation, oil tank vent line solenoid, restricted return line from suction cover,oil tank temp/heater, oil pressure, worn oil seals,refrigerant overcharge w/carryover. Why are cond temps so high? Get temps to about 85/95.
    Dropped oil level it filld back up twice the second time the vent soloniod opened,left system running wit oil at half of sight glass oil left fast but its stedy now, water temps have dropped to 51/61 quickly and settles at that and machince amperager draw is running between 380and 400 (flucuating fast) evap press is 18hg con is 14.con is 94/101

  11. #11
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by deltap10 View Post
    If you must keep the machine on line, drain oil to bottom of lower sight glass. Come back once a day and drain more oil until conditions improve and oil level is no longer rising. You need some vapor space in oil tank for system to work right. How did oil leave? Slow or fast. Some things to check: Eductor operation, oil tank vent line solenoid, restricted return line from suction cover,oil tank temp/heater, oil pressure, worn oil seals,refrigerant overcharge w/carryover. Why are cond temps so high? Get temps to about 85/95.
    Distilling ref right now is out of the question ,but I need to do somethin to get the wtr temps in d 40's

  12. #12
    Join Date
    Aug 2009
    Location
    Prattville, Alabama
    Posts
    4,042
    Post Likes
    I know you're worried about getting chill water temps into the 40's, but don't let that cause you to ignore everthing else. The 2 most obvious problems you appear to have are oil saturated refrigerant and high entering condenser water temps. If you must keep chiller on line, deltap10's advice is good. However it is slow. But at least you can maintain 51 degrees that way. You should quickly work to resolve the problem with the high entering condenser water temperature. That will give immediate results and improvement. That is, assuming you can quickly lower that temp to 85 F or less. Also, the condenser pressure is high for the saturated condensing temperature. Verify proper purge operation. There may be air in the chiller.

  13. #13
    Join Date
    Jan 2009
    Location
    SE Iowa
    Posts
    5,577
    Post Likes
    Quote Originally Posted by mr hottstepper View Post
    Distilling ref right now is out of the question ,but I need to do somethin to get the wtr temps in d 40's

    Sounds like you're not into the 40's because your simply short on capacity since your effciency is crap... meaning you've hit RLA, but just are getting proper heat transfer.

    What are the approach temps?

  14. #14
    Join Date
    Mar 2004
    Location
    ottawa canada
    Posts
    4,011
    Post Likes
    Quote Originally Posted by motoguy128 View Post
    Sounds like you're not into the 40's because your simply short on capacity since your effciency is crap... meaning you've hit RLA, but just are getting proper heat transfer.

    What are the approach temps?
    Hes got 27 gals of waste oil floatin around in there ....... Approach temps dont matter squat right now .
    The toy chest is officially full ... I got a new toy..... 2007 Aston Martin V8 Vantage and yes it still gives me goosebumps
    You bend em" I"ll mend em" !!!!!!!
    I"m not a service tech, I’m retired ….I used to be a thermodynamic transfer analyst & strategic system sustainability specialist
    In the new big shop , greasin', oilin' . tweakin' n shinin' !!

  15. #15
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by Healey Nut View Post
    Hes got 27 gals of waste oil floatin around in there ....... Approach temps dont matter squat right now .
    Analysis shows I 91.2% oil, 1.4% coolant and 7.4% solids.so uess I am gettin out mainly oil yay!....but will I get back lost efficency? because I've removed abt 12 gallons and no improvment water temps still hi like

  16. #16
    Join Date
    Oct 2011
    Location
    Upstate NY
    Posts
    132
    Post Likes
    Actually, I would be interested to see the trend/ relationship between the evap approach and the amount of oil removal...
    If the amount of oil suspected to be in the machine is accurate, the evap approach should be out of sight (10+°) & coupled with the current condenser conditions, I'm surprised that machine isn't in or near stall/surge.
    I agree with earlier post, at 14# head, either non-condesables exist or the instrumentation is Inaccurate...

  17. #17
    Join Date
    Aug 2009
    Location
    Prattville, Alabama
    Posts
    4,042
    Post Likes
    There is so much oil, it probably has some oil floating on top (as Healy Nut said) of the refrigerant/oil mixture in the evaporator. The refrigerant is saturated to the point that it will not "absorb" any more. Conditions won't improve until the "excess" oil floating on top is removed (actually, absorbed into the refrigerant) and then further oil that is removed will decrease the amount of oil that is dissolved in the refrigerant. That oil floating on top can lower the evaporator pressure further. The layer of oil is a restriction.
    Last edited by Nuclrchiller; 07-30-2012 at 05:17 PM. Reason: clarified "refrigerant/oil mixture in the evaporator"

  18. #18
    Join Date
    Aug 2009
    Location
    Prattville, Alabama
    Posts
    4,042
    Post Likes
    Quote Originally Posted by mr hottstepper View Post
    Analysis shows I 91.2% oil, 1.4% coolant and 7.4% solids.so uess I am gettin out mainly oil yay!....but will I get back lost efficency? because I've removed abt 12 gallons and no improvment water temps still hi like
    Has high entering condenser water temp been resolved ?

  19. #19
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by tcy612 View Post
    Actually, I would be interested to see the trend/ relationship between the evap approach and the amount of oil removal...
    If the amount of oil suspected to be in the machine is accurate, the evap approach should be out of sight (10+°) & coupled with the current condenser conditions, I'm surprised that machine isn't in or near stall/surge.
    I agree with earlier post, at 14# head, either non-condesables exist or the instrumentation is Inaccurate...
    I am on my way to d job site should be ther in abt 2 hs,will check approaches den

  20. #20
    Join Date
    Jan 2011
    Location
    tt, west indies
    Posts
    213
    Post Likes
    Thread Starter
    Quote Originally Posted by Nuclrchiller View Post
    Has high entering condenser water temp been resolved ?
    Gonna check on that

+ Reply to Thread
Page 1 of 2 12 LastLast

Quick Reply Quick Reply

Register Now

Please enter the name by which you would like to log-in and be known on this site.

Please enter a password for your user account. Note that passwords are case-sensitive.

Please enter a valid email address for yourself.

Log-in

Posting Permissions

  • You may post new threads
  • You may post replies
  • You may not post attachments
  • You may not edit your posts
  •