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  1. kszyho100

    condensate temperature

    I remember about pressure drop on steam traps. I don't have isometric drawing.
  2. kszyho100

    condensate temperature

    I expect by-passes on traps so I specifed condensate pipes for 180C.
  3. kszyho100

    condensate temperature

    Static head 0,5 bar, friction loss 0,4 bar all togheter about 1 bar loss So for 1 barg I have temperature 120C.
  4. kszyho100

    condensate temperature

    Hi I am designing a condensate pipeline. I have a problem how to determine condensate temperature. The condensate pipeline is about 110 m long. Dividied in to two section in a building and outside. The pressure before steam traps is 6 bar. Behind the steam traps I lift the pipeline by 5 m. Then...
  5. kszyho100

    condensate return pipeline

    Thx, I must overlooked this chapter.
  6. kszyho100

    condensate return pipeline

    Hi I am designing return line which collects condensate from couple of steam traps. Steam pressure upstream control valves is 12 barg, control valves reduces steam pressure to 6 barg. The problem is that I need to lift my common line over a door. Usually I lift condensate from a single steam...
  7. kszyho100

    pipe elbow FEA

    Some additional explanation. I did calculations and I have following results. expansion axial forces transverse forces moments Than I calculated stress by von Mises formula and now I want to compare it to FEA. I tried Autodesk Fusion 360 but I have problem how to put forces. One bend end is...
  8. kszyho100

    pipe elbow FEA

    Hi I want to check stress in carbon steel elbow (this is preinsulated underground hot water pipeline). I know all forces (axial, transverse, moment) but don't know where to put them. Should the elbow at one end should be constrained and on the other one I should put loads? Thanks in advance.
  9. kszyho100

    steam mains air removing

    Steam line has no vacuum rating. I think i will leave open end of air vent to the atmosphere. Thank you for your help.
  10. kszyho100

    steam mains air removing

    Hi At the end of steam mains which works periodic (8 hrs per day) thermostatic air vent is installed. I wonder if there should be fitted check valve after thermostatic air vent to prevent air to come back when steam line is cold. What do you think?
  11. kszyho100

    compressed air drip leg

    Thank you for your help.
  12. kszyho100

    compressed air drip leg

    Hi I just wonder if it is necessary to design drip leg for water residues before air preparation block (filter/regulator w manual drain + lubricator). Compressor is equipped with a refigerant air dryer. All piplines are in heated rooms. Chris
  13. kszyho100

    steampipeline for thermal processing of meat

    Hi I’m designing steampipeline for thermal processing of meat. Steam at 0.5 g will be used in steam chambers for direct moisturizing. My question is what kind of materials I should use for pipes and fittings. I am thinking about 304L and tri-clamp connections. Is it a good choice? Chris
  14. kszyho100

    Biomass drying

    Hi I need to calculate heat demand for biomass drying. I know its weight and properties. For this purpose I would like to use some kind of outside floor heting. Any ideas? Thanks Chris
  15. kszyho100

    medical gases

    Hi Where I can find on the internet information about designing medical gases systems, or maybe anyone could recommend a book? Chris
  16. kszyho100

    Steam trap and temperature controlling valve

    There is a sensor in a hot water pipe, and the steam trap I think is termostatic. Regards Chris
  17. kszyho100

    Steam trap and temperature controlling valve

    Hi I have a question. At a production plant I noticed hot water system heated by 6 bar g steam. Downstream of a heatexchanger was a temperature controlling valve and parallel to that valve was installed a steam trap. Could anyone explain me if it makes any sense bypassing controliing valve with...
  18. kszyho100

    Lifting condensate

    Hi everyone I need to lift condensate from a steam trap to a higher level (it is only 2 metres to discharge well and then drain to waste). Minimal pressure in steam main is 6 bar gauge. I know that 1 metre litft in pipework = 1 m head static pressure = 0.1 bar backpressure. Am I right that it...
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