Can Chloride stress corrosion cracking (ClSCC) occur in a hospital steam sterilizer with tap water. The steam sterilizer is made of 304 grade stanless steel. Thanks in advance.
Operating temperature is 126 ºC
Operating pressure is 1.4 MPa
For a local metal loss assessment, the remaining life of piping elbows can be computed by using the method based upon computation of a minimum required thickness for the intended service conditions? For example, r=(t1-t2)/(2c)
where r=remaining life,years
t1 = the minimum remaining wall...
Can anhydrous ammonia ?vapor or liquid?cause erosion or corrosion for piping elbow and tee made of carbon steel or low alloy steel in refrigeration system?
The piping would be full of liquid anhydrous ammonia for some reasons when in-service inspections are conducted. So my question is how to inpect the piping? Thank you in advance.
what NDT technology or tools can be used for the integrity of FRP pressure vessels? And what recommendations would you like to provide for me when I inspect them from outside and inside. Are there some standards or codes in this field? Thanks in advance.
What are the differences between A335 P11 and A335 P22? For example, the allowable operating temperature for a design life of pipes. Thanks in advance.
What is the weight of Pneumatic Three-way Valve for Power Plant?
Some design data of the valve is following.PN=28.7MPa?t=270??DN=325mm.
Thanks in advance.
I have three questions.
1.Does 'glass-lined' mean 'fiberglass-reinforced Plastics(FRP)'?
2.Are there standards or codes about FRP for pressure equipments?
3.How to inspect a glass-lined pressure equipment effectively?
Thanks in advance.
Can anhydrous hydrogen chloride gas and liquid be corrosive to SA-333 steel and stainless steel at low temperature? Could anyone be kind to provide some references about them? Thanks.
In a piping isometric drawing, there are generally two values about total pipe length. And my question is that why the value in the upper right of the drawing can't be equal to the sum of each pipe length written in it. Thanks a lot.
I find that the minimum design pressure of some pressure vessels is F.V. or -0.1MPa or -0.0175MPa. So I am confused and my question is that whether F.V.(Full vacuum) means -0.1MPa and what -0.0175MPa means? Thanks a lot.
Can steam at ~450C be corrosive to carbon steel, low alloy steel or stainless steel? And it would produce creep of steel? Can steam decompose into hydrogen and oxyen? Thanks a lot.
As for a heat exchanger, is space between the floating head cover and the shell head besides it filled with medium same to the shellside? Thanks a lot.
Maleic anhydride (MA) is produced by n-butane oxidation in a salt cooled tube bundle reactor. Tubeside: n-butane and air. Shellside: molten salt. I want to know corrosion or other degradations of tubes (15Mo3,low-alloy steel)by the reaction of n-butane and air from tubeside and molten salt from...
I am confused when it comes to 15Mo3 and 16Mo3 for seamless tube and shell of pressure vessel respectively, for both of their steel number are 1.5415. Could anyone explain for me or recommend some books or articles for me to read? And is there ASME steels equivalent to 15Mo3 and 16Mo3...
Could anyone recommend reference books or handbooks or other available and believable materials about corrosion rate to determine corrosion allowance for pipe and pressure design? Thanks a lot.
