Pages

Monday, February 13, 2012

Corrosion | What is causing the problem in a urea HP condenser ...

Home » What is causing the problem in a urea HP condenser?

Q: We are facing problem in a urea HP condenser. Cracks are observed in tube to tubesheet region just at a distance of 15 to 20 mm from top tube end (circumferential and transverse cracks). In ECT (eddy current testing) we couldn't trace it due to edge effect. Please advise suitable NDT for detection and the cause as well.

A: More details are required to speculate on potential causes of the cracking you are describing. One must look for failure patterns to aid in this determination. Where the failures are occurring (on random tubes, near supports or baffles, clustered about shell inlets or outlets, on outer u-tube rows or inner u-tube rows, etc,) will narrow down the possibilities. For example, tube failures near a tube sheet in a condensing zone may indicate inadequate venting. ASME Code, Section V, "Nondestructive Examination" is a helpful reference and describes what NDE can disclose. Test methods covered by this standard include acoustic emission (AE), electromagnetic (eddy-current) testing (ET), leak testing (LT), magnetic particle testing (MT), liquid penetrant testing (PT), radiography (RT), ultrasonic testing (UT), and visual testing (VT). Another excellent source of information for your specific situation is the reference book, "Tubular Heat Exchanger Inspection, Maintenance, and Repair" by Andreone and Yokel (McGraw-Hill, 1998). I suggest you obtain copies of both of these references to facilitate finding a resolution to your problem and plan a path forward.

Here are more of the latest questions on: Corrosion

What is causing the problem in a urea HP condenser?
We are facing problem in a urea HP condenser. Cracks are observed in tube to tubesheet region just at a distance of 15 to 20 mm from top tube end (circumferential and transverse cracks). In ECT (eddy current testing) we couldn't trace it due to edge effect. Please advise suitable NDT for detection and the cause as well.

Is 304 stainless steel pipe suitable for handling nitric acid?
Is 304 stainless steel pipe suitable for handling nitric acid (10% to 30% concentration) for a continuous duty application?

Which is a better MOC for carbon black plants?
Which is a better MOC for carbon black plants? We crack heavy oils (with sulfur content) at 800 degrees C to produce carbon black. Is 304 better or 316 better to avoid acid corrosion in our pipelines?

Is it better to use a Hastelloy C alloy or 316L stainless steel?
We need to install a level switch probe in 98% sulfuric acid. Based on corrosion resistance, would it be better to use a Hastelloy C alloy or should we use 316L stainless steel? The storage tank temperature is 70 to 90 degrees F and there is no contamination of the acid.

Do austenitic stainless steels have good resistance to carbonic acid attack?
We have a fin-tube style heat exchanger in which we mix natural gas and liquid water, and use an exhaust gas stream to vaporize the water and preheat the fuel mixture. We have a new water recovery process in which we condense the water out of a carbon dioxide rich exhaust stream and feed this into the heat exchanger. It has been observed that the recovered water is slightly acidic at a pH 4.5, and it has been attribute to the presence of dissolved carbonic acid in the water. The tubes of the heat exchanger are 304H Stainless Steel. Is corrosion something we should be concerned about for the long term operation of this unit?

Back to Ask the Experts

0 comments:

Post a Comment