Coating Long Tubes
Question: I'm a manufacturing engineer who was recently hired on to look at paint problems.
Question:
I'm a manufacturing engineer who was recently hired on to look at paint problems. I've been involved in the powder coating industry for about five years, most of which dealt with painting product for indoor use. My new company manufactures and paints outdoor tubing products ranging from 1– 16 inches in diameter, 5–60 ft in length and 3–11 gage in thickness. We paint over aluminum, mild steel and galvanized using TGIC powder or sometimes liquid. The current painting process in place is as follows: Parts are hung and run through a steel shot blaster, blown off with an air wand, painted and cured. As you can guess, we have an adhesion problem with some of our product in the field but no color problems. We are looking at extending the warranty on these products by possibly installing a wash system but we really have no baseline information that says how long our paint currently lasts. What would be the best test to determine this? I've heard salt spray would be a good test but how does salt spray hours translate to years?
Also, if we were to install a wash system, what type of system would you recommend for washing such long parts of varying substrates? E. F.
Answer:
I'll answer your last question first. Salt spray exposure is an accelerated test. Because of its varying effects on different coating systems, it is best used as a comparative test of their corrosion resistance. After 50 years in the organic coatings business, the best translation I can give you is 300 hours salt spray exposure is equivalent to 300 hours salt spray exposure.
If your production rate requires it, you can install what you call a “wash system,” a conveyorized power spray pretreatment system. For outdoor products, you should use a zinc phosphate pretreatment formulated to handle steel, aluminum and galvanized steel. This will require at least five stages and perhaps as many as seven or more. A five-stage system would be clean, rinse, phosphate, rinse and final rinse (seal). Optional stages would be pre-cleaner, conditioner and DI rinses. On the other hand, if your production rate does not require a conveyorized system, you could use a multistage high-pressure hand-power washer to pretreat the tubes. If you use an immersion system, the tanks must be able to hold the longest part.
Related Content
-
NASF/AESF Foundation Research Project #120: Electrochemical Destruction of Perfluorooctanesulfonate in Electroplating Wastewaters - April 2022-March 2023
This NASF-AESF Foundation research project report covers project work from April 2022 to March 2023 at the University of Illinois at Chicago. The overall objective of this work is to utilize a cost-effective reactive electrochemical membrane (REM) for the removal of PFAS from synthetic electroplating wastewater. Initial results for the oxidation of PFOA with three different catalysts are discussed.
-
NASF/AESF Foundation Research Project #122: Electrochemical Approaches to Treatment of PFAS in Plating Wastewater - 12th Quarterly Report
This NASF-AESF Foundation research project report covers the 12th quarter of project work (October – December 2023) at the University of Georgia. In our previous report, we described our work on performance and effect of surface fluorinated Ti4O7 anodes on PFAS degradation in reactive electrochemical membrane (REM) mode. This quarter, our experiments involved utilizing porous Ti4O7 plates serving both as anodes and membranes. Tests compared pristine and F-18.6 Ti4O7 anodes at current densities of 10 mA/cm2 and 40 mA/cm2. This 12th quarterly report discusses the mechanisms of the effects on EO performance by anode surface fluorination.
-
NASF/AESF Foundation Research Project #122: Electrochemical Approaches to Treatment of PFAS in Plating Wastewater - 10th Quarterly Report
The NASF-AESF Foundation Research Board selected a project addressing the problem of PFAS and related chemicals in plating wastewater streams. This report covers the 10th quarter of work (April-June 2023). Here, we examine the effect of surface fluorination of Ti4O7 anodes on PFAS degradation performance in terms of energy performance as well as formation of chlorate and perchlorate when chloride is present in the solution. The full paper on this work can be accessed and printed at short.pfonline.com/NASF24Feb2.