Pressure Vessel Assessment Report



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Project Information Client: Total Energy Location: Blackwell OK Date: 7/23/2013 Contact: Integrity Mgmt. Advisor: Chuck Easterbrooks - API 510 #2212 Cc: API / UT Inspector: Robert Van Pelt-API 510# 40899 Vessel Description: Propane Storage Tank Vessel Identification: SN-1534 1.0 Summary: An internal and external API 510 inspection and ultrasonic thickness examination was performed on vessels SN# 1534. This vessel was out of service at the time of inspection. There was no U1 or any other documentation available prior to performing the inspection. There is some minor scale and flange seating surface corrosion but overall the shell and heads are in serviceable condition. The limiting factor for this assessment is the absence of original design and material identification data available. Page 1 of 12

Table of Contents 1.0 SUMMARY: 1 2.0 REFERENCES: 3 3.0 GENERAL DISCUSSION: 3 4.0 INSPECTION DETAILS: 3 4.1 EXTERNAL INSPECTION: 3 4.2 INTERNAL INSPECTION: 4 4.3 CONCLUSION: 4 4.4 RECOMMENDATIONS: 4 5.0 ULTRASONIC THICKNESS INSPECTION: 5 5.1 SUMMARY INFORMATION: 5 5.2 UT THICKNESS DATA 6 6.0 PICTURES: 8 Page 2 of 12

2.0 References: API 510 Inspection Code ASME Section VIII Division 1 ASME Section V API 579 Fitness for Service NBIC National Board Inspection Code 3.0 General Discussion: The contents of this report are based on the data acquired during the visual inspection and ultrasonic thickness inspection results. UT data was taken at specific locations to determine the remaining thickness. The internal and external visual inspection results provide an account of the visual condition and presence of any visual degradation. There was not any historical inspection or original design information available for review that positively identifies the material spec or grade or original thickness. 4.0 Inspection Details: 4.1 External Inspection: Saddle Supports: There are 3 saddles supports for this vessel. Each support has a reinforcement band ¼ thick by 9 wide completely encompasses the full circumference of the vessel. The supports are located near each end and in the center. There were no visible distortions and the supports appear to be in serviceable condition. Shell: There is scattered coating failure over the entire vessel. There is mild active oxidation associated with the coating failure with negligible wall loss. There were access platform clips welded to the shell but the platforms were not on site. Nozzles: The nozzles necks were in serviceable condition however the flange sealing surfaces had a tightly adhered combination of atmospheric scale and paint approximately 20 mils thick. The pitting was not evaluated on the sealing surface due to the heavy scale build up. Nozzle labeled N3 had a visible RMS finish under the heavy scale while all of the other flange seating surfaces had no visible serrations. There were reinforcement pads installed on the 6 nozzle and the manway. All the repads had metallic threaded plugs installed in their telltale holes. Inspection of the telltale holes could not be performed. The manway had a heavy atmospheric scale build up on the flange area around the OD of the raised face sealing surface. The sealing surface was in serviceable condition. The scale can be scraped off with a hand scraper. The manway davit arm had been cut off previously leaving only the davit arm hinge clip and a partial remnant of the davit arm inserted into the clip. Heads: The heads are in comparable condition to the shell. Both heads are ellipsoidal. There were no visible distortions observed.. Data Plate: The data plate was intact and legible. Page 3 of 12

4.2 Internal Inspection: Shell & Heads: Manway: The internal surface of the manway displayed no pitting. It had a light surface scale of approximately 10 mils thick. It did not indicate any signs of bulging, blistering or warping. The ID nozzle to shell weld was full profile with no preferential corrosion visible. The weld surface was similar to the nozzle ID surface. Shell: The shell internal surface was generally smooth with no measurable pitting. There was a light surface oxidation throughout the entire ID of the vessel. The welds were full profile and comparable to the shell surface ID. There are 3 internal stiffening rings welded to the shell for the entire ID circumference that are ½ thick X 6 in height. Nozzles: A 2 nozzle on the north east side had a valve and blind installed. Inspection of this nozzle was limited to the ID surface only, It had a heavy rust and scale build up which impeded the ID inspection of the surface. All nozzles, including threaded couplings, were internally back-welded and have some internal projection. All welds are full and complete with no visible porosity, cracking, or discontinuities that would affect the pressure retaining capabilities. Nozzle necks are free from debris and corrosion. All ID nozzle weld surfaces were comparable to the adjacent shell surfaces. Internal Distributor Pipe: A distributor pipe was installed on the south west end of the vessel and traveled to the north for the entire length to the vessel. The north end of the distributor header (approximately 15 foot) had 1/16 holes on the bottom of the pipe. The holes were 2 apart in a linear row. 95% of the holes completely were plugged. HEADS: The ID surfaces of the heads were comparable to the shell ID. The head to shell welds were comparable to the shell ID surface. 4.3 Conclusion: The UT data shows a.079 maximum deviation from the lowest to highest remaining thickness obtained on the shell and.062 deviation on the heads. Pressure vessels in propane service typically were designed with a 0.000 corrosion allowance. The corrosion observed and noted above does not appear to be service related and aside from the gasket surface degradation, is mild in nature and a result of atmospheric corrosion and a period of time out of service without an inert purge. 4.4 Recommendations: The vessel should be abrasively blasted and painted to mitigate future external corrosion. All flange gasket surfaces should be mechanically cleaned and evaluated to ensure suitability for service. Without positive identification of the materials used to construct this vessel, procedures complying with API 510 Section 7.7 or NBIC will need to be followed to ascertain the future service limitations, design conditions, and MAWP. Additionally, any applicable rules for the jurisdiction and a future inspection plan will need to be developed in accordance with API 510. Page 4 of 12

5.0 Ultrasonic Thickness Inspection: Details: Straight beam ultrasonic thickness measurements were taken at various separate locations on the shell plate material and the ellipsoidal heads. UT readings were taken utilizing a KB USM GO instrument with a CA-211A ½ single element transducer, calibrated on 1 mild carbon steel step block. There was not a U-1A form or other documentation available to compare UT thickness readings with. The base material was not known during this examination. The thickness measurements shown below utilize the orientation of the vessel at the time of inspection, whereas the North head is the head with the original data plate affixed to the head. 5.1 Summary Information: Probe : CA-211A Cal Comment : Cal@1.000" on a 1.000" Carbon Steel Test Block SN# 12-3015 Inspector : Jerrad Tidwell Company : MTR A Instrument Type : USM Go Instrument S.N : USMGO1265041 Units : INCH Velocity(in/us) : 0.2329 (UP OR NORTH) H B Max Shell Thickness: 0.644 Min Shell Thickness: 0.565 Max North Head Thickness: 0.784 Min North Head Thickness: 0.746 Max SouthHead Thickness: 0.795 Min South Head Thickness: 0.733 G F E D C Page 5 of 12

5.2 UT Thickness Data Bands A B C D E F G H 1 0.58 0.586 0.575 0.577 2 0.61 0.619 0.601 0.601 3 0.579 0.591 0.576 0.579 4 0.575 0.582 0.581 0.583 5 0.599 0.596 0.601 0.594 6 0.575 0.58 0.581 0.582 7 0.575 0.571 0.566 0.6 8 0.592 0.589 0.592 0.595 9 0.572 0.57 0.572 0.576 10 0.575 0.578 0.572 0.573 11 0.598 0.597 0.59 0.585 12 0.57 0.573 0.57 0.566 13 0.582 0.577 0.569 0.58 14 0.607 0.598 0.607 0.611 15 0.589 0.583 0.577 0.585 16 0.571 0.571 0.565 0.567 17 0.587 0.588 0.579 0.571 18 0.577 0.574 0.573 0.573 19 0.596 0.593 0.61 0.601 20 0.63 0.616 0.644 0.63 21 0.591 0.589 0.607 0.598 22 0.59 0.584 0.58 0.577 23 0.613 0.614 0.602 0.601 24 0.595 0.595 0.592 0.587 25 0.598 0.589 0.596 0.602 26 0.609 0.604 0.621 0.618 27 0.585 0.582 0.588 0.593 28 0.579 0.575 0.568 0.574 29 0.607 0.601 0.599 0.629 30 0.587 0.584 0.578 0.58 31 0.601 0.582 0.567 0.593 32 0.617 0.605 0.605 0.621 33 0.601 0.587 0.569 0.593 34 0.577 0.577 0.575 0.576 35 0.606 0.613 0.614 0.602 36 0.569 0.569 0.565 0.57 Page 6 of 12

UT Data (Cont.): Bands A B C D E F G H 37 0.736 0.739 North Head 0.734 0.741 38 0.731 0.727 0.732 0.734 South Head 39 0.737 0.771 0.712 0.754 40 0.729 0.729 0.722 0.735 Nozzles 41 0.424 0.424 42 1.005 1.006 1.008 1.009 43 0.42 0.432 0.428 0.413 44 0.427 0.418 0.416 0.429 45 0.603 0.586 0.598 0.598 46 0.426 0.429 0.428 0.417 47 0.429 0.425 0.435 0.423 Page 7 of 12

6.0 Pictures: PICTURE 1 DATA PLATE 1534 Page 8 of 12

Platform clips Welded coupling Flange welded to South head ID of North head Page 9 of 12

Saddle Support Reinforcement strap for saddle Davit Arm bracket Man Way Page 10 of 12

Corroded Flange Face Corroded Flange Face ID of welded coupling ID of shell Page 11 of 12

Valve bolted to flange Repad plugged with threaded plug Distributor Pipe ID Stiffener support for saddles (typ 3) Page 12 of 12