By Carlos Molina

According to API 653 3.14, Hot tapping identifies a procedure for installing a nozzle in the shell of a tank that is in service. This means that a tank can continue to be in operation whilst maintenance or modifications are being done to it. This is in complete compliance with the API 653 standard, but following some rules. First of all, for all of you students, let´s review what the BOK of the API 653 March 15 exam has to say.

HOT TAPPING
a) The Inspector should be familiar with the Hot Tapping requirements. (API-653, Paragraph 9.14)
b) The inspector should be able to calculate the minimum spacing between an existing nozzle and a new hot tap nozzle. (API-653 Paragraph 9.14.3)

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By Carlos Molina

Following with the subjects that you should study for the exam, today we will have a short explanation of the reason behind some of weld spacings in tank elements. Boy, I have to tell you, thinking for this article was difficult, because it involves many figures and tables that are present in the API 650 and API 653 standards. And writing it was more difficult, because of the little time I have (As most of you in the Oil and Gas Field).

First let me ask you a question: In which plane are tank shell stresses higher, in a vertical or an horizontal plane?

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By Carlos Molina

Hi friends.

I keep studying about API 653. I have to be a re-certified API 653 Inspector before september 2015.  I obtained my certification back in september 2012, with only one year experience in tank repair and, as I did with my english language skills, most of it was self-taught (I took a course, though). Now I have to regain all the knowledge again, which is really easy if you know how to learn it.

I hope you are studying well for your own exam, taking advantage of what I or others offer, and if you are not, remember it is scheduled for March 15, 2015. So you better  wash out of the holidays inertia and start studying right now.

Today we are going to talk about hydrostatic testing in API 653, more specifically about hydrostatic height calculations. Some of the questions of the exam are from this subject.

WHAT IS AN HYDROTEST?

Hydrostatic testing is (or a least should be) done in every new welded tank for oil storage and it is mandatory for any tank that has been under a major alteration, according to API 653.

And as we are students,  let´s remember the definition of hydrotest of API 653.

Definition of hydrotest per API 653

 

 

As it says, for new or repaired tanks, the purpose of hydrostatic testing is to demonstrate the tank´s fitness for service, and the better you test, the less risk you have once the tank is in operation.

If you are planning to take the exam, you should be familiar with all of the requirements of API 650 and 653 regarding hydrotesting. But right now we will concentrate in calculating hydrostatic test height.

HOW TO CALCULATE HYDROSTATIC TEST HEIGHT

For a tank that has been in operation, several things can happen that may highlight the need for an hydrostatic test

*If the tank is going to be used for a new, more sever service. That means, when the liquid that will be stored has a higher specific gravity than the current stored  product.

*When there have been repairs. Maybe your repairs are perfect, but some corrosion remains in other areas of the tank.

Determination of hydrostatic test height Ht, when you have calculated a controlling thickness for an entire shell course, can be achieved solving for the following equation, where Ht is the height from the bottom of the shell course under consideration to the hydrostatic test height

Hydrotest height over an entire shell course

Over entire shell course

Determination of hydrostatic test height Ht, when you have calculated controlling thickness for a locally thinned area (I haven´t treated the subject of controlling thicknesses here so far, my bad) can be achieved solving for the following equation, where Ht is the height from the bottom of the length, L, (see 4.3.2.1) for the most severely thinned area in each shell course to the hydrostatic test height in feet

Hydrotest height over locally thinned area

Over locally thinned area

So, hydrostatic test height depends on 4 variables, which are.

St is the smaller value between fractions of yield strenght or tensile strenght, or the maximum allowable hydrostatic test stress.

Stress values for hydrostatic height calculus

Stress values for hydrostatic height calculus

E is the joint efficiency. Look how to find joint efficiency here

Tmin is the controlling thickness

D is the diameter of the tank.

Let´s see an example of height calculation. I am assuming you have some background on the formulas  of API 650 and API 653.

EXAMPLE 2.

A tank will be subjected to hydrostatic testing after repairs. After some study, the inspector decides to run calculations for hydrostatic test height over the first shell course and over a locally thinned area close to a vertical seam, 36 inches high in the 4th shell course. Steel is A36 with Y = 36000psi and T=58000psi. Shell courses are 6ft high and the tank is 48ft diameter. First two courses were welded before 1980, and the other courses were added recently. The controlling thickness for the first shell course is 7mm and for the locally thinned area is 6,35mm. What should be the hydrostatic test height?

Solution.

Well, for the equations, values are these

Case 1. Lower shell course

E=0,85. See Table 4-2

St = smaller of 0,88Y or 0,472Y, then St = 27376psi

D= 48

Tmin= 7mm = 0,275in

Hydrotest height for entire shell course

So, hydrostatic test height will be 15,93m.

Case 2. Locally thinned area in 4th course

=1. See Table 4-2.

St = smaller of 0,9Y or 0,519Y, then St = 30102psi

D= 48

Tmin = 6,35mm=0,25in

Hydrotest height for locally thinned area

Hydrostatic test height over the locally thinned area can be 16,7m. (A total height of 23,01m)

Then the tank has a maximum fill height  is 15,93m.

HAVE IN MIND FOR YOUR EXAM

You have to be aware that variables in these and other equations of the standards can have different values depending on year of fabrication, purpose of calculation (design or hydrostatic loads), etc. In the exam, you have to be very careful to avoid mistakes, as they always trhow some confusing questions.

You can notice that the presence of different defects in tank shells implies than more than one value of Tmin or Ht should be calculated in a real tank inspection. This kind of dual example analysis is not common in other literature.

And that´s it for now.

As always, I am open to all kind of comments about the information in this site. And lastly, take a look at the following Ad.

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By Carlos Molina

Hi folks. I hope you are doing well studying for your API 653 certification examination on March 20, 2015.

Here at Apiexam.com, we continue with the explanation of concepts neccessary for passing the API 653 exam. One of the topics you should study in order to pass is calculation of joint efficiencies for shell joints. (more…)

By Carlos Molina

One of the things about API 653 certification is that doesn´t ensure that you are competent in tank inspection. You can pass the exam, and still you don´t always know or remember all you studied in the course, especially if not practiced on a daily basis. One of those things to remember is tank internal inspection interval calculation .

I was wandering the eng-tips forum the other day and I found a question about calculating minimum remaining thickness for a tank bottom.  I saw that forum and decided to write this post in order to clarify the subject more. Besides, this is part of the Body Of Knowledge of the examination, and you know you have to get it right… (more…)