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Designing High-Pressure Pipes

06/25/2009 10:12 PM

Who can help me with the process of designing a 3-inch pipe containing oil to 700 F and must withstand a pressure of 3000 psi

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#1

Re: Desing high pressure pipe

06/25/2009 11:57 PM

Hello omargelvez,

If you need pipe for such an application, call some pipe vendors. They will tell you what you need.

If you want to design and manufacture pipe for such an application, helpful answers from here (or other web forums for that matter) are not sufficient for creating a safe product. The fact that you are asking questions here is a blatant indication that you should not be designing said pipe. If you had sufficient training, you would not need to inquire on the net.

Please get a professional involved, for safety's sake.

Mike

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#2

Re: Desing high pressure pipe

06/26/2009 12:05 AM

Mikerho is right. You're not up to it.

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#3

Re: Desing high pressure pipe

06/26/2009 1:28 AM

Mike if you're not going to help, not scold. I imagine that you are the only competent professional.

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#5
In reply to #3

Re: Desing high pressure pipe

06/26/2009 10:58 PM

It is not a question of scolding. Hot oil at 700F and 3000 PSI is a challenge to contain with safety. the absolute strength of the pipe, the safety factor needed, the type of valves and valve seats and packing glands, and you also need the type of oil, to be sure any seal or gland is not penetrated by the oil and suddenly sprays out as a mist. Will this mist burst into flames at 700F? What is the flash point of this oil? Is it combustible? In addition, 3000 PSI is an explosion hazard on its own with the wrong safety factor and as pipes age and corrode from the outside or inside or fail from fatigue

Then people are going to work around this apparattus. If you make it and it blows and kills some people, you will probably go to jail for many years. In some places, you would be executed.

So we are not chastising you unduly. It is wise advice you would do well to listen to.

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#7
In reply to #5

Re: Desing high pressure pipe

06/26/2009 11:05 PM

Thanks aurizon,

You probably know more about this subject than I do, from reading your past posts - you brought up some very good points.

GA from me

(somebody else please follow up!)

Mike

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#8
In reply to #7

Re: Desing high pressure pipe

06/26/2009 11:20 PM

Just did!

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#6
In reply to #3

Re: Desing high pressure pipe

06/26/2009 11:00 PM

Hi Omar,

I'm not scolding. You should not take this personally. The process conditions you have described can cause a very unpleasant incident if a pipe or flange fails. This could cost someone the use of certain parts of their body or even their life. If anything, you should be thanking me for trying to look out for you.

By the way, what are your engineering qualifications? Are you in management?

Best Regards,

Mike

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#4

Re: Desing high pressure pipe

06/26/2009 3:34 AM

Open a dialogue with a piping distributor, or several of them, without delay.

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#9

Re: Designing High-Pressure Pipes

06/27/2009 12:01 AM

This is the matter of the inside, but in te calculation it is outside diameter of the pipe, its material quality and temperature of the medium in the pipe. Also it is for the designer to estimate the adition for corrosion and the imperfection of the pipe make. This matter is under ASME piping rules and don't play with this matter specially if the medium is gasous or inflammable and choking in close space.

Best regards,

Marijan from Zagreb

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#10

Re: Designing High-Pressure Pipes

06/27/2009 12:25 AM

Omar go to ASME B-31 3 Chapter IX (Seccions K). Take special attention to Valves, Gaskets and INSULATION (Hot Oil Requires are very specific).

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#12
In reply to #10

Re: Designing High-Pressure Pipes

06/27/2009 12:28 AM

Hi atorroja,

I thought your reply was on-topic (and good). Why did you select off-topic?

Mike

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#11

Re: Designing High-Pressure Pipes

06/27/2009 12:26 AM

Omar go to ASME B-31 3 Chapter IX (Seccions K). Take special attention to Valves, Gaskets and INSULATION (Hot Oil Requires are very specific).

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#13

Re: Designing High-Pressure Pipes

06/27/2009 12:39 AM

To give you some idea. Pipe has been made for high pressure for well over 150 years. due to experience, failures, deaths etc a number of regulatory bodies have emerged. The names vary from country to country, but they deal with standards, for wire, pipe etc.

http://www.asme.org/

http://www.astm.org/

there will be a listing of standards for pipe etc, for various pressures, temperatures etc. These manuals, often called pipe schedules, for pipe, wire schedules for wire, and steel beams and cement and so on.

These schedules list the pipe by material, wall thickness, application, and all manner of ways pipe, wire etc is sold. These schedules are are used by professional people to design pipeing, wiring etc that will have a long and safe life and will be an efficient use of materials. There is no point in wasting money with overdesign, nor can you save money and take great risks with underdesign. The people who use them have spent years learning and using them, and getting the experience to use them with safety.

That said, an intelligent person can read the standards and learn how to use them for particular applications fairly easily. Where it gets hard is in the extreme applications. water pipe for a house = dead easy. Boiler piping or hot oil piping at 700F and 3000 PSI = not easy. Vessels that explode at those temperatures and pressures do so with such force that people are shredded into cooked fragments. It is an ultrasonic shock wave that fluidizes flesh, like a bomb blast does to the close by victims, so you do not want any learners doing it. read deep into the links and you will get some idea.

http://www.google.ca/search?hl=en&safe=off&q=ASme+%2B%22pipe+schedules%22&btnG=Search&meta=

http://www.google.ca/search?hl=en&safe=off&q=ASTM+%2B%22pipe+schedules%22&btnG=Search&meta=

http://www.google.ca/search?hl=en&safe=off&q=ASTM+%2B%22wire+schedules%22&btnG=Search&meta=

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#14
In reply to #13

Re: Designing High-Pressure Pipes

06/27/2009 1:01 AM

Much more in-depth than your earlier post and spot-on.

Out of curiousity, what's your background?

Mike

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#15

Re: Designing High-Pressure Pipes

06/27/2009 2:09 AM

Hi Omar,

Please heed the GA already given by Aurizon.

Recognise his advice and proceed with extreme caution.

You didn't give too much info, but by the looks of things 3000psi is wellhead pressure. If this pipe is upstream of the choke valve then API rules normally govern. Downstream, ASME codes prevail. use B31.4 for Oil, BUT if it contains gas then B31.8 governs. If you are within a plant B31.3 should be used. For such a high temperature you will need ASTM A106 (Seamless High Temp) OR if it is linepipe API 5L X52 or X60. If it is sour sevice you need to add in the corrosion allowance, typically 3 to 6 mm, but check with your materials specialist. Best of Luck and be cautious!

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#16

Re: Designing High-Pressure Pipes

06/27/2009 6:04 AM

Determination of pipe wall thickness in accordance with ASME B31.3

Given :

• Design Pressure, P = 3000 psig

• Design Temperature: 700°F

• Nominal Pipe Size, NPS 3

• Pipe material: Carbon steel A 106, Grade B, Seamless

• Corrosion allowance, c = 0.125 in.

• Mill tolerance = 12.5%

Find : Thickness for internal pressure and nominal thickness.

Data: tm = t + c

t = PD / 2(SE + PY) (ASME Code B31.3, Para 304.1.2, Eq. 3a)

c = 0.125 in.

Y = 0.4 (Table 304.1.1)

E = 1.0 (Table 302.3.4 & Appendix A, Table A-1B)

Pipe Outside Diameter, D = 3.5 in. (ASME B36.10M)

S at 700 oF = 16500 psi (Appendix A, Table A-1 )

Wall Thickness Tolerance = 12.5% (ASME B36.10M & ASTM A106)

Solution:

Calculate P/ SE = (3000 psi)/(16500 psi * 1.0) = 0.1818 < 0.385

Also, P(3000 psi) < 1.25 SE (1.25*16500*1.0 = 20625 psi)

So, we can use the equation:

t = PD / 2(SE + PY) = (3000 psi)(3.5 in.) / [2(16500*1.0 + 3000*0.4)] = 0.2966 in.

• Corrosion allowance calculation: tm = t + c = 0.2966+ 0.125 = 0.4216 in.

• Mill tolerance calculation: tnom = tm / (100%-12.5%) = 0.4216 / (1-0.125) = 0.4216/0.875 = 0.4818 in.

The next greater (or equal at least to) commercial wall thickness is found from Table 2 of ASME B36.10M "Dimensions and Weights of Welded And Seamless Wrought Steel Pipe" to be 0.6 inch which corresponds to 3" NPS, Sch. XXS.

Notes.

1. The calculations based on design pressure of 3000 psi, if that pressure is the operating, we have to find the design pressure to be used in equation.

2. The allowable tensile strength of material SA106-B is based on considering design temperature of 700 oF, if that temperature is the operating, you have to find the design temperature and find S at that temperature.

3. The solution based on corrosion allowance c = 0.125 in., if there is another value (depends on type of fluid inside the pipe), you have to apply the correct value.

4. We can select another material of low alloy/high alloy or stainless steel with higher tensile strength which result in lowering the value of pipe wall thickness.

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#17
In reply to #16

Re: Designing High-Pressure Pipes

06/27/2009 6:33 AM

Try to solve the problem by selecting a seamless austenitic stainless steel pipe material in accordance with ASME pipe material SA 312 with the optimum grade to withstand pressure, temperature and corrosion, and try to find the required pipe wall thickness and compare with that of SA106 Grade B.

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#19
In reply to #17

Re: Designing High-Pressure Pipes

06/27/2009 8:40 AM

Important Notes.

1. No way to specify a piping system and nominate it with "high pressure" unless you apply the rules of the ASME B31 code.

When we can specify that such a piping system is "high pressure"?

High Pressure is a service for which the owner specifies the use of Chapter IX of ASME B31.3 for piping design and construction …………… considered to be in excess of Class 2500 (6000 psi, 42 MPa). There are no specified pressure limitations for application of these rules. [K300(a)].

2. To find the flange class of the problem at my post #16 :

• Design Pressure, P= 3000 psig

• Design Temperature = 700°F

• Flange Material: SA 105 (compatible with cs pipe material SA 106 Grade B)

For SA 105, and from Table F2-1.1, Group 1.1 of ASME B16.5, the class of flanges is 2500 (not in excess), where the system can withstand a pressure up to 4230 psi, so we can't considered that piping as "high pressure" as per the definition of Chapter IX of ASME code B31.3 .

3. When you select another flange material (in the same time must be compatible with the pipe material) as high alloy or stainless steel, the class of flange shall be lowered.

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#20
In reply to #19

Re: Designing High-Pressure Pipes

06/27/2009 9:47 AM

Complete explain about this, not to much more to say. May be only: What about PWHT, using A 106 and what if Sa 312 (SS) is selected? Very good Mr Adbel

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#26
In reply to #20

Re: Designing High-Pressure Pipes

06/30/2009 2:10 AM

Another example for determination of pipe wall thickness in accordance with ASME B31.3 using pipe material of high alloy stainless steel of ASME SA312 TP310

Given :

• Design Pressure, P = 3000 psig

• Design Temperature: 700°F

• Nominal Pipe Size, NPS 3

• Pipe material: Austenitic Stainless Steel A 312 TP310, Seamless

• Corrosion allowance, c = 0.0625 in. (1/16")

• Mill tolerance = 12.5%

Find : Thickness for internal pressure and nominal thickness.

Data:

tm = t + c

t = PD / 2(SE + PY) (ASME Code B31.3, Para 304.1.2, Eq. 3a)

c = 0.0625 in.

Y = 0.4 (Table 304.1.1)

E = 1.0 (Table 302.3.4 & Appendix A, Table A-1B)

Pipe Outside Diameter, D = 3.5 in. (ASME B36.10M)

S at 700 oF = 18300 psi (Appendix A, Table A-1 )

Wall Thickness Tolerance = 12.5%

Solution:

Calculate P/ SE = (3000 psi)/(18300 psi * 1.0) = 0.1639 < 0.385

Also, P(3000 psi) < 1.25 SE (1.25*18300*1.0 = 22875 psi)

So, we can use the equation:

t = PD / 2(SE + PY) = (3000 psi)(3.5 in.) / [2(18300*1.0 + 3000*0.4)] = 0.1733 in.

• Corrosion allowance calculation: tm = t + c = 0.1733+ 0.0625 = 0.2358 in.

• Mill tolerance calculation: tnom = tm / (100%-12.5%) = 0.2358 / (1-0.125) = 0.2358/0.875 = 0.2694 in.

The next greater (or equal at least to) commercial wall thickness is found from Table 2 of ASME B36.19M "Stainless Steel Pipe" to be 0.3 inch which corresponds to 3" NPS, Sch. 80S.

For pipe material SA 312 TP310, and from Table A-1 of ASME B31.3, the material is characterized by P. No. 8, and as per ASME B31.3, Table 331.1.1 "Requirements for Heat Treatment", the PWHT for all pipe wall thicknesses is not required.

Note. For pipe material SA 106 Grade B, and from Table A-1 of ASME B31.3, the material is characterized by P. No. 1, and as per ASME B31.3, Table 331.1.1 "Requirements for Heat Treatment", the PWHT for pipe wall t ≤ ¾" is not required as per code (pipe wall thickness of first example t = 0.6 in . t ≤ ¾" ).

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#27
In reply to #26

Re: Designing High-Pressure Pipes

06/30/2009 4:38 PM

Now that is what I call a whole set of very good answers from Mr. Abdel Halim Galala my friend. I have never gave the same poster three GA's at once but I believe you deserve them for those answers. While some would not even answer the posters question and automatically assumed that the OP shouldn't even ask such a question because of safety worries you answered the question exactly and delivered better than most. Your knowledge of the ASME codes is truly impressive. I personally have never worked on the design side of such high temp. and pressure oil other than maybe fitting and welding on high pressure pipe in refineries and chemical plants in my earlier days. Most of my ASME design and stamp implementation experience is with up to 1500 PSI steam in power generation and paper mills. We never see pipe systems with anywhere near those kinds of pressures.

The safety issue with this question is huge and like the others have already said any one wrong move in any aspect of designing, installing, maintaining and operating such a system could be devastating to anyone and/or anything around it. I am not sure why anyone would even want to put an oil under that pressure and temp. and then contain it in a pipe around someone or something living. I was wondering if anyone could give me an example of what would this or a similar high pressure pipe system be used for?

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#28
In reply to #27

Re: Designing High-Pressure Pipes

06/30/2009 9:26 PM

I have been torn between voicing my opinion and staying quiet, and the opinioniated side has won out -

I do not want to come across as demeaning/condescending/ etc ...... because I truly do respect Mr. Galala's knowledge and expertise, plus his ability and desire to help others out. However, I believe that a little knowledge is a dangerous thing!!

This thread only covers one aspect of piping design; what has been left out for a proper/thorough design is, and not limited to: branch connections, welding, NDE, pressure testing, supports, local stresses, thermal expansion, wind, seismic, fatigue, bolting, ........

700 degree F & 3000 psi oil is not for the faint of heart.

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#29
In reply to #28

Re: Designing High-Pressure Pipes

06/30/2009 10:36 PM

My sentiments exactly!

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#30
In reply to #27

Re: Designing High-Pressure Pipes

06/30/2009 11:14 PM

I grant you that 700 deg.f and 3000 psi is nothing to sneeze at, but deep submergence vehicles go to much higher pressure. Also, fluids are tame compared to gas. We routinely test gas cylinders at more than 3000 psi. Others test at twice this pressure and firearms develop more than 10 times this pressure. Also, the race is on to develop portable high pressure hydrogen storage for automobiles. We might as well get used to the fact that the world is becoming a more dangerous place.

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#31
In reply to #30

Re: Designing High-Pressure Pipes

06/30/2009 11:41 PM

Fair enough, and partly true -

I would hazard a guess that 700 F is above the atmospheric boiling point of the oil, and because of that, if a leak developed it would instantaneously flash into vapour (a highly explosive vapour at that); and 700 F is almost assuredly above the fire point of that oil. And possibly over the autoignition temperature.

Note: I work around an operating pressure of 5500 psig syngas - 75% hydrogen.

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#32
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Re: Designing High-Pressure Pipes

07/01/2009 2:24 AM

And I am not talking about small lab scale stuff - I am talking about a few of these smaller beasts for our pressures/volume:

*******

Plus a couple larger 10 cylinder monsters.

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#22
In reply to #19

Re: Designing High-Pressure Pipes

06/27/2009 12:17 PM

I think this is the kind of answer the OP need.

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#24
In reply to #19

Re: Designing High-Pressure Pipes

06/27/2009 8:40 PM

Another great explanation from a great guru.

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#21
In reply to #16

Re: Designing High-Pressure Pipes

06/27/2009 9:47 AM

Brilliant answer Abdel! Up to your usual high standard.

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#18

Re: Designing High-Pressure Pipes

06/27/2009 8:07 AM

You don't state how much of this pipe you require, but if it's a short length, I suggest you locate a surplus 76mm cannon barrel.

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#23

Re: Designing High-Pressure Pipes

06/27/2009 1:17 PM

Thanks to all who expressed their support especially Mr Abdel. Obviously I know than the process conditions can cause a very unpleasant incident if a pipe or flange fails. I just wanted to know which factors could miss out.

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#25

Re: Designing High-Pressure Pipes

06/29/2009 12:33 PM

This is only the beginning...

I would assume that somewhere, this section of pipe is to be connected to a flange of some sort. Therefore:

  • the proper gaskets would need to be selected,
  • adequate flanges would need to be chosen,
  • bolt material must be defined,
  • bolt loads would have to be calculated,
  • applicable and precise bolting methods would have to be specified and,
  • a Bolting Operation QA process would have to be implemented

It's much more fun than simply designing the pipe

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