We have 42'' pipeline salesgas, thickness is 25.4 mm., velocity max 12.2 m/sec.What is the Thermowell immersion length required for best accuracy? Is there any length limitation for gas application?
Is there any velocity collars required?
Pls help me
I don't pretend to be a flow expert.
For liquids I normally insert the thermowell just a couple of inches. with turbulent flow the temperature profile is even, I think with gas I would go about 4 inches.
A lot of guys like to get right in the center of the pipe but if you are not careful the vortex shedding around the probe will put too much stress on the well. I know Rosemount will calculate the likelihood of that happening if you ask.
Bear in mind also that the probe insertion length may effect the accuracy of your flow measurement device.
it is for temperature application. Pipe size is 42'' and thickness is 25.4 mm.
since pipe dia is 42'' what will be the insertion length for best accuracy? 300 mm is ok???
for gas application "u" length is 1/3 of the pipe size is required???
The error in the temperature measurement happens in such cases due to a well know phenomena called "conduction error". One side of the thermowell is in the hot fluid (inside the pipe) and the other side (outside the pipe)is at cold atmosphere and therefore, a temperature gradient is established when an equilibrium stage is reached due to heat conduction and radiation from the thermowell. Due to this temperature gradient, the tip of the thermowell will not achieve the same temperature of the fluid (or near to that) unless the thermowell immersion length inside the fluid is sufficiently immersed. A thermodynamic calculation can be done to find out exactly how much should be the thermowell immersion length taking care of many factors.
However, in Industry we normally don't do this calculation. We use a thumb rule whic is - if the thermowell immersion length is 4 times the thermowell tip dia then the temperature mesurement will be sufficiently accurate.
A typical thermowell tip dia is 18 mm and therefore, in my opinion 4 x18 mm i.e. 72 mm inside the pipe will be sufficient to measure the correct temperature. Since your pipe dia is big and there is sufficient room to penetrate more you can increase the thermowell length more to take care of the temperature gradient if the pipeline is not insulated. Normally we use a maximum length of 200 mm in the flowing fluid. But you have to ask your temperature sensor supplier to check the wake frequency calculation so that this immersion length of 200 mm is passed in the stress and wake frequency calculation.
To summarise, in your application, if the pipe nozzle stand out is 200 mm, you need to consider a thermowell with total insertion length:
200 mm + 72 mm = 272 mm minimum
200 mm + 200 mm = 400 mm maximum if allowed by stress & frequency calculation.
Hope this helps.
The longer and skinnier the well, the better for response time and accuracy. The shorter and fatter it is, the stronger it is.
The rule of thumb is to get to the middle third of the pipe, but before accepting that as your immersion length you need to confirm the design strength per ASME PTC 19.3TW-2010. After all it doesn't help that your well is long and skinny if it breaks or the installed sensor fails due to vibration.
You may want to check out at SwiftyCalc www.jms-se.com/swiftycalc
SwiftyCalc is a free software that will provide you with a quick max insertion length and wake frequency calculation result in seconds applying the ASME 19.3TW calculation.
Here is a link to an article that you may find to be helpful:
Does this 1/3 include the nozzle, if so it wouldn't make sense. It would be ok on your large pipe but not on smaller ones
42"/3 = 14"
a typical flanged nozzle has a projection of 6" so the probe would be in the pipe 14-6 = 8"
for a 12" pipe the U would be
12/3 = 4" and the probe wouldn't reach the pipe.
I like Asok Kumar Haits simple formula.
As for the temperature gradient, usually the pipeline is insulated so the nozzle should be very close to the process temperature and there won't be much gradient.
I try to standardize on just a few different "U" lengths so the probe for a 12" pipe would be the same "U" length as the probe for your 42"
> Does this 1/3 include the nozzle,
> I try to standardize on just a few different "U" lengths so the probe for a
> 12" pipe would be the same "U" length as the probe for your 42"
Good practice. You will want to confirm that the design passes the ASME calculation for all conditions at a standard length
Here is new online tool to calculate your thermowell according to ASME
moderator's note: please make sure you delete any spaces in the long url when you cut and paste this in your browser.
you need to specify what is accurate enough
along with the temperature, pressure, and whether of not the pipe is insulated, including the base of the thermowell.
traditional thermowell length assignments tend to be very risky both from a mechanical integrity point of view, but also in senor reliability and measurement accuracy.
There are special thermowells suited to low pressure, low velocity gasses, that get past the longer is better scenario, but they are typically quite short.
I need to size thermowells for pipe from DN65 to DN700 (air application, velocity around 30m/s, pressure below between 0bar g and 1bar g).
Thermowell data type:
Shank profile: straight
mounting: by threaded 1/2
Problem is my thermowell geometry is out of scope of ASME PTC 19.3TW-2010. support diameter is identical to tip diameter (9mm). Support diameter mini is 15.8mm in ASME code.
Since velocity looks high (i think?) I must check that a thermowell length of ~1/3 1/2 of the pipe Ø fits well.