Can someone provide some examples of reliable and accurate thermocouple and thermowell configurations applied to piping? I am most interested in the mechanical layout and sizing as opposed to the interaction of the sensor and electronics.
I am aiming to minimize heat leak to the process fluid (LNG in this case) and to decrease thermal resistance between the sensor and process fluid. One requirement that makes this difficult is the need for serviceable sensors. Currently T-type 1/4" DIA insertion probes are being used in thermowells similar to those on the site listed below.
In the extreme case of improved performance, a bare sensor could be put in the process stream, but that would be very risky. (reliability, serviceability, damage to downstream equip if it fails, etc.)
I am aiming to minimize heat leak to the process fluid (LNG in this case) and to decrease thermal resistance between the sensor and process fluid. One requirement that makes this difficult is the need for serviceable sensors. Currently T-type 1/4" DIA insertion probes are being used in thermowells similar to those on the site listed below.
In the extreme case of improved performance, a bare sensor could be put in the process stream, but that would be very risky. (reliability, serviceability, damage to downstream equip if it fails, etc.)