A heat exchanger fault diagnosis system and method based on temperature and pressure signal monitoring
A fault diagnosis system and pressure signal technology, applied in the direction of instruments, measuring devices, machine/structural component testing, etc., can solve problems such as poor accuracy of fault diagnosis
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specific Embodiment approach 1
[0240] Specific implementation mode one: combine figure 1 Describe this embodiment, the structure of a heat exchanger fault diagnosis system based on temperature and pressure signal monitoring described in this embodiment is that a temperature sensor 3 and a pressure sensor 7 are arranged on the heat exchange medium-inlet pipe of the heat exchanger 15 and the pressure sensor 11 (the distance between the pressure sensor 7 and the pressure sensor 11 needs to ensure that the pressure difference between the two is relatively obvious, reaching more than 10 times the measurement error of the pressure gauge), and the outlet pipeline is provided with a temperature sensor 4 , pressure sensor 8. A temperature sensor 6 and a pressure sensor 10 are arranged on the heat exchange medium inlet pipe of the heat exchanger, and a temperature sensor 5 and a pressure sensor 9 are arranged on the outlet pipe. The 4 temperature sensors and 5 pressure sensors are connected with the fault diagnostic ...
specific Embodiment approach 2
[0299] Specific implementation mode two: combination figure 2 This embodiment is described. The difference between this embodiment and the first embodiment is that a resistance standard 13 is provided between the pressure sensor 11 and the pressure sensor 7 . In the first embodiment, in order to ensure that the pressure difference between the pressure sensor 11 and the pressure sensor 7 is relatively obvious, the distance between the two pressure sensors is generally required to be relatively long, which is difficult to achieve in some actual situations, and the data sensing The wires are also longer, which is a disadvantage. After the resistance standard part 13 is set, the two pressure sensors can be arranged closer together, and the data lines are also shorter. Others are the same as in the first embodiment.
specific Embodiment approach 3
[0300] Specific implementation mode three: combination image 3 This embodiment is described. The difference between this embodiment and the first embodiment is that a pressure sensor 12 is provided downstream of the pressure sensor 9 at the outlet of the heat exchange medium two. Simultaneously:
[0301] 1. Modify the formula for calculating the pressure difference outside the heat exchange medium 2 under the condition of no failure:
[0302] ΔP s2(k) =P 9(k) -P 12(k) (1≤k≤M)
[0303] 2. Modify the formula for calculating the external pressure difference of heat exchange medium 2 under actual operating conditions as:
[0304] ΔP s2 =P 9 -P 12
[0305] 3. Modify the selected ΔP s1(i) and ΔP s2(k) As the identification parameter of (i, k) working condition. That is, when querying the fault-free working conditions corresponding to the actual operating conditions, firstly, in the data sequence ΔP s1(i) The external pressure difference data ΔP found in the actual oper...
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