Are there any calculations for the device’s flare header?
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Are there any calculations for the device’s flare header?
You can refer to HG/T50270.12-95 on the design of flare systems, which outlines the methods and regulations for designing flare headers.
The Mach number of the torch main pipe should preferably not exceed 0.4
Are there any calculations related to the flare main pipe of the facility? It should be a question about how to calculate the flare main pipe of the facility. Actually, it’s quite simple: the pressure entering the flare system is taken as the water seal pressure plus various resistances such as those associated with the tank’s flare head; these resistances are usually considered to be 900 mmH2O. The gas volume flowing through the flare main pipe corresponds to the maximum volume of gas handled by the facility. The discharge pressure at the starting point is assumed to be less than 0.1 MPa. With this information, it’s possible to determine the pipe diameter. Once the pipe diameter is known, the pressure drop can be calculated accordingly
Thank you. The company is working on a flare, but unfortunately there is still a lot of black smoke, and it does not meet our company’s emission standards. It can only be used as a burner
Which companies are doing well in torches nowadays? ? ? The Luoyang branch is okay, right?