Introduction
Direct fired heaters are used extensively in the oil refining and chemical process industries. In many instances, those heaters are relied on to heat hydrocarbon liquids or gases to temperatures of 900 to 1500°F or higher. At those temperatures, the stationary fluid film on the inside tube surfaces is subject to thermal decomposition, resulting in the deposition of coke at that location. The coke layer behaves as an insulating barrier between the process fluid and the tube wall, gradually increasing in thickness; this causes the tube wall to reach higher and higher temperatures to transfer the required heat input to the fluid. With the passage of a sufficient amount of time, the tube wall temperature reaches the design temperature, and tube damage occurs if operation at design throughput is continued. At that point, the heater must be shut down and the coke deposits removed. This is accomplished mechanically by “pigging,” the process of passing a cleaning plug driven by fluid pressure through the tubes by using compressed air–driven rotary cutting tools passed through the tubes by an armored compressed air cable, or by controlled burning of the coke at a high temperature—about 1300°F—in an oxygen-rich atmosphere. The interval between the start-up with clean tubes and the shutdown for decoking is termed the run length.



