4.3 Article

Employing enhanced geometries in water bath heating system of natural gas pressure drop stations: Comparative study

Journal

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.jngse.2020.103775

Keywords

Natural gas pressure drop station; Heating system; Twisted-insert; Twisted-tube; Corrugated-tube

Funding

  1. Islamic Azad University (IAU) Shahrood Branch and Golestan Province Gas Company

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Three enhanced geometries (TI, TT, and CT) are proposed to enhance thermal performance and reduce fuel consumption in a pressure drop station. Results show that using enhanced models can significantly increase NG temperature, but also increase pressure drop. Enhanced models can effectively reduce the length of the pipeline.
In pressure drop stations (PDSs), the natural gas (NG) is heated before its pressure is reduced. It is commonly performed in a water bath heating system equipped with a serpentine-shaped pipe-line and a fire tube. A part of NG is burned in the fire tube, and the produced heat is transferred to water as heat transfer media. Then, the NG following through the pipe-line achieves the heat, and its temperature goes up. In this study, three enhanced geometries, namely twisted-insert (TI), twisted-tube (TT), and corrugated-tube (CT), are proposed to enhance thermal performance of the pipe-line and reduce fuel consumption of the heating system. Firstly, the obtained results are validated with data collected from a real PDS with the capacity of 1000 m(3)/h. It is found that the mean deviation between the current results and the real data is less than 1%. Then, the enhanced models are examined at three different levels of the specific design factor, i.e. ratio of 360 degrees twist-pitch (or wave-length) to straight-section. It is found that replacing an enhanced model with the reference model can noticeably affect both thermal and hydraulic characteristics of the pipe-line. For given operating conditions, the use of the TI, TT, and CT models can enhance the NG temperature by about 6, 2, and 3 K compared to the reference model. At the same time, the pressure drop of the NG increases about 10, 7, and 12 times higher than the reference model. As a rule of thumb, the TI, TT, and CT models can reduce the length of the pipe-line by about 50%, 25%, and 37.5%, respectively.

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