Optimization Design and Performance Study of a Heat Exchanger for an Oil and Gas Recovery System in an Oil Depot

• Published in: Energies (Basel) 2024-06, Vol.17 (11), p.2631
• Main Authors: Chen, Zengliang, Luo, Ye, Wang, Zhihui, Liu, Yulin, Gai, Limei, Wang, Qichao, Hong, Bingyuan
• Format: Article
• Language: English
• Subjects: Activated carbon; Adsorption; CFD; Design optimization; Efficiency; Energy conservation; Energy consumption; Environmental protection; Equipment and supplies; Fluid dynamics; Heat exchangers; Heat transfer; Heating; High temperature; Natural gas; oil and gas recovery; oil depot; optimization design; Performance evaluation; Petroleum mining; Research methodology; Simulation; Synthesis gas
• ISSN: 1996-1073; 1996-1073
• DOI: 10.3390/en17112631

High summer temperatures pose numerous challenges to the oil and gas recovery process in oil depots, including reduced adsorption tank recovery rates and decreased absorption tower desorption efficiency. This paper introduces a coupling design approach that integrates chemical process design with computational fluid dynamics simulation. The proposed approach is then utilized to investigate the optimal design and performance of the heat exchanger within the oil depot’s oil and gas recovery system. First, according to the given process design parameters, the heat exchanger is preliminary designed to determine the required heat exchange area and heat load. Based on the preliminary design results, a detailed design is carried out, resulting in the following calculations: the hot fluid has inlet and outlet temperatures of 40 °C and 29.52 °C, respectively, with an outlet flow velocity of 9.89 m/s. The cold fluid exhibits inlet and outlet temperatures of 25 °C and 26.98 °C, respectively, with an outlet flow velocity of 0.06 m/s. The specific structure and dimensions of the heat exchanger are determined, including the shell type, pipe specifications, and pipe length. Finally, CFD numerical simulation is utilized to analyze the flow field, velocity field, and pressure field within the designed heat exchanger. The calculations reveal the following findings: the hot fluid exhibited inlet and outlet temperatures of 40 °C and 29.54 °C, respectively, along with an outlet flow velocity of 9.94 m/s. On the other hand, the cold fluid shows inlet and outlet temperatures of 25 °C and 26.39 °C, respectively, with an outlet flow velocity of 0.061 m/s. The results show that the chemical process design and CFD numerical simulation results are consistent and can be mutually verified. The designed heat exchanger can efficiently cool oil and gas from 40 °C to 30 °C, and the oil and gas processing capacity can reach 870 m3/h, which is conducive to realizing the goals of energy saving, environmental protection, and safety.