海洋工程装备与技术 ›› 2015, Vol. 2 ›› Issue (3): 152-156.

• 海洋油气勘探开发技术与装备 • 上一篇    下一篇

丙烷预冷双氮膨胀浮式天然气液化中试装置的规模分析研究

刘淼儿, 李恩道, 尹全森, 邰晓亮   

  1. 中海石油气电集团技术研发中心,北京 100028
  • 收稿日期:2015-05-16 出版日期:2015-06-10 发布日期:2016-01-21
  • 作者简介:

    作者简介:刘淼儿(1973-),男,博士,高级工程师,主要从事天然气液化及液化天然气储存、运输与利用方面的研究。

  • 基金资助:
    国家科技重大专项(2011ZX05026-006)

Study on the Pilot Plant’s Capacity of Floating Liquefied Natural Gas Processed by Propane Pre-Cooling and Dual-Nitrogen-Expansion Sub-Cooling

Miao-er LIU, En-dao LI, Quan-sen YIN, Xiao-liang TAI   

  1. Research & Development Center of CNOOC Gas & Power Group, Beijing 100028, China
  • Received:2015-05-16 Online:2015-06-10 Published:2016-01-21

摘要:

以应用于海上的浮式丙烷预冷双氮膨胀液化装置为原型,拟建设一套液化中试装置。为了确定液化中试装置的规模,提出中试装置与原型装置之间宜遵循流程一致性、关键控制方式一致性、运动相似性和流态相似性等四项原则。上述原则中,分析表明,对于除关键控制方式一致性外,流程一致性、运动相似性和流态相似性对中试装置的规模没有直接的影响。为了与原型装置的关键控制方式保持一致,中试装置的设备选型就显得非常重要,其中对于确定规模影响较大的关键设备为制冷剂压缩机,而冷箱、压缩机驱动器、透平膨胀机及丙烷换热器对规模影响不大。因此,建议中试装置中压缩机的型式与浮式天然气液化装置保持一致,冷箱中换热芯体可以考虑采用两台并联的设计方案。

关键词: 浮式天然气液化装置, 中试装置, 规模, 液化工艺, 丙烷预冷, 双氮膨胀

Abstract:

Based on the propane pre-cooling and dual-nitrogen-expansion sub-cooling (C3-DN2) process used for floating liquefied natural gas production, storage and offloading unit (LNG-FPSO), a pilot unit will be built to test the rationality of process configuration and key control modes, and to study the operability and flexibility of its application in offshore cases. In order to define the capacity, the pilot unit should keep the consistency of process configurations and key control modes, and the similarity of moving and flow regime with LNG-FPSO. The factors affecting the capacity of the pilot unit are further investigated, and the results show that the type of key equipment to keep the consistency of key control mode greatly impacts the capacity, and the other factors have less influence. Among the main devices, the refrigerant compressor should be considered the most carefully when defining the capacity of the pilot unit, and others such as cold box, driver, turbine expander and the heat exchanger for C3 are less important. Therefore, it is better to select the same type of refrigerant compressor in the pilot as that in the LNG-FPSO, and to design two plate-fin heat exchangers in parallel in the cold box.

Key words: floating liquefied natural gas system, pilot unit, capacity, liquefaction process, propane pre-cooling, dual-nitrogen-expansion sub-cooling

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