Supersonic separation in onshore natural gas dew point plant

被引:70
作者
Machado, Priscilla B. [1 ]
Monteiro, Juliana G. M. [1 ]
Medeiros, Jose L. [1 ]
Epsom, Hugh D. [2 ]
Araujo, Ofelia Q. F. [1 ]
机构
[1] Univ Fed Rio de Janeiro, Escola Quim, BR-21941909 Rio De Janeiro, RJ, Brazil
[2] Twister BV, NL-2289 CC Rijswijk, Netherlands
关键词
Natural gas conditioning; Supersonic separator; TEG plus JT/LTS; HCDP; WDP; Process simulation;
D O I
10.1016/j.jngse.2012.03.001
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Conditioning of natural gas (NG) for sales mainly involves meeting water- and hydrocarbon-dew points (WDP and HCDP, respectively) while assuring high heating value (HHV) specifications achievable through minimal extraction of C5+ components (NGL). This paper compares technically and economically a supersonic separator technology Twiste (R) r, which can promote simultaneously WDP, HCDP and enhanced NGL extraction to a conventional gas treating technology, consisting of an onshore natural gas dew pointing plant with TEG Dehydration unit coupled to a Joule-Thomson/Low Temperature Separation unit (TEG + JT/LTS). In Twister (R) technology, water and hydrocarbon dew pointing normally requires pressure drop, which results in more NGL recovery than necessary to meet the established product specifications. An economic scenario was evaluated with NG and crude oil prices of US$ 4.22/GJ and US$ 50/bbl, respectively. The economic performance of each process alternative is evaluated in terms of the net present value (NPV) after 20 years of operation, with an assumed discounted rate of 10%. Twister based process outperformed conventional TEG + JT/LTS process as the additional revenue from the increased NGL production compensates for the lower revenue from the NG sale resulting from decreased flow rate and lower NG HHV. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:43 / 49
页数:7
相关论文
共 10 条
  • [1] Natural gas processing with membranes: An overview
    Baker, Richard W.
    Lokhandwala, Kaaeid
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (07) : 2109 - 2121
  • [2] Brouwer J. M., 2003, 83977 SOC PETR ENG
  • [3] Campbell J.M., 2004, The Equipment Modules., V2
  • [4] Carroll JJ, 2009, NATURAL GAS HYDRATES: A GUIDE FOR ENGINEERS, 2ND EDITION, P1
  • [5] Dehydration of natural gas using solid desiccants
    Gandhidasan, P
    Al-Farayedhi, AA
    Al-Mubarak, AA
    [J]. ENERGY, 2001, 26 (09) : 855 - 868
  • [6] Herring J., 2010, PIPELINE GAS J, P237
  • [7] Mokhatab S., 2009, GPA EUR SOURC GAS PR
  • [8] NEB National Energy Board, 2008, NAT GAS SUPPL COSTS
  • [9] OPIS, 2010, OPIS NGL FORW REP
  • [10] Turton R., 2009, Analysis, Synthesis and Design of Chemical Processes