Pilot Plant Results with Piperazine

被引:17
作者
Chen, Eric [2 ]
Madan, Tarun [1 ]
Sachde, Darschan [1 ]
Walters, Matthew S. [1 ]
Nielsen, Paul [1 ]
Rochelle, Gary T. [1 ]
机构
[1] Univ Texas Austin, Dept Chem Engn, Luminant Carbon Management Program, 200 E Dean Keeton St Stop CO400, Austin, TX 78712 USA
[2] Univ Texas Austin, Capture Pilot Plant Project CO2, Austin, TX 78758 USA
来源
GHGT-11 | 2013年 / 37卷
关键词
CO2; pilot plant; concentrated piperazine; high temperature two-stage flash;
D O I
10.1016/j.egypro.2013.06.033
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
Concentrated (40 wt %) piperazine (PZ) with two-stage flash regeneration is an advanced second generation amine-based process for CO2 capture. Two pilot campaigns with the two-stage flash process were completed in 2011 and successfully demonstrated high temperature stripping at 150 degrees C with concentrated piperazine. Data reconciliation for the absorber with intercooling return spray was completed using Aspen Plus (R) Data-Fit. Data reconciliation for the two-stage flash with warm rich bypass was completed using Aspen Plus (R) Data-Fit and a dynamic model developed in MATLAB (R). The results of data reconciliation analysis found that the CO2 loading in the lean and rich streams needed to be systematically shifted upward, 4.6-4.7 % in the stripper analysis and 7.5% in the absorber analysis. An analysis of the October 2011 campaign pilot plant data identified the two configurations with the lowest equivalent work as the high temperature two-stage flash with warm rich bypass and low pressure simple stripper. The calculated equivalent work for the two-stage flash with warm rich bypass from raw pilot plant data and reconciled pilot plant data is approximately 35 kJ/mol CO2 and 36.6 kJ/mol CO2, respectively. Intercooling with a spray return improved absorber CO2 removal performance by 6-7% at the lower gas rates and was found to be equivalent to a 720% increase in packing height based on reconciled data results. Warm rich bypass to the low pressure flash tank reduced piperazine volatility by factor of two in the condensate. In addition, analysis of the pilot plant piperazine inventory at the end of the campaign identified the following degradation products (mmol/kg): N-formyl PZ (1.3), ethylenediamine (13), aminoethylpiperazine (3.6), Hydroxyethylpiperazine (3.9), formate (1.0), and N-nitrosopiperazine (0.09). The solvent analysis also found that the CO2 capacity has decreased by 17%, with a slight decrease in CO2 absorption rate and heat of vaporization. (C) 2013 The Authors. Published by Elsevier Ltd. Open access under CC BY-NC-ND license. Selection and/or peer-review under responsibility of GHGT
引用
收藏
页码:1572 / 1583
页数:12
相关论文
共 6 条
  • [1] Carbon dioxide capture with concentrated, aqueous piperazine
    Freeman, Stephanie A.
    Dugas, Ross
    Van Wagener, David H.
    Nguyen, Thu
    Rochelle, Gary T.
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2010, 4 (02) : 119 - 124
  • [2] Nielsen PT, 2013, ENERGY PROCEDIA
  • [3] Aqueous piperazine as the new standard for CO2 capture technology
    Rochelle, Gary
    Chen, Eric
    Freeman, Stephanie
    Van Wagener, David
    Xu, Qing
    Voice, Alexander
    [J]. CHEMICAL ENGINEERING JOURNAL, 2011, 171 (03) : 725 - 733
  • [4] Sachde D, 2013, ENERGY PROCEDIA
  • [5] Van Wagener D.H., 2011, THESIS
  • [6] Walters MS, 2013, ENERGY PROCEDIA