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A novel experimental apparatus for the study of low temperature regeneration CO2 capture solvents using hollow fibre membrane contactors

机译:一种新型实验装置,用于使用中空纤维膜接触器研究低温再生CO2捕获溶剂

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摘要

The design, capability and construction of a novel, experimental apparatus for the study of low temperature regeneration CO2 capture agents is presented. The decisions and challenges in developing a new experimental capability are discussed, as well as how it addresses the experimental intermediate between bench scale experiments and large, application specific projects. To demonstrate the utility and capability of the apparatus, a low temperature regenerating CO2 capture protic ionic liquid (PIL) solution - dimethylpropylenediamine acetate + 50% H2O - was used to remove CO(2 )from an incoming gas stream consisting of 10% (v/v) CO2 in air. SuperPhobic (R) 2.5 x 8 hollow fibre membrane contactors were used for both the absorption and regeneration processes. The loading-only experiment achieved pseudo steady state in approximately 12 min, achieving a pseudo steady-state mass transfer rate (K-overall) of (3.66 +/- 0.2) x 10(-5) m s(-1), and a CO(2 )removal rate of 5.15 x 10(-3) g M-2 s(-1). This value is comparable to other ionic liquid CO2 capture agents such as 1-ethyl-3-methylimidazolium ethylsulfate that have also been measured under pseudo-steady state conditions. In continuous operation, where CO2 is absorbed and stripped in series, steady-state was achieved in approximately 15 h. Due to the higher concentration of CO(2 )in the liquid under steady-state conditions, the value of K overall decreased to (1.80 +/- 0.1) x 10(-5) m s(-1), with a CO2 removal rate of 2.89 x 10(-3) g m(-2) s(-1). The effects of several parameters on the steady-state CO(2 )capture rate, namely vacuum pressure of regeneration and liquid flow through the contactor were studied. Several factors were found to affect the stability of the overall CO(2 )removal rate, including H2O loss from the aqueous solution. With the utility and flexibility of the designed system, we have demonstrated that PILs are certainly worthy of further investigation as CO2 capture agents for a range of applications.
机译:提出了一种用于研究低温再生CO2捕获剂的新颖的设计,能力和结构。讨论了开发新的实验能力方面的决策和挑战,以及如何解决工作台规模实验和大型应用特定项目之间的实验中间。为了证明该装置的实用性和能力,使用低温再生CO 2捕获质子离子液体(PIL)溶液 - 二甲基丙二胺乙酸盐+ 50%H 2 O - 用于从10%组成的进入气流中除去CO(2)(V. / v)空气中的二氧化碳。超级(R)2.5×8中空纤维膜接触用于吸收和再生过程。仅在大约12分钟内实现了仅负载实验,实现了(3.66 +/- 0.2)×10(-5)ms(-1)的伪稳态传质速率(K-总体),以及a CO(2)去除率为5.15×10(-3)g m-2 s(-1)。该值与其他离子液体CO 2捕获剂相当,例如在假稳态条件下在伪稳态条件下测量的1-乙基-3-甲基咪唑鎓硫酸盐。在连续操作中,其中CO 2被串联吸收并剥离,在大约15小时内实现稳态。由于稳态条件下液体中较高的CO(2),k的值总体降低至(1.80 +/- 0.1)×10(-5)MS(-1),具有CO 2去除率2.89 x 10(-3)gm(-2)s(-1)。研究了几个参数对稳态Co(2)捕获速率的影响,即通过接触器的再生和液体流动的真空压力。发现了几种因素影响整体CO(2)除去率的稳定性,包括水溶液中的H2O损失。通过设计系统的实用性和灵活性,我们已经证明,PILS肯定值得进一步调查作为一系列应用的CO2捕获剂。

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