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A Multiscale Approach for Modeling Oxygen Production by Adsorption

机译:一种多尺度模拟吸附制氧的方法

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Oxygen production processes using adsorbents for application to CCS technologies (Carbon Capture and Storage) offer potential cost benefits over classical cryogenics. In order to model adsorption processes an approach using three size scales has been developed. This work is being conducted in the framework of the DECARBit European research project. The first scale is at the size of the oxygen adsorption bed to be modelled as a vertical cylinder filled with pellets. Its length is 0.2 m (scale 10-1 m). The bed is homogeneous in the transversal direction so that the problem is 1D (independent variables t, x). The physics in the process include gas species (Cbk (t, x)) convection and dispersion, thermal convection and conduction (T(t, x)) and hydrodynamics (v(t, x)). The gas constituents involved are N2, 02, CO2 and H2O. The second scale is at the size of the pellets that fill the adsorber and which are assumed to be of spherical shape with a typical radius of 5 mm (scale 10-3 m). The independent variable for the pellets is the radius “rp”. At a certain height (x) down in the adsorber all the pellets are the same and are surrounded by the same gas composition but inside the pellets the concentrations may vary. The state variables for the inner part of the pellets are the gas concentrations Cpk(t, x, rp). The pellets are so small that they are assumed to have a uniform temperature. This leads to a 2D transient model for the pellets linked to the 1D transient model for the bulk. The third scale looks into the detailed structure of the pellets that are made of perovskite crystallites. The latter are assumed to be spherical. Oxygen adsorption occurs in the crystallites which have a radius of about 0.5 pm (scale 10-7 m). All the crystallites at the same radius in a pellet are supposed to behave the same and because they are spherical, the only independent variable for a crystallite located at (x, rp) is its radius “rc”. The state variables for the crystallites are then the adsorbed oxygen concentration Cc2 (t, x, rp, re). The crystallites are so small that they are assumed to have a uniform temperature. This leads to a third transient model that is 3D for the crystallite and is linked to the 2D transient model for the pellets which is itself linked to the 1D transient models for the bulk. From the larger to the lower scales, the links between the three models are the following: the bulk concentration and temperature give the boundary conditions surrounding the pellets. The pellet concentration gives the boundary conditions for the crystallites. We chose to solve this multiscale approach that requires the coupling of models of different dimensions in Comsol Multiphysics. The simulator was built to gain knowledge from laboratory experiments in order to estimate whether oxygen separation from air is realistic or not.
机译:使用吸附剂的氧气生产过程应用于CCS技术(碳捕获和储存)比传统的低温技术具有潜在的成本优势。为了模拟吸附过程,已经开发了使用三种尺寸标度的方法。这项工作是在DECARBit欧洲研究项目的框架内进行的。第一个比例是氧气吸附床的尺寸,该尺寸将被建模为充满颗粒的垂直圆柱体。它的长度是0.2 m(比例尺10-1 m)。床在横向方向上是均匀的,因此问题是1D(独立变量t,x)。过程中的物理学包括气体种类(Cbk(t,x))的对流和弥散,热对流和传导(T(t,x))和流体动力学(v(t,x))。涉及的气体成分是N2,O2,CO2和H2O。第二刻度是填充到吸附器中的小球的尺寸,假定为球形,典型半径为5 mm(刻度10-3 m)。颗粒的自变量是半径“ rp”。在吸附器中一定高度(x)处,所有颗粒都是相同的,并且被相同的气体组成所包围,但是颗粒内部的浓度可能会发生变化。颗粒内部的状态变量是气体浓度Cpk(t,x,rp)。颗粒是如此之小,以至于它们被认为具有均匀的温度。这将导致颗粒的2D瞬态模型与块料的1D瞬态模型链接。第三个比例调查了钙钛矿微晶制成的颗粒的详细结构。后者被假定为球形。氧气吸附发生在半径约为0.5 pm(范围为10-7 m)的微晶中。颗粒中半径相同的所有微晶都应具有相同的性能,并且由于它们是球形的,位于(x,rp)处的微晶唯一的独立变量是其半径“ rc”。然后,微晶的状态变量是吸附的氧气浓度Cc2(t,x,rp,re)。微晶是如此之小,以至于它们被认为具有均匀的温度。这导致了第三个瞬态模型,该模型是微晶的3D模型,并链接到小球的2D瞬态模型,而该模型本身又与块体的1D瞬态模型相关。从大到小,三个模型之间的联系如下:堆肥的浓度和温度给出了颗粒周围的边界条件。粒料浓度给出了微晶的边界条件。我们选择解决这种多尺度方法,该方法要求在Comsol Multiphysics中耦合不同维度的模型。该模拟器的建立是为了从实验室实验中获取知识,以便估计与空气中的氧气分离是否现实。

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