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Membrane installation for biogas enrichment-Field tests and system simulation

机译:用于沼气浓缩 - 现场测试和系统仿真的膜装置

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The paper presents results of the field tests on membrane biogas enrichment performed with the application of mobile membrane installation (MMI) with the feed stream up to 10 Nm3/h. The mobile installation equipped with four hollow fibre modules with polyimide type membranes was tested at four different biogas plants. Two of them were using agricultural substrates. The third one was constructed at a municipal wastewater plant and sludge was fermented in a digester and finally in the fourth case biogas was extracted from municipal waste landfill site. Differences in the concentration of bio-methane in feed in all cases were observed and trace compounds were detected as well. High selectivity polyimide membranes, in proper module arrangements, can provide a product of high methane content in all cases. The content of other trace compounds, such as hydrogen sulphide, water vapour and oxygen on the product did not exceed the values stated by standard for a biogas as a vehicle fuel. The traces of hydrogen sulphide and water vapour penetrated faster to the waste stream enriched in carbon dioxide, which could lead to further purification of the product-methane being hold in the retentate (H2O >H2S >CO2 >O2 >CH4 >N2). In the investigated cases, when concentration of N2 was low and concentration of CH4 higher than 50%, it was possible to upgrade methane to concentration above 90% in a two-stage cascade. To perform simulation of CH4 and CO2 permeation through polyimide membrane, MATLAB was used. Simulation program has included permeation gaseous mixture with methane contents as observed at field tests in the range of 50 and 60% vol. The mass transport process was estimated for a concurrent hollow fibre membrane module for given pressure and temperature conditions and different values of stage cut. The obtained results show good agreement with the experimental data. The highest degree of methane recovery was obtained with gas concentrating in a cascade with recycling of the retentate.
机译:本文介绍了使用移动膜装置(MMI)的膜沼气富集的野外试验结果,其进料流高达10nm3 / h。在四种不同的沼气厂测试了配备有聚酰亚胺型膜的四个中空纤维模块的移动装置。其中两个是使用农业基材。第三个是在市政废水植物中构建的,污泥在消化器中发酵,最后在第四种情况下从城市废物填埋场中提取沼气。观察到所有病例中的生物甲烷浓度的差异,也检测到痕量化合物。在适当的模块布置中,高选择性聚酰亚胺膜可以在所有情况下提供高甲烷含量的产物。其他痕量化合物的含量,例如硫化氢,水蒸气和氧气上的产物上的含量不超过沼气标准作为车辆燃料所陈述的值。硫化氢和水蒸气的痕量渗透到富含二氧化碳的废物流,这可能导致在滞留物(H2O> H 2 S> CO 2> O 2> CH 4> O 2)中的产物 - 甲烷进一步纯化。在研究病例中,当N 2的浓度低并且CH4的浓度高于50%时,可以在两级级联中将甲烷升高至90%以上。使用聚酰亚胺膜进行CH4和CO2渗透的模拟,使用MATLAB。仿真程序已经包括在50和60%Vol范围内观察到的甲烷含量的渗透气体混合物。对于给定压力和温度条件和阶段切割的不同值,估计了传质过程的估计。所获得的结果与实验数据吻合良好。通过级联的气体浓缩,在级联中获得最高程度的甲烷回收率。

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