填料塔中的NaOH水溶液脱除空气中微量CO2的传质动力学

在填料吸收塔中测定了25℃时NaOH水溶液吸收空气中微量CO2的体积传质总系数(KGαv)．并研究了进口气体中CO2的含量、气体流量、吸收液喷淋密度以及NaOH浓度对体积传质总系数的影响。进口气体中CO2的含量、气体流量、吸收液喷淋密度对KGαv的影响较小;NaOH浓度对KGαv的影响较大,随着NaOH浓度的增加,KGαv显著提高。     

超(亚)临界CO2中涂料基体的相行为研究

The high-pressure phase behavior of coating -solvent-supercritical or sub-critical carbon dioxide system was investigated experimentally.The coating matrix used was 108-acrylic resin at concentration raging from 10% to 50%(by mass) in mixtures with n-butyl acetate ,The experiments were conducted in a high-pressure view cell for temperatures from 35℃to 65 ℃ and for pressures from 3.0 MPa to 8.0 MPa ,The effect of temperature,pressure and content of every component on the phase behavior of the systems was observed,Finally ,the ternary phase diagram for resin-solvent-CO2 was plotted.     

对数回归模型在CO2提纯塔控制中的应用

利用对数回归方法建立了成品CO2浓度与提纯塔影响因素之间的非线性回归模型，经检验回归方程与回归系数均有较好的显著性。同时，利用改进单纯形法寻找CO3浓度达到99．5％左右时的最佳控制点，得到了令人满意的结果。     

液膜分离二氧化碳气体的研究进展

简要回顾了分离二氧化碳气体的研究现状,分析了液膜种类、结构和传质过程,介绍了近年来改进液膜稳定性方面的发展,并展望了液膜分离二氧化碳气体的前景。     

膜气体吸收法脱除电厂模拟烟气CO_2

介绍了化学吸收法、物理吸收法、吸附法、膜分离法、膜吸收法和低温蒸馏法等烟气减排技术,综述了近几年气体吸收膜法在减少电厂模拟烟气CO2排放中的研究进展及福建省膜研究开发情况,总结了气体吸收膜法发展与应用中存在的不足,指出膜气体吸收法的发展前景。     

A Flat Polymeric Membrane Sensor for Carbon Dioxide/Nitrogen Gas Mixture

A gas sensor was developed to measure the concentration of binary gas mixtures. This sensor works based on the permeability change of different gas mixtures across the polymeric membranes. Although high values of permeability and selectivity are needed for an ideal separation, the performance of this sensor mainly depends on the permeability factor. Polysulfone and silicone rubber were applied as the membrane base and coat, respectively. Moreover, in contrast to existing polymeric sensors that use hollow fibers, the present sensor is made of flat membranes. This new design is cheaper, smaller, and easier to use in comparison to the hollow fiber polymeric sensors. In order to test the sensor applicability, nitrogen and carbon dioxide were used as model gases. The effect of pressure on the response time and sensor accuracy was studied for the aforementioned gases. The response time (T_95%) of this low price sensor was 50?s, and the tolerance of measuring concentration was approximately 1.4% at 2?bar feed pressure. Also, increasing the feed pressure can improve the response time or accuracy of the sensor.     

CO2 Capture Using Activated Amino Acid Salt Solutions in a Membrane Contactor

An activated solution based on amino acid salt was proposed as a CO₂ absorbent. Piperazine (PZ) was selected as an activating agent and added into the aqueous glycine salt to form the activated solution. A coupling process, which associated the activated solution with a PP hollow fiber membrane contactor, was set up. An experimental and theoretical analysis for CO₂ capture was performed. The performances of CO₂ capture by the coupling process were evaluated using the PZ activated solution and the non-activated glycine salt solution. A numerical model for the simulation of the hollow fiber membrane gas–liquid mass transfer was developed. Typical parameters such as outlet gas phase CO₂ concentration, capture efficiency, and mass transfer coefficient for the activated solution were determined experimentally. The effects of operation temperature and liquid CO₂-loading on mass transfer coefficient and capture efficiency were discussed in this work. Axial and radial concentration profiles of CO₂ in the fiber lumen and mass transfer flux were simulated by the model. Results show that the performances of the PZ activated glycine salt solution are evidently better than that of the non-activated glycine salt solution in the membrane contactor for CO₂ capture. Elevation of the operation temperatures can enhance the overall mass transfer coefficient. The activated solution can maintain higher capture efficiency especially in the case of high CO₂-loadings. The gas phase CO₂ concentration with the activated solution is lower than that with the non-activated solution whether along axial or radial distances in the fiber lumen. The model simulation is validated with experimental data.     

回收脱碳闪蒸气及二氧化碳的利用

对碳酸丙烯酯为吸收剂的脱碳工艺,其闪蒸气的放空量和气体成分进行了计算,简述了回暇闪蒸气的重要,重点介绍了ＣＯ２气体的开放利用。     

PTFE多孔膜气体渗透数学模型和膜孔结构的影响

Membrane-based separation processes are new technology combined membrane separation with conventional separation. Hydrophobic porous membranes are often used in these processes. The structure of hydrophobic porous membrane has significant effect on mass transfer process. The permeabilities of five kinds of gas, He, N2,O2, CO2 and water vapor, across six polytetrafluoroethylene(PTFE) fiat membranes were tested experimentally.Results indicated that the greater the membrane mean pore size and the wider the pore size distribution are, the higher the gas permeability. A gas permeation model, including the effects of membrane structure parameter and gas properties, was established. A comprehensive characteristic parameter (including porosity, thickness and tortuosity) was found more effective to express the influence of membrane structure in gas permeation process. The predicted permeation coefficients were in good agreement with experimental data.     

富含二氧化碳的天然气分离及其利用

论述了国内外对富含二氧化碳的天然气分离技术的研究进展,包括：膜分离法、变压吸附（PSA）法、物理吸收法和化学吸收法等,并分析了天然气资源的深加工利用及其产品开发前景。     

二氧化碳脱除原理及工艺

介绍了脱除空气和烟气中二氧化碳的基本原理和相关工艺。根据二氧化碳的脱除原理,详细的阐述和分析了二氧化碳的脱除方法和相关工艺,并对各种技术最新的发展前景进行了分析。     

中空纤维膜吸收烟气二氧化硫

本文综述了国内外用膜吸收法治理烟气二氧化硫的研究现状,对采用中空纤维膜吸收过程中的膜组件操作方式、吸收剂、膜材料以及工艺参数的选择进行了介绍,并应用双膜理论对中空纤维膜吸收二氧化硫过程中的各分传质系数和总传质系数进行了推导,初步探讨了建立膜吸收过程数学模型的方法。     

聚四氟乙烯膜气体吸收数学模型和孔隙率的影响

膜吸收是将膜分离与传统的吸收技术相结合的一种新型分离技术。在这些过程中经常使用多孔膜,多孔膜对过程的传质性能有一定的影响。对不同孔隙率的微孔聚四氟乙烯(PTFE)疏水性平板膜的膜气体吸收过程中液相传质性能进行了实验研究。当采用去离子水-CO2吸收体系时,多孔膜的孔隙率对液相传质性能没有影响;当采用NaOH水溶液-CO2吸收体系时,多孔膜的孔隙率对液相传质性能有明显的影响。在相同流速下,孔隙率大的膜液相传质系数高于孔隙率小的膜。以双膜理论为指导,建立了多孔膜气体吸收过程中液相传质模型。用该模型描述多孔膜孔隙率对液相传质系数的影响,其结果与实验数据具有良好的一致性。