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25篇 您的检索式:作者名="Zuwei Yang"
    题名 作者 年代 出处 被引量
1Modelling and simulation of two-bed PSA process for separating H2 from methane steam reforming显示文摘Methane steam reforming is the main hydrogen production method in the industry. The product of methane steam reforming contains H2, CH4, CO and CO2 and is then purified by pressure swing adsorption(PSA) technology. In this study, a layered two-bed PSA process was designed theoretically to purify H2 from methane steam reforming off gas. The effects of adsorption pressure, adsorption time and purgeto-feed ratio(P/F ratio) on process performance were investigated to design a PSA process with more than99.95% purity and 80% recovery. Since the feed composition of the PSA process changes with the upstream process, the effect of the feed composition on the process performance was discussed as well.The result showed that the increase of CH4 concentration, which was the weakest adsorbate, would have a negative impact on product purity.Huiru Li Zuwei Liao Jingyuan Sun Binbo Jiang Jingdai Wang Yongrong Yang 2019Chinese Journal of Chemical Engineering2019,27,8:9
2Recent advances in mammalian reproductive biology显示文摘Reproductive biology is a uniquely important topic since it is about germ cells, which are central for transmitting genetic information from generation to generation. In this review, we discuss recent advances in mammalian germ cell development,including preimplantation development, fetal germ cell development and postnatal development of oocytes and sperm. We also discuss the etiologies of female and male infertility and describe the emerging technologies for studying reproductive biology such as gene editing and single-cell technologies.Lu Wen Qiang Liu Jingjing Xu Xixi Liu Chaoyi Shi Zuwei Yang Yili Zhang Hong Xu Jiang Liu Hui Yang Hefeng Huang Jie Qiao Fuchou Tang Zi-Jiang Chen 2020Science China(Life Sciences)2020,63,1:6
3Modeling and Optimization of Ethane Steam Cracking Process in An Industrial Tubular Reactor with Improved Reaction Scheme显示文摘Ethane steam cracking process in an industrial reactor was investigated.An one-demsional(1D)steady-state model was developed firstly by using an improved molecular reaction scheme and was then simulated in Aspen Plus.A comparison of model results with industrial data and previously reported results showed that the model can predict the process kinetics more accurately.In addition,the validated model was used to study the effects of different process variables,including coil outlet temperature(COT),steam-to-ethane ratio and residence time on ethane conversion,ethylene selectivity,products yields,and coking rate.Finally,steady-state optimization was conducted to the operation of industrial reactor.The COT and steam-to-ethane ratio were taken as decision variables to maximize the annual operational profit.Mohsin Ali Liao Zuwei Yao Yang Sun Jingyuan Jiang Binbo Wang Jingdai Yang Yongrong 2020China Petroleum Processing & Petrochemical Technology2020,22,4:2
4Design and optimization of an integrated MEMS gas chamber with high transmissivity显示文摘Non-Dispersive InfraRed(NDIR)gas sensor is widely used for gas detection in collieries and the gas chemical industry,etc.The performance of the NDIR gas sensor depends on the volume,optical length and transmittance of the gas chamber.However,the existing gas sensor products have problems of large volume,high cost and incapable of integration,which need to develop towards the miniaturized sensor.This paper first presents the theoretical background of the NDIR gas sensor and the novel structure of a fully integrated infrared gas sensor and its micro-machined gas chamber structure.Then,the light structure and the gas flow of the gas chamber are optimized on Tracepro software and Ansys workbench,respectively,and the technological process for preparing the Micro-Electro-Mechanical System(MEMS)gas chamber is designed.Finally,we produce a gas chamber with a small volume and good transmissivity,which would be the most important part of producing the miniaturized NDIR gas sensor.Yang Jing Cheng Yuhua Yuan Yupeng Li Xiaofei Zhang Zuwei Xu Ming Wang Dengpan Mu Jiangdong Mei Yong Zhang Yuzhe 2021Digital Communications and Networks2021,7,1:2
5Reaction-controlled phase transfer catalysis for styrene epoxidation to styrene oxide with aqueous hydrogen peroxide显示文摘Yang Aoge Gao Shuang Xi Zuwei 2005Organic Process Research & Development2005,9,3:1
6Improving Refinery Profits via Fine Management of Hydrogen Networks显示文摘氢网络管理对 refineries.Various 重要系统的管理技术被开发了改进精炼厂氢 networks.However 的效率,所有对待在处理的氢网络费用和油之间的氢网络 separately.The 折衷的存在方法联网利益没在氢网络管理 yet.A 小说敏感分析计划被探索被介绍拿把网络处理成处理统一哪个是 sensi 的 consideration.OilLiao Zuwei Zhang Yi Rong Gang Yang Yongrong 2010China Petroleum Processing & Petrochemical Technology2010,12,2:1
7Integrating purifiers in refinery hydrogen networks:A retrofit case study显示文摘LIAO Zuwei WANG Jingdai YANG Yongrong 2010Journal of Cleaner Production2010,18,3:1
8Integrating purifiers in refinery hydrogen networks:a retrofit case study显示文摘Liao Zuwei Wang Jingdai Yang Yongrong Rong Gang 2010Journal of Cleaner Production2010,18,:1
9Integrating purifiers in refinery hydrogen networks: a retrofit case study 显示文摘Liao Zuwei Wang Jingdai Yang Yongrong Rong Gang 2010Journal of Cleaner Production2010,18,3:1
10Rigorous algorithmic targeting methods for hydrogen networks ( Ⅰ ): Systems with no hydrogen purification 显示文摘Liao Zuwei Rong Gang Wang Jingdai Yang Yongrong 2011Chemical Engineering Science2011,66,5:1
11Acidity Modification of ZSM-5 for Methane Conversion in Co-feeding Method with MTA Reaction显示文摘Acidity plays a vital role in methane conversion by co-feeding method,which is one of the best strategies to improve the utilization and gentle the reaction conditions of methane.In this work,Zn,Ni,Mo,La,Ga,Fe and Co-impregnated ZSM-5 zeolites have been prepared with the same substitutions to variate the acidities and tested in co-aromatization of methanol with methane.It is demonstrated that the new medium-strong acid sites formed by metal and strong acid sites are the key role to activate methane in co-reaction.Zn-modified ZSM-5 catalyst is preferred to exhibit the best methane conversion of 12%,whose aromatic selectivity increases from 27.2%to 52.2%compared with that of HZSM-5.Besides,the addition of methane further improves the production of high-valued aromatics compared with methanol to aromatics(MTA)reaction.YU Yue XI Zhixiang ZHOU Bingjie JIANG Binbo LIAO Zuwei YANG Yao WANG Jingdai HUANG Zhengliang SUN Jingyuan YANG Yongrong 2022Chemical Research in Chinese Universities2022,38,4:1
12Rigorous algorithmic targeting methods for hydrogen networks (Ⅱ): Systems with one hydrogen purification unit显示文摘Liao Zuwei Rong Gang Wang Jingdai Yang Yongrong 2011Chemical Engineering Science2011,66,5:1
13Integrating purifiers in refinery hydrogen networks:Aretrofit case study显示文摘LIAO Zuwei WANG Jingdai YANG Yongrong 2010Journal of Cleaner Production2010,18,3:1
14Reaction-controlled phase transfer catalysis for styrene epoxidation to styrene oxide with aqueous hydro- gen peroxide 显示文摘Yang Xiaoge Gao Shuang Xi Zuwei 2005Org Process Res Dev2005,9,3:1
15Integrating Puri- fiers in Refinery Hydrogen Networks: A Retrofit Case Study显示文摘Liao Zuwei Wang Jingdai Yang Yongrong 2010JCleanProd2010,18,3:1
16Integrating purifiers in refinery hydrogen networks:A retrofit case study显示文摘LIAO Zuwei WANG Jingdai YANG Yongrong 2010Journal of Cleaner Production2010,18,3:1
17Information hiding algorithm based on PE file icon resource 显示文摘Zuwei Tian Xingming Sun Hengfu Yang 2011Journal of Convergence Information Technology2011,6,6:1
18Integrating Purifiers in Refinery Hydrogen Networks:A Retrofit Case Study显示文摘Liao Zuwei Wang Jingdai Yang Yongrong 2010J Cleaner Prod2010,18,3:1
19Integrating purifiers in refinery hydrogen networks: A retrofit easestudy显示文摘Zuwei Wang Jingdai Yang Yongrong 2010Journal of Cleaner Production2010,18,3:1
20Design Energy Efficient Water Utilization Systems Allowing Operation Split * * Supported by the Major Project of National Natural Science Foundation of China (No.20409205) and National High Technology Research and Development Program of China (No.G2007004显示文摘Zuwei LIAO Jintao WU Binbo JIANG Jingdai WANG Yongrong YANG 2008Chinese Journal of Chemical Engineering2008,,1:1
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