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Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach SCIE
期刊论文 | 2025 , 208 | CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION
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Abstract :

A low-cost and process-intensified synthesis approach of SSZ-35 zeolite via a seed-assisted method is presented. This approach involves the development of a relatively inexpensive template and the application of seeds to minimize crystallization time and template consumption. Herein, N-Ethyl, N-methyl 2,6-cis-dimethylpiperidinium hydroxide (EMDMPOH) is selected as a template to synthesize SSZ-35 zeolite, and a simplified and optimized scheme for the preparation of such a template is proposed. Specially, the high-purity EMDMPOH is prepared by a sequential alkylation of 2,6-dimethylpiperidine with iodoethane and iodomethane, followed by ion exchange. By employing a seed-assisted strategy, the synthesis process of SSZ-35 zeolite is intensified, resulting in a significant reduction in crystallization time from 7 d to 75 h. Systematic characterizations reveal that the synthesized SSZ-35 zeolite has smaller crystals and larger specific surface area in comparison with the reference sample, leading to enhanced selectivity in n-octane hydroisomerization. Moreover, the cost accounting analysis shows a notable decrease in the synthesis cost of SSZ-35 zeolite by using the synthesis route that combines the simplified process for preparing the template and the reduced amount of template.

Keyword :

Crystallization intensification Crystallization intensification Low-cost synthesis Low-cost synthesis Seed-assisted method Seed-assisted method SSZ-35 zeolite SSZ-35 zeolite

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GB/T 7714 Dong, Peng , Wu, Huanliu , Luo, Longhua et al. Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach [J]. | CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION , 2025 , 208 .
MLA Dong, Peng et al. "Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach" . | CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION 208 (2025) .
APA Dong, Peng , Wu, Huanliu , Luo, Longhua , Cui, Qingyan , Li, Tiesen , Shi, Jie et al. Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach . | CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION , 2025 , 208 .
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Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach Scopus
期刊论文 | 2025 , 208 | Chemical Engineering and Processing - Process Intensification
Low-cost and efficient synthesis of SSZ-35 zeolite through a seed-assisted approach EI
期刊论文 | 2025 , 208 | Chemical Engineering and Processing - Process Intensification
Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking SCIE
期刊论文 | 2025 , 449 | CATALYSIS TODAY
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In order to gain insight into the influence of SiO2 support particle size on the vacuum residue (VR) slurry-phase hydrocracking performance of Fe-based catalysts, a series of FeZn/SiO2 catalysts with varying SiO2 particle sizes were prepared. Characterization results show that the surface area and pore volume of the FeZn/SiO2 catalysts increase with the reduction of SiO2 particle sizes. The metals Fe and Zn species on FeZn/SiO2-S catalyst are more readily reducible via H2-TPR analysis. Notably, FeZn/SiO2-S catalyst presents higher metal dispersion and a greater degree of sulfurization compared to the other catalysts by XRD and XPS. Hydrocracking results demonstrate that the FeZn/SiO2-S catalyst achieves the lowest coke and gas yields (11.9 wt% and 0.4 wt%), respectively, and the highest VR conversion among these catalysts. The superior performance of the FeZn/SiO2-S catalyst in VR slurry-phase hydrocracking is ascribed to its enhanced hydrogenation activity, deriving from the higher dispersion and sulfurization of metals species. This suppresses the aggregation of polycyclic aromatic hydrocarbons in VR and the over-cracking of intermediate products. Additionally, the increased mesopore associated with smaller SiO2 particles facilitates to the diffusion of large VR molecules, further promoting the hydrocracking reaction.

Keyword :

FeZn catalyst FeZn catalyst Hydrogenation activity Hydrogenation activity SiO2 particle size SiO2 particle size Slurry-phase hydrocracking Slurry-phase hydrocracking Vacuum residue Vacuum residue

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GB/T 7714 Wang, Jianbo , Yan, Jianteng , Cui, Qingyan et al. Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking [J]. | CATALYSIS TODAY , 2025 , 449 .
MLA Wang, Jianbo et al. "Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking" . | CATALYSIS TODAY 449 (2025) .
APA Wang, Jianbo , Yan, Jianteng , Cui, Qingyan , Li, Tiesen , Shi, Jie , Wang, Tinghai et al. Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking . | CATALYSIS TODAY , 2025 , 449 .
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Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking Scopus
期刊论文 | 2025 , 449 | Catalysis Today
Effect of SiO2 support particle sizes on the performance of FeZn catalysts in VR slurry-phase hydrocracking EI
期刊论文 | 2025 , 449 | Catalysis Today
Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue Scopus
期刊论文 | 2024 , 205 | Chemical Engineering and Processing - Process Intensification
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Abstract :

Natural rectorite modified by the hydrothermal method was employed to prepare a catalyst for the slurry-phase hydrocracking of vacuum residue (VR). The influence of hydrothermal treatment on the properties of rectorite and the performance of the corresponding catalyst was examined. Hydrothermal treatment of the rectorite led to the formation of Fe3O4, as evidenced by H2-TPR analysis. XPS results indicate that the hydrothermal treatment of rectorite can intensify the sulfidation process of Mo species supported on it, possibly due to modifications in the surface properties of the rectorite. Comparative slurry-phase hydrocracking tests showed that the catalyst supported on hydrothermally treated rectorite exhibited significantly higher VR conversion, higher liquid product yield, and higher yields of gasoline and diesel fractions, but lower gas yield compared to the catalyst supported on untreated rectorite. This is ascribed to the high hydrogenation activity of the catalyst supported on hydrothermally treated rectorite, which effectively suppresses the over-cracking reactions of intermediate products that would otherwise produce gas, illustrating the process intensification achieved through hydrothermal treatment. © 2024 Elsevier B.V.

Keyword :

Hydrocracking Hydrocracking Hydrothermal treatment Hydrothermal treatment Mo catalyst Mo catalyst Sulfidation Sulfidation Vacuum residue Vacuum residue

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GB/T 7714 Cui, Q. , Yan, J. , Zhang, H. et al. Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue [J]. | Chemical Engineering and Processing - Process Intensification , 2024 , 205 .
MLA Cui, Q. et al. "Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue" . | Chemical Engineering and Processing - Process Intensification 205 (2024) .
APA Cui, Q. , Yan, J. , Zhang, H. , Feng, W. , Yue, Y. , Li, T. et al. Hydrothermal treatment of natural rectorite enhanced Mo sulfidation for slurry-phase hydrocracking of vacuum residue . | Chemical Engineering and Processing - Process Intensification , 2024 , 205 .
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Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst EI
期刊论文 | 2024 , 374 | Fuel
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To gain a profound understanding of the reaction pathway and the controlling step of residue oil slurry-phase hydrocracking over Fe2O3 catalyst, a six-lumped kinetic model was proposed and employed to acquire the kinetic rate constants based on each fraction yield obtained at 400 to 420 °C under initial H2 pressures of 8 to 10 MPa for 1 to 3 h. The optimal kinetic rate constant for each step of vacuum residue (VR) conversion process was determined via Levenberg-Marquardt algorithm and the sum of squares error (SSE). The results reveal that VR converted into naphtha and diesel is dominant according to their kinetic rate constants, followed by the conversion of vacuum gas oil (VGO) to diesel, diesel to naphtha, and diesel to gas. Furthermore, the sensitivity analysis confirms a strong agreement between the predicted and experimental values. The combination of kinetic rate constants and activation energy illustrates that the gas product primarily originates from naphtha. Additionally, the higher H2 pressure effectively mitigates coke deposition by restricting the aggregation of polycyclic aromatics, as evidenced by the increase in the reaction activation energy for the conversion of VR to coke and the analysis of the used catalyst. © 2024 Elsevier Ltd

Keyword :

Activation analysis Activation analysis Activation energy Activation energy Catalysts Catalysts Coke Coke Hematite Hematite Hydrocracking Hydrocracking Kinetic parameters Kinetic parameters Kinetic theory Kinetic theory Naphthas Naphthas Rate constants Rate constants Sensitivity analysis Sensitivity analysis

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GB/T 7714 Cui, Qingyan , Zheng, Bin , Wang, Boshi et al. Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst [J]. | Fuel , 2024 , 374 .
MLA Cui, Qingyan et al. "Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst" . | Fuel 374 (2024) .
APA Cui, Qingyan , Zheng, Bin , Wang, Boshi , Yan, Jianteng , Liu, Jiangyong , Li, Tiesen et al. Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst . | Fuel , 2024 , 374 .
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Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics SCIE
期刊论文 | 2024 , 70 , 130-138 | CHINESE JOURNAL OF CHEMICAL ENGINEERING
WoS CC Cited Count: 1
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Abstract :

NaY zeolites are synthesized using submolten salt depolymerized natural perlite mineral as the main silica and alumina sources in a 0.94 L stirred crystallizer. Effects of alkalinity ranging from 0.38 to 0.55 ( n (Na 2 O)/ n (SiO 2 )) on the relative crystallinity, textural properties and crystallization kinetics were investigated. The results show that alkalinity exerts a nonmonotonic in fluence on the relative crystallinity and textural properties, which exhibit a maximum at the alkalinity of 0.43. The nucleation kinetics are studied by fitting the experimental data of relative crystallinity with the Gualtieri model. It is shown that the nucleation rate constant increases with increasing alkalinity, while the duration period of nucleation decreases with increasing alkalinity. For n (Na 2 O)/ n (SiO 2 ) ratios ranging from 0.38 to 0.55, the as -synthesized NaY zeolites exhibit narrower crystal size distributions with the increase in alkalinity. The growth rates determined from the variations of average crystal size with time are 51.09, 157.50, 46.17 and 24.75 nm $h -1 , respectively. It is found that the larger average crystal sizes at the alkalinity of 0.38 and 0.43 are attributed to the dominant role of crystal growth over nucleation. Furthermore, the combined action of prominent crystal growth and the longer duration periods of nucleation at the alkalinity of 0.38 and 0.43 results in broader crystal size distributions. The findings demonstrate that control of the properties of NaY zeolite and the crystallization kinetics can be achieved by conducting the crystallization process in an appropriate range of alkalinity of the reaction mixture. (c) 2024 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.

Keyword :

Alkalinity Alkalinity Crystallization kinetics Crystallization kinetics NaY zeolite NaY zeolite Submolten salt depolymerized perlite Submolten salt depolymerized perlite

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GB/T 7714 Qu, Yanli , Dong, Peng , Yang, Li et al. Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics [J]. | CHINESE JOURNAL OF CHEMICAL ENGINEERING , 2024 , 70 : 130-138 .
MLA Qu, Yanli et al. "Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics" . | CHINESE JOURNAL OF CHEMICAL ENGINEERING 70 (2024) : 130-138 .
APA Qu, Yanli , Dong, Peng , Yang, Li , Yue, Yuanyuan , Wang, Haoliang , Cheng, Jingcai et al. Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics . | CHINESE JOURNAL OF CHEMICAL ENGINEERING , 2024 , 70 , 130-138 .
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Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics Scopus CSCD
期刊论文 | 2024 , 70 , 130-138 | Chinese Journal of Chemical Engineering
Synthesis of NaY zeolite from a submolten depolymerized perlite: Alkalinity effect and crystallization kinetics EI CSCD
期刊论文 | 2024 , 70 , 130-138 | Chinese Journal of Chemical Engineering
Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution SCIE
期刊论文 | 2024 , 13 (1) , 321-332 | ACS SUSTAINABLE CHEMISTRY & ENGINEERING
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Abstract :

The catalytic dehydration of glycerol to acrolein offers a sustainable route for efficiently utilizing low-cost and renewable bioglycerol. This work deeply explores glycerol dehydration to acrolein over ZSM-5 zeolite catalysts with various pore structures and aluminum distributions. The results reveal that glycerol conversion is enhanced through the construction of a mesoporous structure and the increase in Br & oslash;nsted acid sites of the catalysts, but acrolein selectivity is not directly related to these factors. Further characterizations, density functional theory calculation, kinetic study, and reaction mechanism analysis demonstrate that the richest Alsingle sites in the zeolite framework and the least Alpair sites in the straight and sinusoidal channels can prevent the generated acrolein from adsorbing on adjacent Al sites. This allows acrolein to immediately escape from the catalyst surface, reducing side reactions and enhancing its selectivity. Therefore, the synergistic between the mesoporous structure and more Alsingle sites in the ZSM-5 zeolite framework promotes acrolein yield. Additionally, a descriptor phi, reflecting the amount of Alsingle sites and the external specific surface area of the ZSM-5 zeolite, is first proposed to more clearly elucidate the structure-performance relationship. This study provides a new perspective for understanding the mechanism of catalytic dehydration of glycerol to acrolein, guiding the development of highly efficient catalysts. It is significant for the sustainable development of the biodiesel and acrolein production industry.

Keyword :

aluminum distribution aluminum distribution catalytic dehydration catalytic dehydration glycerol glycerol pore structure pore structure ZSM-5 zeolitecatalyst ZSM-5 zeolitecatalyst

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GB/T 7714 Luo, Wei , Shi, Jie , Li, Tiesen et al. Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution [J]. | ACS SUSTAINABLE CHEMISTRY & ENGINEERING , 2024 , 13 (1) : 321-332 .
MLA Luo, Wei et al. "Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution" . | ACS SUSTAINABLE CHEMISTRY & ENGINEERING 13 . 1 (2024) : 321-332 .
APA Luo, Wei , Shi, Jie , Li, Tiesen , Wang, Tinghai , Liu, Jiangyong , Cui, Qingyan et al. Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution . | ACS SUSTAINABLE CHEMISTRY & ENGINEERING , 2024 , 13 (1) , 321-332 .
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Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution Scopus
期刊论文 | 2025 , 13 (1) , 321-332 | ACS Sustainable Chemistry and Engineering
Catalytic Dehydration of Glycerol to Acrolein over ZSM-5 Zeolites: Synergistic Effect of Pore Structure and Aluminum Distribution EI
期刊论文 | 2025 , 13 (1) , 321-332 | ACS Sustainable Chemistry and Engineering
分子筛合成母液回用技术研究进展 CSCD PKU
期刊论文 | 2024 , 55 (2) , 110-114 | 石油炼制与化工
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Abstract :

分子筛合成母液回用技术是分子筛制备的一种新方法,能够有效提高原料利用率和减少废液排放.介绍了分子筛合成母液的产生及组成,简述了分子筛合成母液回用技术及其在分子筛合成中的应用情况,重点总结该技术在工业上最具代表性的Y,ZSM-5,SAPO-34分子筛合成中的研究进展,并阐述当前分子筛母液回用技术面临的挑战,展望其在工业生产中的发展前景,为实现分子筛产业高效与可持续发展提供借鉴.

Keyword :

分子筛 分子筛 可持续制备 可持续制备 合成母液 合成母液 回用技术 回用技术

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GB/T 7714 吴岩 , 董鹏 , 王颖 et al. 分子筛合成母液回用技术研究进展 [J]. | 石油炼制与化工 , 2024 , 55 (2) : 110-114 .
MLA 吴岩 et al. "分子筛合成母液回用技术研究进展" . | 石油炼制与化工 55 . 2 (2024) : 110-114 .
APA 吴岩 , 董鹏 , 王颖 , 岳源源 . 分子筛合成母液回用技术研究进展 . | 石油炼制与化工 , 2024 , 55 (2) , 110-114 .
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分子筛合成母液回用技术研究进展 CSCD PKU
期刊论文 | 2024 , 55 (02) , 110-114 | 石油炼制与化工
介孔NiAl催化剂催化己二醇绿色合成1,6-己二胺
期刊论文 | 2024 , 53 (9) , 1237-1244 | 石油化工
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通过溶胶-凝胶法制备了系列介孔NiAl催化剂,研究了不同还原温度下Ni含量为 20%(x)的介孔NiAl(20NA)催化剂在 1,6-己二醇(HDO)催化氨化合成 1,6-己二胺(HMDA)中的催化性能.利用N2 吸附-脱附、H2-TPR、CO-TPD、XRD、SAXS、XPS、SEM、TEM、ICP-OES等方法对试样进行表征.实验结果表明,低温还原后的 20NA催化剂表面金属Ni0 粒径较小,具有较高的HDO转化率.440℃还原的 20NA催化剂在温和反应温度(190℃)下,HMDA最高产率可达30.9%,除低聚物外的高附加值产物的总选择性高达 94.7%(x),HDO转换频率与文献报道的贵金属Ru基催化剂相当.通过调节还原温度可有效控制20NA催化剂表面金属Ni0 位点的纳米尺寸.

Keyword :

1 1 6-己二醇 6-己二醇 介孔NiAl催化剂 介孔NiAl催化剂 催化氨化 催化氨化 己二胺 己二胺

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GB/T 7714 王鹏宇 , 李星局 , 严丽 et al. 介孔NiAl催化剂催化己二醇绿色合成1,6-己二胺 [J]. | 石油化工 , 2024 , 53 (9) : 1237-1244 .
MLA 王鹏宇 et al. "介孔NiAl催化剂催化己二醇绿色合成1,6-己二胺" . | 石油化工 53 . 9 (2024) : 1237-1244 .
APA 王鹏宇 , 李星局 , 严丽 , 岳源源 , 马新宾 , 马雷 . 介孔NiAl催化剂催化己二醇绿色合成1,6-己二胺 . | 石油化工 , 2024 , 53 (9) , 1237-1244 .
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等级孔FAU型分子筛的制备及应用的研究进展 CSCD PKU
期刊论文 | 2024 , 69 (19) , 2718-2728 | 科学通报
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Abstract :

FAU型分子筛因其独特的孔道结构已成为化学工业中应用最广泛、用量最大的催化剂、催化剂载体及吸附剂之一.然而, FAU型分子筛单一的微孔孔道限制了客体分子的扩散,导致其性能严重下降.相比之下,等级孔FAU型分子筛具有微-介/大孔复合的多级孔道结构,能够促进大分子的扩散、提高活性位点的可接近性,进而改善其吸附和催化性能.目前,等级孔分子筛的制备方法主要包括“自下而上”的直接合成法和“自上而下”的后处理法.本文主要介绍了近年来等级孔X型和Y型分子筛制备方法的研究现状,重点总结了等级孔X型和Y型分子筛在吸附、催化等过程中的应用性能,并对等级孔FAU型分子筛的绿色化制备进行展望.

Keyword :

催化 催化 后处理 后处理 吸附 吸附 直接合成 直接合成 等级孔FAU型分子筛 等级孔FAU型分子筛

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GB/T 7714 董鹏 , 朱琳 , 骆龙华 et al. 等级孔FAU型分子筛的制备及应用的研究进展 [J]. | 科学通报 , 2024 , 69 (19) : 2718-2728 .
MLA 董鹏 et al. "等级孔FAU型分子筛的制备及应用的研究进展" . | 科学通报 69 . 19 (2024) : 2718-2728 .
APA 董鹏 , 朱琳 , 骆龙华 , 李铁森 , 王廷海 , 王婵 et al. 等级孔FAU型分子筛的制备及应用的研究进展 . | 科学通报 , 2024 , 69 (19) , 2718-2728 .
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Comparative environmental assessment of zeolites synthesized from chemicals and natural minerals (vol 26, pg 5273, 2024) SCIE
期刊论文 | 2024 , 26 (14) , 8428-8429 | GREEN CHEMISTRY
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Correction for 'Comparative environmental assessment of zeolites synthesized from chemicals and natural minerals' by Xiaoling Chen et al., Green Chem., 2024, 26, 5273-5283, https://doi.org/10.1039/D3GC05146C.

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GB/T 7714 Chen, Xiaoling , Xiao, Guoxi , Li, Tiesen et al. Comparative environmental assessment of zeolites synthesized from chemicals and natural minerals (vol 26, pg 5273, 2024) [J]. | GREEN CHEMISTRY , 2024 , 26 (14) : 8428-8429 .
MLA Chen, Xiaoling et al. "Comparative environmental assessment of zeolites synthesized from chemicals and natural minerals (vol 26, pg 5273, 2024)" . | GREEN CHEMISTRY 26 . 14 (2024) : 8428-8429 .
APA Chen, Xiaoling , Xiao, Guoxi , Li, Tiesen , Wang, Chan , Cui, Qingyan , Bao, Xiaojun et al. Comparative environmental assessment of zeolites synthesized from chemicals and natural minerals (vol 26, pg 5273, 2024) . | GREEN CHEMISTRY , 2024 , 26 (14) , 8428-8429 .
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