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Efficient synthesis of forsterite via high-temperature thermochemical reactions from boron mud waste without briquetting 被引量:2
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作者 Fangling Hu Liangliang Fu +2 位作者 qingjin zhang Guangwen Xu Dingrong Bai 《Particuology》 SCIE EI CAS CSCD 2024年第4期124-132,共9页
Forsterite is a highly demanded material in high-temperature industries due to its superior performance in elevated temperatures.This study proposes synthesizing high-quality forsterite via high-temperature thermochem... Forsterite is a highly demanded material in high-temperature industries due to its superior performance in elevated temperatures.This study proposes synthesizing high-quality forsterite via high-temperature thermochemical reactions using abundant boron mud waste.The new synthesis method capitalizes on the high reactivity of fine raw powder materials,enabling the reaction to reach completion at low temperatures rapidly.The chemical characteristics,microscopic morphology,and structure of synthe-sized samples are systematically studied using XRD and SEM.The results confirm that boron mud can be efficiently transformed into forsterite after 10 min of reactions at 1500℃.The synthesized products attain over 98.7%densification and contain more than 85.0%forsterite with well-developed grains.The activation energy of forsterite grain growth in the 1100-1500℃temperature range is 165.5 kJ/mol.This study provides a low-cost method for producing forsterite and an efficient and environmentally friendly solution for treating solid waste. 展开更多
关键词 Fluidized bed Boron mud FORSTERITE Solid state reaction Activation energy Grain growth
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Temperature influence on minimum fluidization velocity:Complexity,mechanism,and solutions 被引量:1
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作者 qingjin zhang Liangliang Fu +1 位作者 Guangwen Xu Dingrong Bai 《Particuology》 SCIE EI CAS CSCD 2024年第5期344-349,共6页
Fluidized-bed reactors are widely employed in various high-temperature industrial processes.Thus,it is crucial to understand the temperature effect on various fluidization phenomena,specifically the minimum fluidizati... Fluidized-bed reactors are widely employed in various high-temperature industrial processes.Thus,it is crucial to understand the temperature effect on various fluidization phenomena,specifically the minimum fluidization velocity(U_(mf))that governs various aspects of fluidized bed behavior.In this study,we comprehensively analyze U_(mf) data from the literature to unravel the complexity and underlying mechanisms of temperature influence on this critical velocity.The research examines experimental data encompassing a wide range of temperatures,pressures,and solid particles.The analysis reveals that the influence of temperature on U_(mf) is fundamentally determined by the relative importance of hydrodynamic forces and interparticle forces within fluidized beds and is realized by three distinctive temperature-induced changes:gas properties,bed voidage,and physiochemical characteristics of particles.On this basis,an equation is derived to enable predictions of temperature influences on the minimum fluidization velocity under broad temperature conditions. 展开更多
关键词 High-temperature gas-solids fluidized beds Minimum fluidization velocity Hydrodynamic forces Interparticle forces Bed voidage
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The transition to turbulent fluidization in a gas-solid fluidized bed operating from ambient temperature to 1600℃
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作者 qingjin zhang Liangliang Fu +1 位作者 Guangwen Xu Dingrong Bai 《Particuology》 SCIE EI CAS CSCD 2024年第10期111-124,共14页
Turbulent fluidized bed proves effective in industrial processes due to superior heat and mass transfer and chemical reaction performance. However, understanding the transition to turbulent fluidization remains limite... Turbulent fluidized bed proves effective in industrial processes due to superior heat and mass transfer and chemical reaction performance. However, understanding the transition to turbulent fluidization remains limited, especially at temperatures exceeding 1000 ℃, making it challenging to develop high-temperature fluidized bed applications. This paper presents an experimental investigation on the turbulent fluidization onset velocity (U_(c)), measured in a 30 mm diameter bed using corundum particles with average diameters from 0.68 mm to 1.58 mm in temperatures from ambient to 1600 ℃. Experimental results reveal that U_(c) increases with temperature up to 600 ℃, stabilizes within the 600–1200 ℃ range, and then decreases above 1200 ℃, demonstrating the varying relative significance of hydrodynamic and interparticle forces at different temperatures. To help design and operate high-temperature applications of turbulent fluidization, we developed U_(c) correlations based on experimental data from both literature sources and this study, covering temperatures of up to 1600 ℃ and particles of Groups A to D. 展开更多
关键词 High-temperature fluidized beds Turbulent fluidization Transition velocity Pressure fluctuations Hydrodynamic forces Interparticle FORCES
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不同折板絮凝器对薄荷水提液的絮凝效果研究与比较
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作者 冯颖 张庆瑾 +1 位作者 张建伟 张天阳 《过程工程学报》 CAS CSCD 北大核心 2021年第6期695-703,共9页
为了优化折板絮凝器结构及提升折板絮凝器对中药液的絮凝效果,利用FLUENT软件对同波/对波折板絮凝器的内部流场进行了模拟,分析了两种折板絮凝器内的涡旋分布及涡量。以薄荷水提液为研究对象,壳聚糖为絮凝剂,采用不同折板絮凝器对薄荷... 为了优化折板絮凝器结构及提升折板絮凝器对中药液的絮凝效果,利用FLUENT软件对同波/对波折板絮凝器的内部流场进行了模拟,分析了两种折板絮凝器内的涡旋分布及涡量。以薄荷水提液为研究对象,壳聚糖为絮凝剂,采用不同折板絮凝器对薄荷水提液进行絮凝处理,以薄荷水提液澄清层高度、絮体沉降速度、总黄酮保留率、絮凝率、药液吸光度及絮体形态为指标,考察了两种折板絮凝器在不同进液流速下对薄荷水提液的絮凝效果。结果表明,同波折板絮凝器流场内以单侧涡旋为主,对波折板絮凝器内在折板两侧均产生涡旋,相同进液流速下,同波折板絮凝器产生的涡量小于对波折板絮凝器。随进液流速增加,同波/对波折板絮凝器对薄荷水提液的絮凝效果均呈先升高后降低的趋势,同波折板絮凝器最佳进液流速为0.068 m/s,药液总黄酮保留率为91.2%,絮凝率为85.3%;对波折板絮凝器最佳进液流速为0.051 m/s,药液总黄酮保留率为91.8%,絮凝率为85.4%。 展开更多
关键词 折板絮凝器 FLUENT 絮凝 薄荷水提液 壳聚糖
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pH对壳聚糖螯合铜(Ⅱ)的螯合机理及稳定常数的影响 被引量:4
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作者 冯颖 张庆瑾 +1 位作者 王珏程 张建伟 《过程工程学报》 CAS CSCD 北大核心 2020年第6期646-654,共9页
用紫外分光光度法研究了pH值对壳聚糖螯合Cu(Ⅱ)的影响。通过显微图像、X衍射图谱及红外光谱对沉淀物进行分析。结果表明,随体系pH值增加,壳聚糖碳链上的活性基团与铜离子的螯合能力增强。溶液体系pH=5~6时,螯合物的稳定常数最大值为1.1... 用紫外分光光度法研究了pH值对壳聚糖螯合Cu(Ⅱ)的影响。通过显微图像、X衍射图谱及红外光谱对沉淀物进行分析。结果表明,随体系pH值增加,壳聚糖碳链上的活性基团与铜离子的螯合能力增强。溶液体系pH=5~6时,螯合物的稳定常数最大值为1.1×10^8;当pH接近7时,部分螯合产物析出导致稳定常数降低。酸性条件下pH值的变化对螯合物的配位比(n)无明显影响,壳聚糖-铜螯合物的配位比n=2。通过调节pH值可使溶液中壳聚糖铜螯合物析出,随pH增加,Cu^2+浓度降低,当pH约为9时,Cu^2+浓度达最小值1.5 mg/L。壳聚糖的主要活性基团-NH2与铜离子发生螯合,反应生成壳聚糖-铜。 展开更多
关键词 壳聚糖 铜离子 螯合机理 稳定常数 沉淀
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