To adapt to the change of aquaculture workshop site,optimize the shape of aquaculture tanks and improve the utilization rate of breeding space,it is necessary to determine the appropriate length width ratio parameters...To adapt to the change of aquaculture workshop site,optimize the shape of aquaculture tanks and improve the utilization rate of breeding space,it is necessary to determine the appropriate length width ratio parameters of aquaculture tanks.In this paper,computational fluid dynamics(CFD)technology is adopted to study the flow field performance of aquaculture tanks with different L/B ratios(L:the length;B:the width,of aquaculture tank)and different jet direction conditions(lengthways jet and widthways jet).A three-dimensional numerical calculation model of turbulence in rounded rectangle aquaculture tanks in dual-diagonal-inlet layout was established.Jet directions are arranged lengthways and widthways,and the water flow velocity,resistance coefficient change,vorticity,etc.are analyzed under two working conditions.Results show that the flow field performance in aquaculture tank decreases with the increase of the L/B ratio.The flow field performed well when L/B was 1.0-1.3,sharply dropped at 1.4-1.6,and poor at 1.7-1.9.The results provided a theoretical basis for the design and optimization in flow field performance of the industrialized circulating aquaculture tanks.展开更多
In order to further improve the catalytic performance of zeolite catalyst for methanol to aromatics(MTA)technology, the double-tier SAPO-34/ZSM-5/quartz composite zeolite films were successfully synthesized via hydrot...In order to further improve the catalytic performance of zeolite catalyst for methanol to aromatics(MTA)technology, the double-tier SAPO-34/ZSM-5/quartz composite zeolite films were successfully synthesized via hydrothermal crystallization. The Si/Al ratio of SAPO-34 film was used as the only variable to study this material. The composite zeolite material with 0.6Si/Al ratio of SAPO-34 has the largest mesoporous specific surface area and the most suitable acid distribution. The catalytic performance for the MTA process showed that 0.6-SAPO-34/ZSM-5/quartz film has as high as 50.3% benzene-toluenexylene selectivity and 670 min lifetime. The MTA reaction is carried out through the path we designed to effectively avoid the hydrocarbon pool circulation of ZSM-5 zeolite, so as to improve the aromatics selectivity and inhibit the occurrence of deep side reactions to a great extent. The coke deposition behavior was monitored by thermogravimetric analysis and gas chromatograph/mass spectrometer, it is found that with the increase of Si/Al ratio, the active intermediates changed from low-substituted methylbenzene to high-substituted methylbenzene, which led to the rapid deactivation of the catalyst. This work provides a possibility to employ the synergy effect of composite zeolite film synthesizing anti-carbon deposition catalyst in MTA reaction.展开更多
为研究不同流量比的两股射流入射水垫塘后的消能特性,选用非定常不可压缩流动的N-S方程和RNGk-ε紊流模型,采用VOF(Volume of Fluid)法结合溪洛渡双曲拱坝水垫塘进行了数值模拟,分析了流量比对水垫塘底板的冲击压力、临底速度、流态特...为研究不同流量比的两股射流入射水垫塘后的消能特性,选用非定常不可压缩流动的N-S方程和RNGk-ε紊流模型,采用VOF(Volume of Fluid)法结合溪洛渡双曲拱坝水垫塘进行了数值模拟,分析了流量比对水垫塘底板的冲击压力、临底速度、流态特征影响,并定量研究了流场内时均动能的衰减规律。研究表明,随着上游水股射流流量的减小,上游水股对底板的冲击压力在逐渐减小,由上游水股产生的动水垫作用逐渐减弱,使得下游水股对底板的冲击压力在逐渐增大;水垫塘流场呈现为具有动水垫效应的单股射流和动水垫效应微弱的单股射流两种形态。定量计算结果表明:对于上游水股射流,时均流速梯度较大,时均动能衰减较快,且随着上游水股射流流量减小,时均动能衰减速度加快,而下游水股射流的时均流能量比值和时均消能率总体小于上游水股射流消能率。展开更多
基金Supported by the National Natural Science Foundation of China(No.31872609)the Innovation Support Program for High-level Talents of Dalian City(No.2019RD12)+1 种基金the Key Research Project of Liaoning Provincial Department of Education in 2022(No.LJKZZ 20220091)the earmarked fund for CARS-49(CARS-49)。
文摘To adapt to the change of aquaculture workshop site,optimize the shape of aquaculture tanks and improve the utilization rate of breeding space,it is necessary to determine the appropriate length width ratio parameters of aquaculture tanks.In this paper,computational fluid dynamics(CFD)technology is adopted to study the flow field performance of aquaculture tanks with different L/B ratios(L:the length;B:the width,of aquaculture tank)and different jet direction conditions(lengthways jet and widthways jet).A three-dimensional numerical calculation model of turbulence in rounded rectangle aquaculture tanks in dual-diagonal-inlet layout was established.Jet directions are arranged lengthways and widthways,and the water flow velocity,resistance coefficient change,vorticity,etc.are analyzed under two working conditions.Results show that the flow field performance in aquaculture tank decreases with the increase of the L/B ratio.The flow field performed well when L/B was 1.0-1.3,sharply dropped at 1.4-1.6,and poor at 1.7-1.9.The results provided a theoretical basis for the design and optimization in flow field performance of the industrialized circulating aquaculture tanks.
基金supported by the National Natural Science Foundation of China (51974312, 51974308)the National Key Research & Development Program of China (2019YFE0100100)。
文摘In order to further improve the catalytic performance of zeolite catalyst for methanol to aromatics(MTA)technology, the double-tier SAPO-34/ZSM-5/quartz composite zeolite films were successfully synthesized via hydrothermal crystallization. The Si/Al ratio of SAPO-34 film was used as the only variable to study this material. The composite zeolite material with 0.6Si/Al ratio of SAPO-34 has the largest mesoporous specific surface area and the most suitable acid distribution. The catalytic performance for the MTA process showed that 0.6-SAPO-34/ZSM-5/quartz film has as high as 50.3% benzene-toluenexylene selectivity and 670 min lifetime. The MTA reaction is carried out through the path we designed to effectively avoid the hydrocarbon pool circulation of ZSM-5 zeolite, so as to improve the aromatics selectivity and inhibit the occurrence of deep side reactions to a great extent. The coke deposition behavior was monitored by thermogravimetric analysis and gas chromatograph/mass spectrometer, it is found that with the increase of Si/Al ratio, the active intermediates changed from low-substituted methylbenzene to high-substituted methylbenzene, which led to the rapid deactivation of the catalyst. This work provides a possibility to employ the synergy effect of composite zeolite film synthesizing anti-carbon deposition catalyst in MTA reaction.
文摘为研究不同流量比的两股射流入射水垫塘后的消能特性,选用非定常不可压缩流动的N-S方程和RNGk-ε紊流模型,采用VOF(Volume of Fluid)法结合溪洛渡双曲拱坝水垫塘进行了数值模拟,分析了流量比对水垫塘底板的冲击压力、临底速度、流态特征影响,并定量研究了流场内时均动能的衰减规律。研究表明,随着上游水股射流流量的减小,上游水股对底板的冲击压力在逐渐减小,由上游水股产生的动水垫作用逐渐减弱,使得下游水股对底板的冲击压力在逐渐增大;水垫塘流场呈现为具有动水垫效应的单股射流和动水垫效应微弱的单股射流两种形态。定量计算结果表明:对于上游水股射流,时均流速梯度较大,时均动能衰减较快,且随着上游水股射流流量减小,时均动能衰减速度加快,而下游水股射流的时均流能量比值和时均消能率总体小于上游水股射流消能率。
