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目的设计一款适用于现代无线通信系统小型的滤波器天线。方法由一微带开口环谐振器、一段耦合线和一个Г型天线组成一款滤波器天线。这个Г型天线由耦合线激励,在设计中起着导纳变换器的作用。Г型天线不仅起着辐射的作用,同时也是滤波器最后一个谐振器,使滤波器和天线之间基本没有损耗,在仿真调试后,加工成实物进行测试。结果该滤波器天线在反射系数S11<-10 dB的阻抗带宽有12.7%(2.36~2.68 GHz),滤波器天线具有平坦的通带,通带内的最大差异为0.84 dB。滤波器天线通带外增益不到-15 dBi,这说明滤波器天线具有很好的带外抑制性。结论设计的滤波器天线通带内天线增益较为平坦,且拥有良好的带外抑制特性、滤波与辐射特性,并且损耗很低,很适合用于现代无线通信系统的射频前端。 相似文献
74.
由于半干法脱硫工艺对布袋除尘器的特殊要求,使得其配套的布袋除尘器构造不同于以往常规的布袋除尘器.从布袋除尘器的过滤风速、滤料选择、沉降室设置、布风均匀性、灰斗特性、旁路系统的要求做详细的说明. 相似文献
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Cleaning of hollow-fibre polyvinyl chloride (PVC) membrane with di erent chemical reagents after ultrafiltration of algal-rich
water was investigated. Among the tested cleaning reagents (NaOH, HCl, EDTA, and NaClO), 100 mg/L NaClO exhibited the best
performance (88.4% 1.1%) in removing the irreversible fouling resistance. This might be attributed to the fact that NaClO could
eliminate almost all the major foulants such as carbohydrate-like and protein-like materials on the membrane surface, as confirmed by
Fourier transform infrared spectroscopy analysis. However, negligible irreversible resistance (1.5% 1.0%) was obtained when the
membrane was cleaning by 500 mg/L NaOH for 1.0 hr, although the NaOH solution could also desorb a portion of the major foulants
from the fouled PVC membrane. Scanning electronic microscopy and atomic force microscopy analyses demonstrated that 500 mg/L
NaOH could change the structure of the residual foulants on the membrane, making them more tightly attached to the membrane
surface. This phenomenon might be responsible for the negligible membrane permeability restoration after NaOH cleaning. On the
other hand, the microscopic analyses reflected that NaClO could e ectively remove the foulants accumulated on the membrane surface. 相似文献
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Catalytic bubble-free hydrogenation reduction of azo dye by porous membranes loaded with palladium (Pd) nanoparticles was studied for the first time. The effects of Pd loading, dye concentration and reuse repetitions of membranes were investigated. In reduction, the dye concentration decreased whereas the pH rose gradually. An optimal Pd loading was found. The catalytic membranes were able to be reused more than 3 times. 相似文献
79.
Experimental study on filtration and continuous regeneration of a particulate filter system for heavy-duty diesel engines 总被引:1,自引:0,他引:1
This study investigated the filtration and continuous regeneration of a particulate filter system on an engine test bench, consisting of a diesel oxidation catalyst(DOC) and a catalyzed diesel particulate filter(CDPF). Both the DOC and the CDPF led to a high conversion of NO to NO2 for continuous regeneration. The filtration efficiency on solid particle number(SPN) was close to100%. The post-CDPF particles were mainly in accumulation mode. The downstream SPN was sensitively influenced by the variation of the soot loading. This phenomenon provides a method for determining the balance point temperature by measuring the trend of SPN concentration. 相似文献
80.
Fouling behavior along the length of membrane module was systematically investigated by performing simple modeling and lab-scale experiments of forward osmosis (FO) membrane process. The flux distribution model developed in this study showed a good agreement with experimental results, validating the robustness of the model. This model demonstrated, as expected, that the permeate flux decreased along the membrane channel due to decreasing osmotic pressure differential across the FO membrane. A series of fouling experiments were conducted under the draw and feed solutions at various recoveries simulated by the model. The simulated fouling experiments revealed that higher organic (alginate) fouling and thus more flux decline were observed at the last section of a membrane channel, as foulants in feed solution became more concentrated. Furthermore, the water flux in FO process declined more severely as the recovery increased due to more foulants transported to membrane surface with elevated solute concentrations at higher recovery, which created favorable solution environments for organic adsorption. The fouling reversibility also decreased at the last section of the membrane channel, suggesting that fouling distribution on FO membrane along the module should be carefully examined to improve overall cleaning efficiency. Lastly, it was found that such fouling distribution observed with co-current flow operation became less pronounced in counter- current flow operation of FO membrane process. 相似文献