Droplet Entrainment Analysis in a Flash Evaporator with an Image-Based Measurement Technique

Local droplet sizes and volumes of entrained liquid are captured with an image-based measurement technique for comparison with a conventional, integral method for entrainment analysis. Experiments in a forced circulation flash evaporation were performed for different operating conditions and with two different chemical systems. Droplet size and frequency rise with an increase in thermal energy input. The local readings confirm the trends found by the integral measurement method. The modification of the image-based probe enables the detection of small (≈ 10 µm) and at the same time fast droplets under challenging operating conditions, such as vacuum and superheated feed similar to industrial process conditions.     

氯化铵蒸发器结垢成分鉴别及原因分析

多效蒸发器结垢的问题常常发生,影响热效率和装置的正常运行。为明确导致蒸发器结垢的原因和成分,利用X射线衍射（XRD）、等离子发射光谱（ICP）、扫描电镜能谱（SEM-EDS）、偏光显微镜、拉曼光谱和离子色谱等分析测试技术,对浙江大洋生物科技集团股份有限公司的氯化铵多效蒸发器上的不明结垢物做了表征和分析。结果表明,该结垢物的主要成分为磷酸铁、氧化铝和有机物的混合物。探讨了发生上述结垢的原因,并提出相应的解决方案,减少了公司氯化铵蒸发器的结垢。     

An experimental investigation of refrigerant mixture R32/R290 as drop-in replacement for HFC410A in household air conditioners

In the present paper, the refrigerant mixture R32/R290 (68%/32% by weight) is investigated as the drop-in replacement for R410A in household air conditioners. The GWP of it is only 22% of that of R410A. Theoretical and experimental investigations are conducted on the performance of the air conditioners working with both R32/R290 and R410A. Experimental results show that the refrigerant charge amount of R32/R290 is reduced by 30.0%–35.0%; the cooling and heating capacities are increased by 14.0%–23.7%. For further reducing charge amount and flammability, the micro-channel heat exchanger (condenser) is employed to replace the finned tube one. Compared with the R32/R290 system using finned tube heat exchanger, the R32/R290 charge amount and the power consumption are reduced by 34.1% and 0.4%, respectively; the cooling capacity and the COP are increased by 6.4% and 6.8%, respectively.     

动车组司机室空调蒸发器气动噪声数值仿真

为研究动车组司机室空调蒸发器的噪声响应，建立某型司机室分体式空调蒸发器的计算流体动力学模型，采用FLUENT中的大涡模拟（large eddy simulation, LES）计算瞬态气动流场。对瞬态流场数据进行傅里叶变换，得到空气流场的频域数据。基于流场频域数据，采用Virtual.Lab的边界元法计算蒸发器的气动噪声，采用声压法计算蒸发器的辐射声功率，并与测试结果进行对比分析。结果表明：蒸发器出口位置气动噪声最高，最大声压级高于56 dB；最大声功率级出现在125~400 Hz的低频段；声功率级随着频率的增加逐渐降低，但在5 000 Hz的高频辐射中声功率级仍然超过55 dB，这表明空调蒸发器气动噪声属于宽频噪声；计算结果与测试结果吻合良好，验证声压法计算空调蒸发器气动声功率可行。     

Application of a micro-channel reactor for process intensification in high purity syngas production via H2O/CO2 co-splitting

A stainless steel micro-channel reactor was tailor-made to an in house-design for process intensification propose. The reactor was used for a two-step thermochemical cycles of H₂O and CO₂ co-splitting reaction, in the presence of La_0.3Sr_0.7Co_0.7Fe_0.3O₃ (LSCF). LSCF was coated inside the reactor using wash-coat technique. Oxygen storage capacity of LSCF was determined at 4465 μmol/g, using H₂-TPR technique. H₂O-TPSR and CO₂-TPSR results suggested that a formation of surface hydroxyl group was the cause of H₂O splitting favorable behavior of LSCF. Optimal operating reduction/oxidation temperature was found at 700 °C, giving 2266 μmol/g of H₂, 705 μmol/g of CO, and 67% of solid conversion, when the H₂O and CO₂ ratio was 1 to 1, and WSHV was 186,000 mL/g.h. Activation energy of H₂O spitting and CO₂ splitting was estimated at 87.33 kJ/mol, and 102.85 kJ/mol The pre-exponential factor of H2O splitting and CO2 splitting was 595.24 s^?1 and 698.79 s^?1, respectively.     

乙二醇蒸发器大开孔结构应力分析与强度校核

基于分析设计法,利用有限元软件ABAQUS对乙二醇蒸发器大开孔结构和补强圈结构进行应力分析,并进行强度校核,讨论了内压对应力强度的影响规律。结果发现,应力集中位于接管与筒体连接部位,强度校核符合要求,满足强度要求的极限载荷为0.77MPa。     

三效自流蒸发装置运行总结

介绍了离子膜法烧碱三效自流蒸发工艺流程、设备选材及装置特点,针对运行中存在的问题（如仪表风压低,视镜破裂,预热器管线振动,密封垫片泄漏）提出了改进措施.     

25万 t／a 硝酸铵装置建设及生产运行情况技术总结

介绍了25万t/a硝酸铵装置的生产工艺流程,并对工艺及设备进行了完善,提供了多孔（工业）硝酸铵装置工艺运行参数及质量与物料消耗参数,针对成品硝酸铵水分较高提出了改进措施。     

满液式螺杆冷水机组动态特性实验研究

实验研究了满液式螺杆冷水机组动态特性,得到了关于电子膨胀阀-液位,电子膨胀阀-排气过热度等参数的动态响应特性和部分负荷性能,结果可作为机组的设计和运行控制的基础。     

电子膨胀阀及其在蒸发器过热度自适应控制中的应用

详细剖析了电子膨胀阀的硬件构成，在分析了蒸发器过热度电子控制的现状后提出，以自校正自适应控制作为蒸发器过热度控制的核心，可实现对蒸发器慢时变工作条件自动适应的最优控制。仿真结果表明自校正自适应控制在制冷窑对象中有良好的工作性能和发展前景。