摘要
设计了一套带有气液分离精馏设备的吸收扩散制冷装置,试验研究了提升管结构、热源加热温度、氨水浓度、充气压力对制冷装置的影响。新型的精馏结构在提高发生氨气纯度的同时,也可减少冷凝器的负荷(冷凝器进口温度为55℃左右)。实验在环境温度T0为25-35℃,溶液浓度ξ为25%-35%,充注压力P0为13-18 MPa,加热功率Pg为220-320 W的范围内进行。结果表明:浓度的提高可获得较大的冷量,一般28-32%为宜;适当的增加系统压力可降低蒸发温度;系统的冷量随加热功率的增加而提高;确定了提升管结构参数的选取。
An improved experimental system of diffusion - absorption refrigeration based on ammonia (refrigerant) and water ( absorb- ent) as the working fluids together with helium as inert gas was set up. A new rectifier was adopted with the aim of purifying the ammonia vapor from the generator and cutting down the load of the condenser. ( the temperature of the inlet of the condenser was about 55 ℃ ) The experimental was undertaken to analysis some parameters affecting the refrigeration performance, in the condition of ambient temperature 25 - 35 ℃ ; concentration of rich solution 25% -35% , charge pressure 13 - 18MPa, heat power 220 -320W. The experimental data show: the larger cooling capacity can be obtained by increasing the concentration of the solution (28 - 32% was recommended) or increasing the heat input to the generator; the evaporate temperature can be decreased by increasing the system pressure property; the selection of the con.figuration of bubble pump was suggested.
出处
《低温与超导》
CAS
CSCD
北大核心
2007年第1期79-83,共5页
Cryogenics and Superconductivity
基金
上海市重点学科建设项目(T0503)
关键词
扩散吸收制冷
氨水浓度
充气压力
性能
提升管
Diffusion - absorption refrigeration, Concentration, Charge pressure, Performance, Bubble pump