• 대한화학회지
• /
• 제39권8호
• /
• pp.589-597
• /
• 1995

물과 에탄올 혼합 용매에서 전도도법으로 염의 한계 당량 전도도를 구한 후, TATB법으로 이온의 당량전도도를 구하고 Nightingale법으로 이온의 보정 유효반지름을 얻고, 이온에 용매화된 용매의 부피를 계산하여 몇가지 용매화수를 제안하고 이들중에서 해당 이온에 가장 타당한 용매화수$(h_{H_2O}/+h_o)$를 구하고, 해당 이온에 대한 등용매화점을 얻었다. 물과 에탄올 혼합 용매에서의 해당 이온에 대한 등용매화점이 물과 메탄올 혼합 용매에서의 해당 이온에 대한 등용매화점보다 높은 곳에서 나타남을 알 수 있었다. 이는 용매의 $E_T$의 경향과 잘 일치했으며, 이 경향으로 결과 해석이 가능했다. 그리고 해당 이온에 가장 타당한 용매화수로부터 물과 에탄올 혼합 용매의 조성이 바뀜에 따라 해당 이온에 선택적으로 용매화하는 용매를 알았다.

• 한국가스학회지
• /
• 제6권1호
• /
• pp.92-97
• /
• 2002

가스흡수식 냉온수기의 작동매체로 사용되고 있는 LiBr 수용액 중에서 열교환기 세관용 재료인 동 세관 및 동합금재인 큐프로니켈 세관의 부식특성에 관한 연두를 하기 위하여 $62\%$ LiBr 수용액 중에서 각 재료에 대한 전기화학적 분극실험을 실시하여 부식특성을 고찰한 결과 다음과 같은 결론을 얻었다 1) 열교환기 세관재의 분극저항은 $30\%$ 큐프로니켈 세관 > $10\%$ 큐프로니켈 세관 > 동 세관의 순으로 높게 나타난다 2) 큐프로니켈 세관의 개로전위는 동 세관보다 귀전위화되면서 부식전류밑도는 더 억제된다 3) $30\%$ 큐프로니켈 세관의 부동태 영역은 $10\%$ 큐프로니켈 세관보다 전위구간이 더 크게. 나타나면서 부동태유지 전류밀도는 더 낮아진다.

• Journal of Mechanical Science and Technology
• /
• 제17권4호
• /
• pp.581-589
• /
• 2003

Film absorption involves simultaneous heat and mass transfer in the gas-liquid system. While the non-absorbable gas does not participate directly In the absorption process. its pretence does affect the overall heat and mass transfer. An experimental study was performed to investigate the heat and mass transfer characteristics of LiBr-H$_2$O solution flow ing over 6-row horizontal tubes with the water vapor absorption in the pretence of non-absorbable gases. The volumetric concentration of non-absorbable gas, air, was varied from 0.17 to 10.0%. The combined effects of the solution flow rate and its concentration on the heat and mass transfer coefficients were also examined. The presence of 2％ volumetric concentration of air resulted in a 25% reduction in the Nusselt number and 41% reduction in the Sherwood number Optimum film Reynolds number was found to exist at which the heat and mass transfer reach their maximum value independent of air contents. Reduced Nusselt and Sherwood numbers. defined as the ratio of Nusselt and Sherwood numbers at given non-absorbable gas content to that with pure water vapor, were correlated to account for the reduction in the heat and mass transfer due to non-absorbable gases in a falling film absorption process.

• International Journal of Air-Conditioning and Refrigeration
• /
• 제14권2호
• /
• pp.41-48
• /
• 2006

Absorption performance at the vertical interface between refrigerant vapor and liquid solution of $LiBr-H_{2}O$ solution was enhanced by the waves formed due to the interfacial shear stress. The present study investigated experimentally and analytically the improvements of absorption performance in a falling film by wavy film flow. The dynamic parameter was the film Reynolds numbers ranged from 50 to 150. The energy and diffusion equations were solved simultaneously to find the temperature and concentration profiles at the interface of liquid solution and refrigerant vapor. Absorption characteristics due to heat and mass transfer were analyzed for the falling film of the LiBr aqueous solution contacted by refrigerant vapor in the absorber. Absorption performance showed a peak value at the solution flow rate of $Re_{f}>100$. Absorption performance for the wavy film flow was found to be greater by approximately 10% than that for uniform film flow. Based on numerical and experimental results, the maximum absorption rate was obtained for the wavy flow caused by spring insert. The difference between the measured and the predicted results were ranged from 5.8 to 12%.

• 설비공학논문집
• /
• 제29권7호
• /
• pp.373-384
• /
• 2017

The objective of this study was to determine the effect of refrigerant heat exchanger on the performance of type II absorption heat pump performance using numerical analysis. Two heat exchange installation methods were used: solution to refrigerant and waste hot water to refrigerant. These methods were compared to the standard model of hot water flow without using refrigerant heat exchanger. When waste hot waters were bypassed to refrigerant heat exchanger, COP was not affected. However, steam mass generation rates were increased compared to those of the standard model. When solutions were bypassed to the refrigerant heat exchanger, results were different depending on the place where the solution rejoined. COP and steam mass generation rates were lower compared to those when waste heat water was passed to refrigerant heat exchanger. Thus, it is possible to obtain higher steam mass generation rates by using waste water and installing refrigerant heat exchanger.

• International Journal of Air-Conditioning and Refrigeration
• /
• 제14권4호
• /
• pp.131-137
• /
• 2006

The absorber in which heat and mass transfer phenomena occur simultaneously is one of the most critical components in the absorption system. It has the most significant influence on the performance and the size of the absorption system. During the absorption process, heat and mass transfer resistances exist in both liquid and vapor regions, so that the heat transfer mode should be carefully selected to reduce them. The objective of this paper is to review the previous papers analysing mathematical models of simultaneous heat and mass transfer phenomena during the absorption process. The most conventional working fluids ($H_2O$LiBr and $NH_3/H_2O$) are considered and the most common absorption modes (falling film and bubble mode) are dealt with in this review.

• 대한설비공학회:학술대회논문집
• /
• 대한설비공학회 2008년도 하계학술발표대회 논문집
• /
• pp.109-114
• /
• 2008

A dynamic model has been developed to simulate dynamic operation of a real double-effect absorption chiller. Dynamic behavior of working fluids in main components was modeled in first-order nonlinear differential equations based on heat and mass balances. Mass transport mechanisms among the main components were modeled by valve throttling, 'U' tube overflow and solution sub-cooling. The nonlinear dynamic equations coupled with the subroutines to calculate thermodynamic properties of working fluids were solved by a numerical method. The dynamic performance of the model was compared with the test data of a commercial medium chiller. The model showed a good agreement with the test data except for the first 5,000 seconds during which different flow rates of the weak solution caused some discrepancy. It was found that the chiller dynamics is governed by the inlet temperatures of the cooling water and the chilled water when the heat input to the chiller is relatively constant.

• 설비공학논문집
• /
• 제20권12호
• /
• pp.781-788
• /
• 2008

A dynamic model has been developed to simulate dynamic operation of a real double-effect absorption chiller. Dynamic behavior of working fluids in main components was modeled in first-order nonlinear differential equations based on heat and mass balances. Mass transport mechanisms among the main components were modeled by valve throttling, 'U' tube overflow and solution sub-cooling. The nonlinear dynamic equations coupled with the subroutines to calculate thermodynamic properties of working fluids were solved by a numerical method. The dynamic performance of the model was compared with the test data of a commercial medium chiller. The model showed a good agreement with the test data except for the first 5,000 seconds during which different flow rates of the weak solution caused some discrepancy. It was found that the chiller dynamics is governed by the inlet temperatures of the cooling water and the chilled water when the heat input to the chiller is relatively constant.

• 설비공학논문집
• /
• 제15권1호
• /
• pp.19-24
• /
• 2003

The objectives of this paper are to develop a new method of wettability mea-surement and to study the effect of surface roughness on the wettability in a $H_2O$/LiBr falling film absorber. Two absorber tubes with micro-scale roughness and a bare tube are tested in a falling film absorber installed in a test rig. Inlet solution temperature, concentration and mass flow rate are considered as key parameters. A new method is proposed to estimate the wettability of a tube by measuring a minimum mass flow rate to wet the tube completely. The wettability for the structured surfaces was higher than that for the bare tube. The wettability decreased linearly along the vertical location. The wettability increased with increasing the solution temperature and the solution mass flow rate. The experimental correlations of the wettability for the bare and the micro-hatched tubes were developed with error bands of$\pm20%\;and\;\pm10%$, respectively. This work can be used in the design of absorbers with micro-scale roughness.

• 대한기계학회논문집B
• /
• 제32권9호
• /
• pp.676-682
• /
• 2008

Numerical analysis was carried out to examine the heat transfer and pressure drop characteristics of plate heat exchangers for absorption application using Computational Fluid Dynamics(CFD) technique. A commercial CFD software package, FLUENT was used to predict the characteristics of heat transfer, pressure drop and flow distribution within plate heat exchangers. In this paper, a welded plate heat exchanger with the plate of chevron embossing type was numerically analyzed by controlling mass flow rate, solution concentration, and inlet temperatures. The working fluid is $H_2O$/LiBr solution with the LiBr concentration of 50-60% in mass. The numerical simulation shows reasonably good agreement with the experimental results. Also, the numerical results show that plate of the chevron shape gives better results than plate of the elliptical shape from the view points of heat transfer and pressure drop. These results provide a guideline to apply the welded PHE for the solution heat exchanger of absorption systems.