• 공업화학
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• 제10권3호
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• pp.400-406
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• 1999

고효율 가스흡수식 냉방기를 위한 신 작동매체로 기존의 $LiBr-H_2O$ 용액에 $LiNO_3$, LiCl, LiI 성분을 첨가하여 4성분 용액을 제조하였다. 본 연구를 통하여 제조된 4성분계의 작동매체에 대한 용해도와 증기압을 측정하여 기존의 $LiBr-H_2O$계와 비교 분석하였으며, 이들에 대한 최적혼합 몰비를 각각 구하였다. 용해도 측면에서 $LiBr-LiNO_3-LiCl$계는 5:1:1~2, $LiBr-LiNO_3-LiCl$계는 5:1:1, LiBr-LiI-LiCl계의 경우 5:1:0.5~1로 나타났다. 한편 $LiBr-LiNO_3-LiCl-H_2O$계를 제외하고 모두 증기압이 $LiBr-H_2O$계에 비해 높게 나타났다. $LiBr-LiNO_3-LiCl-H_2O$계를 이용한 흡수성능 실험시 $LiBr-H_2O$계 보다 우수한 특성을 지녔다.

• 한국태양에너지학회 논문집
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• 제25권3호
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• pp.27-35
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• 2005

In this paper, a thermodynamic analysis was performed to provide design data for a double-effect absorption heating system with water-LiBr-LiSCN mixture which utilizes solar energy as evaporator heat source. In addition, a comparative study of the water-LiBr-LiSCN mixture against the water-LiBr pair was conducted by a computer simulation. The computer simulation is based on mass, material and heat balance equations for each part of the system. Coefficients of performance and flow ratios for effects of different operating temperatures are investigated. It is found that the heating COP is higher for the water-LiBr-LiSCN mixture than for the water-LiBr pair, and FR is lower for the former.

• 한국가스학회지
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• 제2권4호
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• pp.47-52
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• 1998

수냉식 흡수식 냉동기에 주로 사용되고 있는 LiBr/water 흡수용액을 대체할 수 있는 신흡수 용액으로 제안된 흡수용액중 4성분계 흡수용액($LiBr+LiNO_3+LiC1+H_2O$)의 수증기 흡수성능을 수직관 흡수기를 사용하여 시험하였다. 시험변수로는 입구농도, 입구온도, 냉각수 입구온도, 용액유량을 변경하였다. 수증기 흡수특성 시험 결과 4성분계 용액이 LiBr/water용액보다 $2\%$ 높은 농도에서 대둥한 흡수력을 가짐을 알 수 있었다. 그러나 4성분계 흡수용액이 LiBr/water용액보다 $3\%$정도 용해도가 높으므로 실제 흡수식 냉동기에 적용시 LiBr용액보다 우수한 흡수능력을 가질 수 있어 소형, 공냉형 흡수식 냉동기에 적용이 가능하다.

• 한국산학기술학회논문지
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• 제19권5호
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• pp.27-34
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• 2018

최근 들어 공기의 제습에 액체 제습제를 사용하는 방법이 각광을 받고 있다. LiCl과 LiBr은 우수한 열물성으로 인하여 액체 제습 시스템에 널리 사용되고 있다. 본 연구에서는 LiCl과 LiBr 수용액을 사용하여 상용 Celdek 소자의 제습 성능을 실험하였다. 실험은 입구 건습구 온도를 $35^{\circ}C/28^{\circ}C$로 유지하고 전방 풍속을 2.0 m/s에서 4.0 m/s로 변화시키며 수행되었다. 수용액의 입구 온도와 농도는 $20^{\circ}C$, 50%, 수용액의 순환량은 50 kg/h로 유지하였다. 실험 결과 제습량은 풍속이 증가할수록 증가하였다. 또한 LiCl의 제습 성능은 LiBr보다 평균 27% 크게 나타났다. 이는 LiCl의 포화 절대 습도가 LiBr의 포화 절대습도보다 작기 때문이다. 반면 LiBr의 압력 손실은 LiCl보다 평균 12% 크게 나타났다. 한편 LiCl 과 LiBr의 Sherwood 수는 비교적 잘 일치하였다. 이로부터 제습제가 Sherwood 수에 미치는 영향은 미미함을 알 수 있다. 기존 상관식들은 본 실험의 Sherwood 수를 현저히 높게 예측하였다.

• 공업화학
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• 제9권1호
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• pp.82-88
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• 1998

고효율 공냉형 흡수식 냉방기를 위한 신작동매체로 기존의 $LiBr-H_2O$계에 높은 흡수성과 용해성를 지닌 $LiNO_3$과 LiCl 무기물을 각각 첨가하여 제조하였다. 본 연구를 통하여 제조된 다성분계의 작동매체에 대한 용해도와 증기압을 측정하여 $LiBr-H_2O$계와 비교 분석하였으며, 이들에 대한 최적혼합비를 각각 구하였다. 용해도 측면에서 $LiBr-LiNO_3-H_2O$계의 경우, LiBr과 $LiNO_3$의 최적혼합 몰비는 5:1이었으며, 반면 $LiBr-LiNO_3-LiCl-H_2O$계의 경우 LiBr, $LiNO_3$, LiCl의 최적혼합몰비는 5:1:2로 나타났다. 한편 증기압은 $LiBr-H_2O$계에 $LiNO_3$의 첨가량이 증가하였으나, LiCl의 경우에는 첨가량이 증가함에 따라 감소하는 경향을 각각 나타내었다.

• 한국태양에너지학회 논문집
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• 제26권4호
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• pp.73-81
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• 2006

In this paper, with water-LiBr-LiSCN mixture which utilizes solar energy as mid temperature range evaporator heat source, a thermodynamic analysis was performed to provide design data for a double-effect absorption heating system. A comparative study of the water-LiBr-LiSCN mixture against the water-LiBr pair was conducted by a computer simulation. The computer simulation is based on mass, material and heat balance equations for each part of the system. Coefficients of performance and flow ratios for effects of different operating temperatures are investigated. It is found that the heating COP is higher for the water-LiBr-LiSCN mixture than for the water-LiBr pair, and FR is lower for the former.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.228-233
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• 2000

An experimental study has been performed regarding heat and mass transfer in a falling film absorber of domestic small-sized absorption chiller/heater. Components were concentrically arranged in cylindrical form : from the center, with a series of low temperature generator, absorber and evaporator. The arrangement of such helical-typed heat exchangers allows to make the system more compact as compared to conventional one. Experimental measurements were conducted with a helical absorber using $LiBr+LiI+LiNO_3+LiCl$ and LiBr solutions. As a result, the heat and mass flux performance of $LiBr+LiI+LiNO_3+LiCl$ solution shows the tendency of $2{\sim}5%$ increase. Therefore, $LiBr+LiI+LiNO_3+LiCl$ solution can be taken consideration into applying to small-sized absorption chiller/heater because of using without crystal through high concentration as 4wt% comparing with LiBr solution.

• 설비공학논문집
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• 제9권2호
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• pp.163-170
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• 1997

Solubility on $(LiBr+CaCl_2)$ in water has been measured systematically and compared with those of pure LiBr. It has been observed that there exists optimum value of $CaCl_2(LiBr+CaCl_2)$ in solubility when total$(LiBr+CaCl_2)$ concentration is higher than 57wt%. As total concentration increases up to 65wt%, it is found that the optimum value also increases monotonically. From the experimental results, a master plot has been constructed, with which optimum ratio of LiBr to $CaCl_2$ can be found in terms of total concentration. Vapor pressure of $H_2O/(LiBr+CaCl_2)$ solution with optimum contents of $CaCl_2$ has been observed to be changed negligibly at relatiely low temperature. However, as temperature increases, it is found that increasement in vapor pressure is significant.

• 설비공학논문집
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• 제7권2호
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• pp.196-206
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• 1995

Experimental investigations on heat and mass transfer characteristics in a vertical tube absorber have been carried out. Three different copper tubes with a length of 1.5m have been tested using LiBr solution and LiBr-$CaCl_2$ solution. The effects of solution flow rate, cooling water temperature, solution inlet temperature and evaporation temperature have been investigated in detail. It is found that heat transfer coefficient increases gradually with the increase of solution flow rate, but decreases rapidly for the flow rates less than 0.02kg/ms. The grooved tube generally shows better heat transfer performances than the smooth tube. LiBr solution shows almost no absorption capability for the cooling water temperatures over $40^{\circ}C$. LiBr-$CaCl_2$ gives less decreasing rate in absorption capability at these temperatures and the heat transfer coefficient becomes less dependent on the types of tubes in use. Considering heat and mass transfer rates, LiBr-$CaCl_2$ solution is found to be more suitable than LiBr solution for air cooled absorber, which operates at higher temperature than water cooled absorber.

• Journal of Advanced Marine Engineering and Technology
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• 제22권6호
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• pp.792-799
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• 1998

Further improvement of existing $H_{2}O/LiBr$ absorption refrigeration machine is absolutely neces-sary to promote the utilization of gas-cooling system Among various methods to improve the per-formance of the absorption refrigeration machine this research has focused on the use of a new working fluid that has better properties than the existing $H_{2}O/LiBr$ working fluid. In the series of the research, $H_{2}O/LiBr+HO{(CH_{2})}_{3}OH$ system was selected as the most promisable candidate. The absorption refrigeration machine is water-cooled double-effect, $H_{2}O/LiBr+HO{(CH_{2})}_{3}OH$ sys-tem with series flow type. In this study we found out the characteristic of new working solution through the cycle simulation and compared the result with that of LiBr solution to evaluate. Theoptimum designs and operating conditions were determined based on the operating constraints and the coefficient of performance. Results demonstrate that new working fluid subsrantially increases COP by as much as 10% and has a wider working range with 8% higher crystallization limits compared to the conventional $H_{2}O/LiBr$.