• Title/Summary/Keyword: Lithium Bromide aqueous solution

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Evaporation of Water in an Aqueous Lithium Bromide Solution flowing over a Horizontal Tube

  • Kim, Dong-Kwan;Kim, Moo-Hwan
    • International Journal of Air-Conditioning and Refrigeration
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    • v.9 no.3
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    • pp.57-62
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    • 2001
  • Falling film heat transfer analyses with aqueous lithium bromide solution were performed to investigate the transfer characteristics of the copper tubes. Finned (knurled) tube and a smooth tube were selected as test specimens. Averaged generation fluxes of water and the heat flux were obtained. As the film flow rate of the solution increased, the generation fluxes of water decreased for both tubes due to the fact that the heat transfer resistance increased with the film thickness. The effect of the enlarged surface area at the knurled tube was supposed to be dominant at a small flow rate. The generation fluxes of water increased with the increasing degree of tube wall superheat. Nucleate boiling is supposed to occur at a wall superheat of 20K for a smooth tube, and at 10K for a knurled tube. The increased performance of the knurled tube was supposed to mainly come from the effect of the increased heating surface area.

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Heat Transfer Enhancement Characteristics for Falling-Film Evaporation on Horizontal Enhanced Tubes with Aqueous LiBr Solution (LiBr 수용액을 이용한 수평관 유하액막 증발의 촉진관 전열향상 특성)

  • Kim, Dong Kwan;Kim, Moo Hwan
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.22 no.9
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    • pp.1267-1276
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    • 1998
  • Falling-film evaporation experiments with aqueous lithium bromide (LiBr) solution were performed to investigate the heat transfer characteristics of enhanced copper tubes. Enhanced tubes (a knurled tube, a spirally grooved tube, and a tube coated with $20{\mu}m$ aluminum particles) and a bare tube were selected as test specimens. Averaged evaporation fluxes of water were obtained from horizontal tubes with various film Reynolds numbers, system pressures, LiBr concentrations and degrees of wall superheat. The enhanced performance of steam generation was compared between tubes with varying parameters. The knurled tube geometry showed the most excellent performance among the tubes tested. The specified enhanced tubes were more useful for generating steam on a low grade heat source such as waste heat.

Falling Film Heat Transfer on a Horizontal Single Tube (수평단관 상의 유하액막 열전달)

  • 김동관;김무환
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.12 no.7
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    • pp.642-648
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    • 2000
  • Falling film heat transfer analyses with aqueous lithium bromide solution were peformed to investigate the transfer characteristics of the copper tubes. Finned(knurled) tube and a smooth tube were selected as test specimens. Averaged generation fluxes of water and the heat transfer performances(heat flux, heat transfer coefficient) were obtained. The results of this work were compared with the data reported previously. As the film flow rate of the solution increased, the generation fluxes of water decreased for both tubes. The reason is estimated by the fact that the heat transfer resistance with the film thickness increased as the film flow rate increased. The effect of the enlarged surface area at the knurled tube was supposed to be dominant at a small flow rate. The generation fluxes of water increased with the increasing degree of tube wall superheat. Nucleate boiling is supposed to occur at a wall superheat of 20 K for a smooth tube, and at 10 K for a knurled tube. The heat transfer performance of the falling film was superior to pool boiling at a low wall superheat below 10 K for both tubes tested. The knurled tube geometry showed good performance than the smooth tube, and the increased performance was mainly came from the effect of the increased heating surface area.

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Fluorescent Silk Fibroin Nanoparticles Prepared Using a Reverse Microemulsion

  • Myung, Seung-Jun;Kim, Hun-Sik;Kim, Yeseul;Chen, Peng;Jin, Hyoung-Joon
    • Macromolecular Research
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    • v.16 no.7
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    • pp.604-608
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    • 2008
  • Color dye-doped silk fibroin nanoparticles were successfully fabricated using a microemulsion method. An aqueous silk fibroin solution was prepared by dissolving cocoons (Bombyx mori) in a concentrated lithium bromide solution followed by dialysis. A color dye solution was also mixed with the aqueous silk fibroin solution. The surfactants used for the microemulsion were then removed by methanol and ethanol, yielding color dye-doped silk fibroin nanoparticles, approximately 167 nm in diameter. The secondary structure of the nanoparticles showed a $\beta$-sheet conformation, as characterized by Fourier transform infrared spectroscopy. The morphology of the nanoparticles was determined by field emission scanning electron microscopy, transmission electron microscopy and atomic force microscopy, and their size and size distribution were measured by dynamic light scattering. The color dye-doped silk fibroin nanoparticles were examined by confocal laser scanning microscopy.

The characteristics of heat transfer coefficient for falling-film evaporation on a horizontal tube with aqueous LiBr solution (LiBr 수용액의 수평관 유하액막 증발에 있어서의 열전달계수 특성)

  • Ji, Yong-Hae
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.21 no.2
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    • pp.294-302
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    • 1997
  • Falling-film evaporation experiments for aqueous solution of lithium bromide (LiBr) were performed on a horizontal smooth 19.05-mm-dia copper tube. Average heat transfer coefficients were obtained with varied film Reynolds numbers, system pressures, LiBr concentrations and degrees of wall superheat. Heat transfer coefficients increase with increasing system pressure and decreasing concentration. For degrees of wall superheat, the heat transfer coefficient did not't show the distinct trend. For this experimental ranges, heat transfer coefficients showed maximum values at an optimal film Reynolds number. The results of this work were compared with pool boiling data reported previously, and it was shown that the heat transfer performance is superior to the pool boiling.

Effects of non-absorbable gases in the absorption process of water vapor Into the Lithium Bromide-water solution film on horizontal tube bank (수평관군에서 리튬브로마이드 수용액 막의 수증기 흡수과정에 대한 비흡수가스의 영향)

  • 김병주;권기석
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.12 no.2
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    • pp.218-225
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    • 2000
  • In the present study, the effects of film Reynolds number (60∼200) and volumetric content of non-absorbable gases (0∼10%) in water vapor on the absorption process of aqueous LiBr solution were investigated experimentally. The formation of solution film on the horizontal tubes of six rows were observed to be complete for Re>100. Transition film Reynolds number were found to exist above which the Nusselt number and Schmidt number diminishes with solution flow rate. As the concentration of non-absorbable gases increased, mass transfer rate decreased more seriously than heat transfer rate did. The degradation effects of non-absorbable gases seemed to be significant especially when small amount of non-absorbable gases were introduced to the pure water vapor.

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Effects of Non-Absorbable Gases on the Absorption Process of Aqueous LiBr Solution Film in a Vertical Tube (II) (수직관내 리튬브로마이드 수용액막의 흡수과정에 대한 비흡수가스의 영향)

  • Kim, Byeong-Ju;Lee, Chan-U
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.22 no.4
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    • pp.499-509
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    • 1998
  • In the absorption process of water vapor in a liquid film, the composition of the gas phase, in which a non-absorbable gas is combined with the absorbate influences the transport characteristics remarkably. In the present study, the absorption processes of water vapor into aqueous solution of lithium bromide in the presence of non-absorbable gases were investigated analytically. The continuity, momentum, energy and diffusion equations for the solution film and gas phase were formulated in integral forms and solved numerically. It was found that the mass transfer resistance in gas phase increased with the concentration of non-absorbable gas. However the primary resistance to mass transfer was in the liquid phase. As the concentration of non-absorbable gas in the absorbate increased, the liquid-vapor interfacial temperature and concentration of absorbate in solution decreased, which resulted in the reduction of absorption rate. The reduction of mass transfer rate was found to be significant for the addition of a small amount of non-absorbable gas to the pure vapor, especially at the outlet of an absorber where non-absorbable gases accumulated. At higher non-absorbable gas concentration, the decrease of absorption flux was almost linear to the volumetric concentration of non-absorbable gas.

Structure and Mechanical Properties of Silk Fiber Stretched in Aqueous Solution of LiBr (Lithium Bromide 수용액중에서 연신된 견의 구조와 물성)

  • 김동건;최진협;소서효
    • Journal of Sericultural and Entomological Science
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    • v.37 no.1
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    • pp.33-38
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    • 1995
  • The mechanical properties and structure of degummed silk fiber stretched after being treated with 8M LiBr aqueous solution were investigated. The mechanical properties of degummed silk fiber were depended upon the treatment temperature of 8M LiBr aqueous solution. That is, the strength and elongation had a tendancy to increase with the temperature, whereas the Young's modulus tended to decrease. The X-ray diffraction pattern showed that the crystalline orientation was disordered by 8$0^{\circ}C$ treatment neverthless destruction of the crystallites did not occur. rho silk fiber could be successfully stretched up 160% under the condition of 8M LiBr aqueous solution at 80 * after immersed for 1hr. For the highly stretched sample(160%), the tensile strength and Young's modulus were significantly improved in spite of lower elongation at break. According to the examination of X-ray diffraction pattern and SEM, the orientation tends to be occured more and more with stretching ratio. From the DSC thermograms, it shows that the thermal decomposition behavior was different between untreated and treated specimen with 8M LiBr aqueous solution. The maximun endothermic peak of thermal decomposition tends to increase to high temperature with the increase of stretching ratio.

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Experimental Investigation of Heat Transfer in Absorber with Small Diameter Tube

  • Phan Thanh Tong;Moon Choon-Geun;Kim Jae-Dol;Yoon Jung-In
    • Proceedings of the Korean Society of Marine Engineers Conference
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    • 2006.06a
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    • pp.261-262
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    • 2006
  • The effect of tube diameter on heat transfer characteristics of absorber in absorption chiller/heater using LiBr solution as a working fluid has been investigated by experimental study to develop a high performance and compact absorber. A system Includes a tube absorber, a generator, solution distribution system and cooling water system was set up. The diameter of the heat exchanger tube inside absorber was changed from 15.88mm to 12.7mm and 9.52mm. The experimental results show that the heat transfer coefficient, Nusselt number and heat flux increase as solution flow rate and cooling water flow rate increase. The heat transfer performance increases as tube diameter decreases. Among three different tube diameters, the smallest tube diameter 9.52mm has highest heat transfer performance. A comparison of the heat transfer coefficient obtained by the present study with those of previous experimental results showed good overall agreement.

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Integral Analysis of the Effects of Non-absorbable gases on the Heat Mass Transfer of Laminar Falling Film

  • Kim, Byong-Joo
    • International Journal of Air-Conditioning and Refrigeration
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    • v.6
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    • pp.56-66
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    • 1998
  • The absorption process of water vapor in a liquid film is an important process in LiBr-Water absorption system. The composition of the gas phase, in which a non-absorbable gas is combined with the absorbate, influences the transport characteristics. In the present work, the absorption processes of water vapor into aqueous solutions of lithium bromide in the presence of non-absorbable gas are investigated. The continuity, momentum, energy and diffusion equations for the solution film and gas are formulated in integral forms and solved numerically. It is found that the mass transfer resistance in gas phase increases with the concentration of non-absorbable gas. However the primary resistance to mass transfer is in the liquid phase. As the concentration of non-absorbable gas in the absorbate increases, the interfacial temperature and concentration of absorbate in solution decrease, which results in the reduction of absorption rate. The reduction of mass transfer rate is found to be significant for the addition of a small amount of non-absorbable gas to the pure vapor, especially at the outlet of tube where the non-absorbable gas accumulates. At higher non-absorbable gas concentration, the decrease of absorption rate seems to be linear to the concentration of non-absorbable gas.

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