• Title/Summary/Keyword: C.C.M system

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An Experiment on Evaporating Heat Transfer of HCFC-22 for Transport Refrigeration System (HCFC-22 냉매사용 차량냉동시스템의 증발 열전달에 관한 실험)

  • Oh, M.D.;Kim, S.C.
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.6 no.2
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    • pp.166-174
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    • 1994
  • An experimental study has been performed to identify the evaporation characteristics of HCFC-22 for transport refrigeration system. Heat transfer coefficients were measured in a horizontal, smooth evaporating tube with an inner diameter of 10.7mm and a length of 2.8m. The refrigerant was heated electrically by surface-wrapped heaters and uniform power is applied along the tube. The entire tube was divided into 7 sections. Surface temperatures of tube and refrigerant temperature in each test section were measured. Pressure drops in each section and the inlet pressure were also measured. The mass flowrate of the refrigerant was controlled and measured. A single tube evaporation test was conducted for different ranges of mass flux of refrigerant, heat flux of evaporator and condensing temperature of transport refrigeration system. The evaporation heat transfer coefficients of HCFC-22 were compared with predictions from the well known Chen's correlations. Averaged heat transfer coefficients in this experiment range from $2kW/m^2/^{\circ}C$ to $3kW/m^2/^{\circ}C$. Most of the experimental results differ from the predicted ones by less than ${\pm}30%$.

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A Study on Microorganisms Decontamination Using a Vapor-Phase Hydrogen Peroxide System (과산화수소 증기 시스템을 이용한 미생물 제독에 관한 연구)

  • Kim, Yun Ki;Kim, Min Cheol;Yoon, Sung Nyo;Hwang, Hyun Chul;Ryu, Sam Gon
    • Journal of Environmental Health Sciences
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    • v.39 no.3
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    • pp.279-288
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    • 2013
  • Objectives: Effectiveness and conditions of vapor-phase hydrogen peroxide (VPHP) system on decontamination of Geobacillus stearothermophilus(GS) spores, Escherichia coli (E.coli) and Enterobacteria phage felix01 (felix01) were determined. Methods: The VPHP system was designed to vaporize 35% (w/w) solution of hydrogen peroxide, continuously to inject and withdraw VPHP. The system and VHP 1000ED (Steris) were operated such that dehumidification and conditioning were initiated without samples in the chamber. Then the samples were loaded into and removed. Coupons (glass, anodizing, silicon, viton) with GS spores ($1{\times}10^6$ colony forming unit/mL [CFU/mL]), E.coli ($1{\times}10^7$ CFU/mL) and felix01 ($1{\times}10^7$ plaque forming unit/mL[PFU/mL]), and Biological Indicator (BI) with GS spores ($1{\times}10^6$ CFU/mL) on stainless steel coupons were used. The tested samples were sonicated and vortexed, and then were plated for enumeration, followed by incubation at $55^{\circ}C$, 24 hr for GS spores, and at $37^{\circ}C$, 24 hr for E.coli and felix01. BI analysis in broth culture was only qualitative. Results: The efficacy of the VPHP system on decontamination was almost equivalent to that of VHP 1000ED. The conditions for complete decontamination with the VPHP system was as follows: concentration; 700~450 ppm, relative humidity; approximately 55%, and temperature; $34{\sim}32^{\circ}C$. When comparing the decontamination efficiency among different kinds of coupons, glass was the most effective, however, all kinds of coupons were decontaminated completely after 60 min exposure in both systems. Conclusion: The VPHP system can be recommended as an alternative system for traditional system using ethylene oxide, formaldehyde or chlorine dioxide.

Commercial Production for the Hydrogen Generation with Alkaline Electrode Cells (수소 생산을 위한 알칼라인 수전해장치 상용품 제작)

  • KIM, BO YEON;KIM, DONG JIN;KANG, EUN YOUNG;KIM, TAE WAN;SIM, HUI CHAN;LEE, TAECK HONG
    • Journal of Hydrogen and New Energy
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    • v.26 no.3
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    • pp.206-211
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    • 2015
  • For the hydrogen production, Gas Lab and Gnc make alkaline watrer electrolyzer and found optimized condition of experimental parameters of cell material and operating procedures. For the commercial production, we saved electric power consumption and caloric based efficiency with over 70%. Used cell pressures are 10 bar, 30 bar and consumed electricity is $4,000A/m^2$, 4.19 kW ($T=100^{\circ}C$) at 10 bar. Another data is $2,000A/m^2$, 3.92 kW ($T=95^{\circ}C$) at 30 bar. Applied voltage is 1.75 V ($100^{\circ}C$, 10 bar), 1.64 V ($95^{\circ}C$, 10 bar), 1.81 V ($85^{\circ}C$, 30 bar), 1.76 V ($95^{\circ}C$, 30 bar). As cell temperature increase, applied voltage has been decreased and current has been increased. The concentration of KOH solution is 30 weight %.

Addition Effects of Alkali Metal Oxide on Some Properties of Porous Glass-Ceramics in the $CaO-TiO_2-P_2O_5$ System ($CaO-TiO_2-P_2O_5$계 다공질 결정화 유리의 물성에 미치는 알카리 금속 산화물의 첨가효과)

  • 장순규;최세영
    • Journal of the Korean Ceramic Society
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    • v.31 no.11
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    • pp.1337-1345
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    • 1994
  • Glasses in the system of 45CaO-25TiO2-30P2O5 containing 1 mole% of M2O(M=Li, Na, K) were melted and crystallized. And their crystal phases were Ca3(PO4)2, CaTi4(PO4)6, and TiO2. Porous glass-ceramics with skeleton of two crystal phase CaTi4(PO4)6 and TiO2 were prepared by selective leaching of Ca3(PO4)2 with 0.1 N-HCl. Glass transition temperature(Tg) and crystallization temperature(Tc) were decreased by addition of 1 mole% alkali metal oxide. Pore size of porous glass-ceramics was increased with increasing heat treatment temperature and its dependence on heat treatment temperature was decreased with addition of Na2O and K2O. It was found that porous glass-ceramics of parent glass and containing 1mole% M2O(M=Li, Na, K) composition had maximum specific surface area, porosity and maximum of crystallzed phase by heat treatment at 80$0^{\circ}C$, 76$0^{\circ}C$, 78$0^{\circ}C$, 80$0^{\circ}C$ respectively.

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A Study on the Press Belt Motion in the Fusing Press M/C (심지융착기의 압착벨트 운동에 대한 연구)

  • Huh You;Ahn Seong-Gi;Jang Seung-Ho
    • Textile Coloration and Finishing
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    • v.17 no.5 s.84
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    • pp.53-60
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    • 2005
  • Fusing press m/c is used for heating and pressing the specimens that are fed into between the two moving belts. Therefore the belt movement, belt temperature, and the pressure between belts must be kept constant. Especially, the belts should move in a limited operation range. When the belts run far out of the operation point, the machine has to be stopped, which results in a product defect because the fusing conditions, e.g., temperature and pressure, change during the transient process time period. It is important to avoid the belt stopping by maintaining the belt movement in a limited range. This study reports about the movement of the endless fusing belt in a long-span roller fusing m/c. The belt position changes as the 1st-order system does; if the roller axes are slanting each other with a certain angle, the belt running around the two rolls shows a dynamic behavior with the time that deviates fastly at the beginning from the initial condion and slows down. Then it reaches at a final position. The skewer the axes, the greater the position change. The inital change rate of the belt becomes large as the skewness of the axes between the two rollers increases.

A Study on the Advanced Treatment of Wastewater by Plants (식물을 이용한 오수의 고도처리에 관한 연구)

  • 이용두;김현희
    • Journal of Environmental Science International
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    • v.8 no.1
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    • pp.75-81
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    • 1999
  • In recent years increasing production and disposal of wastewater have caused an accelerated eutrophication of receiving waters. Therefore, in order to alleviate the detrimental impact of wastewater discharge, there is an increasing demand for removing the main nutrients, nitrogen and phosphorus, as well as the organic content of the waste water prior to disposal. This is effectively achieved by extended conventional treatment technology. However, the working expenses and energy requirements of such advanced treatment systems are rather high. So in a sparsely populated rural community is required development of wastewater treatment system combined with the regional characteristics. In this study, the systems are planted with Reeds and Amaryllis In A.C and estimated purification potential of system. The results obtained are as follows. BOD removal rate is 20% in the early stage, the last removal rate is 35% in A.C process and is 65% in Amaryllis+A.C process and is 50% in Reed+A.C process. T-N removal rate by Amaryllis is average 2.6g/$m^3$ㆍd, T-N removal rate by Reed is average 1.76g/$m^3$ㆍd. T-P removal rate by Amaryllis is average 0.27g/$m^3$ㆍd, T-P removal rate by Reed is average 0.25g/$m^3$ㆍd. BOD removal rate constant with retention time is 1.4494(1/d), T-N removal rate constant is 0.5428(1/d), T-P removal rate constant is 0.5287(1/d).

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Expression of Pseudorabies Virus (PRV) Glycoproteins gB, gC and gD using Bacterial Expression System

  • Yun, Bit-Na-Rae;Bae, Sung-Min;Lee, Jun-Beom;Kim, Hee-Jung;Woo, Soo-Dong
    • International Journal of Industrial Entomology and Biomaterials
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    • v.23 no.1
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    • pp.147-153
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    • 2011
  • The Pseudorabies (PR), also called Aujeszky's disease (AD), is an infectious viral disease caused by an alpha herpes virus and has domestic and wild pigs, as well as a wide range of domestic and wild animals, as the natural host. Pseudorabies virus (PRV) virions contain several envelope glycoproteins. Among them, gB, gC and gD are regarded as the major immunogenic proteins. We expressed these glycoproteins using the bacterial expression system and analyzed recombinant proteins. Expression of glycoproteins gC and gD were observed on SDS-PAGE or Western blot analysis, but gB was not. Optimal concentration of IPTG and inducing time were determined as 1.0 mM and 4 h, respectively, for the expression of both gC and gD in E. coli. A sodium dodecyl sulfate (SDS) was the most efficient detergent in solubilizing insoluble recombinant protein.

Preparation of Sialyloligosaccharide from Raw Egg Yolk in Biphasic System (Biphasic system에 의한 생난황으로부터 시알산 함유 올리고당의 제조)

  • 김상진;임한진;안병용;최동성
    • KSBB Journal
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    • v.15 no.1
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    • pp.55-59
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    • 2000
  • Protease-catalyzed liberation of sialyloligosaccharide from raw egg yolk was investigated in biphasic system, water-immiscible hexane system. Biphasic system 1, in which water was the continuous phase, was better than the opposite biphasic system ll in sialyloligosaccharide liberation. The optimal conditions of temperature, water content and reaction time were $30^{\circ}C$, 20% and 12 hours, respectively. Protease activity was strongly influenced by the amount of water present in the reaction mixture. The liberation of sialyloligosaccharide was accelerated by protease pre-treatment at $30^{\circ}C$ in 0.2 M NaCl solution, prior to addition of hexane (Biphasic system I).

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Construction and Analysis of cDNA Library from Porphyra yezoensis (방사무늬 김의 cDNA Library 제조 및 분석)

  • 서수분;이은경;김영진
    • Journal of Life Science
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    • v.9 no.5
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    • pp.531-536
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    • 1999
  • As an attempt to preserve resources in marine biological organisms, we first constructed a cDNA library from the red alga Porphyra yezoensis. The library construction method from P. yezoensis consists of three steps; those include protoplast presparation, RNA isolation, and phage library construction. Protoplast was prepared in order to remove much of the carbohydrate compounds which are characteristics of algal cell walls. Carbohydrate contamination in the purified RNA may inhibit further enzyme reactions, those carbohydrates should be removed. RNA samples prepared from protoplast still seemed to contain residual amount of carbohydrate because mRNA isolation with conventional method failed. We therefore developed a method with Poly ATtract mRNA isolation system. The constructed phage library was tested by analyzing cDNA insert in phage vector from randomly picked ten independent white plagues. All of the phages contained cDNA inserts with sizes ranging 0.5kb and 2.0kb.

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An Application of the Water Mist System for Underground Utility Tunnel (지하구 미분무수 소화설비 적용에 관한 연구)

  • 김운형;김종훈;박승민;김태수;민인홍;전동일;김상욱
    • Fire Science and Engineering
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    • v.16 no.1
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    • pp.66-76
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    • 2002
  • This paper includes new nozzle design, basic design factors of water mist system that minimize a thermal damage of cable causing business interruption and applying underground utility tunnel. A underground concrete structure (2.5 m(H)$\times$2.5 m(W)$\times$25 m(D)) is constructed in order to test a nozzle performance. Under the designing fire scenario, critical thermal damage of cable sheath ($400^{\circ}c$) reached within a 2 minutes with unsuppressed fire, but type 1 nozzle (SMD 470 $\mu{m}$) and type 2 nozzle (SMD 650 $\mu{m}$) control cable temperature below $400^{\circ}c$. A system performance and fundamental design factors; K factor, flow rate, spray angle, size distribution, nozzle pressure, spray density are analyzed and proposed for system optimization.