• Title/Summary/Keyword: Paper Heat exchanger

Search Result 477, Processing Time 0.033 seconds

Numerical Evaluation of Heat Transfer un Ground Heat Exchanger Considering Flow through U-loop (파이프 순환수의 수치해석 모사를 통한 수직 밀폐형 지중열교환기 단면의 열전달 효율 평가)

  • Gil, Hu-Jeong;Lee, Chul-Ho;Lee, Kang-Ja;Choi, Hang-Seok
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 2009.06a
    • /
    • pp.583-587
    • /
    • 2009
  • This paper presents a series of numerical simulations on the thermal performance and sectional efficiency of a closed-loop vertical ground heat exchanger (U-loop) equipped in a geothermal heat pump system (GHP). A 3-D finite volume analysis (Fluent) was used to simulate the operating process of the closed-loop vertical ground heat exchanger by considering the effect of the thickness of HDPE pipe and grout thermal properties, distance between the inflow and outflow pipes, and the effectiveness of the latticed HDPE pipe system. It was observed that the thermal interference between the two strands of U-loop is of importance in determining the efficiency of the ground heat exchanger, and thus it is highly recommendable to modify the cross section configuration of the conventional U-loop system by including a thermally insulating latice between the two strands.

  • PDF

A Study on Performance Analysis of the Bubble Pump in Solar Water Heater System (태양열 온수기 시스템에 적용된 기포펌프의 성능평가에 대한 연구)

  • Lee, Kwang-Sung;Li, Xuesong;Jin, Zhenhua;Jeong, Hyo-Min;Chung, Han-Shik
    • Proceedings of the KSME Conference
    • /
    • 2008.11b
    • /
    • pp.2310-2315
    • /
    • 2008
  • In this paper, study on performance analysis of bubble pump on the domestic solar water heater system is presented. Device of this experiment is consisted of bubble pump, solar collector and heat exchanger. At the mean time, this system have attached temperature sensors and pressure sensors at bubble pump. In addition, the flow meter was installed at outlet of heat exchanger. And then result of experimental study, average value of the heat exchange amount in heat exchanger was about 7.9kcal/hr, the maximum value of the heat amount in water tank($0.4m^3$) was 489.7kcal/hr and the maximum value of the mass flow rate in bubble pump was about $0.5{\ell}/min$.

  • PDF

Performance Analysis of Refrigeration Cycle of Hydrocarbon Refrigerant using Suction-Line Heat Exchanger (흡입관 열교환기를 이용한 탄화수소계 냉매용 냉동사이클의 성능 분석)

  • Ku, Hak-Keun
    • Journal of the Korea Academia-Industrial cooperation Society
    • /
    • v.10 no.9
    • /
    • pp.2195-2201
    • /
    • 2009
  • This paper considers the influence of suction-line heat exchangers on the efficiency of a refrigeration cycle using hydrocarbon refrigerants such as R290, R600a and R1270. These suction-line heat exchangers can, in some cases, yield improved system performance while in other cases they degrade system performance. A steady state mathematical model is used to analyze the performance characteristics of refrigeration cycle with suction-line heat exchanger. The influence of operating conditions, such as the mass flowrate of hydrocarbon refrigerants, inner diameter tube and length of suction-line heat exchanger, to the performance of the cycle is also analyzed in the paper. Results showed that the mass flowrate of hydrocarbon refrigerants, inner diameter tube and length of suction-line heat exchanger, and effectiveness have an effect on the cooling capacity, compressor work and RCI(Relative Capacity Index) of this system. With a thorough grasp of these effect, it is necessary to design the compression refrigeration cycle of hydrocarbon refrigerants using suction-line heat exchanger.

A Study on Development of a Plugging Margin Evaluation Method Taking Into Account the Fouling of Shell-and-Tube Heat Exchangers

  • Hwang, Kyeong-Mo;Jin, Tae-Eun;Kim, Kyung-Hoon
    • Journal of Mechanical Science and Technology
    • /
    • v.20 no.11
    • /
    • pp.1934-1941
    • /
    • 2006
  • As the operating time of heat exchangers progresses, fouling caused by water-borne deposits and the number of plugged tubes increase and thermal performance decreases. Both fouling and tube plugging are known to interfere with normal flow characteristics and to reduce thermal efficiencies of heat exchangers. The heat exchangers of Korean nuclear power plants have been analyzed in terms of heat transfer rate and overall heat transfer coefficient as a means of heat exchanger management. Except for fouling resulting from the operation of heat exchangers, all the tubes of heat exchangers have been replaced when the number of plugged tubes exceeded the plugging criteria based on design performance sheet. This paper describes a plugging margin evaluation method taking into account the fouling of shell-and-tube heat exchangers. The method can evaluate thermal performance, estimate future fouling variation, and consider current fouling level in the calculation of plugging margin. To identify the effectiveness of the developed method, fouling and plugging margin evaluations were performed at a component cooling heat exchanger in a Korean nuclear power plant.

A Study on the Development of Plugging Margin Evaluation Method Reflected the Fouling of a Shell-and-Tube Heat Exchanger (다관원통형 열교환기의 파울링 현상을 고려한 관막음 여유 평가법 개발 연구)

  • Hwang, Kyeong-Mo;Jin,Tae-Eun
    • Transactions of the Korean Society of Mechanical Engineers B
    • /
    • v.28 no.11
    • /
    • pp.1384-1389
    • /
    • 2004
  • As operating time of heat exchangers progresses, fouling generated by water-borne deposits and the number of plugged tubes increase and thermal performance decreases. Both fouling and tube plugging are known to interfere with normal flow characteristics and to reduce thermal efficiencies of heat exchangers. The heat exchangers of domestic nuclear power plants have been analyzed in terms of the heat flux and heat transfer coefficient at test conditions as a means of heat exchanger management. Except for the fouling level generated in operation of heat exchangers, also, all of the tubes of heat exchangers have been replaced when the number of plugged tubes exceeds the plugging criteria based on design performance sheet. This paper describes the plugging margin evaluation mettled reflected the fouling of shell-and-tube heat exchangers, which can evaluate the thermal performance for heat exchangers, estimate the future fouling variations, and reflect the current fouling level. To identify the effectiveness of the developed method, the fouling and plugging margin evaluations were performed for a component cooling heat exchanger in a nuclear power plant.

An Analysis of Heat Transfer and Pressure Drop Characteristics for Optimum Design of Cryogenic Heat Exchanger used for Liquid Nitrogen Cooling (액체질소 냉각용 극저온 열교환기의 최적설계를 위한 열전달 및 압력강하 특성 분석)

  • Ko, Ji Woon;Jeon, Doong Soon
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
    • /
    • v.30 no.1
    • /
    • pp.24-32
    • /
    • 2018
  • In this paper, analytical studies were conducted to obtain optimal design factors and analysis parameters of liquid nitrogen cooling exchanger applied in cryogenic refrigerator. The target value of heat transfer rate was more than 1 kW and pressure drop was less than 40 kPa. Design factors of cryogenic heat exchanger included width of channel and configuration of paths. Analytical factors of liquid nitrogen cooling exchanger included temperatures of coolant header surface and inlet liquid nitrogen. The width and number of channels in the design parameters were 0.0050~0.0150 m and 4~8, respectively. The configuration of channel path was 4 ways. Temperatures of coolant header surface and inlet liquid nitrogen in analytical parameters were 74 to 78K and 82 to 86K, respectively. As result, the design factor and analysis parameter satisfying the target values were obtained. The biggest heat transfer rate was 1.36 kW with pressure drop of 32.26 kPa.

Tube Plugging Criteria for the Non-Regenerative Heat Exchanger in the Steam Generator Blowdown System of Nuclear Power Plant (증기발생기 취출수계통 비재생열교환기 전열관 관막음 기준 설정)

  • Kim, Hyeong-Nam;Choe, Seong-Nam;Yu, Hyeon-Ju;Choe, Jin-Hyeok
    • Proceedings of the KWS Conference
    • /
    • 2006.10a
    • /
    • pp.38-40
    • /
    • 2006
  • Nuclear power plants are urged to reduce operating and maintaining costs to remain competitive as well as to increase the safety preventing the radioactive material to the atmosphere. To reduce the cost and to increase the safety, the inspection of balance-of-plant heat exchanger becomes important. However, there are some problems for plugging the heat exchanger tubes since the criterion and its basis are not clearly described. The codes and standards related to show the tube plugging criteria may not exist currently. In this paper, a method to establish the tube plugging criteria of BOP heat exchangers is introduced and the tube plugging criteria for the non-regenerative heat exchanger in the steam generator blow-down system of nuclear power plant. This method relies on the similar method used to establish the plugging criteria for the steam generator tubes.

  • PDF

Performance Analysis of Ground Thermal Conductivity by Ground Heat Exchanger (지중열교환기의 지중열전도도 성능 분석)

  • Kim, Young-Jun;Choi, Jae-Sang;Kang, Yong-Tae
    • Proceedings of the SAREK Conference
    • /
    • 2005.11a
    • /
    • pp.161-166
    • /
    • 2005
  • The objectives of this paper are to estimate the ground thermal conductivity by ground heat exchangers in two different places - Chooncheon and Wonjoo, and to analyze the effect of ground thermal conductivity on the ground thermal diffusivity and the size of the ground heat exchanger. In Chooncheon area, a single-U type HDPE pipe (25mm diameter) with borehole diameter of 150mm, length of 150m is installed. In Wonjoo area, a single-U type HDPE pipe (40mm diameter) with borehole diameter 150mm, length of 200m is installed. It is found that the ground thermal conductivities are estimated as 2.69 $W/m^{\circ}C$ and 2.99 $W/m^{\circ}C$ in Chooncheon and Wonjoo, respectively. It is also found that the ground heat exchanger size is reduced by 8.6% with 25% increase of ground thermal conductivity, and increase by 11.8% with 25% decrease of ground thermal conductivity.

  • PDF

Analysis of the cooling system for a superconducting generator (초전도발전기의 냉각시스템 해석)

  • Kim, K.W.;Chung, T.E.;Shin, H.-C.
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
    • /
    • v.9 no.4
    • /
    • pp.446-453
    • /
    • 1997
  • The superconducting winding in rotor of a superconducting generator should be kept at extremely low temperature of 4-5 K to maintain the superconducting state. For this purpose the liquefied helium is used for the coolant and it is very important to analyze and design a cooling system making effective use of the coolant. In this paper, the typical heat exchanger of a superconducting generator with the flow passage is analyzed with regard to the thermal equilibrium. An experimental constant relevant to the flow condition in the flow passage is determined with heat exchange experiments in cryostat. Also a new heat exchanger with porous material is proposed and designed. Results of the numerical analysis for the temperature distributions for the torque tube and the coolant are reported and the efficiency of the heat exchanger is discussed from the viewpoint of amounts of coolant needed.

  • PDF

Flow Distribution Characteristics in a Multi-Pass Heat Exchanger (다패스 열교환기에서의 유량분배 특성)

  • Kim, Min-Soo;Kang, Soo-Jin;Lee, Kwan-Soo
    • Proceedings of the SAREK Conference
    • /
    • 2006.06a
    • /
    • pp.737-742
    • /
    • 2006
  • This paper numerically investigates to evaluate the performance according to the number of passes and the inlet/outlet diameter in a multi-pass multi-branch heat exchanger. A JF factor is used as an evaluation characteristic value to consider the heat transfer rate and the pressure drop simultaneously. It estimates the performance according to the number of passes and the inlet diameter of the reference heat exchanger. When the ratio of the inlet diameter to the header height is about 0.5, the optimum number of passes is selected along with the inlet diameter.

  • PDF