• 제목/요약/키워드: Heat transfer deterioration

검색결과 49건 처리시간 0.026초

Fouling Reduction Characteristics of a Fluidized Bed Heat Exchanger for Flue Gas Heat Recovery (연도가스 열회수용 순환유동층 열교환기의 오염저감특성)

  • 이금배;전용두
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • 제16권8호
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    • pp.770-777
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    • 2004
  • Fouling and cleaning tests are performed for a uniquely designed 7,000 ㎉/hr fluidized bed heat exchanger for exhaust gas heat recovery. Fuel rich condition is maintained in the combustor for a limited time period to generate soot that is to be deposited on the heat transfer surfaces (fouling) and 600 Um glass beads are circulated inside the heat exchanger system for cleaning and enhancing the heat transfer performance. According to the present experimental study, performance degradation mode could be monitored and the effect of particle circulation on the heat transfer improvement could be identified. Through the present study, it is demonstrated that circulating particles contribute not only to the fouling reduction in gas side, but also to the heat transfer enhancement of the unit, while other possible aging factors including water side corrosion seemed to contribute to the accumulated performance deterioration.

Effects of Bottom Inflow Area on Pool Boiling Heat Transfer in a Vertical Annulus (하부 유로단면적이 수직 환상공간 내부 풀비등열전달에 미치는 영향)

  • Kang, Myeong-Gie;Yoo, Joo-Sik
    • Transactions of the Korean Society of Mechanical Engineers B
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    • 제31권7호
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    • pp.604-610
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    • 2007
  • To investigate effects of the inflow area on pool boiling heat transfer in a vertical annulus, the inflow area at its bottom has been changed from 0 to $1060.3mm^2$. For the test, a heated tube of 34 mm diameter and water at atmospheric pressure have been used. To elucidate effects of the inflow area on heat transfer results of the annulus are compared to the data of a single unrestricted tube. The change in the inflow area at the bottom of the annulus results in much variation in heat transfer coefficients. When the inflow area is $113.1mm^2$ the deterioration point of heat transfer coefficients gets moved up to the higher heat fluxes because of the convective flow at the bottom regions.

Effect of Liquid Subcooling on Pool Boiling Heat Transfer in Vertical Annuli with Closed Bottoms (액체과냉도가 하부폐쇄 수직환상공간 내부의 풀비등 열전달에 미치는 영향)

  • Kang Myeong-Gie
    • Transactions of the Korean Society of Mechanical Engineers B
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    • 제29권2호
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    • pp.239-246
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    • 2005
  • Effects of subcooling on pool boiling heat transfer in vertical annuli with closed bottoms have been investigated experimentally. For the test, a tube of 19.1mm diameter and the water at atmospheric pressure have been used. Three annular gaps of 7.05, 18.15, and 28.20 have been tested in the subcooled water and results of the annuli are compared with the data of a single unrestricted tube. The increase in pool subcooling results in much change in heat transfer coefficients. At highly subcooled regions, heat transfer coefficients for the annuli are much larger than those of a single tube. As the heat flux increases and subcooling decrease, a deterioration of heat transfer coefficients is observed at the annulus of 7.05mm gap. Single-phase natural convection and liquid agitation are the governing mechanisms for the single tube while liquid agitation and bubble coalescence are the major factors at the bottom closed annuli.

Direct Numerical Simulation of Turbulent Heat Transfer to Water at Supercritical Pressure Flowing in Vertical Pipes (수직원형관내 초임계압 물의 난류 열전달에 관한 직접수치모사)

  • Lee, Sang-Hoon;Bae, Joong-Hun;Yoo, Jung-Yul
    • Proceedings of the KSME Conference
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    • 대한기계학회 2008년도 추계학술대회B
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    • pp.2471-2476
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    • 2008
  • Turbulent flow and heat transfer to water at supercritical pressure flowing in vertical pipes is investigated using direct numerical simulation (DNS). A conservative space-time discretization scheme for variable-density flows at low Mach numbers is adopted in the present study to treat steep variations of fluid properties at supercritical pressure just above the thermodynamic critical point. The fluid properties at these conditions are obtained using PROPATH and used in the form of tables in the simulations. The buoyancy influence induced by strong variation of density across the pseudo-critical temperature proved to play an important role in turbulent flow and heat transfer at supercritical state. Depending on the degree of buoyancy influence, turbulent heat transfer may be enhanced or significantly deteriorated, resulting in local hot spots along the heated surface.

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Experimental study on heat transfer characteristics of supercritical carbon dioxide natural circulation

  • Wang, Pengfei;Ding, Peng;Li, Wenhuai;Xie, Rongshun;Duan, Chengjie;Hong, Gang;Zhang, Yaoli
    • Nuclear Engineering and Technology
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    • 제54권3호
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    • pp.867-876
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    • 2022
  • An experimental study has been conducted to investigate the heat transfer characteristics of supercritical carbon dioxide (sCO2) uniformly heated in the horizontal circular smooth tube. The results illustrated that there was a significant difference in heat transfer between the top wall and bottom wall due to the buoyancy. Bulk flow acceleration cannot be negligible in the high heat flux region, which leads to heat transfer deterioration. A new heat transfer correlation is proposed, in which the buoyancy parameter and bulk flow acceleration have been taken into account. The new correlation and six classic correlations for sCO2 are examined in horizontal tubes. The comparison indicates that the new correlation has a better performance for sCO2 flowing through a horizontal heating tube under natural circulation conditions. For example, 94.9% of the calculated results using the new heat transfer correlation were within ±30% of the experimental results while only 87.9% of that using the Jackson correlation (the best of the six) were within the same error bands.

An experimental study on nucleate boiling of ternary refrigerant R407C (삼중 혼합 냉매 R407C의 핵비등 열전달 특성에 관한 실험적 연구)

  • Kim, S.H.;Kwak, K.M.;Bai, C.H.;Chung, M.
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • 제9권3호
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    • pp.276-283
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    • 1997
  • The nucleate boiling heat transfer experiments are performed using a ternary refrigerant R407C which is a candidate of alternatives of HCFC 22. The boiling phenomena for R-32, R-125, and R-134a which are the constituent refrigerants of R407C are also investigated to give the foundation of theoretical research for the mixture component boiling. The nucleate boiling heat transfer coefficients of R407C is less than those of HCFC 22 which has the similar physical and transport properties. Since the experimental results show the deterioration of boiling heat transfer coefficients of ternary mixture refrigerants R407C, the boiling heat transfer coefficients of R407C cannot be obtained by the linear combination of boiling heat transfer coefficients from its constituent components R-32, R125, and R134a.

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Evaluation of the Nip Pressure Profile and Analysis of Heat Transfer in Soft Nip Calender (소프트닙 캘린더의 닙 압력 프로파일 평가와 닙 내 열전달 현상에 대한 해석)

  • 이사용;이학래;박선규
    • Journal of Korea Technical Association of The Pulp and Paper Industry
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    • 제32권2호
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    • pp.26-34
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    • 2000
  • Understanding the nip geometry and heat transfer phenomena of soft nip calenders, which has been used in the production of newsprint and coated papers for many years, is very important since improper setting of soft nip calendering conditions causes deterioration of paper quality and productivity. In this study theoretical analysis on nip pressure and heat transfer phenomena in the nip of soft nip calenders has been made. The variables examined were calendering pressure, surface temperature of the heating roll, nip residence time and ingoing sheet moisture, By measuring nip widths and maximum nip pressure with Prescale film at a normal temperature, accurate line load has been obtained. With this line load, nip pressures at different temperature and nip widths were calculated. Results showed that as temperature increased, nip widths increased and nip pressures decreased. Equations derived for the heat conduction phenomena in soft nip calender nip were derived based on the semi-infinite plate and finite difference method and were used for the analysis of heat transfer within the nip. Temperature profiles in z-direction of paper within the nip were obtained. Finite difference method allowed more accurate analysis of the heat transfer in the calender nip. In this study newsprint and coated paper were considered as a single plate and two-layer plate consisted of sheet and coating layers, respectively. Heat trans-fer to paper increased as heated roll surface temperature and nip residence time were increased.

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Prediction of Heat and Water Distribution in Concrete due to Changes in Temperature and Humidity (온도와 습도의 변화에 따른 콘크리트 내부의 열, 수분 분포 예측)

  • Park, Dong-Cheon;Lee, Jun-Hae
    • Proceedings of the Korean Institute of Building Construction Conference
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    • 한국건축시공학회 2020년도 봄 학술논문 발표대회
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    • pp.31-32
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    • 2020
  • Concrete changes its internal moisture distribution depending on the external environment, and changes in the condition of the material's interior over time affect the performance of the concrete. These effects are closely related to the long-term behavior and durability of concrete, and the degree of deterioration varies from climate to climate in each region. In this study, we use actual climate data from each region with distinct climates. A multi-physical analysis based on the method was conducted to predict the difference and degree of deterioration rate by climate.

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Prediction of Nucleate Pool Boiling Heat Transfer Coefficients of Ternary Refrigerant R407C

  • Kwak, Kyung-Min;Bai, Cheol-Ho;Chung, Mo
    • International Journal of Air-Conditioning and Refrigeration
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    • 제6권
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    • pp.93-103
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    • 1998
  • The nucleate boiling heat transfer experiments are performed using a ternary refrigerant R407C which is a candidate of alternatives of HCFC 22. The boiling phenomena of R-32, R-125 and R-134a which are the constituent refrigerants of R407C are also investigated. The nucleate boiling heat transfer coefficients of R407C are less than those of HCFC 22 which have the similar physical and transport properties. In our experimental pressure range, which is similar to the operational pressure of air conditioning system, the deterioration of boiling heat transfer coefficients of mixture refrigerant R407C does not appear for moderate wall superheat region. Since nucleate boiling heat transfer coefficients cannot be obtained from ideal mixing law of mixture, Thome's method was used to predict. To account for the heat flux effect and system pressure in Thome's method, the correcting factor, a(P.L1T), was introduced and obtained from experiments for ternary refrigerant R407C.

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Experimental Study on the Heat Transfer Characteristics under the Supercritical Pressures (초임계압 열전달 특성에 관한 실험 연구)

  • Kang, Kyoung-Ho;Youn, Young-Jung;Park, Jong-Kuk;Choo, Yeon-Jun;Chun, Se-Young;Song, Chul-Hwa
    • Proceedings of the KSME Conference
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    • 대한기계학회 2008년도 추계학술대회B
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    • pp.2242-2247
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    • 2008
  • A series of experiments have been performed in a vertical tube of 9.4 mm inner diameter using the Freon, HFC-134a as working fluid medium under the supercritical pressure range. Two kinds of experiments, i.e. steady-state and pressure transient, have been carried out. As for the steady-state heat transfer experiment, the mass flux was in the range between 600 and $2000\;kg/m^2s$ and the maximum heat flux was $160\;kW/m^2$. The selected pressures were 4.1, 4.3 and 4.5 MPa which correspond to 1.01, 1.06 and 1.11 times the critical pressure, respectively. In the pressure transient experiments, the inlet pressures were varied from 3.8 to 4.5 MPa and vice versa in the pressure transient simulations. In this study, heat transfer correlation and criterion for the heat transfer deterioration are suggested under the supercritical pressures. And also heat transfer characteristics during the pressure transient are examined.

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