• Title/Summary/Keyword: Gas bypassing

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Performance characteristics of hot-gas bypass refrigerator with the variation of operation conditions (운전조건 변화에 따른 hot-gas 바이패스 냉동장치의 성능 특성)

  • Baek, Seung-Moon;Son, Chang-Hyo;Heo, Jeong-Ho;Choi, In-Soo;Yoon, Jung-In
    • Journal of Advanced Marine Engineering and Technology
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    • v.38 no.9
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    • pp.1021-1026
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    • 2014
  • In this paper, among various systems applying hot-gas bypass control, outdoor temperature, outlet temperature of water cooler, superheating and subcooling degree, which are the factors affecting the performance of the system bypassing hot-gas to evaporator inlet were analyzed. The main results were summarized as following. Frist of all, performance of refrigeration system bypassing hot-gas to evaporator inlet was affected by outdoor temperature, outlet temperature of water cooler, superheating and sub cooling degree. Thus, providing basic planning date of refrigeration system obtained through optimization of variables is expectable. Thus, providing the basic design data of refrigeration system can be offered by performing the optimization of these variables. Also, the feasibility of this refrigeration system proposed in this paper was obtained by analyzing operating characteristics of the system bypassing hot-gas to evaporator inlet.

Performance Comparison of Hot-gas Bypass Types with the Variation of Refrigeration Load (부하변화에 따른 hot-gas 바이패스 방식별 성능 비교)

  • Baek, Seung-Moon;Yoon, Jung-In;Son, Chang-Hyo;Heo, Jung-Ho
    • Journal of Power System Engineering
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    • v.18 no.5
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    • pp.48-54
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    • 2014
  • In this paper, three refrigeration systems bypassing hot-gas to compressor outlet, compressor and condenser outlet and evaporator inlet are theoretically compared to offer basic design data for performance depending on cooling load using a HYSYS program. The main results are summarized as follows : First, the COP of third system is the highest. Next, the COP of second system is higher than first one. And, the temperature of compressor inlet of third system is constant for all cooling load. Compared to first and second system, the compressor inlet temperature of the first system is higher than second one for all cooling loads. From the above results, third system, which is bypassing hot-gas to evaporator inlet, is more advantageous when considering the precise temperature control and excellent performance of oil and water cooler of industrial machine.

Solid Flow Rate and Gas Bypassing with Operating Variables of J-valve in Multistage Annular Type Fluidized Beds (다단 환원형 유동층에서 J-valve의 운전변수에 따른 고체 흐름량 및 기체 우회)

  • Hong, Yoon-Seok;Kang, Gyung-Soo;Park, Joo-Sik;Lee, Dong-Hyun
    • Clean Technology
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    • v.17 no.1
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    • pp.62-68
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    • 2011
  • Hydrodynamic characteristics in multistage annular type fluidized bed (riser: $0.01{\times}0.025{\times}2.8m^3$, J-valve: $0.009{\times}0.015m^2$)were investigated. Glass beads ($d_p=101{\mu}m$, ${\rho}_b=1,590kg/m^3$, $U_{mf}=1.25{\times}10^{-2}m/s$, Geldart classification B) was used as a bed material. Accumulated weight by the electronic balance was measured to determine the solid flow rate in batch-type. In circulation condition, we measured the accumulated weight of particle transported from riser. At the steady state condition, solid circulation rate was calculated from time interval of the heated bed material passing between two thermocouples. Solid flow rate increased with increasing inlet gas velocity ($1.2-2.6U_{mf}$) and the static bed height (z, 0.24-0.68 m) from 2.2 to 23.4 kg/s. However, mean residence time decreased with increasing inlet gas velocity ($1.2-2.6U_{mf}$) and the static bed height (z, 0.24-0.68 m) from 1,438 to 440 s. The solid holdup in the riser was determined by measuring pressure differences according to the riser height. These results showed a similar trend to that of simple exponential decay type except for the top section of the riser. To verify the gas bypassing from top bubbling beds to middle bubbling beds, $CO_2$ gas was injected by tracer gas in constant ratio, and then was measured $CO_2$ concentration in outlet gas by gas chromatography. Gas bypassing occurred below 2.6% which is negligible value.

Effect of Gas Bypass at Turbine Inlet on Design of a Pressurized Solid Oxide Fuel Cell / Gas Turbine Hybrid System (가압형 고체산화물 연료전지 / 가스터빈 하이브리드 시스템 설계에서 터빈입구 바이패스의 효과)

  • Park, S.K.;Sohn, J.L.;Kim, T.S.
    • The KSFM Journal of Fluid Machinery
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    • v.11 no.1
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    • pp.33-39
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    • 2008
  • Hybrid power generation systems combining a solid oxide fuel cell and a gas turbine is promising due to their high efficiency. In the pressurized hybrid system, the operating condition of the gas turbine may play a critical role in designing the hybrid system. In particular, prevention of surge of the compressor can be a critical issue. The existence of fuel cell between the compressor and the turbine may cause an additional pressure loss and thus compressor operating points tend to approach the surge if the original turbine inlet temperature is pursued. In this study, bypassing some of the turbine inlet gas directly to the turbine exit side is simulated. Its effects on suppressing the surge problem and change in performance characteristics are discussed.

A Study on the Reduction of $NO_x$ Emission from Dual Fuel Engine for Co-generation System (열병합발적용 Dual Fuel Engine의 질소산화물 배출저감에 관한 연구)

  • 정일래;김용술;심용식
    • Journal of Korean Society for Atmospheric Environment
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    • v.7 no.1
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    • pp.31-40
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    • 1991
  • This study shows the correlation between $NO_x$ emission in the exhaust gas and various operation factors of dual fuel engine for Co-generation system. General tendency was shown that the thermal efficiency was lowered by the change of operation factors. However these were not confirmed on this experiment. Increasing T4 temperature (exhaust gas temperature at turbo-charger inlet) reduces $NO_x$ emission rate. The higher T4 temperature requires lower excess air as the excess air ratio is controlled by T4 temperature on gas mode operation. Another tendency was that $NO_x$ emission rate is reduced in case of increasing boost air temperature, quantity of pilot oil or bypassing flue gas through the exhaust gas boiler. The diameter of the fuel injection nozzle was changed smaller than design value and the injection timing was readjusted. Thus $NO_x$ emission rate could be reduced as retarding injection timing and changing hole diameter of fuel injection nozzle, however maxium engine out-put was decreased by changing fuel nozzle on the diesel mode operation.

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Analysis of Start-up Characteristics of a Heat Recovery Steam Generator Considering Thermal Constraints (열적 제한요소를 고려한 열회수 증기발생기의 시동 특성 해석)

  • Kim, Young Il;Kim, Tong Seop;Kim, Jae Hwan;Ro, Sung Tack;Kauh, Sang Ken
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.23 no.11
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    • pp.1410-1417
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    • 1999
  • A thorough understanding of the transient behavior during start-up is essential in the design and operation of the heat recovery steam generator(HRSG). During this period of time, material that is exposed to high temperature and experiences a large temperature variation is subject to high thermal stress. In this work, a transient formulation of the HRSG is constructed including the estimation of the thermal stress and fatigue of the drum wall. Start-up behavior of a single-pressure HRSG is analyzed and the effect of bypassing part of the gas turbine exhaust flow on the thermal stress evolution is examined. It is found that the modulation of the gas flow rate using a bypass damper is very useful in view of reducing the thermal stress of the drum and ensuring the fatigue lifetime.

Operating Characteristics of a Continuous Two-Stage Bubbling Fluidized-Bed Process (연속식 2단 기포 유동층 공정의 운전특성)

  • Youn, Pil-Sang;Choi, Jeong-Hoo
    • Korean Chemical Engineering Research
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    • v.52 no.1
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    • pp.81-87
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    • 2014
  • Flow characteristics and the operating range of gas velocity was investigated for a two-stage bubbling fluidized-bed (0.1 m-i.d., 1.2 m-high) that had continuous solids feed and discharge. Solids were fed in to the upper fluidized-bed and overflowed into the bed section of the lower fluidized-bed through a standpipe (0.025 m-i.d.). The standpipe was simply a dense solids bed with no mechanical or non-mechanical valves. The solids overflowed the lower bed for discharge. The fluidizing gas was fed to the lower fluidized-bed and the exit gas was also used to fluidize the upper bed. Air was used as fluidizing gas and mixture of coarse (< $1000{\mu}m$ in diameter and $3090kg/m^3$ in apparent density) and fine (< $100{\mu}m$ in diameter and $4400kg/m^3$ in apparent density) particles were used as bed materials. The proportion of fine particles was employed as the experimental variable. The gas velocity of the lower fluidized-bed was defined as collapse velocity in the condition that the standpipe was emptied by upflow gas bypassing from the lower fluidized-bed. It could be used as the maximum operating velocity of the present process. The collapse velocity decreased after an initial increase as the proportion of fine particles increased. The maximum took place at the proportion of fine particles 30%. The trend of the collapse velocity was similar with that of standpipe pressure drop. The collapse velocity was expressed as a function of bulk density of particles and voidage of static bed. It increased with an increase of bulk density, however, decreased with an increase of voidage of static bed.