• Title/Summary/Keyword: Industrial Waste Heat

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Research Investigations at the Municipal (2×35) and Clinical (2×5 MW) Waste Incinerators in Sheffield, UK

  • Swithenbank, J.;Nasserzadeh, V.;Ewan, B.C.R.;Delay, I.;Lawrence, D.;Jones, B.
    • Clean Technology
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    • v.2 no.2
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    • pp.100-125
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    • 1996
  • After recycle of spent materials has been optimised, there remains a proportion of waste which must be dealt with in the most environmentally friendly manner available. For materials such as municipal waste, clinical waste, toxic waste and special wastes such as tyres, incineration is often the most appropriate technology. The study of incineration must take a process system approach covering the following aspects: ${\bullet}$ Collection and blending of waste, ${\bullet}$ The two stage combustion process, ${\bullet}$ Quenching, scrubbing and polishing of the flue gases, ${\bullet}$ Dispersion of the flue gases and disposal of any solid or liquid effluent. The design of furnaces for the burning of a bed of material is being hampered by lack of an accurate mathematical model of the process and some semi-empirical correlations have to be used at present. The prediction of the incinerator gas phase flow is in a more advanced stage of development using computational fluid dynamics (CFD) analysis, although further validation data is still required. Unfortunately, it is not possible to scale down many aspects of waste incineration and tests on full scale incinerators are essencial. Thanks to a close relationship between SUWIC and Sheffield Heat&Power Ltd., an extended research programme has been carried out ar the Bernard Road Incinerator plant in Sheffield. This plant consists of two Municipal(35 MW) and two Clinical (5MW) Waste Incinerators which provide district heating for a large part of city. The heat is distributed as hot water to commercial, domestic ( >5000 dwelling) and industrial buildings through 30km of 14" pipes plus a smaller pipe distribution system. To improve the economics, a 6 MW generator is now being added to the system.

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Performance Analysis of Fin-Tube Heat Exchangers with Various Fin Shapes for Waste Gas Heat Recovery (핀 형상에 따른 폐열회수용 핀-튜브 열교환기의 성능분석)

  • Maeng, Jae-Hun;Koo, Byeong-Soo;Jun, Yong-Du;Lee, Kum-Bae
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.23 no.9
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    • pp.627-632
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    • 2011
  • As an innovative effort to secure economically viable heat recovery system, various fin shapes for industrial fin-tube heat exchangers have been studied for better performance. In this study, the waste gas heat recovery from four different fin shapes was experimentally performed for heat transfer rate and pressure drop. According to the tested results, the twist and wavy shape fins of rectangular type show the superior performance in terms of Goodness factor and jH/f factor ratio, whereas the circular spiral fin shows the inferior values. Experimental results shows good comparison with the numerical results with a slight discrepancy of 5%, which is quite resonable.

The Study of Validity on the High Temperature Heat Pump System using Dyeing Wastewater (염색폐수를 이용한 고온수 히트펌프 시스템 타당성 연구)

  • Kim, Jeong-Yeol;Chung, Dong-Yeol;Park, Shung-Sang;Peck, Jong-Hyeon
    • Proceedings of the SAREK Conference
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    • 2009.06a
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    • pp.996-1001
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    • 2009
  • The purposes of this work were suggested and validated the methods of heat recovery from dyeing wastewater exhausted in Sihwa and Banwol dyeing industrial park. We analyzed the present conditions of heat supplies and demands. So it was made a selection of the system combined heat exchanger for waste heat recovery and the high temperature heat pump. We decided the specifications of the heat recovery facilities. After this, economical assessment is performed to this system. The payback periods are within 4 years, 20 years and 5 years in case of K company, S company and A company. In addition, when they are produced the heat of same capacity, quantities of pollutants from used fuels were calculated.

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Effects of Operation Conditions on the Performance of Type II LiBr-H2O Absorption Heat Pump (제 2종 LiBr-H2O 흡수식 히트펌프의 운전 변수에 따른 성능 특성 수치 해석)

  • Yoon, Jun Seong;Kwon, Oh Kyung;Cha, Dong An;Bae, Kyung Jin;Kim, In Gwan;Kim, Min Soo;Park, Chan Woo
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.29 no.1
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    • pp.7-14
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    • 2017
  • This study carried out a numerical analysis of the effects of hot waste water supply on the performance of a Type II absorption heat pump. There are two types of hot waste water supply, regular series flow and reverse series flow. Also it investigated the interaction between each type of flow and heat exchange solutions. As the effectiveness of heat exchange solutions increase, the steam generation and (COP) increase as well. If the effectiveness of a heat exchange solution is lower than 0.566, the steam generation rate of the reverse flow is lower than that of the regular series flow. A high effectiveness of heat exchange solution is therefore required to make a larger amount of steam in reverse series flow than with ordinary series flow. The COP difference between the two types of flow decreases with the increasing effectiveness of the heat exchange solution. Thus, a reverse flow type absorption heat pump can match the high steam generation rate and COP of the ordinary flow type when a highly effective heat exchange solution is applied.

Experimental Study on Heating Performance Characteristic of 100 kW Heat Pump to Generate ℃ Steam (120℃ 스팀 생성을 위한 100 kW급 히트펌프의 실험적 연구)

  • Wang, Eunseok;Na, Sun-Ik;Lee, Gilbong;Baik, Young-Jin;Lee, Young-Soo;Lee, Beomjoon
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.30 no.2
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    • pp.100-106
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    • 2018
  • Recently, the development of a heat pump technology to recover process waste heat and to generate steam of $120^{\circ}C$ or higher required for industrial processes, has attracted attention. The research of conventional heat pump utilizing the available energy is used primarily for air conditioning, and the production temperature is about $60^{\circ}C$, so it is difficult to utilize it for industrial use. Therefore, in this study, we developed a steam heat pump (SGHP) which recovers the waste heat of process and generates steam at $120^{\circ}C$. The low-pressure refrigerant R245fa, considered to be an eco-friendly refrigerant, has been selected as the refrigerant for SGHP in this study since its Ozone Depletion Potential (ODP) is zero and the Global Warming Potential (GWP) is relatively low. A flash tank functioning as a phase separator was installed in the rear stage of the condenser, and the saturated water of high temperature was decompressed to generate steam. It was started at the initial temperature of $70^{\circ}C$, and it was confirmed that $120^{\circ}C$ steam was produced after the system stabilized. We have conducted experiments by modifying the system, and ultimately achieved a heating capacity of 101.4 kW and a COP of 3.05.

A Study on a Resorption Beat Pump Using Methanol-Glycerine (메탄올-글리세린을 이용한 재흡수 열펌프의 열역학적 모사 연구)

  • Min, Byong-Hun
    • Journal of Energy Engineering
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    • v.15 no.4 s.48
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    • pp.284-290
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    • 2006
  • The improvement of energy recovery is mandatory to decrease consumption of fossil fuels and to minimize negative impacts on the environment which originates from large cooling and heating demand. The absorption heat pump technology has a large potential for energy saving in this respect. Absorption heat pump is a means to upgrade waste heat without addition of extra thermal energy. In this study, resorption heat pump for energy recovery has been investigated using methanol-glycerine. The simulated calculation of theoretical thermal efficiency was performed based on the thermodynamic properties of the working fluid over various operating conditions. The thermal efficiency of higher than 0.4 was obtained by raising industrial waste heat, $70{\sim}80^{\circ}C$, by $40^{\circ}C$ in this system.

A study on the evaluation of lower heating value using heat balance method in industrial waste incineration facilities (열정산방법을 이용한 사업장폐기물 소각시설의 저위발열량 분석·평가 연구)

  • Ko, Youngjae;Kang, Jun-Gu;Kwon, Young-Hyun;Yoo, Ha-Nyoung;Kwon, Jun-Hwa;Jang, Mi-Jeong;Jeon, Tae-Wan;Shin, Sun-Kyoung
    • Analytical Science and Technology
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    • v.31 no.1
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    • pp.31-38
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    • 2018
  • The energy recovery rate estimation method proposed through the Waste Control Act does not take into account the energy used in practice. In addition, the method for measuring a lower heating value, which is the main factor of the energy recovery rate, was carried out through a small sampling amount, and thus the representative value of the waste was not reflected. With the revised estimation method (Notification No. 2015-215 of the Ministry of Environment), the energy recovery rate should be estimated based on the actual amount of energy used, and a heat balance method was proposed as a way to estimate the lower heating value. In this study, the lower heating value was estimated for seven industrial waste incineration facilities according to the revised estimation method. All data used in the estimations were achieved from measurement instruments applied to each of the incinerators and through direct measurements taken by the operators for the purposes of calculation. As a result, the lower heating value was estimated to be about 3,404.7 kcal/kg for the seven industrial waste incineration facilities.

Technology of Waste Heat Recovery Using Heat Pipe Heat Exchanger for Industrial Practice (중고온 히트파이프를 이용한 열회수기술에 관한 연구)

  • Lee Young-Soo;Kim Jong-Ryul;Chang Ki-Chang;Baik Young-Jin
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.16 no.11
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    • pp.1044-1050
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    • 2004
  • The present study has been conducted to develop a heat pipe heat exchanger for middle-high temperature ranged from 300 to $600^{\circ}C$. Heat transfer rate, overall heat transfer coefficient and temperature effectiveness were investigated using a heat pipe heat exchanger with Dowtherm A as working fluid. Theoretical analysis was also conducted, and the followings were obtained: (1) Heat exchange rate increased as waste gas temperature supplied to evaporator and frontal velocity in condenser increased, (2) Overall heat transfer coefficient increased by $3{\sim}7\%$ as frontal velocity in evaporator and condenser increased, (3) Temperature effectiveness was about $30\%$ in evaporator and was about $40\%$ in condenser, (4) Heat recovery rate was about $38\%$, (5) Pressure drop did not exceed $8\;mmH_{2}O$ under the running condition of $1{\sim}3Nm/s$, (6) Simulation results were corresponded with experimental results.

R&D OF FREEZING AND REFRIGERATION SYSTEM USING CHP. (가역 화학 열 펌프(CHP)를 이용한 냉장.냉동 시스템 개발 연구)

  • 이종호;김석종
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 1996.04a
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    • pp.132-135
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    • 1996
  • This study is to develop an ammonia based chemical heat pump(STELF) for a freezing and refrigeration system coupled to gas, fuel and/or waste from industrial processes as heat sources. Recently it has been continually taking a growing interest in chemical heat pumps without electric power and having higher COP's than those of existing compression type refrigeration systems using freon. By introducing STELF technology, efficient heat recovery utilizing enormous amount of waste heat in energy consuming large scale industries or building for their own refrigeration purposes is possible. Moreover, air-conditioning systems coupled to city gas for small scale industries or building can be realized. Therefore, STELF technology can contribute much for overall energy savings and efficient energy management.

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