Investigation and optimization of the depth of flue gas heat recovery in surface heat exchangers; Thermal Engineering; Vol. 64, iss. 9
| Parent link: | Thermal Engineering Vol. 64, iss. 9.— 2017.— [P. 680-685] |
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| Auteur principal: | |
| Collectivité auteur: | |
| Autres auteurs: | , |
| Résumé: | Title screen Economic issues associated with designing deep flue gas heat recovery units for natural gas-fired boilers are examined. The governing parameter affecting the performance and cost of surface-type condensing heat recovery heat exchangers is the heat transfer surface area. When firing natural gas, the heat recovery depth depends on the flue gas temperature at the condenser outlet and determines the amount of condensed water vapor. The effect of the outlet flue gas temperature in a heat recovery heat exchanger on the additionally recovered heat power is studied. A correlation has been derived enabling one to determine the best heat recovery depth (or the final cooling temperature) maximizing the anticipated reduced annual profit of a power enterprise from implementation of energy-saving measures. Results of optimization are presented for a surface-type condensing gas–air plate heat recovery heat exchanger for the climatic conditions and the economic situation in Tomsk. The predictions demonstrate that it is economically feasible to design similar heat recovery heat exchangers for a flue gas outlet temperature of 10°?. In this case, the payback period for the investment in the heat recovery heat exchanger will be 1.5 years. The effect of various factors on the optimal outlet flue gas temperature was analyzed. Most climatic, economical, or technological factors have a minor effect on the best outlet temperature, which remains between 5 and 20°? when varying the affecting factors. The derived correlation enables us to preliminary estimate the outlet (final) flue gas temperature that should be used in designing the heat transfer surface of a heat recovery heat exchanger for a gas-fired boiler as applied to the specific climatic conditions. Режим доступа: по договору с организацией-держателем ресурса |
| Langue: | anglais |
| Publié: |
2017
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| Sujets: | |
| Accès en ligne: | https://doi.org/10.1134/S0040601517090026 |
| Format: | Électronique Chapitre de livre |
| KOHA link: | https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=655597 |
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| 200 | 1 | |a Investigation and optimization of the depth of flue gas heat recovery in surface heat exchangers |f V. V. Bespalov, V. I. Bespalov, D. V. Melnikov | |
| 203 | |a Text |c electronic | ||
| 300 | |a Title screen | ||
| 320 | |a [References: p. 685 (8 tit.)] | ||
| 330 | |a Economic issues associated with designing deep flue gas heat recovery units for natural gas-fired boilers are examined. The governing parameter affecting the performance and cost of surface-type condensing heat recovery heat exchangers is the heat transfer surface area. When firing natural gas, the heat recovery depth depends on the flue gas temperature at the condenser outlet and determines the amount of condensed water vapor. The effect of the outlet flue gas temperature in a heat recovery heat exchanger on the additionally recovered heat power is studied. A correlation has been derived enabling one to determine the best heat recovery depth (or the final cooling temperature) maximizing the anticipated reduced annual profit of a power enterprise from implementation of energy-saving measures. Results of optimization are presented for a surface-type condensing gas–air plate heat recovery heat exchanger for the climatic conditions and the economic situation in Tomsk. The predictions demonstrate that it is economically feasible to design similar heat recovery heat exchangers for a flue gas outlet temperature of 10°?. In this case, the payback period for the investment in the heat recovery heat exchanger will be 1.5 years. The effect of various factors on the optimal outlet flue gas temperature was analyzed. Most climatic, economical, or technological factors have a minor effect on the best outlet temperature, which remains between 5 and 20°? when varying the affecting factors. The derived correlation enables us to preliminary estimate the outlet (final) flue gas temperature that should be used in designing the heat transfer surface of a heat recovery heat exchanger for a gas-fired boiler as applied to the specific climatic conditions. | ||
| 333 | |a Режим доступа: по договору с организацией-держателем ресурса | ||
| 461 | |t Thermal Engineering | ||
| 463 | |t Vol. 64, iss. 9 |v [P. 680-685] |d 2017 | ||
| 610 | 1 | |a электронный ресурс | |
| 610 | 1 | |a труды учёных ТПУ | |
| 610 | 1 | |a энергосберегающие технологии | |
| 610 | 1 | |a водяной пар | |
| 610 | 1 | |a теплообменники | |
| 700 | 1 | |a Bespalov |b V. V. |c specialist in the field of informatics and computer technology |c Lead Programmer, Associate Professor of Tomsk Polytechnic University, Candidate of Technical Sciences |f 1965- |g Viktor Vladimirovich |3 (RuTPU)RU\TPU\pers\33055 |9 16889 | |
| 701 | 1 | |a Bespalov |b V. I. |c specialist in the field of heat and power engineering |c Associate Professor of Tomsk Polytechnic University, candidate of technical sciences |f 1941- |g Vladimir Il'ich |3 (RuTPU)RU\TPU\pers\36598 | |
| 701 | 1 | |a Melnikov |b D. V. |g Denis Vladimirovich | |
| 712 | 0 | 2 | |a Национальный исследовательский Томский политехнический университет (ТПУ) |b Энергетический институт (ЭНИН) |b Кафедра атомных и тепловых электростанций (АТЭС) |3 (RuTPU)RU\TPU\col\18683 |
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| 856 | 4 | |u https://doi.org/10.1134/S0040601517090026 | |
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