海水源热泵对海参育苗废水热能回收的工程应用

该文针对水产生物工厂化育苗水体升温技术需求,开展了利用育苗废水作热源为育苗水体升温的海水源热泵集成技术应用示范,探讨了集成系统对海参育苗水体升温和废水热能的回收效果。结果表明,进入I级换热器的育苗废水和新鲜海水温度分别为10.3~14.9℃和-1.9~4.9℃时,新鲜海水出水温度提升4.6~5.8℃,废水热能最大回收率达到59.2%;海水源热泵的废水热源温度和流量一定时,新鲜海水的温升幅度随其入流流量和温度升高而降低,入流温度分别为7.3和10.3℃的新鲜海水,流量不超过15和20 m~3/h时,出水温度均保持在15℃以上,满足海参育苗水温要求。热泵对废水热能的最大回收率为40.7%,COP（...

Full description

Saved in:
Bibliographic Details
Published in农业工程学报 Vol. 33; no. 9; pp. 218 - 223
Main Author 李秀辰 邓伟 张殿光 母刚 张国琛 陈帅 车全
Format Journal Article
LanguageChinese
Published 大连海洋大学辽宁省渔业装备工程技术研究中心,大连,116023%大连鑫玉龙海洋珍品有限公司,大连,116222 2017
Subjects
加热
废水
水体升温
海参
海水源热泵
温度
热能回收
水体升温
waste water
海参
加热
seawater-source heat pump
water heating
heat recovery
热能回收
温度
海水源热泵
temperature
heating
sea cucumber
废水
Online AccessGet full text
ISSN1002-6819
DOI10.11975/j.issn.1002-6819.2017.09.028

Cover

More Information
Summary:该文针对水产生物工厂化育苗水体升温技术需求,开展了利用育苗废水作热源为育苗水体升温的海水源热泵集成技术应用示范,探讨了集成系统对海参育苗水体升温和废水热能的回收效果。结果表明,进入I级换热器的育苗废水和新鲜海水温度分别为10.3~14.9℃和-1.9~4.9℃时,新鲜海水出水温度提升4.6~5.8℃,废水热能最大回收率达到59.2%;海水源热泵的废水热源温度和流量一定时,新鲜海水的温升幅度随其入流流量和温度升高而降低,入流温度分别为7.3和10.3℃的新鲜海水,流量不超过15和20 m~3/h时,出水温度均保持在15℃以上,满足海参育苗水温要求。热泵对废水热能的最大回收率为40.7%,COP（coefficient of performance）在5.03以上;集成升温系统比传统锅炉升温综合节能37.6%以上,减排二氧化碳约2 200 t/a,当年内可收回设备投资费用。
Bibliography:Li Xiuchen1, Deng Wei1, Zhang Dianguang1, Mu Gang1, Zhang Guochen1, Chen Shuai1, Che Quan2 （ 1. R ＆D Center of Fisheries Equipment and Engineering of Liaoning Province, Dalian Ocean University, Dalian 116023, China; 2. Dalian Xinyulong Seafood lndustry Co. Ltd, Dalian 116222, China）
11-2047/S
waste water; heating; temperature; sea cucumber; water heating; seawater-source heat pump; heat recovery
In order to cut down energy consumption, heat loss and air pollution for water heating in indoor aquaculture system, a seawater-source heat pump system, which comprised 2 heat exchangers （namely I-stage exchangers） and a seawater-source heat pump and employed waste water as heating source, was developed and applied in an aquatic organism indoor nursing system. The onsite flow rate of waste water and fresh seawater in I-stage exchangers were regulated to 400 m3/h, respectively. The flow rate of waste water in the seawater-source heat pump was 20 m3/h, while the flow rate of fresh seawater increased from 10 to 20 m3/h duri
ISSN:1002-6819
DOI:10.11975/j.issn.1002-6819.2017.09.028