化工进展 ›› 2021, Vol. 40 ›› Issue (3): 1643-1652.DOI: 10.16085/j.issn.1000-6613.2020-0868
蒋旭光1(), 魏邦吉1, 胡林飞2, 王汝佩2, 宋菲菲2, 陈少卿2
收稿日期:
2020-05-19
出版日期:
2021-03-05
发布日期:
2021-03-17
通讯作者:
蒋旭光
作者简介:
蒋旭光(1965—),男,博士,教授,博士生导师,研究方向为废弃物能源化和资源化。E-mail:基金资助:
JIANG Xuguang1(), WEI Bangji1, HU Linfei2, WANG Rupei2, SONG Feifei2, CHEN Shaoqing2
Received:
2020-05-19
Online:
2021-03-05
Published:
2021-03-17
Contact:
JIANG Xuguang
摘要:
循环流化床垃圾焚烧炉作为一种新型焚烧处理技术,具有适用范围广、燃烧稳定、排放低等优点。布置外置换热器可以在提高锅炉蒸汽的压力、温度参数及容量的同时避免过热器高温腐蚀,灵活调节床温。虽然目前国内外对外置换热器已有相关研究,但以电站燃煤锅炉为主。垃圾焚烧炉由于锅炉蒸汽的压力和温度参数较低,采用外置换热器还很少。本文综述了带外置换热器的循环流化床垃圾焚烧炉的研究现状,同时介绍了具有相同换热原理、极具参考价值的带外置床的循环流化床燃煤锅炉的国内外研究现状,分析了与床内传热系数、流化特性相关的影响因素,指出在试验和实炉运行时存在受热面出口壁温热偏差较大、边壁区域流化质量不佳的问题,并提出了改进措施。最后总结当前的研究重点,提出了针对试验台和实炉测试的改进措施,并针对垃圾流化床外置换热器的研发提出了研究思路,为今后建设高参数垃圾焚烧炉提供了合理建议。
中图分类号:
蒋旭光, 魏邦吉, 胡林飞, 王汝佩, 宋菲菲, 陈少卿. 循环流化床锅炉外置换热器的研究现状及在垃圾焚烧炉中的应用[J]. 化工进展, 2021, 40(3): 1643-1652.
JIANG Xuguang, WEI Bangji, HU Linfei, WANG Rupei, SONG Feifei, CHEN Shaoqing. Research status of external heat exchanger for circulating fluidized bed boiler and its application and development in garbage furnace[J]. Chemical Industry and Engineering Progress, 2021, 40(3): 1643-1652.
维美德 | 年份 | 合作厂家 | 锅炉类型 | 适用燃料 | 功率或处理能力 |
---|---|---|---|---|---|
国内项目 | 2018 | 山东淄博绿能新能源有限公司 | CFB垃圾焚烧炉 | 城市垃圾 | 装机容量70MW |
2019 | 乌鲁木齐京环环境&能源有限公司 | 垃圾焚烧炉 | 垃圾衍生燃料(RDF) | 年处理RDF100万吨 | |
国外项目 | 2014 | 芬兰Lohja的K-irkniemi纸厂 | CFB锅炉 | 树皮、其他木质燃料和煤 | 蒸汽装机容量88MW |
2014 | 芬兰Nokianvirr-an Energia公司 | CFB锅炉 | 生物质 | 蒸汽生产能力68MW | |
2016 | 日本JFE工程公司 | 生物质CFB锅炉 | 木屑、棕榈壳和煤等 | 75MW | |
2016 | 哥本哈根Amager-v?rket热电厂 | 生物CFB锅炉 | 木屑 | 150MW | |
2017 | 芬兰TSE新NA4发电厂 | CFB锅炉 | 燃煤、木质及农作物生物质、泥炭、固体再生燃料 | 146MW |
表1 维美德近年生产锅炉信息汇总
维美德 | 年份 | 合作厂家 | 锅炉类型 | 适用燃料 | 功率或处理能力 |
---|---|---|---|---|---|
国内项目 | 2018 | 山东淄博绿能新能源有限公司 | CFB垃圾焚烧炉 | 城市垃圾 | 装机容量70MW |
2019 | 乌鲁木齐京环环境&能源有限公司 | 垃圾焚烧炉 | 垃圾衍生燃料(RDF) | 年处理RDF100万吨 | |
国外项目 | 2014 | 芬兰Lohja的K-irkniemi纸厂 | CFB锅炉 | 树皮、其他木质燃料和煤 | 蒸汽装机容量88MW |
2014 | 芬兰Nokianvirr-an Energia公司 | CFB锅炉 | 生物质 | 蒸汽生产能力68MW | |
2016 | 日本JFE工程公司 | 生物质CFB锅炉 | 木屑、棕榈壳和煤等 | 75MW | |
2016 | 哥本哈根Amager-v?rket热电厂 | 生物CFB锅炉 | 木屑 | 150MW | |
2017 | 芬兰TSE新NA4发电厂 | CFB锅炉 | 燃煤、木质及农作物生物质、泥炭、固体再生燃料 | 146MW |
图1 中科通用设计的整体锅炉系统[26]1—炉膛;2—污泥给料口;3—垃圾给料口;4—给煤装置;5—燃烧室;6—炉内脱硫;7—空气预热器;8—流化风室;9—布风板;10—风帽;11—二次风喷口;12—排渣管;13—滚筒水冷除渣机;14—振动筛;15—旋风分离器;16—返料器;17—换热器;18—低温过热器;19—对流管束;20—斜管;21—竖井烟道;22—省煤器;23—锅筒;24—水冷壁
模型分类 | 提出年份 | 主要观点及模型假设条件 | 补充说明 |
---|---|---|---|
包更新模型[ | 1955 | 相邻粒子间无相对运动;在壁面处没有气膜或固体构成的膜状层作为热阻 | 只适用于长时间与换热壁面接触的乳化相,后续采用此模型的研究学者均在此基础上进行了补充改进 |
SPE模型[ | 2005 | 认为在壁面与乳化相之间存在一层颗粒通过导热形式换热 | 球形颗粒可进一步简化为与壁面不直接接触的等效圆柱颗粒 |
颗粒团更新模型[ | 2008 | 颗粒团与壁面之间没有完全接触,中间有一层气膜;既有气体换热也有固体换热 | 气膜厚度与角度有关,也会在换热过程中被颗粒冲刷而降低,从而强化换热 |
表2 各类换热模型的主要介绍
模型分类 | 提出年份 | 主要观点及模型假设条件 | 补充说明 |
---|---|---|---|
包更新模型[ | 1955 | 相邻粒子间无相对运动;在壁面处没有气膜或固体构成的膜状层作为热阻 | 只适用于长时间与换热壁面接触的乳化相,后续采用此模型的研究学者均在此基础上进行了补充改进 |
SPE模型[ | 2005 | 认为在壁面与乳化相之间存在一层颗粒通过导热形式换热 | 球形颗粒可进一步简化为与壁面不直接接触的等效圆柱颗粒 |
颗粒团更新模型[ | 2008 | 颗粒团与壁面之间没有完全接触,中间有一层气膜;既有气体换热也有固体换热 | 气膜厚度与角度有关,也会在换热过程中被颗粒冲刷而降低,从而强化换热 |
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