CN205137498U - 一种利用烟气余热加热水和提水一体化回收利用装置 - Google Patents
一种利用烟气余热加热水和提水一体化回收利用装置 Download PDFInfo
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- CN205137498U CN205137498U CN201520914002.1U CN201520914002U CN205137498U CN 205137498 U CN205137498 U CN 205137498U CN 201520914002 U CN201520914002 U CN 201520914002U CN 205137498 U CN205137498 U CN 205137498U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwLjAnIGhlaWdodD0nMzAwLjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMDAuNScgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5IPC90ZXh0Pgo8dGV4dCB4PScxMjYuMScgeT0nMTg2LjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID4yPC90ZXh0Pgo8dGV4dCB4PScxMzguMCcgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 109
- 239000003546 flue gas Substances 0.000 title claims abstract description 61
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 239000002918 waste heat Substances 0.000 title abstract description 7
- 238000004062 sedimentation Methods 0.000 claims abstract description 20
- 230000003009 desulfurizing Effects 0.000 claims abstract description 12
- 239000007921 spray Substances 0.000 claims abstract description 7
- 238000011010 flushing procedure Methods 0.000 claims description 14
- 239000003517 fume Substances 0.000 claims description 11
- 239000008236 heating water Substances 0.000 claims description 9
- 238000009833 condensation Methods 0.000 abstract description 4
- 230000005494 condensation Effects 0.000 abstract description 4
- 238000006477 desulfuration reaction Methods 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 3
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Abstract
本实用新型公开了一种利用烟气余热加热水和提水一体化回收利用装置，包括通过补水系统的管道连接的热泵和烟气换热器装置；锅炉烟道穿过烟气换热器装置；补水系统和烟气换热器装置连接的管道上设置有管道过滤器和第一支路；烟气换热器装置与冲洗水系统相连接；下部设置有集液槽，集液槽下方设置有沉淀池，沉淀池的通过管道与脱硫塔的喷淋入水口连接，连接的管道上设置有沉淀池水泵；热泵与热网供水系统连接。本实用新型利用烟气余热和烟气中水蒸气的凝结潜热使水温升高，热水在热泵中充分换热，将热量供给热网系统，实现余热回收利用的同时可提取烟气中的水分、飞灰及硫化物，并将回收的水分供脱硫使用，达到节能环保的目的。
Description
技术领域
[0001]本实用新型涉及一种回收利用装置，尤其涉及一种利用烟气余热加热水和提水一体化回收利用装置。
背景技术
[0002]我国是水资源匮乏的国家，人均水资源占有量仅为世界水平的1/4，尤其西北部地区缺水更为严重，然而这些地区煤炭资源较为丰富，燃煤电厂发展迅速。然而燃煤电厂耗水量大，且燃煤后的烟气在湿法脱硫后会携带走大量水分，这些水分随烟气排往大气，造成水资源极大浪费。
[0003]煤粉在锅炉内燃烧产生大量的烟气，通常烟气经处理后直接通过烟道排出，而排出的烟气温度具有很高的温度还含有大量水蒸气，这样烟气的热量和水蒸气就白白浪费掉了，造成了能源的巨大损失。如果能对脱硫后烟气中的水分和热量进行回收利用，那么对于水资源匮乏的地区具有重要意义。
实用新型内容
[0004]为了解决上述技术所存在的不足之处，本实用新型提供了一种利用烟气余热加热水和提水一体化回收利用装置。
[0005]为了解决以上技术问题，本实用新型采用的技术方案是:一种利用烟气余热加热水和提水一体化回收利用装置，包括热栗、烟气换热器装置、补水系统和锅炉烟道，热栗和烟气换热器装置通过补水系统的管道连接;锅炉烟道穿过烟气换热器装置;补水系统和烟气换热器装置连接的管道上设置有第一支路;第一支路上依次连接有第一前截止阀、第一循环水栗、第一逆止阀和第一后截止阀;第一支路和补水系统之间设置有管道过滤器；
[0006]烟气换热器装置在顶部设置有冲洗水口，冲洗水口通过管道与冲洗水系统相连接;冲洗水系统与烟气换热器装置连接的管道之间设置有电动阀；烟气换热器装置的下部设置有集液槽，集液槽下方的出水口通过管道与沉淀池的进水口相连接;沉淀池的出水口通过管道与脱硫塔的喷淋入水口连接，连接的管道上设置有沉淀池水栗;热栗与热网供水系统连接。
[0007] 补水系统上连接有稳压罐。
[0008]补水系统和烟气换热器装置连接的管道上设置有第二支路;第二支路和第一支路并联连接;第二支路上依次连接有第二前截止阀、第二循环水栗、第二逆止阀和第二后截止阀。
[0009]补水系统3的管道上和锅炉烟道的管道上均设置有温度传感器，补水系统的管道上设置有压力传感器。
[0010]补水系统和管道过滤器之间设置有电动阀。
[0011]本实用新型的结构设计体现了节能环保要求，有效利用了锅炉烟道中烟气的余热和烟气中水蒸气的凝结潜热，通过回收烟气中的热量使水温升高，加温后的热水在热栗中充分换热，将热量供给热网系统，实现余热的回收利用；并且，本实用新型在进行烟气余热利用的同时可提取烟气中的水分，并将回收的水分供脱硫使用，达到节水目的；此外，还可去除烟气中残余部分飞灰及硫化物，达到再次净化烟气的作用。
附图说明
[0012]下面结合附图和具体实施方式对本实用新型作进一步详细的说明。
[0013]图1为本实用新型的整体结构示意图。
[0014]图中:1、热栗;2、烟气换热器装置;3、补水系统;4、第一前截止阀；5、第一循环水栗;6、第一逆止阀；7、第一后截止阀；8、管道过滤器;9、稳压罐；10、集液槽；11、冲洗水系统；12、沉淀池；13、沉淀池水栗；14、脱硫塔；15、热网供水系统；16、烟囱；17、温度传感器(TE) ; 18、压力传感器(PI);实线箭头表示为水流方向；虚线箭头表示为烟气方向。
具体实施方式
[0015]如图1所示，本实用新型包括热栗1、烟气换热器装置2、补水系统3和锅炉烟道，热栗1和烟气换热器装置2通过补水系统3的管道连接;锅炉烟道穿过烟气换热器装置2;烟气换热器装置2设置在脱硫塔14和烟囱16之间；烟气换热器装置2的外部与烟道焊接固定在一起，这种布置加工方便，经济实用，可在原有锅炉烟道上进行改装即可。补水系统3和烟气换热器装置2连接的管道上设置有第一支路;第一支路上依次连接有第一前截止阀4、第一循环水栗5、第一逆止阀6和第一后截止阀7;第一支路和补水系统3之间设置有管道过滤器8;
[0016]补水系统3和烟气换热器装置2连接的管道上设置有第二支路;第二支路和第一支路并联连接;第二支路上依次连接有第二前截止阀、第二循环水栗、第二逆止阀和第二后截止阀。第二支路作为第一支路的后备支路，结构设置与第一支路完全一样，当第一支路出现故障或者需要单独清洗等情况时，可以关闭第一支路打开第二支路保证整个装置的正常循环使用。
[0017]烟气换热器装置2在顶部设置有冲洗水口，冲洗水口通过管道与冲洗水系统11相连接;冲洗水系统11与烟气换热器装置2的冲洗水口连接的管道之间设置有电动阀；烟气换热器装置2的下部设置有集液槽10，集液槽10下方的出水口通过管道与沉淀池12的进水口相连接;沉淀池12的出水口通过管道与脱硫塔14的喷淋入水口连接，连接的管道上设置有沉淀池水栗13;热栗1与热网供水系统15连接。
[0018]沉淀池12和脱硫塔14的喷淋管道之间连接有沉淀池水栗13，沉淀池水栗13可为喷淋送水提供驱动力。
[0019]补水系统3上连接有稳压罐9，可以起到稳定水压的作用。
[0020]补水系统3的管道上和锅炉烟道的管道上均设置有温度传感器，补水系统3的管道上设置有压力传感器。通过温度传感器和压力传感器可以方便监测管道内的温度和压力值，便于进行相应的流量调节和压力大小调节。
[0021 ]补水系统3和管道过滤器8之间设置有电动阀。
[0022]本实用新型的具体工作过程为:补水系统3的出水口通过管道与烟气换热器装置2的进水口连接，冷水经过管道流经烟气换热器装置2后由锅炉烟道内的烟气余热及烟气中水蒸气凝结潜热将冷水加热，加热后的水经过烟气换热器装置2的出水口通过管道与热栗1的进水口连接，然后在热栗1进行充分换热从而将热网系统15的水加热，实现余热的回收利用。烟气换热器装置2顶部的冲洗水口实际上也是冲洗水系统11的入口，冲洗水系统的水由烟气换热器装置2的顶部引入，对烟气换热器装置2的外壁进行冲洗，冲洗后的液体汇入集液槽10。通过冲洗水清洗避免烟气换热器装置2的外壁积灰结渣，提高了换热效率。当烟气温度降低至水露点以下，烟气中的水蒸气凝结放热后形成水珠同冲洗水一并沉积至集液槽10，另外烟气中残余部分的飞灰及硫化物同凝结水吸附聚集后汇入集液槽10—起排出，达到再次净化烟气的作用。集液槽10通过底部的出水口将集液槽10里面的水排放到沉淀池12里面，沉淀池12的水再经过出水口与脱硫塔1喷淋入水口连接，从而达到烟气中水分的回收利用目的。最后，烟道内的烟气经过烟气换热器装置2后经烟囱16排出。
[0023]由于热栗的水经过换热后还存在一定余温，如果就此排出会造成一定程度的能量浪费，因此本实用新型将热栗1的出水口通过管道过滤器8后经第一支路与烟气换热器装置2的进水口连接，这样经热栗1出来后尚有余温的水在烟气换热器装置2里再一次加热的时间缩短，有效避免了能量的浪费，起到了能量循环利用的作用。
[0024]上述实施方式并非是对本实用新型的限制，本实用新型也并不仅限于上述举例，本技术领域的技术人员在本实用新型的技术方案范围内所做出的变化、改型、添加或替换，也均属于本实用新型的保护范围。
Claims (5)
1.一种利用烟气余热加热水和提水一体化回收利用装置，包括热栗(1)、烟气换热器装置(2)、补水系统(3)和锅炉烟道，其特征在于:所述热栗(1)和烟气换热器装置(2)通过补水系统(3)的管道连接;所述锅炉烟道穿过烟气换热器装置(2);所述补水系统(3)和烟气换热器装置(2)连接的管道上设置有第一支路;所述第一支路上依次连接有第一前截止阀(4)、第一循环水栗(5)、第一逆止阀(6)和第一后截止阀(7);所述第一支路和补水系统(3)之间设置有管道过滤器(8)； 所述烟气换热器装置(2)在顶部设置有冲洗水口，冲洗水口通过管道与冲洗水系统(11)相连接;所述冲洗水系统(11)与烟气换热器装置(2)连接的管道之间设置有电动阀;所述烟气换热器装置(2)的下部设置有集液槽(10)，集液槽(10)下方的出水口通过管道与沉淀池(12 )的进水口相连接;所述沉淀池(12 )的出水口通过管道与脱硫塔(14)的喷淋入水口连接，所述沉淀池(12)与脱硫塔(14)连接的管道上设置有沉淀池水栗(13);所述热栗(1)与热网供水系统(15)连接。
2.根据权利要求1所述的利用烟气余热加热水和提水一体化回收利用装置，其特征在于:所述补水系统(3)上连接有稳压罐(9)。
3.根据权利要求1所述的利用烟气余热加热水和提水一体化回收利用装置，其特征在于:所述补水系统(3)和烟气换热器装置(2)连接的管道上设置有第二支路;所述第二支路和第一支路并联连接;所述第二支路上依次连接有第二前截止阀、第二循环水栗、第二逆止阀和第二后截止阀。
4.根据权利要求1所述的利用烟气余热加热水和提水一体化回收利用装置，其特征在于:所述补水系统(3)的管道上和锅炉烟道的管道上均设置有温度传感器;补水系统(3)的管道上设置有压力传感器。
5.根据权利要求1所述的利用烟气余热加热水和提水一体化回收利用装置，其特征在于:所述补水系统(3)和管道过滤器(8)之间设置有电动阀。
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| CN110252085A (zh) * | 2019-06-13 | 2019-09-20 | 国家能源投资集团有限责任公司 | 净烟气提水装置以及集成式电厂间接空冷塔 |
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| CN110252085A (zh) * | 2019-06-13 | 2019-09-20 | 国家能源投资集团有限责任公司 | 净烟气提水装置以及集成式电厂间接空冷塔 |
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