CN204026622U - 蒸汽锅炉 - Google Patents
蒸汽锅炉 Download PDFInfo
- Publication number
- CN204026622U CN204026622U CN201420432874.XU CN201420432874U CN204026622U CN 204026622 U CN204026622 U CN 204026622U CN 201420432874 U CN201420432874 U CN 201420432874U CN 204026622 U CN204026622 U CN 204026622U
- Authority
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- China
- Prior art keywords
- flue
- steam
- still
- steam generation
- heat
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 206010022000 Influenza Diseases 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 31
- 239000003546 flue gas Substances 0.000 abstract description 31
- 239000007789 gas Substances 0.000 abstract description 7
- 239000002918 waste heat Substances 0.000 abstract description 3
- 239000000498 cooling water Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型提供了蒸汽锅炉，包括蒸汽发生釜、预热箱、水泵和超导热棒，所述预热箱的出水口通过水泵与所述蒸汽发生釜的入水口连通，蒸汽发生釜内腔中固定多个烟道，烟道的热源进气口及出气口分别从所述蒸汽发生釜的两侧壁伸出，所述超导热棒的一端设置于所述烟道的腔体中，另一端设置于所述预热箱内，使所述烟道中的热量传输到所述预热箱中。利用蒸汽发生釜中的多个烟道，将高温烟气分道通行，则流通平稳匀速，采用超导热材质的烟道传热壁，传热性能好且传热均匀，换热效率高。同时，利用在烟道的出烟口和预热箱之间设置的超导热棒，将排出的烟气中的余热传导至预热箱内，将预热箱内的冷水进行预热，充分利用高温烟气中的热量。
Description
技术领域
[0001] 本实用新型涉及蒸汽锅炉技术领域，尤其涉及带余热利用装置的蒸汽锅炉。
背景技术
[0002]目前，蒸汽锅炉是利用燃煤、燃气、燃油或者电能等能源的化学能、电能或者燃烧产生的高温烟气对水媒介等进行加热，产生蒸汽的锅炉。传统的利用高温烟气加热的蒸汽锅炉采用传统的换热管，传热不均匀，烟气流速也不均匀，换热效率低，而且大量携带热量的烟气被排放，导致锅炉大量消耗能源，不利于节能减排。
实用新型内容
[0003] 本实用新型的目的是提供蒸汽锅炉，解决现有蒸汽锅炉采用传统的换热管，传热不均匀，烟气流速也不均匀，换热效率低，而且大量携带热量的烟气被排放，造成能源浪费的技术问题。
[0004] 为了达到上述目的，本实用新型提供如下技术方案:
[0005] 蒸汽锅炉，包括，蒸汽发生釜、预热箱、水泵和超导热棒；所述预热箱的出水口通过水泵与所述蒸汽发生釜的入水口连通，蒸汽发生釜内腔中固定多个烟道，烟道的热源进气口及出气口分别从所述蒸汽发生釜的两侧壁伸出，所述超导热棒的一端设置于所述烟道的腔体中，另一端设置于所述预热箱内，使所述烟道中的热量传输到所述预热箱中。
[0006] 进一步地，所述烟道为水平设置。
[0007] 进一步地，所述烟道的侧壁采用超导热材质，例如，烟道采用超导热管。
[0008] 进一步地，所述超导热棒为一端为锥形的棒体，该锥形端设置于所述烟道的腔体中。
[0009] 进一步地，还包括总进烟口，在多个烟道的热源进气口端连接总进烟口，总进烟口与蒸汽发生釜的外壁密封连接。
[0010] 进一步地，还包括总出烟口，在多个烟道的出气口端连接总出烟口，总出烟口与蒸汽发生釜的外壁密封连接。
[0011] 进一步地，还包括，蒸汽釜，所述蒸汽釜固定在蒸汽发生釜的上方，蒸汽发生釜的顶部固定上升管，所述上升管从蒸汽釜的底部伸入蒸汽釜内腔中，蒸汽釜的出水与蒸汽发生釜的另一入水口连通。将蒸汽釜的出水口与蒸汽发生釜连通，将由上升管流入蒸汽釜内的水回流至蒸汽发生釜内，循环利用。
[0012] 进一步地，所述蒸汽发生釜入水口和另一入水口均设置在蒸汽发生釜的底部。
[0013] 本实用新型的蒸汽锅炉，利用在蒸汽发生釜中设置的多个烟道，将高温烟气分道通行，则高温烟气的流通更平稳，匀速，进一步采用超导热材质为侧壁的烟道，传热性能好且传热均匀，使得烟道中的高温烟气的热量对蒸汽发生釜中的水进行很好的加热，换热效率高。同时，利用在烟道和预热箱之间设置的超导热棒，将排出的烟气中的余热传导至预热箱内，将预热箱内的冷水进行预热，充分利用高温烟气中的热量。
[0014] 进一步地，将烟道在蒸汽发生釜中水平设置，并在多个烟道的进烟口外设置总进烟口，总进烟口与各烟道的进烟口之间的空间为高温烟气提供了缓冲空间，使得进入烟道的高温烟气的平稳性增强。总出烟口的设置方便了烟气的统一排放处理。
附图说明
[0015] 为了更清楚地说明本实用新型实施例或现有技术中的技术方案，下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本实用新型的一些实施例，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获得其他的附图。
[0016] 图1是本实用新型的一种带余热利用装置的蒸汽锅炉的内部结构示意图；
[0017] 图中，1、蒸汽发生釜，11、上升管，2、烟道，21、总进烟口，22、总出烟口，3、超导热棒，4、预热箱，41、冷水进口，5、水泵，6、蒸汽釜，61、蒸汽出口。
具体实施方式
[0018] 下面将结合本实用新型的附图，对本实用新型的技术方案进行清楚、完整地描述，显然，所描述的实施例仅仅是本实用新型一部分实施例，而不是全部的实施例。基于本实用新型中的实施例，本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例，都属于本实用新型保护的范围。
[0019] 根据图1所示，说明本实用新型的具体实施方式的蒸汽锅炉，包括蒸汽釜、蒸汽发生釜、预热箱、水泵和超导热棒；蒸汽发生釜内腔中水平地固定多个烟道，烟道采用超导热管，传热性能好且传热均匀，超导热管烟道的热源进气口及出气口分别从所述蒸汽发生釜的两侧壁伸出，并使得超导热管烟道与蒸汽发生釜的两侧壁密封连接，超导热棒的一端设置于所述烟道的腔体中，该端部由烟道的出气口伸入烟道的腔体，另一端设置于所述预热箱内，穿过预热箱的侧壁后伸入预热箱内，并与预热箱的侧壁密封连接，高温烟气由烟道的热源进气口进入后，平稳地流动，其携带的热量经由超导热管传导至蒸汽发生釜内，至出烟口时，烟气中的余热经由超导热棒传导至预热箱内，将预热箱内的冷水进行预热，充分利用高温烟气中的剩余热量，热量利用率高，节能环保；预热箱的顶部开设冷水进口，预热箱的底部开设出水口，蒸汽发生釜的底部开设入水口，所述预热箱的出水口通过水泵与所述蒸汽发生釜的入水口连通，利用水泵将预热箱内预热后的温水输送至蒸汽发生釜内，并使温水经由蒸汽发生釜的底部向顶部运动，在向上运动的过程中，烟道中的高温烟气的热量将温水继续加热至变成蒸汽，蒸汽由蒸汽发生釜顶部固定的并伸入上方蒸汽釜内的多根上升管进入蒸汽釜内(如，4根上升管)，并由蒸汽釜上的蒸汽出口排出，也有部分加热后的水经由上升管流出至蒸汽釜内，保证该上升管的管口要高于蒸汽釜内水面的高度，在蒸汽釜的靠近底部的侧壁上开设出水口，该出水口与蒸汽发生釜底部开设的另一入水口连通，使得蒸汽釜和蒸汽发生釜循环连通，实现蒸汽釜与蒸汽发生釜间水的流动。
[0020] 为了充分利用即将排出烟道的烟气中的热量，将超导热棒设计为一端为锥形的棒体，并将锥形端由烟道的出气口伸入烟道的腔体内，并控制该端部不超过烟道的中间部位，增加了超导热棒在烟道内的热传导表面积，提高了热量利用率。
[0021] 高温烟气进入蒸汽发生釜前，其流速是很快的，如果高温烟气直接通入烟道，很容易使烟道内的高温烟气不平稳，流速快，热量不能很好地传递至蒸汽发生釜内，因此，在多个烟道的热源进气口端连接总进烟口，总进烟口与蒸汽发生釜的外壁密封连接。高温烟气在总进烟口与多个烟道的热源进气口间有一个缓冲空间，使得进入烟道的高温烟气的平稳性增强，速度均匀。
[0022] 在烟气排出前，为了环保，需要将烟气进行统一处理达到排放标准后再进行排放，由于有多个烟道，因此，为了方便对排出的烟气进行处理，在多个烟道的出气口端连接总出烟口，总出烟口与蒸汽发生釜的外壁密封连接。排出的烟气经由总出烟口排出，方便进行统一处理。
[0023] 以上所述，仅为本实用新型的具体实施方式，但本实用新型的保护范围并不局限于此，任何熟悉本技术领域的技术人员在本实用新型揭露的技术范围内，可轻易想到变化或替换，都应涵盖在本实用新型的保护范围之内。因此，本实用新型的保护范围应所述以权利要求的保护范围为准。
Claims (7)
1.蒸汽锅炉，其特征在于:包括，蒸汽发生釜、预热箱、水泵和超导热棒；所述预热箱的出水口通过水泵与所述蒸汽发生釜的入水口连通，蒸汽发生釜内腔中固定多个烟道，烟道的热源进气口及出气口分别从所述蒸汽发生釜的两侧壁伸出，所述超导热棒的一端设置于所述烟道的腔体中，另一端设置于所述预热箱内，使所述烟道中的热量传输到所述预热箱中。
2.根据权利要求1所述的蒸汽锅炉，其特征在于:所述烟道为水平设置。
3.根据权利要求1或2所述的蒸汽锅炉，其特征在于:所述超导热棒为一端为锥形的棒体，该锥形端设置于所述烟道的腔体中。
4.根据权利要求1或2所述的蒸汽锅炉，其特征在于:还包括总进烟口，在多个烟道的热源进气口端连接总进烟口，总进烟口与蒸汽发生釜的外壁密封连接。
5.根据权利要求4所述的蒸汽锅炉，其特征在于:还包括总出烟口，在多个烟道的出气口端连接总出烟口，总出烟口与蒸汽发生釜的外壁密封连接。
6.根据权利要求1、2或5所述的蒸汽锅炉，其特征在于:还包括，蒸汽釜，所述蒸汽釜固定在蒸汽发生釜的上方，蒸汽发生釜的顶部固定上升管，所述上升管从蒸汽釜的底部伸入蒸汽釜内腔中，蒸汽釜的出水口与蒸汽发生釜的另一入水口连通。
7.根据权利要求1、2或5所述的蒸汽锅炉，其特征在于:所述烟道的侧壁采用超导热材质。
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