CN207049946U - 提高垃圾焚烧电厂发电效率的系统 - Google Patents
提高垃圾焚烧电厂发电效率的系统 Download PDFInfo
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- CN207049946U CN207049946U CN201720861017.5U CN201720861017U CN207049946U CN 207049946 U CN207049946 U CN 207049946U CN 201720861017 U CN201720861017 U CN 201720861017U CN 207049946 U CN207049946 U CN 207049946U
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- 239000010813 municipal solid waste Substances 0.000 claims abstract description 46
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000003546 flue gas Substances 0.000 claims abstract description 32
- 235000019504 cigarettes Nutrition 0.000 claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 21
- 239000002918 waste heat Substances 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000004056 waste incineration Methods 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 4
- 239000000428 dust Substances 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 4
- 229920002456 HOTAIR Polymers 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000003517 fume Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 description 8
- 239000002893 slag Substances 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 210000003800 Pharynx Anatomy 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
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- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
Abstract
本实用新型提供一种提高垃圾焚烧电厂发电效率的系统，所述系统包括垃圾焚烧锅炉、余热锅炉、低温省煤器、烟冷器和空预器，所述垃圾焚烧锅炉排出的烟气依次经过所述余热锅炉、所述低温省煤器和所述烟冷器，所述空预器排出的低温给水进入所述烟冷器，以降低所述烟冷器排出的烟气的温度。根据本实用新型，能够降低锅炉排烟温度、提高锅炉效率，从而解决垃圾焚烧发电厂发电效率低的问题，提高垃圾焚烧电厂的效益。
Description
提高垃圾焚烧电厂发电效率的系统
技术领域
[0001] 本实用新型涉及垃圾焚烧领域，具体而言涉及一种提高垃圾焚烧电厂发电效率的 系统。
背景技术
[0002] 对于目前的垃圾焚烧电厂而言，由于垃圾的硫和氯含量较高，容易产生高温腐蚀 和低温腐蚀，故垃圾焚烧锅炉的蒸汽参数较低、排烟温度较高，导致锅炉效率低，电厂发电 效率低。
[0003] 为了提高垃圾焚烧发电厂发电效率，垃圾焚烧锅炉的蒸汽参数由中温中压4MPa/ 400°C不断提高，目前提高到中温超高压13.7MPa/450°C，给水温度也由130°C提高到253°C， 但此时排烟温度约300°C，远高于常规垃圾焚烧锅炉的排烟温度190°C-210°C。 实用新型内容
[0004] 针对现有技术的不足，本实用新型提供一种提高垃圾焚烧电厂发电效率的系统， 所述系统包括垃圾焚烧锅炉、余热锅炉、低温省煤器、烟冷器和空预器，所述垃圾焚烧锅炉 排出的烟气依次经过所述余热锅炉、所述低温省煤器和所述烟冷器，所述空预器排出的低 温给水进入所述烟冷器，以降低所述烟冷器排出的烟气的温度。
[0005] 在一个示例中，所述烟冷器排出的烟气的温度为190°C-21(TC。
[0006] 在一个示例中，所述空预器排出的热空气进入所述垃圾焚烧锅炉中与垃圾焚烧产 生的烟气混合进行燃烧。
[0007] 在一个示例中，主给水的一部分通入所述空预器加热进入所述空预器的冷空气， 所述主给水的另一部分与所述烟冷器排出的升温后的给水混合后通入所述低温省煤器，与 进入所述低温省煤器的烟气进行换热。
[0008] 在一个示例中，所述垃圾焚烧锅炉的蒸汽参数为13.7MPa/450°C，所述主给水的温 度为240°C-260°C。
[0009] 在一个示例中，进入所述垃圾焚烧锅炉的一次风的温度为220°C-240°C。
[0010] 在一个示例中，所述烟冷器排出的烟气进入烟气净化系统，经过所述烟气净化系 统处理后通过烟囱排到大气中。
[0011] 在一个示例中，所述烟气净化处理系统包括依次实施的SNCR脱硝、半干法脱酸、干 法脱酸降温、活性炭吸附、布袋除尘、蒸汽加热、低温SCR脱硝、烟气换热、湿法脱酸和烟气脱 除白雾。
[0012] 在一个示例中，所述垃圾焚烧锅炉的炉排采用往复式机械炉排，包括给料炉排和 焚烧炉排。
[0013] 根据本实用新型，能够降低锅炉排烟温度、提高锅炉效率，从而解决垃圾焚烧发电 厂发电效率低的问题，提高垃圾焚烧电厂的效益。
附图说明
[0014] 本实用新型的下列附图在此作为本实用新型的一部分用于理解本实用新型。附图 中示出了本实用新型的实施例及其描述，用来解释本实用新型的原理。
[0015] 附图中：
[0016] 图1为现有的垃圾焚烧机械炉排炉的示意性剖面图；
[0017] 图2为根据本实用新型示例性实施例的提高垃圾焚烧电厂发电效率的系统的示意 图。
具体实施方式
[0018] 在下文的描述中，给出了大量具体的细节以便提供对本实用新型更为彻底的理 解。然而，对于本领域技术人员而言显而易见的是，本实用新型可以无需一个或多个这些细 节而得以实施。在其他的例子中，为了避免与本实用新型发生混淆，对于本领域公知的一些 技术特征未进行描述。
[0019] 为了彻底了解本实用新型，将在下列的描述中提出详细的方法步骤和/或结构。显 然，本实用新型的施行并不限定于本领域的技术人员所熟悉的特殊细节。本实用新型的较 佳实施例详细描述如下，然而除了这些详细描述外，本实用新型还可以具有其他实施方式。
[0020] 应当理解的是，本实用新型能够以不同形式实施，而不应当解释为局限于这里提 出的实施例。相反地，提供这些实施例将使公开彻底和完全，并且将本实用新型的范围完全 地传递给本领域技术人员。在附图中，为了清楚，层和区的尺寸以及相对尺寸可能被夸大。 自始至终相同附图标记表示相同的元件。
[0021] 应当理解的是，当在本说明书中使用术语“包含”和/或“包括”时，其指明存在所述 特征、整体、步骤、操作、元件和/或组件，但不排除存在或附加一个或多个其他特征、整体、 步骤、操作、元件、组件和/或它们的组合。单数形式的“一”、“一个”和“所述/该”也意图包括 复数形式，除非上下文清楚指出另外的方式。
[0022] 现有的垃圾焚烧锅炉以直接焚烧为主，机械炉排炉为其主流。图1示出了一种机械 炉排炉，包括进料口 1 〇 1、给料炉排102、位于炉膛内的用于垃圾焚烧的炉排103、位于焚烧炉 排下部的一次风供风系统104、位于炉喉部的二次风供风系统1〇5以及排渣机1〇6。一次风从 焚烧炉排底部的风室送入，二次风从垃圾焚烧炉的炉喉部送入。
[0023] 焚烧炉排整体构成用于焚烧垃圾的炉床，所述炉床沿纵向分为干燥段、燃烧段和 燃尽段，焚烧炉排整体沿纵向分为多个焚烧单元，通常为5个单元，每一焚烧单元由多个滑 动炉排片、翻动炉排片和固定炉排片组成。垃圾从进料口倒入垃圾焚烧锅炉，通过给料炉排 的往复推动作用使垃圾进入垃圾焚烧锅炉内的炉床上进行焚烧，在干燥段垃圾被烘干、脱 水，垃圾主要在燃烧段进行燃烧，经过燃尽段的垃圾已经燃烧殆尽，之后剩余的炉渣进入排 澄机，由排渣机排出炉外。
[0024] 对于现有的垃圾焚烧锅炉而言，由于垃圾的硫和氯含量较高，容易产生高温腐蚀 和低温腐蚀，故垃圾焚烧锅炉的蒸汽参数较低、排烟温度较高，导致锅炉效率低，电厂发电 效率低。
[0025] 在现有的技术中，为了提高垃圾焚烧电厂循环热效率，将垃圾焚烧锅炉的蒸汽参 数提高到中温超高压13.7MPa/450°C，给水温度提高到253°C，但此时排烟温度约300°C，远 高于常规垃圾焚烧锅炉的排烟温度190°C-210°C，导致锅炉排烟温度偏高，锅炉效率低，电 厂发电效率低。
[0026]为了解决现有的垃圾焚烧锅炉所具有的上述技术问题，本实用新型提供一种提高 垃圾焚烧电厂发电效率的系统，该系统采用烟冷器和空预器组合的方式降低锅炉排烟温 度，达到余热利用的目的，提高电厂循环热效率，提高垃圾焚烧电厂的效益。
[0027][示例性实施例]
[0028]图2示出了本实用新型提出的提高垃圾焚烧电厂发电效率的系统的结构组成。 [0029]如图2所示，本实用新型提出的提高垃圾焚烧电厂发电效率的系统由垃圾焚烧锅 炉①、余热锅炉②、低温省煤器③、烟冷器④、空预器⑤等组成。
[0030] 垃圾焚烧锅炉①排出的烟气，进入余热锅炉②进行热量利用。然后，高温烟气进入 余热锅炉②尾部的低温省煤器③，加热进入低温省煤器③的给水，低温省煤器③排出的烟 气进入烟冷器④进一步热量利用。主给水⑥的一部分进入空预器⑤换热，加热进入空预器 ⑤的冷空气⑦，空预器⑤排出的热空气⑨进入垃圾焚烧锅炉①中与垃圾焚烧产生的烟气混 合进行燃烧。空预器⑤排出的换热之后的低温给水进入烟冷器④，与低温省煤器③排出的 烟气进行换热升温，将烟冷器④排出的锅炉排烟⑧的温度降至190°C-21(TC。烟冷器④排出 的升温后的给水与主给水⑥的另一部分混合后进入低温省煤器③，与进入低温省煤器③的 高温烟气进行换热。
[0031] 垃圾焚烧锅炉①的炉排采用一般的往复式机械炉排，待焚烧的垃圾进入垃圾进料 斗后，从垃圾进料斗的底部落入给料炉排，通过给料炉排的往复推动作用将垃圾送入位于 炉膛内的焚烧炉排。位于焚烧炉排下部的一次风供风系统将一次风从焚烧炉排底部的风室 送入炉膛，位于垃圾焚烧锅炉①炉拱上部的二次风供风系统将二次风从炉拱上部送入炉 膛。垃圾焚烧锅炉①的蒸汽参数为13.7MPa/450°C，主给水⑥温度为240°C-26(TC，优选253 °C，一次风温度为 22(TC-24(TC，优选230°C。
[0032]焚烧炉排整体构成用于焚烧垃圾的炉床，所述炉床沿纵向分为干燥段、燃烧段和 燃尽段，焚烧炉排整体沿纵向分为多个焚烧单元，通常为5个单元，每一焚烧单元由多个滑 动炉排片、翻动炉排片和固定炉排片组成。在干燥段，垃圾被烘干、脱水，垃圾主要在燃烧段 进行燃烧，经过燃尽段的垃圾已经燃烧殆尽，之后剩余的炉渣进入排渣机，由排渣机排出炉 外。
[0033]烟冷器④排出的锅炉排烟⑧经过烟气净化系统处理后通过烟囱排到大气中。示例 性地，所述烟气净化系统包括依次实施的SNCR脱硝、半干法脱酸、干法脱酸降温、活性炭吸 附、布袋除尘、蒸汽加热、低温SCR脱硝、烟气换热、湿法脱酸和烟气脱除白雾，所述SNCR脱硝 在SNCR装置内进行，所述半干法脱酸在半干法反应塔内进行，所述干法脱酸降温在干法脱 酸塔内进行，所述活性炭吸附和所述布袋除尘在布袋除尘器内进行，所述蒸汽加热在设置 于所述布袋除尘器和低温SCR装置之间的蒸汽加热器内进行，所述低温SCR脱硝在所述低温 SCR装置内进行，所述烟气换热在设置于所述低温SCR装置和湿法洗涤塔之间的烟气/烟气 换热器内进行，所述湿法脱酸在所述湿法洗涤塔内进行，所述烟气脱除白雾在另一蒸汽加 热器内进行。
[0034] 本实用新型具有以下优点：在垃圾焚烧锅炉①的蒸汽参数为13.7MPa/450°C、主给 水㈨W度为240°C-26(TC (优选253。〇时，采用烟冷器④和空预器⑤组合的方式降低锅炉排 烟⑧的温度，同时将送入垃圾焚烧锅炉①的一次风加热到22(TC-24(TC (优选230。〇，达到 余热利用的目的，提高电厂循环热效率，提高垃圾焚烧电厂的效益。
[0035]本实用新型已经通过上述实施例进行了说明，但应当理解的是，上述实施例只是 用于举例和说明的目的，而非意在将本实用新型限制于所描述的实施例范围内。此外本领 域技术人员可以理解的是，本实用新型并不局限于上述实施例，根据本实用新型的教导还 可以做出更多种的变型和修改，这些变型和修改均落在本实用新型所要求保护的范围以 内。本实用新型的保护范围由附属的权利要求书及其等效范围所界定。
Claims (9)
1. 一种提高垃圾焚烧电厂发电效率的系统，其特征在于，所述系统包括垃圾焚烧锅炉、 余热锅炉、低温省煤器、烟冷器和空预器，所述垃圾焚烧锅炉排出的烟气依次经过所述余热 锅炉、所述低温省煤器和所述烟冷器，所述空预器排出的低温给水进入所述烟冷器，以降低 所述烟冷器排出的烟气的温度。
2. 根据权利要求1所述的系统，其特征在于，所述烟冷器排出的烟气的温度为19〇 °C -21(TC。
3. 根据权利要求1所述的系统，其特征在于，所述空预器排出的热空气进入所述垃圾焚 烧锅炉中与垃圾焚烧产生的烟气混合进行燃烧。
4. 根据权利要求1所述的系统，其特征在于，主给水的一部分通入所述空预器加热进入 所述空预器的冷空气，所述主给水的另一部分与所述烟冷器排出的升温后的给水混合后通 入所述低温省煤器，与进入所述低温省煤器的烟气进行换热。
5. 根据权利要求4所述的系统，其特征在于，所述垃圾焚烧锅炉的蒸汽参数为13.7MPa/ 450°C，所述主给水的温度为240°C-260°C。
6. 根据权利要求1所述的系统，其特征在于，进入所述垃圾焚烧锅炉的一次风的温度为 220°C_240°C。
7. 根据权利要求1-6中任一项所述的系统，其特征在于，所述烟冷器排出的烟气进入烟 气净化系统，经过所述烟气净化系统处理后通过烟囱排到大气中。
8. 根据权利要求7所述的系统，其特征在于，所述烟气净化处理系统包括依次实施的 SNCR脱硝、半干法脱酸、干法脱酸降温、活性炭吸附、布袋除尘、蒸汽加热、低温SCR脱硝、烟 气换热、湿法脱酸和烟气脱除白雾。
9.根据权利要求1所述的系统，其特征在于，所述垃圾焚烧锅炉的炉排采用往复式机械 炉排，包括给料炉排和焚烧炉排。
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| CN110397481B (zh) * | 2019-07-02 | 2022-04-12 | 光大环保技术研究院（南京）有限公司 | 提升主蒸汽参数的垃圾焚烧发电装置 |
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