CN203907646U - 火力发电厂锅炉烟气余热干燥褐煤系统 - Google Patents
火力发电厂锅炉烟气余热干燥褐煤系统 Download PDFInfo
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- CN203907646U CN203907646U CN201420180737.1U CN201420180737U CN203907646U CN 203907646 U CN203907646 U CN 203907646U CN 201420180737 U CN201420180737 U CN 201420180737U CN 203907646 U CN203907646 U CN 203907646U
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- boiler
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- drying
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- 239000003077 lignite Substances 0.000 title claims abstract description 36
- 238000001035 drying Methods 0.000 title claims abstract description 30
- 239000000779 smoke Substances 0.000 title claims abstract description 21
- 239000002918 waste heat Substances 0.000 title claims abstract description 21
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 42
- 239000003546 flue gas Substances 0.000 claims description 35
- 238000011084 recovery Methods 0.000 claims description 18
- 238000006477 desulfuration reaction Methods 0.000 claims description 17
- 239000003517 fume Substances 0.000 claims description 8
- 238000004891 communication Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
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Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
本实用新型公开了一种火力发电厂锅炉烟气余热干燥褐煤系统，包括通过烟气管道依次连通的锅炉、省煤器、烟气余热回收装置以及脱硫吸收塔，所述烟气管道上还设置有用于将锅炉排烟引至脱硫吸收塔的烟气引风机；所述烟气余热回收装置通过水管道连通一暖风器，暖风器的热风出口通过进风管道连通褐煤干燥塔，褐煤干燥塔的顶部通过干燥风管道连通锅炉的二次风进口，干燥风管道上设置有干燥引风机。本实用新型利用能量分级利用的原理，能够在实现用低品位热能实现提高高品位热能利用率的基础上，通过锅炉回收的烟气热量，加热电厂燃用的高水分褐煤，从而提高入炉煤的品质，在不浪费能源的情况下，最大幅度利用烟气热量，提高火力发电机组的经济性。
Description
技术领域
[0001] 本实用新型涉及火力发电厂中的余热回收系统，特别是一种利用烟气余热对褐煤 进行干燥的辅助系统。
背景技术
[0002] 火力发电厂中多使用燃煤锅炉进行发电，煤炭燃烧发电的过程中锅炉的排烟热损 失是锅炉热损失中最大的，锅炉排出的高温烟气一般是经过省煤器后在引风机的作用下输 送至脱硫吸收塔中，最后再通过烟囱排出；在脱硫吸收塔的入口安装GGH系统(烟气余热回 收利用装置)，使烟气与凝结水直接进行热交换，对烟气进行降温处理，以减少脱硫吸收塔 的工艺水蒸发量，增加烟气抬升高度，减轻烟气对烟®的腐蚀以及烟®冒白烟的现象；但 是，锅炉的排烟温度一般在120〜150°C之间，限制了被加热的凝结水温升和凝结水抽出点 的位置，被排挤的汽轮机的抽汽做功能力有限；另外，GGH系统易积灰和结垢，降低了系统 脱硫效率，影响脱硫系统安全可靠运行。因此，目前新上大型火力发电机组的烟气系统中大 多取消了 GGH系统，这就使得进入脱硫系统的烟气温度较高，一般为在120〜150°C之间，褐 煤机组可能达到145 °C。
[0003] 为了脱硫工艺达到最佳的工作温度，即烟气温度80°C〜90°C，目前，许多新建脱 硫系统设置了喷淋降温系统。然而进入脱硫系统的烟气温度与最佳脱硫工作温度之间几十 度的温差，蕴含着巨大的热量，采用喷淋降温系统必然会将此部分热量浪费掉。一般来说， 锅炉排烟温度每降低10°c，锅炉的热效率即可提高约0. 5%至0. 6%，因此锅炉排烟是一项 潜力很大的余热资源，对该部分烟气余热的回收利用是非常必要的。 实用新型内容
[0004] 本实用新型需要解决的技术问题是提供一种能够对火力发电厂锅炉烟气进行充 分利用的烟气余热系统，以提高火力发电机组的经济性。
[0005] 为解决上述技术问题，本实用新型所采用的技术方案是：
[0006] 火力发电厂锅炉烟气余热干燥褐煤系统，包括通过烟气管道依次连通的锅炉、省 煤器、烟气余热回收装置以及脱硫吸收塔，所述烟气管道上还设置有用于将锅炉排烟引至 脱硫吸收塔的烟气引风机；所述烟气余热回收装置通过水管道连通一暖风器，暖风器的热 风出口通过进风管道连通褐煤干燥塔，褐煤干燥塔的顶部通过干燥风管道连通锅炉的二次 风进口，干燥风管道上设置有干燥引风机。
[0007] 本实用新型的改进在于：所述省煤器与烟气引风机之间的烟气管道上设置有除尘 器。
[0008] 由于采用了上述技术方案，本实用新型取得的技术进步是：
[0009] 本实用新型应用在燃用褐煤煤质的电厂中，利用能量分级利用的原理，能够在实 现用低品位热能实现提高高品位热能利用率的基础上，通过锅炉回收的烟气热量，加热电 厂的燃用的高水分褐煤，从而提高入炉煤的品质，在不浪费能源的情况下，最大幅度利用烟 气热量，提高火力发电机组的经济性。烟气管道上除尘器的设置，能够在烟气进入烟气余 热回收装置及脱硫吸收塔之前有效清除烟气中的粉尘颗粒，避免烟气余热回收装置出现积 灰、结垢现象。
附图说明
[0010] 图1为本实用新型的系统结构图；
[0011] 其中：1.锅炉，2.省煤器，3.旁路省煤器，4.除尘器，5.烟气余热回收装置，6.脱 硫吸收塔，7.烟气引风机，8.暖风器，9.闭式循环水泵，10.褐煤干燥塔，11.干燥引风机， 12.空气预热器。
[0012] 图中虚线箭头方向为烟气走向，单实线箭头方向为干燥风走向，双实线箭头方向 为褐煤走向。
具体实施方式
[0013] 下面结合附图对本实用新型做进一步详细说明：
[0014] 一种火力发电厂锅炉烟气余热干燥褐煤系统，其结构如图1所示。包括锅炉1、省 煤器2、除尘器4、烟气引风机7、烟气余热回收装置5、脱硫吸收塔6、暖风器8以及褐煤干燥 塔10。
[0015] 其中：锅炉1、省煤器2、除尘器4、烟气引风机7、烟气余热回收装置5以及脱硫吸 收塔6通过烟气管道依次连通；烟气余热回收装置5通过水管道连通暖风器8,暖风器8的 热风出口通过进风管道连通褐煤干燥塔10,褐煤干燥塔的顶部通过干燥风管道连通锅炉1 的二次风进口，干燥风管道上设置有干燥引风机11。省煤器2也可以设置旁路省煤器3，省 煤器中还设置有空气预热器12,用于加热冷二次风，为锅炉提供热二次风。
[0016] 除尘器用于去除烟气中的粉尘颗粒。烟气引风机7用于将锅炉排烟引至脱硫吸收 塔。烟气余热回收装置5用于将锅炉烟气从140°C降低到脱硫入口要求的80°C左右，从而 可使锅炉热量损失减少60°C，锅炉折算效率提高约5%左右。
[0017] 烟气余热回收装置通过水管道与暖风器形成一个闭式回路，回收的这部分热量利 用闭式循环水通过暖风器来加热用于干燥高水分褐煤用的干燥风。
[0018] 本实用新型的烟气余热回收利用过程如下：
[0019] 从锅炉排出的烟气在烟气引风机的作用下，经省煤器后经过除尘器除尘后在烟气 余热回收装置进行热交换，锅炉烟气经烟气余热回收装置从140°c降低到脱硫吸收塔入口 要求的80°C左右后，进入脱硫吸收塔，最后经烟囱排出。烟气的走向如图1中的虚线箭头方 向。
[0020] 烟气余热回收装置吸收的热量通过闭式循环水将热量带至暖风器，用于加热冷 风；冷风被加热成热干燥风后经进风管道引入褐煤干燥塔下部，热干燥风在褐煤干燥塔内 由下至上运行，用于风干高水分褐煤，变成含有部分煤尘和煤挥发粉的空气，含有煤尘和煤 挥发粉的空气在干燥引风机作用下通过干燥风管道被送到锅炉的热二次风管道内，进入炉 膛，参与锅炉燃烧，此系统不会损失原煤内的有效热量。根据等效焓降理论，则此时回收的 烟气热量利用率更高。干燥风的走向如图1中的单实线箭头方向。
[0021] 褐煤干燥塔中的褐煤自顶部给煤机给料后自上而下掉落，高水分褐煤在自上而下 掉落的过程中与热干燥风进行热交换，热干燥风将褐煤中的水分带走，从而起到干燥褐煤 的作用；被干燥后的褐煤从褐煤干燥塔底部出料。褐煤的走向如图1中的双实线箭头方向。
Claims (2)
1. 火力发电厂锅炉烟气余热干燥褐煤系统，包括通过烟气管道依次连通的锅炉（1)、 省煤器（2)、烟气余热回收装置（5)以及脱硫吸收塔（6)，所述烟气管道上还设置有用于将 锅炉排烟引至脱硫吸收塔的烟气引风机（7);其特征在于：所述烟气余热回收装置（5)通过 水管道连通一暖风器（8)，暖风器（8)的热风出口通过进风管道连通褐煤干燥塔（10)，褐煤 干燥塔的顶部通过干燥风管道连通锅炉（1)的二次风进口，干燥风管道上设置有干燥引风 机（11)。
2. 根据权利要求1所述的火力发电厂锅炉烟气余热干燥褐煤系统，其特征在于：所述 省煤器（2)与烟气引风机（7)之间的烟气管道上设置有除尘器（4)。
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| CN104775933A (zh) * | 2015-04-09 | 2015-07-15 | 山东电力工程咨询院有限公司 | 一种发电内燃机余热梯级利用系统 |
| CN104791818A (zh) * | 2015-04-17 | 2015-07-22 | 杭州兴环科技开发有限公司 | 一种提高电除尘装置效率的锅炉烟气余热回收方法及系统 |
| CN105115286A (zh) * | 2015-08-21 | 2015-12-02 | 广西立盛茧丝绸有限公司 | 一种利用锅炉烟气余热的烘干装置 |
| CN109373332A (zh) * | 2018-09-07 | 2019-02-22 | 上海明华电力技术工程有限公司 | 一种燃煤耦合垃圾发电的烟气余热回收系统和方法 |
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| CN104775933A (zh) * | 2015-04-09 | 2015-07-15 | 山东电力工程咨询院有限公司 | 一种发电内燃机余热梯级利用系统 |
| CN104791818A (zh) * | 2015-04-17 | 2015-07-22 | 杭州兴环科技开发有限公司 | 一种提高电除尘装置效率的锅炉烟气余热回收方法及系统 |
| CN105115286A (zh) * | 2015-08-21 | 2015-12-02 | 广西立盛茧丝绸有限公司 | 一种利用锅炉烟气余热的烘干装置 |
| CN109373332A (zh) * | 2018-09-07 | 2019-02-22 | 上海明华电力技术工程有限公司 | 一种燃煤耦合垃圾发电的烟气余热回收系统和方法 |
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