CN205700119U - 一种高效脱硫塔 - Google Patents
一种高效脱硫塔 Download PDFInfo
- Publication number
- CN205700119U CN205700119U CN201620582213.4U CN201620582213U CN205700119U CN 205700119 U CN205700119 U CN 205700119U CN 201620582213 U CN201620582213 U CN 201620582213U CN 205700119 U CN205700119 U CN 205700119U
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- Prior art keywords
- valve
- spray
- tower
- slurry pool
- controller
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 230000003009 desulfurizing Effects 0.000 title claims abstract description 43
- 239000007921 spray Substances 0.000 claims abstract description 63
- 238000005507 spraying Methods 0.000 claims abstract description 38
- 239000002002 slurry Substances 0.000 claims abstract description 34
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound 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OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型涉及一种高效脱硫塔，包括塔体，所述塔体内由下而上依次设置有浆液池、喷雾层、喷淋层及除雾器，所述塔体的下方侧壁上设有烟气接入口，所述塔体的顶部设有净烟出口，所述喷雾层中设置有喷雾管道，所述喷雾管道上设置有雾化喷嘴，所述喷淋层中设有一根喷淋管道，所述喷淋管道上均设置有螺旋喷淋头；所述烟气接入口上密封连接有进烟管，所述进烟管上安装有气体流量控制阀；还包括钠碱石灰池，所述钠碱石灰池的侧壁下端部分安装有出料管，所述出料管与所述浆液池联通，所述浆液池上安装有pH值监测仪；还包括搅拌器，所述搅拌器安装在所述浆液池中；还包括控制器，所述控制器独立设置并位于所述塔体的外部。
Description
技术领域
[0001]本实用新型涉及燃煤电厂脱硫领域，尤其涉及一种高效脱硫塔。
背景技术
[0002]目前，我国各种工业锅炉、炉窑均通过以煤为主的燃料燃烧进行工作，该过程会产生大量的含有二氧化硫和烟尘的废气，直接排放到大气中会导致严重的环境污染问题，如酸雨，雾霾天气等。随着国家以及民众对环保问题的日益重视，污染废气的排放标准及其执行的力度都越来越严格，在众多的湿法脱硫装置中，喷淋塔系统占有突出的地位，然而，面临新的二氧化硫排放标准(GB13223-2011)，将会有一大批的喷淋塔脱硫装置难以满足要求。
[0003]由于燃煤会产生的烟尘、硫化物等污染物。此类污染物的治理方法包括干法、湿法和半湿法，其中应用较多的是石灰石一石膏湿法脱硫。然而，现有技术提供的脱硫塔气流不够均匀，气液两相接触分布不均会导致脱硫效果不够理想。
[0004]现有的脱硫塔大多采用喷淋塔，由于喷淋液滴粒径较大等因素，常存在雾液接触不充分、烟气容易逃逸等问题。而如采用喷雾工艺，由于雾滴粒径很小，上升的烟气往往会抑制雾滴的下落，影响气液反应效果，烟气携带大量雾滴上行还容易造成除雾器的阻塞等问题。
[0005] 我国电力脱硫工艺以石灰石-石膏法湿法脱硫为主，通过调节脱硫剂的pH值和液气比可使脱硫剂被充分利用，脱硫效率有达到98%以上的潜力，但是目前湿法脱硫实际脱硫率大部分在95%，甚至以下。造成这种现象的主要原因是脱硫塔内气液混合效果差，受烟气温度流速影响很大;上游设备控制和工况发生改变时，如果不能及时调整，不仅会造成脱硫效率降低或脱硫剂浪费，还可能会引起设备的堵塞和结垢，脱硫产物的品位下降。因此如何结合上游设备控制和工况信息，即时调节液气比，合理调节脱硫剂pH值是是脱硫技术要解决的问题。
[0006]有鉴于上述的缺陷，本设计人，积极加以研究创新，以期创设一种高效脱硫塔，使其更具有产业上的利用价值。
实用新型内容
[0007]为解决上述技术问题，本实用新型的目的是提供一种能够随时调节脱硫剂pH值和液气比，提尚脱硫效率的尚效脱硫塔。
[0008]本实用新型的一种高效脱硫塔，其特征在于:包括塔体，所述塔体内由下而上依次设置有浆液池、喷雾层、喷淋层及除雾器，所述塔体的下方侧壁上设有烟气接入口，所述烟气接入口设置在所述浆液池与所述喷雾层之间，所述塔体的顶部设有净烟出口，所述喷雾层中均匀间隔水平设置有若干喷雾管道，所述喷雾管道上均匀间隔设置有若干雾化喷嘴，所述喷雾层与所述喷淋层之间设置有填料层，所述喷淋层中设有一根喷淋管道，所述喷淋管道水平位于所述喷淋层上端的中间，所述喷淋管道上均匀间隔设置有若干螺旋喷淋头，所述喷雾管道和喷淋管道均通过连接管道与所述浆液池连接，所述连接管道上安装有循环栗;
[0009]所述烟气接入口上密封连接有进烟管，所述进烟管上安装有气体流量控制阀；
[0010]还包括钠碱石灰池，所述钠碱石灰池密封设置在所述塔体的外部，所述钠碱石灰池的上端安装有清水管和进料管，所述钠碱石灰池的侧壁下端部分安装有出料管，所述出料管与所述浆液池联通，所述出料管上安装有出料阀，所述浆液池上安装有PH值监测仪；
[0011]还包括搅拌器，所述搅拌器安装在所述浆液池中，所述搅拌器上连接有伺服电机，所述伺服电机安装在所述塔体的外壁上；
[0012]还包括控制器，所述控制器独立设置并位于所述塔体的外部；
[0013]所述螺旋喷淋头、循环栗、气体流量控制阀均、出料阀、pH值监测仪和伺服电机均与所述控制器通信连接。
[0014]进一步的，所述浆液池中安装有液位计，所述液位计与所述控制器通信连接。
[0015]进一步的，所述浆液池的下方两侧分别设有进液管和排液管，所述进液管和排液管上分别安装有进液阀和排液阀，所述进液阀和排液阀均与所述控制器通信连接。
[0016]进一步的，所述喷雾管道上安装有喷雾阀，所述喷雾阀与所述控制器通信连接。
[0017]进一步的，所述喷淋管道上安装有喷淋阀，所述喷淋阀与所述控制器通信连接。
[0018]进一步的，所述喷雾管道为四个，每个喷雾管道上均匀间隔设置有五个雾化喷嘴。
[0019]进一步的，所述喷淋管道上螺旋喷淋头的数量为五个。
[0020]进一步的，所述出料阀、进液阀、排液阀、喷雾阀和喷淋阀均为电磁阀。
[0021]借由上述方案，本实用新型至少具有以下优点:该高效脱硫塔通过进烟管上的气体流量控制阀控制进烟量，从而调节液气比，通过PH值监测仪随时监测浆液池这脱硫剂的PH值，当脱硫剂的pH值低于设定范围时，通过将钠碱石灰池中调配的钠碱石灰液，输送到浆液池中，从而调节脱硫剂的PH值，进而提高脱硫剂的脱硫效率，通过浆液池中的搅拌器，能够不停地搅拌脱硫剂，使脱硫剂与烟气充分反应，进一步提高脱硫效率，再通过喷淋工艺和喷雾工艺，大幅提高了脱硫效率，在处理量较大及烟气二氧化硫浓度较高的情况下，亦能满足排放要求。该脱硫塔结构简易、容易实施、造价成本低，尤其适合传统喷淋脱硫塔的改造项目。
[0022]上述说明仅是本实用新型技术方案的概述，为了能够更清楚了解本实用新型的技术手段，并可依照说明书的内容予以实施，以下以本实用新型的较佳实施例并配合附图详细说明如后。
附图说明
[0023]图1是本实用新型高效脱硫塔的结构示意图；
[0024]图2是本实用新型中喷雾管道的结构示意图。
具体实施方式
[0025]下面结合附图和实施例，对本实用新型的具体实施方式作进一步详细描述。以下实施例用于说明本实用新型，但不用来限制本实用新型的范围。
[0026]实施例:一种高效脱硫塔，包括塔体I，所述塔体内由下而上依次设置有浆液池2、喷雾层3、喷淋层4及除雾器5，所述塔体的下方侧壁上设有烟气接入口 6，所述烟气接入口设置在所述浆液池与所述喷雾层之间，所述塔体的顶部设有净烟出口7，所述喷雾层中均匀间隔水平设置有若干喷雾管道31，所述喷雾管道上均匀间隔设置有若干雾化喷嘴32，所述喷雾层与所述喷淋层之间设置有填料层8，所述喷淋层中设有一根喷淋管道41，所述喷淋管道水平位于所述喷淋层上端的中间，所述喷淋管道上均匀间隔设置有若干螺旋喷淋头42，所述喷雾管道和喷淋管道均通过连接管道与所述浆液池连接，所述连接管道上安装有循环栗9；
[0027]所述烟气接入口上密封连接有进烟管61，所述进烟管上安装有气体流量控制阀62，所述气体流量控制阀与所述控制器通信连接。
[0028]还包括钠碱石灰池12，所述钠碱石灰池密封设置在所述塔体的外部，所述钠碱石灰池的上端安装有清水管13和进料管14，所述钠碱石灰池的侧壁下端部分安装有出料管15，所述出料管与所述浆液池联通，所述出料管上安装有出料阀16，所述浆液池上安装有pH值监测仪17;
[0029]还包括搅拌器18，所述搅拌器安装在所述浆液池中，所述搅拌器上连接有伺服电机19，所述伺服电机安装在所述塔体的外壁上；
[0030]还包括控制器10，所述控制器独立设置并位于所述塔体的外部；
[0031]所述螺旋喷淋头、循环栗、气体流量控制阀均、出料阀、pH值监测仪和伺服电机均与所述控制器通信连接。
[0032]所述浆液池中安装有液位计11，所述液位计与所述控制器通信连接。
[0033]所述浆液池的下方两侧分别设有进液管21和排液管22，所述进液管和排液管上分别安装有进液阀23和排液阀24，所述进液阀和排液阀均与所述控制器通信连接。
[0034]所述喷雾管道上安装有喷雾阀33，所述喷雾阀与所述控制器通信连接。
[0035]所述喷淋管道上安装有喷淋阀43，所述喷淋阀与所述控制器通信连接。
[0036]所述喷雾管道为四个，每个喷雾管道上均匀间隔设置有五个雾化喷嘴。
[0037]所述喷淋管道上螺旋喷淋头的数量为五个。
[0038]所述出料阀、进液阀、排液阀、喷雾阀和喷淋阀均为电磁阀。
[0039]该高效脱硫塔通过进烟管上的气体流量控制阀控制进烟量，从而调节液气比，通过PH值监测仪随时监测浆液池这脱硫剂的pH值，当脱硫剂的pH值低于设定范围时，通过将钠碱石灰池中调配的钠碱石灰液，输送到浆液池中，从而调节脱硫剂的PH值，进而提高脱硫剂的脱硫效率，通过浆液池中的搅拌器，能够不停地搅拌脱硫剂，使脱硫剂与烟气充分反应，进一步提高脱硫效率，再通过喷淋工艺和喷雾工艺，大幅提高了脱硫效率，在处理量较大及烟气二氧化硫浓度较高的情况下，亦能满足排放要求。该脱硫塔结构简易、容易实施、造价成本低，尤其适合传统喷淋脱硫塔的改造项目。
[0040]以上所述仅是本实用新型的优选实施方式，并不用于限制本实用新型，应当指出，对于本技术领域的普通技术人员来说，在不脱离本实用新型技术原理的前提下，还可以做出若干改进和变型，这些改进和变型也应视为本实用新型的保护范围。
Claims (8)
1.一种高效脱硫塔，其特征在于:包括塔体，所述塔体内由下而上依次设置有浆液池、喷雾层、喷淋层及除雾器，所述塔体的下方侧壁上设有烟气接入口，所述烟气接入口设置在所述浆液池与所述喷雾层之间，所述塔体的顶部设有净烟出口，所述喷雾层中均匀间隔水平设置有若干喷雾管道，所述喷雾管道上均匀间隔设置有若干雾化喷嘴，所述喷雾层与所述喷淋层之间设置有填料层，所述喷淋层中设有一根喷淋管道，所述喷淋管道水平位于所述喷淋层上端的中间，所述喷淋管道上均匀间隔设置有若干螺旋喷淋头，所述喷雾管道和喷淋管道均通过连接管道与所述浆液池连接，所述连接管道上安装有循环栗； 所述烟气接入口上密封连接有进烟管，所述进烟管上安装有气体流量控制阀； 还包括钠碱石灰池，所述钠碱石灰池密封设置在所述塔体的外部，所述钠碱石灰池的上端安装有清水管和进料管，所述钠碱石灰池的侧壁下端部分安装有出料管，所述出料管与所述浆液池联通，所述出料管上安装有出料阀，所述浆液池上安装有PH值监测仪； 还包括搅拌器，所述搅拌器安装在所述浆液池中，所述搅拌器上连接有伺服电机，所述伺服电机安装在所述塔体的外壁上； 还包括控制器，所述控制器独立设置并位于所述塔体的外部； 所述螺旋喷淋头、循环栗、气体流量控制阀均、出料阀、PH值监测仪和伺服电机均与所述控制器通信连接。
2.根据权利要求1所述的一种高效脱硫塔，其特征在于:所述浆液池中安装有液位计，所述液位计与所述控制器通信连接。
3.根据权利要求2所述的一种高效脱硫塔，其特征在于:所述浆液池的下方两侧分别设有进液管和排液管，所述进液管和排液管上分别安装有进液阀和排液阀，所述进液阀和排液阀均与所述控制器通信连接。
4.根据权利要求3所述的一种高效脱硫塔，其特征在于:所述喷雾管道上安装有喷雾阀，所述喷雾阀与所述控制器通信连接。
5.根据权利要求4所述的一种高效脱硫塔，其特征在于:所述喷淋管道上安装有喷淋阀，所述喷淋阀与所述控制器通信连接。
6.根据权利要求5所述的一种高效脱硫塔，其特征在于:所述喷雾管道为四个，每个喷雾管道上均匀间隔设置有五个雾化喷嘴。
7.根据权利要求6所述的一种高效脱硫塔，其特征在于:所述喷淋管道上螺旋喷淋头的数量为五个。
8.根据权利要求7所述的一种高效脱硫塔，其特征在于:所述出料阀、进液阀、排液阀、喷雾阀和喷淋阀均为电磁阀。
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