CN205174413U - 锅炉烟尘旋风分离回收利用装置 - Google Patents
锅炉烟尘旋风分离回收利用装置 Download PDFInfo
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- CN205174413U CN205174413U CN201520932348.4U CN201520932348U CN205174413U CN 205174413 U CN205174413 U CN 205174413U CN 201520932348 U CN201520932348 U CN 201520932348U CN 205174413 U CN205174413 U CN 205174413U
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- boiler
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- 239000000779 smoke Substances 0.000 title claims abstract description 20
- 238000000926 separation method Methods 0.000 title claims abstract description 15
- 239000000428 dust Substances 0.000 claims abstract description 52
- 239000000463 material Substances 0.000 claims abstract description 17
- 238000007906 compression Methods 0.000 claims abstract description 5
- 239000004744 fabric Substances 0.000 claims description 19
- 238000007599 discharging Methods 0.000 claims description 11
- 229910052571 earthenware Inorganic materials 0.000 claims description 3
- 230000005611 electricity Effects 0.000 abstract description 5
- 210000003437 Trachea Anatomy 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 15
- 239000003546 flue gas Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 8
- 239000003500 flue dust Substances 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型涉及一种锅炉烟尘旋风分离回收利用装置。采用的技术方案是：包括带有返料器的锅炉的烟道设有电袋除尘器，锅炉烟道与电袋除尘器间设并列的两旋风分离器，旋风分离器的下料端设第一下料阀，第一下料阀的下方管道通入第一仓泵中，电袋除尘的下料端设第二下料阀和第二仓泵，第一仓泵与第二仓泵的出料口管道串联通入灰尘管道，灰尘管道两端分别通入锅炉的返料器和灰场，第一仓泵的出料口管道连接于灰尘管道的近锅炉返料器端，第二仓泵的出料口管道连接灰尘管道的远锅炉返料器端；第一仓泵与第二仓泵分别接入压缩气管通入可控压缩空气；第一仓泵出料口管道设有尘泵一台，灰尘管道在第一仓泵出料口管道接入处的两端设控制阀a和控制阀b。
Description
技术领域
[0001] 本实用新型涉及一种锅炉烟尘旋风分离回收利用装置，属于一种环保设备。
背景技术
[0002] 仅设有电袋除尘的循环流化床锅炉烟气处理装置，由于烟气中灰尘浓度大，除尘 过程对电袋除尘器造成的负荷大，故障率高。而且排出的烟气中灰尘浓度也高，不能符合环 保生产要求。
[0003] 循环流化床锅炉烟气浓度大，排出的烟气中含碳量高，说明燃料的燃烧率低，而且 排烟温度低需要通入较多的燃料，能耗高，灰尘在仅仅收集后做其他处理浪费也严重。
发明内容
[0004] 本实用新型的目的是提供一种锅炉烟尘旋风分离回收利用装置及其烟尘回收利 用的方法，解决排出烟尘中国灰尘浓度高的问题，同时提高能源利用率。
[0005] 为实现上述目的，本实用新型采用的技术方案是：
[0006] -种锅炉烟尘旋风分离回收利用装置，带有返料器的锅炉的烟道设有电袋除尘 器，其特征是，锅炉烟道与电袋除尘器间设并列的两旋风分离器，旋风分离器的下料端设第 一下料阀，第一下料阀的下方管道通入第一仓栗中，电袋除尘的下料端设第二下料阀和第 二仓栗，第一仓栗与第二仓栗的出料口管道串联通入灰尘管道，灰尘管道两端分别通入锅 炉的返料器和灰场，第一仓栗的出料口管道连接于灰尘管道的近锅炉返料器端，第二仓栗 的出料口管道连接灰尘管道的远锅炉返料器端;第一仓栗与第二仓栗分别接入压缩气管通 入可控压缩空气;第一仓栗出料口管道设有尘栗一台，灰尘管道在第一仓栗出料口管道接 入处的两端设控制阀a和控制阀b。
[0007] 作为优选，所述锅炉的烟道分别通入两旋风分离器的入口，两旋风分离器的出口 接入同一烟道后通入电袋除尘器。
[0008] 作为优选，所述旋风分离器的直径为3m。
[0009] 作为优选，所述灰尘管道使用耐磨陶瓷管道。
[0010] 利用锅炉烟尘旋风分离回收利用装置进行烟尘回收利用的方法，，包括以下步骤：
[0011] 将锅炉烟道中烟气在电除尘器之前通过旋风分离器进行灰尘分离，烟气中的多数 灰尘经旋风分离器分离后沉淀，含尘量较小的烟气通入电袋除尘器继续处理；
[0012] 上一步骤分离后的灰尘在开启第一下料阀后通过第一下料阀进入第一仓栗中；
[0013] 锅炉需要提高出烟温度时，开启控制阀a，关闭控制阀b，将第一仓栗中灰尘通入压 缩气体后经栗将灰尘输送至锅炉的返料器内，输送至锅炉返料器内的灰尘通入锅炉的炉膛 下部中燃烧；
[0014] 锅炉不需要提高出烟温度时，开启控制阀b，关闭控制阀a，将第一仓栗中灰尘通入 压缩气体后经栗将灰尘输送至灰场。
[0015]本实用新型的优点在于：
[0016] 将旋风分离器收集下来的灰尘通过仓栗输送至返料器下灰管段进入炉膛燃烧室， 降低排烟浓度，减少飞灰含碳量，提高炉膛上部温度，增强吸热力，提高锅炉热效率，提高了 炉膛出口烟气及返料器出口温度。减少了电袋除尘器布袋的磨损，提高了石灰石使用的效 率。
附图说明
[0017] 图1是本实用新型的各部件连接示意图。
[0018] 1、锅炉，2、烟道，3、旋风分离器，4、电袋除尘器，5、烟囱，6、冷气分离器，7、返料器， 8、灰尘管道，9、控制阀a，10、第一下料阀，11、第一仓栗，12、控制阀b，13、压缩气管，14、第二 下料阀，15、第二仓栗。
具体实施方式
[0019] 本实用新型的各部件结构图如图1
[0020] 锅炉烟尘旋风分离回收利用装置，带有返料器的锅炉的烟道设有电袋除尘器，锅 炉烟道与电袋除尘器间设并列的两旋风分离器，旋风分离器的下料端设第一下料阀，第一 下料阀的下方管道通入第一仓栗中，电袋除尘的下料端设第二下料阀和第二仓栗，第一仓 栗与第二仓栗的出料口管道串联通入灰尘管道，灰尘管道两端分别通入锅炉的返料器和灰 场，第一仓栗的出料口管道连接于灰尘管道的近锅炉返料器端，第二仓栗的出料口管道连 接灰尘管道的远锅炉返料器端；第一仓栗与第二仓栗分别接入压缩气管通入可控压缩空 气;第一仓栗出料口管道设有尘栗一台，灰尘管道在第一仓栗出料口管道接入处的两端设 控制阀a和控制阀b。
[0021] 锅炉的烟道分别通入两旋风分离器的入口，两旋风分离器的出口接入同一烟道后 通入电袋除尘器。旋风分离器的直径为3m。灰尘管道使用耐磨陶瓷管道。
[0022] 利用锅炉烟尘旋风分离回收利用装置进行烟尘回收利用的方法，包括以下步骤：
[0023] 将锅炉烟道中烟气在电除尘器之前通过旋风分离器进行灰尘分离，烟气中的多数 灰尘经旋风分离器分离后沉淀，含尘量较小的烟气通入电袋除尘器继续处理；
[0024] 上一步骤分离后的灰尘在开启第一下料阀后通过第一下料阀进入第一仓栗中；
[0025] 锅炉需要提高出烟温度时，开启控制阀a，关闭控制阀b，将第一仓栗中灰尘通入压 缩气体后经栗将灰尘输送至锅炉的返料器内，输送至锅炉返料器内的灰尘通入锅炉的炉膛 下部中燃烧；
[0026] 锅炉不需要提高出烟温度时，开启控制阀b，关闭控制阀a，将第一仓栗中灰尘通入 压缩气体后经栗将灰尘输送至灰场。
[0027]本实用新型的运行工作原理:将旋风分离器收集下来的灰尘通过仓栗输送至返料 器下灰管段进入炉膛燃烧室，灰尘进入炉膛燃烧室后能够有效降低排烟浓度，由于灰尘的 粒径小，在炉膛内能够与氧气充分接触，燃烧充分，有效减少飞灰含碳量，灰尘燃烧能够提 高炉膛上部温度，提高锅炉热效率，同时提高了炉膛出口烟气及返料器出口温度。锅炉的排 灰尘浓度降低，这能够减少电袋除尘器布袋的磨损，提高了石灰石使用的效率。整体上降低 设备的运行成本和燃料消耗。
[0028]以260t/h循环流化床锅炉一台为例，首先在循环流化床锅炉烟气半干法脱硫塔与 电袋除尘器之间增设2台旋风分离器，旋风分离器与返料器下灰管段之间。用耐磨陶瓷管路 连接，所述耐磨陶瓷管路上设有仓栗一台、蝶阀、流量计各一台。旋风分离器收集下来的烟 尘经过耐磨陶瓷管路输送至返料器下灰管进入炉膛下部燃烧。
[0029]本实用新型的实际投资改造费用为20万元。
[0030]改装前后锅炉运行状况的比较分析：
[0032] 从表中可以看出：
[0033] (I )260t/h锅炉改造前后，在同等负荷条件下，蒸汽压力及温度变化不大，均达设 计值，
[0034] (2)炉膛出口烟温提高较多，提高了约80°C，
[0035] (3)返料器温度也相应提高较多，约75°C，这对飞灰含碳量的减少起了很大作用，
[0036] (4)飞灰含碳量由原来的12%减至4%，降低了8%。经测试计算每年可节约原煤5700 吨左右，
[0037] (5)排烟浓度由原来的20mg/m3降至10mg/m3，
[0038] (6)提高了石灰石使用效率，降低了脱硫成本，
[0039]总之，一种循环流化床锅炉新型旋风分离器烟尘回收装置在260t/h循环流化床锅 炉的应用取得了较好的经济效益和社会效益。
Claims (4)
1. 一种锅炉烟尘旋风分离回收利用装置，带有返料器(7)的锅炉（1)的烟道(2)设有电 袋除尘器（4)，其特征是，锅炉（1)的烟道（2)与电袋除尘器（4)间设并列的两旋风分离器 (3 )，旋风分离器(3 )的下料端设第一下料阀（10 )，第一下料阀（10 )的下方管道通入第一仓 栗（11)中，电袋除尘器(7)的下料端设第二下料阀（14)和第二仓栗（15)，第一仓栗（11)与第 二仓栗（15)的出料口管道串联通入灰尘管道(8)，灰尘管道(8)两端分别通入锅炉的返料器 (7) 和灰场，第一仓栗的出料口管道连接于灰尘管道的近锅炉返料器端，第二仓栗（15)的出 料口管道连接灰尘管道(8)的远锅炉返料器(7)端;第一仓栗（11)与第二仓栗（15)分别接入 压缩气管（13)通入可控压缩空气，灰尘管道在第一仓栗出料口管道接入处的两端设控制阀 a(9)和控制阀b(12)。
2. 根据权利要求1所述的锅炉烟尘旋风分离回收利用装置，其特征是，所述锅炉（1)的 烟道(2)分别通入两旋风分离器(3)的入口，两旋风分离器(3)的出口接入同一烟道(2)后通 入电袋除尘器(4)。
3. 根据权利要求1或2所述的锅炉烟尘旋风分离回收利用装置，其特征是，所述旋风分 离器(3)的直径为3m。
4. 根据权利要求1所述的锅炉烟尘旋风分离回收利用装置，其特征是，所述灰尘管道 (8) 使用耐磨陶瓷管道。
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN105485706A (zh) * | 2015-11-20 | 2016-04-13 | 张建存 | 锅炉烟尘旋风分离回收利用装置及其烟尘回收利用的方法 |
| CN105779077A (zh) * | 2016-05-23 | 2016-07-20 | 成都弗吉亚科技有限公司 | 一种燃煤锅炉节煤减排一体式方法 |
| CN107255282A (zh) * | 2017-05-05 | 2017-10-17 | 浙江新都绿色能源有限公司 | 一种垃圾焚烧过程中飞灰的循环利用工艺 |
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| CN105485706A (zh) * | 2015-11-20 | 2016-04-13 | 张建存 | 锅炉烟尘旋风分离回收利用装置及其烟尘回收利用的方法 |
| CN105779077A (zh) * | 2016-05-23 | 2016-07-20 | 成都弗吉亚科技有限公司 | 一种燃煤锅炉节煤减排一体式方法 |
| CN107255282A (zh) * | 2017-05-05 | 2017-10-17 | 浙江新都绿色能源有限公司 | 一种垃圾焚烧过程中飞灰的循环利用工艺 |
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