CN204911100U - 一种水浴除尘脱硫器 - Google Patents
一种水浴除尘脱硫器 Download PDFInfo
- Publication number
- CN204911100U CN204911100U CN201520438251.8U CN201520438251U CN204911100U CN 204911100 U CN204911100 U CN 204911100U CN 201520438251 U CN201520438251 U CN 201520438251U CN 204911100 U CN204911100 U CN 204911100U
- Authority
- CN
- China
- Prior art keywords
- water
- dust
- pipe
- sedimentation basin
- sieve tray
- Prior art date
Links
- 239000011901 water Substances 0.000 title claims abstract description 117
- 238000004062 sedimentation Methods 0.000 claims abstract description 48
- 230000003009 desulfurizing Effects 0.000 claims abstract description 24
- 239000011257 shell materials Substances 0.000 claims abstract description 9
- 239000003513 alkali Substances 0.000 claims abstract description 8
- 239000000428 dust Substances 0.000 claims abstract description 8
- 239000000779 smoke Substances 0.000 claims abstract description 8
- 230000000694 effects Effects 0.000 claims abstract description 7
- 238000005260 corrosion Methods 0.000 claims abstract description 5
- 239000007921 sprays Substances 0.000 claims abstract description 5
- 239000011150 reinforced concrete Substances 0.000 claims abstract description 4
- 239000011499 joint compounds Substances 0.000 claims description 21
- 239000003570 air Substances 0.000 claims description 17
- 239000003500 flue dust Substances 0.000 claims description 16
- 210000000214 Mouth Anatomy 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 5
- 238000005086 pumping Methods 0.000 claims description 5
- 239000002585 bases Substances 0.000 claims description 4
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 4
- 239000000292 calcium oxide Substances 0.000 claims description 4
- 235000012255 calcium oxide Nutrition 0.000 claims description 4
- 229910000118 calcium oxide Inorganic materials 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 4
- 235000017550 sodium carbonate Nutrition 0.000 claims description 4
- 239000011649 sodium carbonate Substances 0.000 claims description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Chemical compound 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[Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 4
- 238000005516 engineering processes Methods 0.000 abstract description 4
- 238000006477 desulfuration reactions Methods 0.000 abstract description 3
- 239000010802 sludge Substances 0.000 abstract 3
- 280000765563 Bamboo companies 0.000 abstract 1
- 235000017166 Bambusa arundinacea Nutrition 0.000 abstract 1
- 240000003917 Bambusa tulda Species 0.000 abstract 1
- 235000017491 Bambusa tulda Nutrition 0.000 abstract 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 abstract 1
- 239000011425 bamboo Substances 0.000 abstract 1
- 239000002184 metals Substances 0.000 abstract 1
- 238000003466 welding Methods 0.000 abstract 1
- 239000007789 gases Substances 0.000 description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound 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[Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000006243 chemical reactions Methods 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 3
- 238000000034 methods Methods 0.000 description 3
- 150000003463 sulfur Chemical group 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 239000002253 acids Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound 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O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxides Inorganic materials 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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Abstract
一种水浴除尘脱硫器，包括：进气管、喷水管、水泵、筛孔板、排气管、外壳、沉淀池、加碱机、溢水管、水泵真空器、清水池、排尘泥绞龙、链斗提升机；其特征是：脱硫器外壳用钢筋砼现浇或不锈钢板焊制而成，下脚与沉淀池相连，沉淀池上有溢水管，出口与清水池相接，清水池上有溢水管，水泵在清水池内的进水管只安装滤网罩不装底阀，上端安装有水泵自吸真空器，并与水泵进水口相连，水泵出水管与喷水管相接；烟尘进气管经顶盖和筛孔板中心串过直扦水位线上，筛孔板焊于进气管上；气水分离器除水后与引风机相连；沉淀池上安装有加碱机；沉淀池底部由排尘泥绞龙和链斗提升机排尘泥，其工艺先进，设备简单，耗电少，除尘脱硫效果好。
Description
一种水浴除尘脱硫器
[0001] 技术领城
[0002] 本实用新型涉及一种水浴除尘脱硫器，属环保除尘设备技术领城。
背景技术
[0003] 沸腾炉及各种热源炉的尾部烟尘排放，是一项力求完善的课题，达标排放是一种目标，烟尘中的含硫和二氧化碳等气体含量非常高，如不进行处理，将对生态环境造成非常严重破坏，并引响人类的生产、生活和身体健康。
发明内容
[0004] 本实用新型要解决的问题是提供一种水浴除尘脱硫器，对沸腾炉及各种热源炉的尾部烟尘进行有效处理。
[0005] 为了解决以上技术问题，本实用新型提供一种水浴除尘脱硫器，包括:烟尘进气管、除尘脱硫器顶盖、喷水管、喷水嘴、水栗出水管、筛孔板、除尘脱硫器排气口、除尘脱硫器外壳、进气管出口、沉淀池、水位线、加碱机、沉淀池溢水管、水栗自吸真空器、水栗、清水池溢流管、排尘泥口、清水池、回水管、气水分离器排气口、低速排尘泥绞龙、低速链斗提升机及链斗提升机电机；其特征是:除尘脱硫器外壳用钢筋砼现浇或不锈钢板焊制而成，下脚与沉淀池相连，沉淀池的水位线上有一根溢水管，出口与清水池相接，清水池的水位线上也有一清水池溢水管，调整水位；水栗的进水管安装有水栗自吸真空器，在清水池内前端安装有滤网罩，不需安装底阀，水栗出水管与水浴除尘脱硫塔上部的喷水管相接，喷水管上安装有喷水嘴，水从喷水嘴喷出，在筛孔板上形成水雾，汽流遇到筛孔板上的水雾，小型尘粒溶入水中流入沉淀池；烟尘进气管从除尘脱硫器顶盖和筛孔板中心串过直扦到沉淀池水位线，烟尘进气管出口与沉淀池水位线相距为“h”，筛孔板使用不锈钢板，上面钻满圆孔，筛孔板焊于进气管上；除尘脱硫器上部安装有排气管，纯净气流径筛孔出去进入气水分离器，所带水滴由于离心力和重力的作用经过回水管流入沉淀池，气流经气水分离器排气口出去与引风机相连；水池上面安装有加碱机，定量定时向水池内加纯碱或生石灰，调整水池内水的酸碱度，并与含硫等气体反应生成钙盐沉淀，沉淀池的尘泥由低速排泥绞龙及电机将尘泥送往低速链斗提升机进料口，由低速链斗提升机将尘泥由排泥口排出沉淀池外，全工作过程闭路遁环，节约水源，不污染环境。
[0006] 筛孔板钻孔直径Φ30_40πιπι，钻孔面积为筛孔板总面积的35_40 %。
[0007] 喷水管上的喷嘴孔直径Φ3_5πιπι。
[0008] “h” =±30mm(水上30_或入水30mm)根据工艺要求调整“h”数值。
[0009] 在沸腾炉及各种热源炉的出口安装除尘脱硫器后有以下进步:1.烟尘由于引风机的吸力，风速加快，进入进气管的烟尘因离心力的作用，突然与水接触，大颗粒沉入沉淀池中。2.向上的气流又遇到从筛孔板向下的水雾将小粒烟尘浸湿，混入水中下降到沉淀池中。3.上升的气流由于受筛孔板的导流，将带尘粒的水流入沉淀池中。4.沸腾炉或热源炉的高温含硫气体遇水会生成弱酸，向水池内加纯碱或生石灰，调整水池内水的酸碱度，并与含硫等气体反应生成钙盐沉淀。5.由于烟尘经过水洗，并经碱水脱硫，排向烟囱的烟气TSP浓度能达标排放。
附图说明
[0010] 下面结合附图对本实用新型作进一步说明。
[0011] 附图1是本实用新型结构示意图。
[0012] 附图2是附图1的A-A剖视图。
[0013] 附图1，2中:1.烟尘进气管，2.除尘脱硫器顶盖，3.喷水管，4.喷水嘴，5.水栗出水管，6.筛孔板，7.排气管，8.除尘脱硫器外壳，9.进气管出口，10.沉淀池，11.水位线，12.加碱机，13.沉淀池溢水管，14.水栗自吸真空器，15.水栗，16.清水池溢流管，17.排尘泥口，18.清水池，19.回水管，20.气水分离器排气口，21.气水分离器，22.低速排泥绞龙及电机，23.低速链斗提升机，24.链斗提升机电机。
具体实施方式
[0014] 下面结合附图和具体实施方式对本实用新型作进一步说明。
[0015] 参照附图1、附图2，除尘脱硫器外壳8用钢筋砼现浇或不锈钢板焊制而成，下脚与沉淀池10相连，沉淀池10的水位线11上有一沉淀池溢水管13，出口与清水池18相接，清水池18的水位线上也有一清水池溢水管16，用来调整水位，水栗15的进水管在清水池18内，进水管上安装有水栗自吸真空器14，水栗能自吸真空，不须要安装底阀，进水管前端安装滤网罩，进水管与水栗15进水口相连，水栗15出水管与除尘脱硫器8上部的喷水管3相接，喷水管3上安装有喷水嘴4 ;烟尘进气管I从除尘脱硫器顶盖2和筛孔板6中心串过直扦到沉淀池10的水位线11上边，烟尘进气管出口 9与沉淀池10水位线11相距为‘h’，筛孔板6上钻满圆孔，焊于进气管I上；除尘脱硫器8上部安装有排气管7向下进入气水分离器21，所带水滴由于离心力和重力的作用经过回水管19流入沉淀池10，气流经气水分离器21排气口 20出去与引风机相连，气水分离器21回水管19与沉淀池10相连；沉淀池10上面安装有加碱机12，定量定时向沉淀池10内加纯碱或生石灰，调整沉淀池10内水的酸碱度，并与含硫等气体反应生成钙盐沉淀，沉淀池10的尘泥由低速排泥绞龙及电机22将尘泥送往低速链斗提升机23进料口，由低速链斗提升机23将尘泥经排泥口 17排出沉淀池10外，全工作程序闭路遁环，节约水源，不污染环境。
[0016] 参照附图1、附图2，工作时沸腾炉及各种热源炉的尾部烟尘由引风机所产生的吸力经水浴除尘脱硫器中间的进气管I快速进入，当气流遇到水位线11的水时，由于惯性力的作用，大颗粒尘粒进入沉淀水中，气流开始上行时，清水池18的清水径水栗15进水管进入自吸真空器14，再进入水栗15，从水栗15出水管5进入喷水管3从喷水嘴4喷出，在筛孔板6上形成水雾，汽流遇到筛孔板6上的水雾，小型尘粒溶入水中流入沉淀池10，纯净气流径筛孔6出去进入排气管7向下进入气水分离器21，所带水滴由于离心力和重力的作用经过回水管19流入沉淀池，气流经气水分离器排气口 20出去进入引风机排向烟囱；沉淀池10的尘泥由低速排泥绞龙及电机22将尘泥送往低速链斗提升机23进料口，由低速链斗提升机23将尘泥经排泥口 17排出沉淀池10外，安装水浴除尘脱硫器对沸腾炉或热源炉的高温含硫含尘气体进行水浴除尘脱硫，其工艺先进，设备简单，耗电少，除尘脱硫效果良好，而且闭路遁环，废水不外排，节约水源，不污染环境，无需专人操作，是值得推广的一种先进的除尘脱硫设备。
Claims (6)
1.一种水浴除尘脱硫器，包括:烟尘进气管、除尘脱硫器顶盖、喷水管、喷水嘴、水栗出水管、筛孔板、除尘脱硫器排气口、除尘脱硫器外壳、进气管出口、沉淀池、水位线、加碱机、沉淀池溢水管、水栗自吸真空器、水栗、清水池溢流管、排尘泥口、清水池、回水管、气水分离器排气口、气水分离器、低速排尘泥绞龙、低速链斗提升机、链斗提升机电机；其特征是:除尘脱硫器外壳用钢筋砼现浇或不锈钢板焊制而成，下脚与沉淀池相连，沉淀池的水位线上有溢水管，出口与清水池相接，清水池的水位线上也有溢水管，调整水位，清水池内水栗进水管安装有滤网罩，并与水栗进水口相连，水栗出水管与水浴除尘脱硫器上部的喷水管相接，喷水管上有喷水嘴，水从喷水嘴喷出，在筛孔板上形成水雾，汽流遇到筛孔板上的水雾，小型尘粒溶入水中流入沉淀池；烟尘进气管从除尘脱硫器顶盖和筛孔板中心串过直扦到沉淀池水位线上；筛孔板上钻满圆孔，焊于进气管上；除尘脱硫器外壳上部安装有排气管进入气水分离器，所带水滴由于离心力和重力的作用经过回水管流入沉淀池，气流经过气水分离器排气口出去与引风机相连；沉淀池底部的尘泥由低速排泥绞龙及电机将尘泥送往低速链斗提升机进料口，由低速链斗提升机将尘泥经排泥口排出沉淀池外。
2.根据权利要求1所述的一种水浴除尘脱硫器，其特征是:水栗进水口上端安装有水栗自吸真空器，进水管前端只安装滤网罩，不须要安装底阀。
3.根据权利要求1所述的一种水浴除尘脱硫器，其特征是:喷水管上安装有喷水嘴，喷水嘴直径0 3-4mm。
4.根据权利要求1所述的一种水浴除尘脱硫器，其特征是:烟尘进气管出口与沉淀池水位线相距为h，h=±30mm，设水位线为O，按工艺要求调整h数值。
5.根据权利要求1所述的一种水浴除尘脱硫器，其特征是:筛孔板上钻满直径为0 30-40mm的圆孔，钻孔面积为筛孔板总面积的35-40 %。
6.根据权利要求1所述的一种水浴除尘脱硫器，其特征是:沉淀池上面安装有加碱机，按工艺要求定量定时向沉淀池内加纯碱或生石灰，调整沉淀池内水的酸碱度。
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105920962A (zh) * | 2016-06-18 | 2016-09-07 | 澧县方石坪镇杨朴矿山机械厂 | 一种烟囱下脚水浴除尘脱硫方法 |
| CN106377960A (zh) * | 2016-11-14 | 2017-02-08 | 杨朴 | 一种稻壳锅炉水浴除尘塔 |
| CN106492610A (zh) * | 2016-11-20 | 2017-03-15 | 杨朴 | 一种水浴除尘脱硫及尘泥处理方法 |
| CN109260932A (zh) * | 2018-11-08 | 2019-01-25 | 澧县金辉石膏制品有限责任公司 | Stainless steel alkaline water dust removal and desulfurization tower |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105920962A (zh) * | 2016-06-18 | 2016-09-07 | 澧县方石坪镇杨朴矿山机械厂 | 一种烟囱下脚水浴除尘脱硫方法 |
| CN105920962B (zh) * | 2016-06-18 | 2018-08-24 | 澧县方石坪镇杨朴矿山机械厂 | 一种烟囱下脚水浴除尘脱硫方法 |
| CN106377960A (zh) * | 2016-11-14 | 2017-02-08 | 杨朴 | 一种稻壳锅炉水浴除尘塔 |
| CN106492610A (zh) * | 2016-11-20 | 2017-03-15 | 杨朴 | 一种水浴除尘脱硫及尘泥处理方法 |
| CN109260932A (zh) * | 2018-11-08 | 2019-01-25 | 澧县金辉石膏制品有限责任公司 | Stainless steel alkaline water dust removal and desulfurization tower |
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