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一、概述=
span>
针对发展中国家=
投入到烟气脱硫的资=
7329;不多,特别是面广ດ=
7;大的中小型锅炉用户&=
#65292;对排
烟脱=
硫费用承受能力有限=
5292;又不便于集中统一=
9;理实际情况,开发一&=
#31181;投资省,运行费用=
302;,
便于=
维护,适合我国国情=
0340;除尘脱硫装置,即ߌ=
8;台设备同时除尘又脱&=
#30827;,从而降低系统的=
237;
资费=
用和占地面积。对此=
1407;则是:首先要求主߮=
7;设备“低阻高效”。=
2312;不增加动力的前提ߍ=
9;,
对细=
微尘粒有较高的扑集=
5928;率和较强的脱硫功೦=
1;;其次是采用来源广&=
#20215;格低廉的脱硫剂,=
253;
括可=
利用的碱性废渣、废=
7700;,从而降低运行费ஷ=
2;。
我厂研制成功的=
SC型系列高效脱硫=
除尘器,集中了我国=
0446;前各厂家生产的旋ཇ=
8;,水膜,
等各=
类除尘器之优点,加=
0197;改进的更新换代的ਫ=
2;产品。克服了大型的&=
#38500;尘设备装置及庞大=
340;
管道=
系统,运行阻力大等=
2570;点。因闭路循环用=
0;,加上二氧化硫中和&=
#21058;,还可达到除去部=
998;
S02的目的。=
35813;系列除尘器具有除ë=
76;效率高,一次性投资=
少,造型美观、结构=
2039;凑、占地面
积小=
、节水效果明显(比一般除尘器低=
40%左右),使=
用易操作,维修方便=
1561;特点。是冶金、
建材=
、矿山、机械各种窑=
8809;、锅炉,尤其是生૬=
3;锅炉等区域性的消烟&=
#38500;尘,防止污染,净=
270;
环境=
的理想设备。
二、主要=
25216;术指标
|
型号规格=
|
进口风速=
(米/秒)
|
处理风量=
(米3/时)
|
阻力(MPa)=
|
耗水量(=
吨)
|
效率%
|
外形尺寸=
mm
|
重量(公=
斤)
|
|
SC-1
|
18
|
5000
|
0.15
|
0.16
|
98
|
φ1270
|
|
|
SC-2
|
18
|
10000
|
0.15
|
0.23
|
98
|
φ1500
|
|
|
SC-3
|
18
|
15000
|
0.15
|
0.33
|
98
|
φ1800
|
|
|
SC-4
|
18
|
20000
|
0.15
|
0.46
|
98
|
φ2200
|
|
|
SC-5
|
18
|
25000
|
0A=
294;15
|
0A=
294;52
|
98
|
φ2500
|
|
|
SC-6
|
18
|
30000
|
0A=
294;15
|
0A=
294;56
|
98
|
φ2800
|
|
&nb=
sp;
该产品显=
33879;特点能适应于锅炉z=
89;窑炉的负荷变化大,=
使用煤的品种广等优=
8857;。
三、基本=
24037;作原理
湿法除尘=
26159;人为地往除尘器内ę=
55;加各种各样的,填充=
材料接触表面,以形=
5104;更多的液膜。
拉希=
格环是空心圆柱体,=
0854;外径等于其高度。ߌ=
8;般,在浸湿的填料中&=
#28082;体和气体是平行运=
160;
的。=
气流的方向主要是平=
4892;于液膜的表面,当=
8;体和液体从一个拉希&=
#26684;环到另一个环时,=
165;
有少=
数的中断现象发生。=
7668;流垂直于液流现象࠰=
0;乎观察不到。气体和&=
#28082;体的运动,是顺向=
320;
通过=
填料塔。在顺向流动=
0340;情况中,流动方向ࡨ=
1;上。当湿式填料除尘&=
#22120;在泛流情况下工作=
102;,
除尘=
效率能得到改善。液=
0307;向上升的气流所阻ఎ=
1;。在填料内部两种相&=
#24577;进行强烈的混合, =
780;
尘粒=
和液体界面之间的相=
3545;速度是很小的。这स=
1;是为什么在多数情况&=
#19979;,尘粒的收集在填=
009;
表面=
上,除尘器进一步改=
6827;除尘效率可用紧密=
6;靠的平行管束。管束&=
#24067;置在任意填料或其=
182;
填料=
组件的顶部。气体和=
8082;体呈同向运动。气߮=
7;和流体迫使产生独特&=
#30340;柱形气泡和液膜。$=
825;
些气=
泡被压差推动通过管=
6463;,气体和液体之间=
0;相对速度对提高除尘&=
#25928;率是有利的 锅炉含尘
气体=
切线进入除尘器,首=
0808;进行高速旋转,由ߛ=
0;离心力的作用,达到&=
#38500;去大颗粒粉尘的目=
340;。
然后=
,烟气进入雾化区,=
2463;分级雾化处理,小ག=
3;粒的粉尘受水雾的粘&=
#28382;作用,吸水增重下=
785;,
加上=
重力的作用,沿筒壁=
8543;壁面水膜流入集尘ૠ=
4;水孔。
SC型除尘脱硫装置=
其主体设备 为一立式塔,塔ࠦ=
9;兼用了干、湿结合的&=
#32467;构型式,下部
为湿=
式除尘段,中部装有=
3073;水板,是脱水设有༊=
0;雾装置。湿式除尘器&=
#36890;常由两个过程来完=
104;,
第一=
个过程是由洗涤来捕=
8598;尘粒,第二个过程=
9;除掉捕集了尘粒的液&=
#28404;和混有二次飞扬尘=
890;
的液=
体。除了特别的场合=
5292;这些液滴的大小一ഄ=
4;在数十微米以上。去&=
#38500;这些液滴不像去掉 =
454;
小粉=
尘那样困难。捕集以=
9979;微细水雾可像捕集ࢰ=
2;体粒子那样来处理。&=
#38500;去较大的液滴并非$=
731;
而易=
举的过程。把液滴分=
1163;装置附属并归入湿ঁ=
5;收尘装置内进行了分&=
#31867;。液滴与固体粒子=
981;
同,=
由于在捕集后相互聚=
8598;并汇成液体流而被࠳=
8;离,因此,在多数场&=
#21512;反而比固体。
粒子容易=
22788;理。由于接触角小ñ=
82;且润湿性较好的液体=
,滞留在充填层内的=
8082;体增多,从
而妨=
碍气体通过并增大压=
1147;损失,故不能使用ࠠ=
5;填率太大的脱水装置&=
#12290;
干式除尘=
27573;的主要作用是除去Ɔ=
63;粒较大的粉尘。筛板=
上布吸收液,在烟气=
0340;冲击作用下
呈沸=
腾状,其主要作用是=
3073;除SO2和除去微=
32454;粉尘。脱水装置的È=
27;要作用是脱水,防止=
烟气
带水=
。除雾器的作用是防=
7490;烟气中蒸汽凝成的=
0;珠被带出。塔体为普&=
#36890;钢板制成,内衬防!=
104;、
耐磨=
、耐热材料。为主体=
5774;备配套的辅助设备ࡍ=
3;括循环池、再生罐等&=
#12290;
由于采用=
20102;干湿相结合的结构à=
11;式,大部分粉尘被高=
速旋转预先除去,因=
2780;筛板上粉尘
的负=
荷较小,循环池中沉=
8195;量也相应减少。特࠷=
5;适用于6t/h以下小型层燃炉=
配套使用。
除尘脱硫=
24037;艺流程:含法烟气Ĭ=
01;塔的中部进入干式除=
尘段,除去大部分粉=
3576;的烟气由中
间芯=
管上升到筛板段,在=
1579;板段除去微细粉尘ࡴ=
4;SO3。循环池=
20013;的沉淀物定时清除z=
90;其适用
于碱=
性、双碱法及液相催=
1270;氧化法脱硫。影响༊=
0;尘脱硫效率的主要因&=
#32032;包括空塔速度、吸=
910;
液的=
PH值、液气比等。=
空塔速度是在设计时=
0830;定的,液气比、吸ਟ=
0;液的PH值等则是根据实=
际需=
要在设备运行中加以=
5511;制的。
四、安装=
26041;法
1<=
/span>、除尘安=
35013;时(见安装图另附<=
span
lang=3DEN-US style=3D'font-size:12.0pt'>),泄水孔的高低=
因场地而宜。
=
o:p>
五、注意=
20107;项及维修
1=
、除尘器=
20999;勿在无水状态下运Ŝ=
92;。&n=
bsp;
2、使=
用前沉淀池要保证水=
0301;
3=
、在烟气=
36827;入除尘器之前,雾Ô=
70;装置必须开启。&n=
bsp;
4、定=
期清除沉淀池中的污=
7877;。
5=
、为了防=
27490;污水的污染,主要į=
40;是控制用水量、减少=
排放,并尽可能合理=
2320;循环使
用。=
但这些仍不能完全控=
1046;污染,为此要对污=
0;进行处理和回收利用&=
#12290;
6=
、要除去=
span>SO2要在池中=
32463;常放些生石灰。
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