CN116809235A - System and method for purifying and circulating acid-making flue gas - Google Patents
System and method for purifying and circulating acid-making flue gas Download PDFInfo
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Abstract
本发明公开了一种制酸烟气净化循环系统及净化方法,其中循环系统包括:电除雾器、二级动力波、一级动力波、气体冷却塔、事故水高位槽以及溢流堰,电除雾器的出液口与二级动力波的进液口相连通;二级动力波的出液口与一级动力波进液口相连通;气体冷却塔的进气口与一级动力波相连通;气体冷却塔的出液口与事故水高位槽的进液口相连通;事故水高位槽的出液口与溢流堰的进液口相连通,溢流堰的出液口与一级动力波的进液口相连通。本发明中的净化循环系统可以减小循环液含尘量,提高生产效率。
The invention discloses an acid-making flue gas purification circulation system and a purification method. The circulation system includes: an electric demister, a second-level power wave, a first-level power wave, a gas cooling tower, an accident water high-level tank and an overflow weir. The liquid outlet of the electric demister is connected to the liquid inlet of the secondary power wave; the liquid outlet of the secondary power wave is connected to the liquid inlet of the primary power wave; the air inlet of the gas cooling tower is connected to the primary power wave. The waves are connected; the liquid outlet of the gas cooling tower is connected with the liquid inlet of the accident water high-level tank; the liquid outlet of the accident water high-level tank is connected with the liquid inlet of the overflow weir, and the liquid outlet of the overflow weir is connected with the liquid inlet of the overflow weir. The liquid inlets of the first-level power wave are connected. The purification circulation system in the present invention can reduce the dust content of the circulating liquid and improve production efficiency.
Description
技术领域Technical field
本发明涉及除尘技术领域,更具体的说是涉及一种制酸烟气净化循环系统及净化方法。The present invention relates to the technical field of dust removal, and more specifically to an acid-making flue gas purification circulation system and a purification method.
背景技术Background technique
现工业制取硫酸过程中,烟气净化方式很多采取稀酸循环酸洗的形式。此酸洗方式具有适应性强、操作方便、技术可靠、可调整污酸排放量;烟气净化效果指标稳定。一般采用的工艺流程是:一级动力波—气体冷气塔—二级动力波—两级电除雾器的净化方式除去烟气中尘、杂质、酸雾、热量等。因为烟气温度较高,净化段基本都会设置一个高位槽装满清水或循环稀酸,在一级动力波循环泵跳停的情况下,高位槽中的液体可用于保护烟气管道,但事故水高位槽使用一级动力波循环液时,由于一级动力波循环液含尘较大而堵塞事故水管道,可造成烟气管道损坏。In the current industrial production of sulfuric acid, many flue gas purification methods take the form of dilute acid cycle pickling. This pickling method has strong adaptability, easy operation, reliable technology, adjustable acid emission, and stable flue gas purification effect indicators. The generally used process flow is: first-level power wave - gas cooling tower - second-level power wave - two-stage electric demister purification method to remove dust, impurities, acid mist, heat, etc. in the flue gas. Because the flue gas temperature is high, a high-level tank is basically set up in the purification section to be filled with clean water or circulating dilute acid. When the first-level power wave circulation pump stops, the liquid in the high-level tank can be used to protect the flue gas pipeline, but the accident When the water high-level tank uses first-level dynamic wave circulating fluid, the first-level dynamic wave circulating fluid contains large dust and blocks the accident water pipe, which may cause damage to the flue gas pipeline.
因此,研究出一种可以减小循环液含尘量,提高生产效率的制酸烟气净化循环系统及净化方法是本领域技术人员亟需解决的问题。Therefore, developing an acid-making flue gas purification circulation system and purification method that can reduce the dust content of the circulating liquid and improve production efficiency is an urgent problem that those skilled in the art need to solve.
发明内容Contents of the invention
有鉴于此,本发明提供了一种可以减小循环液含尘量,提高生产效率的制酸烟气净化循环系统及净化方法。In view of this, the present invention provides an acid-making flue gas purification circulation system and a purification method that can reduce the dust content of the circulating liquid and improve production efficiency.
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above objects, the present invention adopts the following technical solutions:
一种制酸烟气净化循环系统,包括:An acid-making flue gas purification cycle system, including:
电除雾器,electric defogger,
二级动力波,所述电除雾器的出液口与二级动力波的进液口相连通;Secondary power wave, the liquid outlet of the electric demister is connected with the liquid inlet of the secondary power wave;
一级动力波,所述二级动力波的出液口与一级动力波进液口相连通;A first-level power wave, the liquid outlet of the second-level power wave is connected with the liquid inlet of the first-level power wave;
气体冷却塔,所述气体冷却塔的进气口与一级动力波相连通;A gas cooling tower, the air inlet of the gas cooling tower is connected with the first-level power wave;
事故水高位槽,所述气体冷却塔的出液口与事故水高位槽的进液口相连通;A high-level accident water tank, the liquid outlet of the gas cooling tower is connected with the liquid inlet of the high-level accident water tank;
溢流堰,所述事故水高位槽的出液口与溢流堰的进液口相连通,所述溢流堰的出液口与一级动力波的进液口相连通。Overflow weir, the liquid outlet of the accident water high-level tank is connected with the liquid inlet of the overflow weir, and the liquid outlet of the overflow weir is connected with the liquid inlet of the primary power wave.
采用上述技术方案的有益效果是,本发明中气体冷却塔内的循环液含尘量很少,将气体冷却塔内的循环液补入到事故水高位槽内,可以避免堵塞事故水高位槽,可以提高生产效率。The beneficial effect of adopting the above technical solution is that the circulating liquid in the gas cooling tower of the present invention contains very little dust. The circulating liquid in the gas cooling tower is replenished into the accident water high-level tank, which can avoid clogging the accident water high-level tank. Can improve production efficiency.
优选的,所述二级动力波的进液口与新水补入管路相连通。在二级动力波内的循环液不足时,可以通过新水补入管路向二级动力波内补入新水。Preferably, the liquid inlet of the secondary power wave is connected to the new water supply pipeline. When the circulating fluid in the secondary power wave is insufficient, new water can be replenished into the secondary power wave through the new water supply pipeline.
优选的,所述一级动力波的出液口连接有圆锥沉降槽。一级动力波内多余的水分可以排入到圆锥沉降槽内。Preferably, the liquid outlet of the first-stage power wave is connected to a conical settling tank. Excess water in the first-level dynamic wave can be discharged into the conical settling tank.
优选的,所述圆锥沉降槽的出液口连接有稀酸槽。Preferably, the liquid outlet of the conical settling tank is connected to a dilute acid tank.
优选的,所述稀酸槽的出液口连接有污酸处理池。Preferably, the liquid outlet of the dilute acid tank is connected to a waste acid treatment tank.
一种制酸烟气净化循环系统的净化方法,包括如下净化步骤:A purification method for an acid-making flue gas purification cycle system, including the following purification steps:
1)将电除雾器收集的烟气中的酸雾及部分水分,经管道流入二级动力波内,当二级动力波液位高于1.8m时,开启串酸阀门,将多余的循环液输送至一级动力波内;1) The acid mist and part of the moisture in the flue gas collected by the electric demister flow into the secondary power wave through the pipeline. When the liquid level of the secondary power wave is higher than 1.8m, open the acid string valve to circulate the excess The liquid is transported into the first-level power wave;
2)因一级动力波作用是绝热降温,大量的水汽由烟气带入到气体冷却塔内,使气体冷却塔内的液位增高,气体冷却塔内液位增高后,会将循环液输送到事故水高位槽内;2) Because the first-level dynamic wave acts as adiabatic cooling, a large amount of water vapor is brought into the gas cooling tower from the flue gas, which increases the liquid level in the gas cooling tower. After the liquid level in the gas cooling tower increases, the circulating liquid will be transported Go to the accident water high-level tank;
3)打开事故水高位槽出液口的调节阀门,事故水高位槽内的循环液会流入到溢流堰内,溢流堰内的水会进入到一级动力波内,形成一个循环;3) Open the regulating valve at the liquid outlet of the accident water high-level tank. The circulating liquid in the accident water high-level tank will flow into the overflow weir, and the water in the overflow weir will enter the first-level dynamic wave to form a cycle;
4)在循环过程中一级动力波产生的多余水分会进入到圆锥沉降槽内,圆锥沉降槽的液体溢流进入到稀酸槽内,然后在由泵输送到污酸处理池内进行处理。4) During the circulation process, the excess water generated by the first-level dynamic wave will enter the conical settling tank, and the liquid overflow from the conical settling tank will enter the dilute acid tank, and then be transported by the pump to the sewage acid treatment tank for treatment.
优选的,所述一级动力波和二级动力波的液位为1-1.8mm。Preferably, the liquid levels of the first-stage power wave and the second-stage power wave are 1-1.8 mm.
优选的,所述气体冷却塔的液位为1-2mm;所述事故水高位槽的液位为1.5-2m。Preferably, the liquid level of the gas cooling tower is 1-2mm; the liquid level of the accident water high-level tank is 1.5-2m.
经由上述的技术方案可知,与现有技术相比,本发明公开提供了一种一种制酸烟气净化循环系统及净化方法,其有益效果为:It can be seen from the above technical solutions that compared with the existing technology, the present invention provides an acid-making flue gas purification circulation system and a purification method, and its beneficial effects are:
(1)本发明中根据净化各槽的循环液中含尘量最小的气体冷却塔内的循环液做为事故水高位槽的补水,避免了堵塞事故水高位槽,提高生产效率;(1) In the present invention, the circulating liquid in the gas cooling tower with the smallest dust content in the circulating liquid of each tank is used as the water supply for the accident water high-level tank, which avoids clogging the accident water high-level tank and improves production efficiency;
(2)本发明中的循环系统适应性强、操作简单、操作费用低,整体循环液串酸更加流畅。(2) The circulation system in the present invention has strong adaptability, simple operation, low operating cost, and the overall circulating liquid acid flow is smoother.
附图说明Description of the drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description are only These are embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on the provided drawings without exerting creative efforts.
图1为本发明提供的净化循环系统的结构示意图。Figure 1 is a schematic structural diagram of the purification circulation system provided by the present invention.
其中,图中,Among them, in the figure,
1-电除雾器;2-二级动力波;3-一级动力波;4-气体冷却塔;5-事故水高位槽;6-溢流堰;7-新水补入管路;8-圆锥沉降槽;9-稀酸槽;10-污酸处理池。1-Electric demister; 2-Second-level power wave; 3-First-level power wave; 4-Gas cooling tower; 5-Accident water high-level tank; 6-Overflow weir; 7-New water supply pipeline; 8- Conical settling tank; 9-dilute acid tank; 10-sewage acid treatment tank.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
本发明实施例公开了一种制酸烟气净化循环系统,包括:The embodiment of the present invention discloses an acid-making flue gas purification circulation system, which includes:
电除雾器1,Electric defogger 1,
二级动力波2,电除雾器1的出液口与二级动力波2的进液口相连通;Secondary power wave 2, the liquid outlet of the electric demister 1 is connected with the liquid inlet of the secondary power wave 2;
一级动力波3,二级动力波2的出液口与一级动力波3进液口相连通;The liquid outlet of the first-level power wave 3 and the second-level power wave 2 is connected with the liquid inlet of the first-level power wave 3;
气体冷却塔4,气体冷却塔4的进气口与一级动力波3相连通;Gas cooling tower 4, the air inlet of the gas cooling tower 4 is connected with the first-level power wave 3;
事故水高位槽5,气体冷却塔4的出液口与事故水高位槽5的进液口相连通;The accident water high-level tank 5, the liquid outlet of the gas cooling tower 4 is connected with the liquid inlet of the accident water high-level tank 5;
溢流堰6,事故水高位槽5的出液口与溢流堰6的进液口相连通,溢流堰6的出液口与一级动力波3的进液口相连通。循环酸液由电除雾器1进入二级动力波2,在二级动力波2循环液不足时,可进行补入新水,然后直接进入一级动力波3,气体冷却塔4循环液进入事故水高位槽5,流经溢流堰6后进入一级动力波3,一级动力波3循环液进入圆锥沉降槽8后,溢流进入稀酸槽9,进行污酸处理,形成一种循环液新的循环系统。The overflow weir 6, the liquid outlet of the accident water high level tank 5 is connected with the liquid inlet of the overflow weir 6, and the liquid outlet of the overflow weir 6 is connected with the liquid inlet of the primary power wave 3. The circulating acid liquid enters the second-level power wave 2 from the electric demister 1. When the circulating liquid of the second-level power wave 2 is insufficient, new water can be added, and then directly enters the first-level power wave 3, and the circulating liquid of the gas cooling tower 4 enters The accident water high-level tank 5 flows through the overflow weir 6 and enters the first-level power wave 3. After the circulating liquid of the first-level power wave 3 enters the conical settling tank 8, it overflows into the dilute acid tank 9 for waste acid treatment, forming a New circulation system for circulating fluid.
为了进一步地优化上述技术方案,二级动力波2的进液口与新水补入管路7相连通。In order to further optimize the above technical solution, the liquid inlet of the secondary power wave 2 is connected with the new water supply pipeline 7 .
为了进一步地优化上述技术方案,一级动力波3的出液口连接有圆锥沉降槽8。一级动力波3排出多余的水分进入圆锥沉降槽8,溢流后进入稀酸槽9,由泵打至污酸处理进行处理。In order to further optimize the above technical solution, the liquid outlet of the primary power wave 3 is connected to a conical settling tank 8 . The first-level power wave 3 discharges excess water into the conical settling tank 8. After overflow, it enters the dilute acid tank 9 and is pumped to the waste acid treatment for treatment.
为了进一步地优化上述技术方案,圆锥沉降槽8的出液口连接有稀酸槽9。In order to further optimize the above technical solution, the liquid outlet of the conical settling tank 8 is connected to a dilute acid tank 9 .
为了进一步地优化上述技术方案,稀酸槽9的出液口连接有污酸处理池10。In order to further optimize the above technical solution, the liquid outlet of the dilute acid tank 9 is connected to a sewage acid treatment tank 10 .
一种制酸烟气净化循环系统的净化方法,包括如下净化步骤:A purification method for an acid-making flue gas purification cycle system, including the following purification steps:
1)将电除雾器1收集的烟气中的酸雾及部分水分,经管道流入二级动力波2内,当二级动力波2液位高于1.8m时,开启串酸阀门,将多余的循环液输送至一级动力波3内;1) The acid mist and part of the moisture in the flue gas collected by the electric demister 1 flow into the secondary power wave 2 through the pipeline. When the liquid level of the secondary power wave 2 is higher than 1.8m, open the acid string valve and The excess circulating fluid is transported to the first-level power wave 3;
2)因一级动力波3作用是绝热降温,大量的水汽由烟气带入到气体冷却塔4内,使气体冷却塔4内的液位增高,气体冷却塔4内液位增高后,会将循环液输送到事故水高位槽5内;2) Since the function of the primary dynamic wave 3 is adiabatic cooling, a large amount of water vapor is brought into the gas cooling tower 4 by the flue gas, causing the liquid level in the gas cooling tower 4 to increase. After the liquid level in the gas cooling tower 4 increases, it will Transport the circulating fluid to the accident water high-level tank 5;
3)打开事故水高位槽5出液口的调节阀门,事故水高位槽5内的循环液会流入到溢流堰6内,溢流堰6内的水会进入到一级动力波3内,形成一个循环;3) Open the regulating valve at the liquid outlet of the accident water high-level tank 5. The circulating liquid in the accident water high-level tank 5 will flow into the overflow weir 6, and the water in the overflow weir 6 will enter the first-level dynamic wave 3. form a cycle;
4)在循环过程中一级动力波3产生的多余水分会进入到圆锥沉降槽8内,圆锥沉降槽8的液体溢流进入到稀酸槽9内,然后在由泵输送到污酸处理池10内进行处理。4) During the circulation process, the excess water generated by the first-level dynamic wave 3 will enter the conical settling tank 8. The liquid overflow from the conical settling tank 8 will enter the dilute acid tank 9, and then be transported to the sewage acid treatment tank by the pump. Processed within 10 days.
为了进一步地优化上述技术方案,图1中的箭头所指示的是循环液的流动方向,一级动力波3的烟气不会携带灰尘,一级动力波3内的烟气进入到气体冷却塔4内,不会有灰尘进入到气体冷却塔4内。In order to further optimize the above technical solution, the arrow in Figure 1 indicates the flow direction of the circulating liquid. The flue gas in the first-level power wave 3 will not carry dust. The flue gas in the first-level power wave 3 enters the gas cooling tower. 4, no dust will enter the gas cooling tower 4.
为了进一步地优化上述技术方案,因净化工段属于半绝热降温,一级动力波3损失水量最多,而气体冷却塔4是收集水量最多,因此气体冷却塔4无需加新水来维持液位。In order to further optimize the above technical solution, since the purification section is a semi-adiabatic cooling, the first-level power wave 3 loses the most water, while the gas cooling tower 4 collects the most water, so the gas cooling tower 4 does not need to add new water to maintain the liquid level.
为了进一步地优化上述技术方案,一级动力波3和二级动力波2的液位为1-1.8mm。In order to further optimize the above technical solution, the liquid levels of the first-level power wave 3 and the second-level power wave 2 are 1-1.8mm.
为了进一步地优化上述技术方案,气体冷却塔4的液位为1-2mm;事故水高位槽5的液位为1.5-2m。In order to further optimize the above technical solution, the liquid level of the gas cooling tower 4 is 1-2mm; the liquid level of the accident water high-level tank 5 is 1.5-2m.
本说明书中各个实施例采用递进的方式描述,每个实施例重点说明的都是与其他实施例的不同之处,各个实施例之间相同相似部分互相参见即可。Each embodiment in this specification is described in a progressive manner. Each embodiment focuses on its differences from other embodiments. The same and similar parts between the various embodiments can be referred to each other.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments enables those skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be practiced in other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202310321176.6A CN116809235A (en) | 2023-03-29 | 2023-03-29 | System and method for purifying and circulating acid-making flue gas |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202590565U (en) * | 2012-05-10 | 2012-12-12 | 阳谷祥光铜业有限公司 | Purifying equipment for acid making with flue gas |
CN109731424A (en) * | 2019-01-28 | 2019-05-10 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | overflow weir system |
CN112774386A (en) * | 2021-01-20 | 2021-05-11 | 中国瑞林工程技术股份有限公司 | Complex flue gas treatment system |
CN219377505U (en) * | 2023-03-29 | 2023-07-21 | 呼伦贝尔驰宏矿业有限公司 | System for purifying and circulating acid-making flue gas |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202590565U (en) * | 2012-05-10 | 2012-12-12 | 阳谷祥光铜业有限公司 | Purifying equipment for acid making with flue gas |
CN109731424A (en) * | 2019-01-28 | 2019-05-10 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | overflow weir system |
CN112774386A (en) * | 2021-01-20 | 2021-05-11 | 中国瑞林工程技术股份有限公司 | Complex flue gas treatment system |
CN219377505U (en) * | 2023-03-29 | 2023-07-21 | 呼伦贝尔驰宏矿业有限公司 | System for purifying and circulating acid-making flue gas |
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