CN1180995C - Treatment method of high concentration sulfur dioxide waste liquid - Google Patents
Treatment method of high concentration sulfur dioxide waste liquid Download PDFInfo
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- CN1180995C CN1180995C CNB031265944A CN03126594A CN1180995C CN 1180995 C CN1180995 C CN 1180995C CN B031265944 A CNB031265944 A CN B031265944A CN 03126594 A CN03126594 A CN 03126594A CN 1180995 C CN1180995 C CN 1180995C
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Abstract
Description
技术领域technical field
本发明涉及一种工业废水处理技术,更具体地说,它涉及一种高浓度二氧化硫废液处理方法。The invention relates to a technology for treating industrial waste water, more specifically, it relates to a method for treating high-concentration sulfur dioxide waste liquid.
背景技术Background technique
工业上,高浓度二氧化硫废液来自对原料气二氧化硫的水洗净化;目前,国内外对其处理多采用脱洗塔,回收二氧化硫循环使用,余下污水送污水处理厂处理或再处理。这种方式投资大,耗能高,一般中、小型生产厂难以承受。因此,国内一些中、小型生产厂家,往往是未加处理,便直接将高浓度二氧化硫废液排入江、河、湖、海,给环境造成了严重污染。高浓度二氧化硫废液为强酸的浓溶液,直接与碱氢氧化钠溶液或石灰水反应将造成严重的二次污染,一方面是反应太剧烈,难于控制,且要放出大量的热;另一方面高浓度二氧化硫废液很不稳定,受热将大量挥发到空气中。若将高浓度二氧化硫废液直接与颗粒状大理石或石灰石反应,反应很难进行到底,原料利用率不高,且仍然有大量的二氧化硫气体放出,也将造成严重的二次污染。Industrially, high-concentration sulfur dioxide waste liquid comes from the water washing and purification of raw material gas sulfur dioxide; at present, stripping towers are mostly used at home and abroad to recover sulfur dioxide for recycling, and the remaining sewage is sent to sewage treatment plants for treatment or reprocessing. This method requires large investment and high energy consumption, which is unbearable for general medium and small production plants. Therefore, some domestic small and medium-sized manufacturers often directly discharge high-concentration sulfur dioxide waste liquid into rivers, rivers, lakes, and seas without any treatment, causing serious pollution to the environment. High-concentration sulfur dioxide waste liquid is a concentrated solution of strong acid, which will cause serious secondary pollution if it directly reacts with alkali sodium hydroxide solution or lime water. High-concentration sulfur dioxide waste liquid is very unstable, and will volatilize in large quantities into the air when heated. If the high-concentration sulfur dioxide waste liquid is directly reacted with granular marble or limestone, it will be difficult to carry out the reaction to the end, the utilization rate of raw materials is not high, and there will still be a large amount of sulfur dioxide gas released, which will also cause serious secondary pollution.
发明内容Contents of the invention
本发明的目的在于提供一种能让高浓度二氧化硫废液与大理石或石灰石能温和地、完全的反应;不向环境放出二氧化硫气体,不会造成二次污染,且能将其废渣转化成石膏的一种高浓度二氧化硫废液处理方法。The purpose of the present invention is to provide a kind of can make high-concentration sulfur dioxide waste liquid and marble or limestone can react mildly and completely; do not release sulfur dioxide gas to the environment, will not cause secondary pollution, and can convert its waste slag into gypsum A method for treating high-concentration sulfur dioxide waste liquid.
本发明的目的是通过下述的技术方案予以实现。The purpose of the present invention is to be achieved through the following technical solutions.
本发明的高浓度二氧化硫废液处理方法,依次包括以下步骤:The high-concentration sulfur dioxide waste liquid treatment method of the present invention comprises the following steps successively:
(a).将大理石或石灰石的其中一种,粉碎成200目以上的粉末;(a). One of marble or limestone is crushed into a powder of more than 200 mesh;
(b).在反应池中将上述的粉末与水按1∶5的重量比制成料浆;(b). In the reaction tank, the above-mentioned powder and water are made into a slurry in a weight ratio of 1:5;
(c).在搅拌下,按粉末∶废液重量1∶1的比例,从反应池的中下部用多孔注入高浓度二氧化硫废液;(c). Under stirring, according to the ratio of powder: waste liquid weight 1: 1, inject high-concentration sulfur dioxide waste liquid from the middle and lower part of the reaction tank with holes;
(d).加完废液后,继续搅拌反应至pH值变至6.4,通入空气将亚硫酸钙氧化为硫酸钙;(d). After adding the waste liquid, continue to stir and react until the pH value changes to 6.4, and feed air to oxidize calcium sulfite to calcium sulfate;
(e).离心分离出含水硫酸钙制品;(e). Centrifuge to separate the calcium sulfate product containing water;
(f).焙烧步骤e所得制品,制成石膏。(f). Calcining the product obtained in step e to make gypsum.
步骤(a)粉末的粒度为200目。The particle size of step (a) powder is 200 mesh.
步骤(c)所述的高浓度二氧化硫废液的密度为1.56g/cm3-1.64g/cm3,搅拌速度为20-30转/分,高浓度二氧化硫的加料速度为0.5dm3/s。The density of the high-concentration sulfur dioxide waste liquid in step (c) is 1.56g/cm 3 -1.64g/cm 3 , the stirring speed is 20-30 rpm, and the high-concentration sulfur dioxide feeding speed is 0.5dm 3 /s.
本发明通过改进二氧化硫和大理石或石灰石反应的工艺条件,让高浓度二氧化硫废液与大理石或石灰石能温和地、完全的反应;不向环境放出二氧化硫气体,不会造成二次污染,且能将其废渣转化成石膏,达到了合理利用资源,防止污染的有益效果。In the present invention, by improving the technological conditions for the reaction between sulfur dioxide and marble or limestone, the high-concentration sulfur dioxide waste liquid can react mildly and completely with marble or limestone; no sulfur dioxide gas is released to the environment, no secondary pollution is caused, and it can be The waste slag is converted into gypsum, which achieves the beneficial effects of rationally utilizing resources and preventing pollution.
附图说明Description of drawings
图1是本发明的工艺流程示意图。Fig. 1 is a process flow diagram of the present invention.
图中:粉碎机1 反应池2 废液加料管3 离心分离机4 焙烧炉5In the figure: pulverizer 1 reaction tank 2 waste liquid feeding pipe 3 centrifuge 4 roasting furnace 5
具体实施方式Detailed ways
下面结合附图对本发明作进一步地描述。The present invention will be further described below in conjunction with the accompanying drawings.
按如图1中所示的工艺流程,本发明的具体实施例采用大理石,其碳酸钙的含量不少于99%,将1吨的大理石在粉碎机1中粉碎成200目的粉末;加入有约5吨水的10M3的反应池2中,与水制成料浆;启动搅拌,搅拌速度为25转/分,从反应池中下部的多孔废液加料管3,注入1吨密度为1.61g/cm3的高浓度二氧化硫废液,加料速度为0.5dm3/s;加料完毕,继续搅拌反应约2小时至pH值降至6.4,通入空气将亚硫酸钙氧化为硫酸钙;将上述的悬浮液加入离心分离机4中,离心分离出含水硫酸钙;将上述的含水硫酸钙放入焙烧炉5中,焙烧制成石膏。According to the technological process as shown in Figure 1, the concrete embodiment of the present invention adopts marble, and the content of its calcium carbonate is not less than 99%, and 1 ton of marble is pulverized into 200 mesh powders in pulverizer 1; In the reaction tank 2 of 10M 3 of 5 tons of water, make a slurry with water; start stirring, and the stirring speed is 25 rpm, and inject 1 ton of density into 1.61g from the porous waste liquid feeding pipe 3 in the lower part of the reaction tank /cm 3 of high-concentration sulfur dioxide waste liquid, the feeding speed is 0.5dm 3 /s; after the feeding is completed, continue to stir the reaction for about 2 hours until the pH value drops to 6.4, and feed air to oxidize calcium sulfite to calcium sulfate; Add the suspension into the centrifuge 4, and centrifuge to separate the hydrous calcium sulfate; put the above-mentioned hydrous calcium sulfate into the roasting furnace 5, and roast it to make gypsum.
用大理石或石灰石为原料对高浓度二氧化硫废液进行处理,其原理是利用大理石或石灰石中碳酸钙,与高浓度二氧化硫进行反应生成亚硫酸钙,同时放出二氧化碳,反应式如下:Using marble or limestone as raw material to treat high-concentration sulfur dioxide waste liquid, the principle is to use calcium carbonate in marble or limestone to react with high-concentration sulfur dioxide to generate calcium sulfite and release carbon dioxide at the same time. The reaction formula is as follows:
在反应池中通入空气,空气中的氧将亚硫酸钙氧化为硫酸钙,反应式如下:Air is introduced into the reaction tank, and the oxygen in the air oxidizes calcium sulfite to calcium sulfate. The reaction formula is as follows:
焙烧是去除含水硫酸钙的部分结晶水,制成石膏,反应式如下:Roasting is to remove part of the crystal water of hydrous calcium sulfate to make gypsum. The reaction formula is as follows:
应当说明的是,为何采用200目左右的大理石或石灰石粉,因粒径大,反应不完全,原料利用率低,且生成的硫酸钙纯度低;粒径太小,离心分离有一定的困难,并且加工费用也会提高。若高浓度二氧化硫废液的密度改变,大理石或石灰石的碳酸钙含量发生的变化,可根据实际情况对其重量比作适当调整。反应池加一搅拌装置,使二氧化硫废液充分与粉浆接触,防止局部反应过快,温度过高,使未反应的二氧化硫以气体形式放出,造成二次污染。搅拌速度以20-30转/分为宜。同时搅拌也有利于二氧化碳放出,缩短反应时间。从反应池中下部用多孔注入高浓度二氧化硫废液,确保反应能充分的进行,且即使有少量二氧化硫放出,也能在其上升到反应池面之前又溶于水,而下会污染空气。二氧化硫废液放入反应池的流量要适宜,防止局部反应过快,温度过高,使未反应的二氧化硫以气体形式放出,造成二次污染。It should be explained why marble or limestone powder of about 200 mesh is used, because the particle size is large, the reaction is incomplete, the utilization rate of raw materials is low, and the purity of the generated calcium sulfate is low; the particle size is too small, and centrifugal separation is difficult. And the processing cost will also increase. If the density of high-concentration sulfur dioxide waste liquid changes, the calcium carbonate content of marble or limestone changes, and its weight ratio can be adjusted appropriately according to the actual situation. A stirring device is added to the reaction tank to fully contact the sulfur dioxide waste liquid with the powder slurry to prevent the local reaction from being too fast and the temperature too high, so that the unreacted sulfur dioxide is released in the form of gas, causing secondary pollution. The stirring speed is preferably 20-30 rpm. At the same time, stirring is also conducive to the release of carbon dioxide and shortens the reaction time. Inject high-concentration sulfur dioxide waste liquid from the middle and lower part of the reaction tank to ensure that the reaction can be fully carried out, and even if a small amount of sulfur dioxide is released, it can be dissolved in water before it rises to the surface of the reaction tank, and the bottom will pollute the air. The flow rate of the sulfur dioxide waste liquid into the reaction tank should be appropriate to prevent the local reaction from being too fast and the temperature too high, so that the unreacted sulfur dioxide is released in the form of gas, causing secondary pollution.
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| WO2007107111A1 (en) | 2006-03-23 | 2007-09-27 | Mg Century Mining Corporation | Mg-slag brick with high strength and method for preparing the same |
| CN104355475B (en) * | 2014-11-13 | 2016-02-24 | 湖北华巳新能源环保工程有限公司 | A kind for the treatment of process of G salt mother liquor |
| CN105032149A (en) * | 2015-07-07 | 2015-11-11 | 沈阳化工大学 | Calcium carbonate/calcium hydrate-gypsum wet desulphurization and dedusting process for flue gas |
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