[go: up one dir, main page]

CN1180995C - Treatment method of high concentration sulfur dioxide waste liquid - Google Patents

Treatment method of high concentration sulfur dioxide waste liquid Download PDF

Info

Publication number
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
Authority
CN
China
Prior art keywords
waste liquid
sulfur dioxide
concentration sulfur
powder
marble
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CNB031265944A
Other languages
Chinese (zh)
Other versions
CN1451616A (en
Inventor
彭梦侠
陈梓云
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiaying University
Original Assignee
Jiaying University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiaying University filed Critical Jiaying University
Priority to CNB031265944A priority Critical patent/CN1180995C/en
Publication of CN1451616A publication Critical patent/CN1451616A/en
Application granted granted Critical
Publication of CN1180995C publication Critical patent/CN1180995C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a method for treating high-concentration sulfur dioxide waste liquid, aiming at providing a method which can lead the high-concentration sulfur dioxide waste liquid to react with marble or limestone mildly and completely; a treatment method which does not emit sulfur dioxide gas to the environment, does not cause secondary pollution and can convert waste residues into gypsum; the invention is that marble or limestone is crushed into powder with more than 200 meshes, and mixed with water to prepare slurry with the weight ratio of 1: 5, waste liquid is injected from bottom holes of a reaction tank according to the weight ratio of 1: 1 of powder to waste liquid under stirring, air is introduced when the pH value is changed to 6.4 after reaction, then suspension is centrifugally separated to obtain hydrous calcium sulfate, and the hydrous calcium sulfate is prepared into gypsum after roasting.

Description

高浓度二氧化硫废液处理方法Treatment method of high concentration sulfur dioxide waste liquid

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.

Claims (3)

1.一种高浓度二氧化硫废液处理方法,依次包括以下步骤:1. A high-concentration sulfur dioxide waste liquid treatment method, comprising 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. 2.根据权利要求1所述的处理方法,步骤(a)粉末的粒度为200目。2. The processing method according to claim 1, the particle size of step (a) powder is 200 orders. 3.根据权利要求1或2所述的处理方法,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。3. The treatment method according to claim 1 or 2, the density of the high-concentration sulfur dioxide waste liquid described in step (c) is 1.56g/cm 3 -1.64g/cm 3 , and the stirring speed is 20-30 rpm , the feeding rate of high-concentration sulfur dioxide is 0.5dm 3 /s.
CNB031265944A 2003-05-16 2003-05-16 Treatment method of high concentration sulfur dioxide waste liquid Expired - Fee Related CN1180995C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB031265944A CN1180995C (en) 2003-05-16 2003-05-16 Treatment method of high concentration sulfur dioxide waste liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB031265944A CN1180995C (en) 2003-05-16 2003-05-16 Treatment method of high concentration sulfur dioxide waste liquid

Publications (2)

Publication Number Publication Date
CN1451616A CN1451616A (en) 2003-10-29
CN1180995C true CN1180995C (en) 2004-12-22

Family

ID=29222899

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB031265944A Expired - Fee Related CN1180995C (en) 2003-05-16 2003-05-16 Treatment method of high concentration sulfur dioxide waste liquid

Country Status (1)

Country Link
CN (1) CN1180995C (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Also Published As

Publication number Publication date
CN1451616A (en) 2003-10-29

Similar Documents

Publication Publication Date Title
CN114505323B (en) Harmless treatment method and equipment for electrolytic manganese slag
CN108660326A (en) A method of reduction acidolysis-leaching is simultaneously except iron handles manganese oxide ore
CN101531384A (en) Technique for preparing electronic grade magnesium hydrate and ammonium sulphate by cycle serum featuring in flue gas desulfurization by method of magnesium oxidization
CN109970089A (en) A kind of method and system for preparing barium sulfate by utilizing barium slag
CN118880429A (en) A method for preparing high aspect ratio calcium carbonate whiskers by carbon fixation in steel smelting slag leachate
CN106495215B (en) A kind of method that magnesium arsenate is produced containing arsenic waste solution
CN117206306B (en) A combined dry and wet method for the harmless treatment of electrolytic manganese slag
WO2025039666A1 (en) Method for recovering heavy metal and soluble chlorine salt from fly ash generated by incineration of domestic waste
CN118343817A (en) Method for preparing nano calcium carbonate by industrial solid waste gypsum carbon fixation
CN1180995C (en) Treatment method of high concentration sulfur dioxide waste liquid
CN102153219A (en) Treatment method for waste water after purification of graphite
CN110563007B (en) Method for converting sodium sulfate into sodium bicarbonate by using calcium oxide and carbon dioxide
CN102153127B (en) Method for preparing gypsum by removing sulfate radicals from mineral salts with waste distillation liquid from ammonia alkali factory
CN114804673A (en) Comprehensive utilization method of red mud
CN1377830A (en) Producing light calcium carbonate from calcium carbide waste slurry
CN102285653A (en) Method for removing carbon impurities in silicon carbide micropowder
CN101823745A (en) Method for producing superfine light calcium carbonate, ammonium chloride and carbon powder by using combined alkali waste liquid and carbide slag
CN209721798U (en) A device for recovering magnesium in high-magnesium desulfurization wastewater
CN101838005A (en) Method for producing ultrafine light calcium carbonate and white carbon black with co-production of sodium chloride and carbon powder
CN207031141U (en) A kind of power plant desulfurization wastewater pretreatment unit
CN109081382A (en) A kind of processing technology of bodied ferric sulfate
CN113603127B (en) Method for concentrated sulfuric acid treatment of calcium chloride wastewater and co-production of chemical gypsum
CN1223689C (en) Full-wet method manganese leaching method for manganese dedusting ash
CN105254070A (en) Method for recovering elemental sulfur from high-sulfur-content wastewater through reaction and separation coupling
CN213012311U (en) Desulfurization waste water mud innocent treatment device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee