CN108675294A - A kind of production method of coaly activated carbon powder - Google Patents
A kind of production method of coaly activated carbon powder Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及一种活性炭粉的生产方法,具体是一种利用回转窑生产还原钛铁矿产生的固体废物—细煤灰生产煤质活性炭粉的生产方法。The invention relates to a production method of activated carbon powder, in particular to a production method for producing coal-based activated carbon powder by using fine coal ash, the solid waste produced by reducing ilmenite in a rotary kiln.
背景技术Background technique
煤质活性炭是一种黑色多孔的固体炭质,活性炭内孔隙结构发达,具有较大的表面积,有很强的物理吸附性能,能吸附气体、液体或胶态固体。煤质活性炭是以优质原煤为原料,通过粉碎、成型活化生产而成。Coal-based activated carbon is a black porous solid carbon. The activated carbon has a well-developed pore structure, a large surface area, and strong physical adsorption properties. It can adsorb gases, liquids or colloidal solids. Coal-based activated carbon is produced from high-quality raw coal through crushing and molding activation.
煤质活性炭强度高对各种水中的有机质、游离氯以及空气中有害气体有极强的吸附能力,广泛用于环保行业污水治理及城市饮用水深度净化的优良吸附剂,也应用于脱除空气中细菌及毒害气体。Coal-based activated carbon has high strength and has a strong adsorption capacity for organic matter, free chlorine and harmful gases in the air. It is widely used as an excellent adsorbent for sewage treatment in environmental protection industries and deep purification of urban drinking water. It is also used to remove air. Bacteria and toxic gases.
回转窑生产还原钛铁矿是以烟煤为燃料,煤在生产过程中一方面作为加热燃料,另一方面作为还原剂产生CO使钛精矿还原成为还原钛铁矿。烟煤在生产过程中并未完全燃烧,经筛分后,粗的未完全燃烧煤粒返回循环使用,细的煤粒及粉状煤灰(统称为细煤灰)由于有一定热值,通常被运往制砖厂作为内燃剂使用。The production of reduced ilmenite by rotary kiln is based on bituminous coal. In the production process, coal is used as a heating fuel on the one hand, and on the other hand, it is used as a reducing agent to generate CO to reduce ilmenite concentrate to reduced ilmenite. The bituminous coal is not completely burned during the production process. After screening, the coarse incompletely burned coal particles are returned for recycling, and the fine coal particles and powdered coal ash (collectively referred to as fine coal ash) are usually used due to their certain calorific value. Shipped to the brick factory for use as an internal combustion agent.
发明内容Contents of the invention
本发明的目的在于提供一种煤质活性炭粉的生产方法,该方法不需要再单独对原煤进行破碎、活化处理,减少了能源消耗,节约了煤质活性炭生产成本。The purpose of the present invention is to provide a production method of coal-based activated carbon powder, which does not need to separately crush and activate raw coal, reduces energy consumption, and saves the production cost of coal-based activated carbon.
为实现上述的目的,本发明提供以下的技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种煤质活性炭粉的生产方法,该方法按以下步骤进行:A kind of production method of coal-based activated carbon powder, the method is carried out according to the following steps:
步骤1:控制还原窑中烟煤与钛精矿加入体积比不低于1:1,还原窑内高温区温度不低于1100℃,产生细煤灰;Step 1: Control the volume ratio of bituminous coal and titanium concentrate in the reduction kiln to not be lower than 1:1, and the temperature in the high temperature zone in the reduction kiln is not lower than 1100°C to produce fine coal ash;
步骤2:将细煤灰经磁场强度1000-1500GS磁选机进行磁选;Step 2: Carry out magnetic separation of the fine coal ash through a magnetic separator with a magnetic field strength of 1000-1500GS;
步骤3:将磁选后的细煤灰过10-40目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the fine coal ash after magnetic separation through a 10-40 mesh screen, and the coal particles on the sieve are then removed by a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve After the wind power separator removes relatively heavy impurities and wastes, pure coal ash is obtained;
步骤4:将纯净的煤粒和煤灰合并通过雷蒙磨磨粉,即得煤质活性碳粉;Step 4: Combine pure coal particles and coal ash through Raymond mill to obtain coal-based activated carbon powder;
其中,回转窑生产还原钛铁矿用烟煤选用固定碳不低于48%、挥发份不低于25%、灰分不大于8%的精烟煤。Among them, the bituminous coal used for the reduction of ilmenite in the rotary kiln is selected from clean bituminous coal with fixed carbon not less than 48%, volatile matter not less than 25%, and ash content not greater than 8%.
上述中,烟煤的固定碳为52-56%。Among the above, the fixed carbon of bituminous coal is 52-56%.
上述中,烟煤的挥发份为33-35%。Among the above, the volatile content of bituminous coal is 33-35%.
上述中,烟煤的灰分为7.0-8%。Among the above, the ash content of bituminous coal is 7.0-8%.
上述中,还原窑中烟煤与钛精矿加入的体积比为1-1.5:1。In the above, the volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1-1.5:1.
上述中,还原窑内高温区温度为1100-1120℃。Among the above, the temperature in the high temperature zone in the reduction kiln is 1100-1120°C.
本发明具有以下特点:The present invention has the following characteristics:
1、利用回转窑生产还原钛铁矿废弃的细煤灰生产煤质活性炭粉,不需要再单独对原煤进行破碎、活化处理,减少了能源消耗,节约了煤质活性炭生产成本。1. Using the rotary kiln to produce and reduce the waste fine coal ash of ilmenite to produce coal-based activated carbon powder does not need to separately crush and activate the raw coal, which reduces energy consumption and saves the production cost of coal-based activated carbon.
2、对还原钛铁矿生产产生的固废进行了有效综合利用,可以变废为宝,节约资源,同时保护了环境。2. Effective and comprehensive utilization of the solid waste produced in the production of reduced ilmenite can turn waste into treasure, save resources and protect the environment.
3、通过将粉煤灰综合加工成煤质活性炭粉,创造了较好的经济效益。3. Through the comprehensive processing of fly ash into coal-based activated carbon powder, better economic benefits have been created.
具体实施方式Detailed ways
实施例1Example 1
本实施例提供的回转窑生产还原钛铁矿用煤选用的烟煤技术指标为:固定炭:52%;挥发份34%;灰分:8%。The technical indicators of bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 52%; volatile matter: 34%; ash content: 8%.
步骤1:控制还原窑中烟煤与钛精矿加入体积比为1:1,还原窑内高温区温度1100℃,产生细煤灰。Step 1: Control the volume ratio of bituminous coal and titanium concentrate in the reduction kiln to 1:1, and the temperature in the high temperature zone in the reduction kiln is 1100°C to produce fine coal ash.
步骤2:将细煤灰通过磁场强度1000GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:5%,符合生产煤质活性炭的要求;Step 2: Carry out magnetic separation and separation of fine coal ash through a magnetic separator with a magnetic field strength of 1000GS to obtain non-magnetic fine coal ash. The ash content of the coal particles after inspection is: 5%, which meets the requirements for the production of coal-based activated carbon;
步骤3:将非磁性细煤灰通过30目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒,筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 30-mesh sieve. The coal particles on the screen are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles. The coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;
步骤4:将纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine pure coal particles and pure coal ash through a Raymond mill and sieve through a 200-mesh sieve to obtain coal-based activated carbon powder.
煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.
经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:
这种煤质活性炭粉符合制造净化水用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for water purification.
实施例2Example 2
本实施例提供的回转窑生产还原钛铁矿用煤选用的精烟煤技术指标为:固定炭:54%;挥发份33%;灰分:7.5%。The technical indicators of the clean bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 54%; volatile matter: 33%; ash content: 7.5%.
步骤1:还原窑中烟煤与钛精矿加入体积比为:1.2:1,还原窑内高温区温度1150℃,产生细煤灰。Step 1: The volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1.2:1, and the temperature in the high temperature zone in the reduction kiln is 1150°C to produce fine coal ash.
步骤2:将细煤灰通过磁场强度1300GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:3.3%,符合生产煤质活性炭的要求;Step 2: The fine coal ash is separated by magnetic separation through a magnetic separator with a magnetic field strength of 1300GS to obtain non-magnetic fine coal ash. The ash content of the coal particles is 3.3% after inspection, which meets the requirements for the production of coal-based activated carbon;
步骤3:将非磁性细煤灰通过40目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 40-mesh sieve, and the coal particles on the screen are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;
步骤4:将步骤3得到的纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine the pure coal particles and pure coal ash obtained in step 3 and pass them through a Raymond mill, and sieve them through a 200-mesh sieve to obtain coal-based activated carbon powder.
煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.
经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:
这种煤质活性炭粉符合制造空气净化用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for air purification.
实施例3Example 3
本实施例提供的回转窑生产还原钛铁矿用煤选用的精烟煤技术指标为:固定炭:56%;挥发份35%;灰分:7.0%。The technical indicators of the clean bituminous coal used in the reduction of ilmenite produced by the rotary kiln provided in this example are: fixed carbon: 56%; volatile matter: 35%; ash content: 7.0%.
步骤1:还原窑中烟煤与钛精矿加入体积比为:1.5:1,还原窑内高温区温度1200℃,得到细煤灰。Step 1: The volume ratio of bituminous coal and titanium concentrate in the reduction kiln is 1.5:1, and the temperature in the high temperature zone in the reduction kiln is 1200°C to obtain fine coal ash.
步骤2:将细煤灰通过磁场强度1500GS磁选机进行磁选分离,得到非磁性细煤灰,经检验煤粒的灰分为:4.0%,符合生产煤质活性炭的要求;Step 2: The fine coal ash is separated by magnetic separation through a magnetic separator with a magnetic field strength of 1500GS to obtain non-magnetic fine coal ash. The ash content of the coal particles after inspection is: 4.0%, which meets the requirements for the production of coal-based activated carbon;
步骤3:将非磁性细煤灰通过20目筛网筛分,筛上的煤粒再经干式跳汰机去除较重的杂质废物,得到纯净的煤粒;筛下煤灰经过风力选粉机去除比较重的杂质废物,得到纯净的煤灰;Step 3: Sieve the non-magnetic fine coal ash through a 20-mesh sieve, and the coal particles on the sieve are then passed through a dry jig to remove heavier impurities and waste to obtain pure coal particles; the coal ash under the sieve is separated by wind power The machine removes relatively heavy impurities and wastes to obtain pure coal ash;
步骤4:将步骤3得到的纯净的煤粒和纯净的煤灰合并一起通过雷蒙磨磨粉,并通过200目筛网筛分,即得煤质活性碳粉。Step 4: Combine the pure coal particles and pure coal ash obtained in step 3 and pass them through a Raymond mill, and sieve them through a 200-mesh sieve to obtain coal-based activated carbon powder.
煤质活性炭粉产品可根据用途需要制成各种煤质活性炭制品。Coal-based activated carbon powder products can be made into various coal-based activated carbon products according to the needs of the application.
经检验煤质活性炭粉技术指标如下:The technical indicators of coal-based activated carbon powder after inspection are as follows:
这种煤质活性炭粉符合制造载体用煤质颗粒活性炭国家标准技术指标。This coal-based activated carbon powder meets the technical indicators of the national standard for manufacturing coal-based granular activated carbon for carriers.
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| PB01 | Publication | ||
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| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 525000 C-03, zone 2, Henan, southwest area, Maoming hi tech Zone, Maoming City, Guangdong Province Applicant after: Guangdong Yueqiao New Material Technology Co.,Ltd. Applicant after: Guangxi Yueqiao New Material Technology Co.,Ltd. Address before: 22nd floor, Jiayan Yinghui international building, 111 Zhanqian 5th Road, Maoming, Guangdong 525000 Applicant before: MAOMING UBRIDGE GROUP MINERAL INDUSTRY Co.,Ltd. Applicant before: GUANGXI FANGCHENGGANG HUACHEN MINING INDUSTRY Co.,Ltd. Address after: 538001 Gongche Town, Gangkou District, Fangchenggang City, Guangxi Zhuang Autonomous Region Applicant after: Guangxi Yueqiao New Material Technology Co.,Ltd. Applicant after: Guangdong Yueqiao New Material Technology Co.,Ltd. Address before: 525000 C-03, zone 2, Henan, southwest area, Maoming hi tech Zone, Maoming City, Guangdong Province Applicant before: Guangdong Yueqiao New Material Technology Co.,Ltd. Applicant before: Guangxi Yueqiao New Material Technology Co.,Ltd. |
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| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181019 |