CN101397136A - Method for preparing high specific surface area granular activated carbon by physical activation process - Google Patents
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一、技术领域 1. Technical field
本发明涉及一种物理活化法制备高比表面积颗粒活性炭的方法,属于材料制备技术领域。The invention relates to a method for preparing granular activated carbon with a high specific surface area by a physical activation method, and belongs to the technical field of material preparation.
二、背景技术 2. Background technology
活性炭是一种多孔炭材料,在化工、环保、冶金、电子和能源等领域有着广泛的应用。近几年来,随着科学技术的发展,活性炭应用领域不断扩大,对吸附性能提出了新的、更高的要求,在“高吸附、多功能、高强度”的总要求下,出现了对专用活性炭需求量越来越多的趋势。目前高比表面积活性炭通常采用化学法活化法制备而成,以KOH、NaOH等活化剂制备2000m2/g以上的高比比表面积活性炭,使其能应用于双电层电容器的电极、储氢、储甲烷等领域。但该法对设备具有腐蚀性,且所制备的活性炭多为粉末状不具有强度,为其应用带来一定局限性;同时活化完后还需要对产品进行酸洗和水洗,这就带来废水等二次污染物,造成环境污染。而物理活化法虽然对环境不产生污染,但目前在制备高比表面积的活性炭时,往往需要很长的时间才能使其比表面积达到2000m2/g以上,这就造成物理法制备具有高比表面积活性炭需要的能耗高,时间长,且所得产品的得率低,降低了原料利用率,造成其生产成本的大幅提高。Activated carbon is a kind of porous carbon material, which has a wide range of applications in the fields of chemical industry, environmental protection, metallurgy, electronics and energy. In recent years, with the development of science and technology, the application field of activated carbon has continued to expand, and new and higher requirements have been put forward for the adsorption performance. Under the general requirements of "high adsorption, multi-function, high strength", special-purpose The demand for activated carbon is increasing. At present, activated carbon with high specific surface area is usually prepared by chemical activation method. KOH, NaOH and other activators are used to prepare activated carbon with high specific surface area above 2000m 2 /g, so that it can be used in electrodes, hydrogen storage, and storage of electric double layer capacitors. Methane and other fields. However, this method is corrosive to the equipment, and the prepared activated carbon is mostly powdery and has no strength, which brings certain limitations to its application; at the same time, the product needs to be pickled and washed with water after activation, which brings waste water. and other secondary pollutants, causing environmental pollution. Although the physical activation method does not pollute the environment, it often takes a long time to make the specific surface area reach more than 2000m 2 /g when preparing activated carbon with a high specific surface area, which results in a high specific surface area prepared by the physical method. Activated carbon requires high energy consumption and long time, and the yield of the obtained product is low, which reduces the utilization rate of raw materials and causes a substantial increase in its production cost.
在专利号为200510010670.2的专利中,公开了一种“生产高比表面积活性炭的方法”,以烟杆为原料,KOH为活化剂,用微波辐射后进行酸洗、水洗和烘干,得到活性炭产品。这种方法由于加入了化学药品等试剂,一方面对设备具有较强的腐蚀性,另一方面需要对其产品酸洗和水洗,带来二次污染。In the patent No. 200510010670.2, a "method for producing activated carbon with high specific surface area" is disclosed, using tobacco rods as raw materials, KOH as activator, pickling, washing and drying after microwave radiation to obtain activated carbon products . Due to the addition of reagents such as chemicals, this method has strong corrosiveness to equipment on the one hand, and needs pickling and water washing of its products on the other hand, which brings secondary pollution.
苏伟等在《林产化学与工业》2006年第2期发表的《椰壳炭制备高比表面积活性炭的研究》中以水蒸气和CO2为共同活化气体,分阶段来制备活性炭,该法制备比表面积大于2000m2/g以上的活性炭至少需10小时以上的时间,且得率低于19.4%。从文献中可看出:该法在制备过程中需要对混合气体(水蒸气和CO2)在不同阶段的比例进行精确控制,这为制备过程带来了一定的难度。在专利号为200510010669.X的专利中,公开了一种“物理法处理烟杆废弃物制造活性炭”的方法,以烟杆为原料,水蒸气为活化气体,虽然所需时间较短,但其产品仅能达到常用活性炭产品的要求,远远达不到双电层电容器的电极、储氢、储甲烷等领域的应用要求,且得率也较低(低于30%)。In "Research on Preparation of Activated Carbon with High Specific Surface Area by Coconut Shell Charcoal" published by Su Wei and others in "Forest Products Chemistry and Industry" No. 2, 2006, water vapor and CO 2 were used as co-activation gases to prepare activated carbon in stages. Activated carbon with a specific surface area greater than 2000m 2 /g needs at least 10 hours or more, and the yield is lower than 19.4%. It can be seen from the literature that this method requires precise control of the ratio of the mixed gas (water vapor and CO 2 ) at different stages during the preparation process, which brings certain difficulties to the preparation process. In the patent No. 200510010669.X, a method of "physically treating tobacco rod waste to make activated carbon" is disclosed. The tobacco rod is used as the raw material, and water vapor is used as the activation gas. Although the required time is relatively short, its The product can only meet the requirements of commonly used activated carbon products, far from the application requirements of electrodes, hydrogen storage, methane storage and other fields of electric double layer capacitors, and the yield is also low (less than 30%).
与上述技术相比,本发明所使用的活化气体为水蒸气和CO2气体,克服了化学活化法对设备的腐蚀和环境的污染;对原料需以经过高温炭化后椰壳炭化料为原料,活性炭产品的得率高(大于40%),有利于提高原料资源的利用;采用微波作为加热源,通过调整微波功率,实现其对温度的控制,且所制备活性炭为颗粒状,提高了应用范围。Compared with the above-mentioned technology, the activated gas used in the present invention is water vapor and CO 2 gas, which overcomes the corrosion of equipment and the pollution of the environment by chemical activation; The yield of activated carbon products is high (greater than 40%), which is conducive to improving the utilization of raw material resources; microwave is used as a heating source, and the temperature control is realized by adjusting the microwave power, and the prepared activated carbon is granular, which improves the application range .
三、发明内容 3. Contents of the invention
本发明的目的在于提供一种物理活化法制备高比表面积颗粒活性炭的方法,首先将椰壳在高温下进行炭化,随后将进行破碎、筛分后的炭化料置于微波辐射装置中,通过控制活化温度,调节活化时间和活化气体流量,对原料进行活化处理,得到比表面积为2200m2/g以上的颗粒活性炭产品。The object of the present invention is to provide a method for preparing granular activated carbon with a high specific surface area by a physical activation method. First, the coconut shell is carbonized at a high temperature, and then the carbonized material after crushing and sieving is placed in a microwave radiation device. Activation temperature, activation time and activation gas flow are adjusted, and raw materials are activated to obtain granular activated carbon products with a specific surface area of 2200m 2 /g or more.
本发明通过如下工艺步骤实现,图1为其工艺流程图。The present invention is realized through the following process steps, and Fig. 1 is its process flow chart.
(1)将椰壳在炭化炉中在800~1200℃下炭化1~3小时;(1) Coconut shells are carbonized at 800-1200°C for 1-3 hours in a carbonization furnace;
(2)将炭化后的椰壳炭化料进行破碎、筛分,取粒径为4~30目的颗粒;(2) crushing and sieving the carbonized coconut shell carbonized material, and getting a particle size of 4 to 30 mesh particles;
(3)破碎后的椰壳炭化料置于微波辐射装置中,加热至800~950℃时,通入活化气体进行活化,得到高比表面积活性炭产品。(3) The crushed coconut shell carbonized material is placed in a microwave radiation device, and when heated to 800-950 ° C, activated gas is passed through to activate, and a high specific surface area activated carbon product is obtained.
其中当以水蒸气为活化气体时,其流量为0.5~4L/min.Kg(每公斤炭每分钟的水蒸气流量);以CO2为活化气体时,其流量为1~5L/min.Kg(每公斤炭每分钟的CO2气流量);以CO2和水蒸气的混合气体为活化气体时,CO2和水蒸气的比例为5~1:1,其流量为0.5~6L/min.Kg(每公斤炭每分钟的混合气体流量)。Among them, when water vapor is used as the activation gas, the flow rate is 0.5-4L/min.Kg (water vapor flow rate per kilogram of carbon per minute); when CO2 is used as the activation gas, the flow rate is 1-5L/min.Kg (CO 2 gas flow rate per kilogram of charcoal per minute); when the mixed gas of CO 2 and water vapor is used as the activation gas, the ratio of CO 2 and water vapor is 5-1:1, and the flow rate is 0.5-6L/min. Kg (mixed gas flow per minute per kilogram of charcoal).
本发明具有以下优点:The present invention has the following advantages:
(1)采用水蒸气、CO2的一种或混合气体为活化气体,不产生三废,对环境无污染,对设备腐蚀性小;(1) One or mixed gas of water vapor and CO2 is used as the activation gas, which does not produce three wastes, has no pollution to the environment, and has little corrosion to equipment;
(2)利用高温炭化,提高椰壳炭化料的微孔结构,为制备高比表面积活性炭提供了具有较为发达孔隙结构的原料;有利于提高椰壳炭化料的有序结构,减少炭在活化过程中的烧蚀,提高活性炭产品的得率;(2) Using high-temperature carbonization to improve the microporous structure of coconut shell carbonized materials, it provides a raw material with a relatively developed pore structure for the preparation of activated carbon with high specific surface area; it is beneficial to improve the ordered structure of coconut shell carbonized materials and reduce carbon in the activation process. The ablation in the medium increases the yield of activated carbon products;
(3)利用微波对物料的内加热和选择性加热特性,克服物料内部的温度梯度,有利于活化气体在物料内部的扩散,加快反应速度,缩短活化时间,达到节能降耗,有利于活性点与活化气体反应,有效的促进了孔隙的形成,提高了活性炭的得率;(3) Utilize the internal heating and selective heating characteristics of microwaves to overcome the temperature gradient inside the material, which is conducive to the diffusion of activated gas inside the material, speed up the reaction speed, shorten the activation time, achieve energy saving and consumption reduction, and benefit the active point Reaction with activated gas effectively promotes the formation of pores and improves the yield of activated carbon;
(4)所制备的活性炭为颗粒活性炭,提高了其应用范围;(4) The activated carbon prepared is granular activated carbon, which improves its scope of application;
四、具体实施方式 4. Specific implementation
实施例1:取高温炭化后的椰壳炭化料200g,置于微波辐射装置中,加热至900℃,通入水蒸气,其水蒸气流量为0.5L/min,活化1.25小时后,得到具有高比表面积的活性炭产品。其得率为42.2%,碘吸附值为1569.47mg/g,比表面积为2279m2/g,孔容积为1.212cm3/g。Example 1: Take 200g of coconut shell carbonized material after high-temperature carbonization, place it in a microwave radiation device, heat it to 900 ° C, feed water vapor, and its water vapor flow rate is 0.5L/min. After activating for 1.25 hours, a high specific surface area of activated carbon products. The yield is 42.2%, the iodine adsorption value is 1569.47mg/g, the specific surface area is 2279m 2 /g, and the pore volume is 1.212cm 3 /g.
实施例2:取高温炭化后的椰壳炭化料150g,置于微波辐射装置中,加热至850℃,通入CO2,其中CO2流量为0.6L/min,活化3小时后,得到具有高比表面积的活性炭产品。其得率、碘吸附值、比表面积和孔容积分别为49.2%、1456.37mg/g、2203m2/g和1.255cm3/g。Example 2: Take 150 g of coconut shell carbonized material after high-temperature carbonization, place it in a microwave radiation device, heat it to 850 ° C, and feed CO 2 , wherein the flow rate of CO 2 is 0.6 L/min. After 3 hours of activation, a high specific surface area of activated carbon products. Its yield, iodine adsorption value, specific surface area and pore volume are 49.2%, 1456.37mg/g, 2203m 2 /g and 1.255cm 3 /g respectively.
实施例3:取高温炭化后的椰壳炭化料250g,置于微波辐射装置中,加热至900℃,通入水蒸气和CO2的混合气体,其中CO2和水蒸气的比例为3:1,混合气体流量为0.8L/min,活化1小时后,得到具有高比表面积的活性炭产品。其得率为50.6%,碘吸附值为1485.03mg/g,比表面积为2250m2/g,孔容积为1.157cm3/g。Embodiment 3: Get 250g of coconut shell carbonized material after high-temperature carbonization, place it in a microwave radiation device, heat to 900°C, feed water vapor and CO Mixed gas, wherein the ratio of CO and water vapor is 3:1, The flow rate of the mixed gas is 0.8L/min, and after 1 hour of activation, an activated carbon product with a high specific surface area is obtained. The yield is 50.6%, the iodine adsorption value is 1485.03mg/g, the specific surface area is 2250m 2 /g, and the pore volume is 1.157cm 3 /g.
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