CN105129797A - Preparation method of ammoniation-activation plant activated carbon - Google Patents
Preparation method of ammoniation-activation plant activated carbon Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 108
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 239000002994 raw material Substances 0.000 claims abstract description 26
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 12
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 12
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 12
- 239000004202 carbamide Substances 0.000 claims abstract description 12
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims abstract description 11
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims abstract description 11
- 239000001099 ammonium carbonate Substances 0.000 claims abstract description 11
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 10
- 241000196324 Embryophyta Species 0.000 claims description 37
- 239000000463 material Substances 0.000 claims description 30
- 235000014676 Phragmites communis Nutrition 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 26
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 14
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 244000273256 Phragmites communis Species 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 239000012190 activator Substances 0.000 claims description 8
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 7
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 4
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 4
- 238000004176 ammonification Methods 0.000 claims description 4
- 238000002791 soaking Methods 0.000 claims description 3
- 238000002203 pretreatment Methods 0.000 claims description 2
- 235000013311 vegetables Nutrition 0.000 claims 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims 1
- 241000209128 Bambusa Species 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 235000019083 Osmanthus fragrans Nutrition 0.000 claims 1
- 244000242564 Osmanthus fragrans Species 0.000 claims 1
- 229910021529 ammonia Inorganic materials 0.000 claims 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 125000000524 functional group Chemical group 0.000 abstract description 15
- 238000003763 carbonization Methods 0.000 abstract description 6
- 230000004913 activation Effects 0.000 abstract description 4
- 238000005470 impregnation Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000003213 activating effect Effects 0.000 abstract description 3
- 238000005406 washing Methods 0.000 abstract description 3
- 235000013877 carbamide Nutrition 0.000 abstract description 2
- 238000001035 drying Methods 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract 2
- 238000007796 conventional method Methods 0.000 abstract 1
- 238000002156 mixing Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 11
- 239000000843 powder Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- 238000001179 sorption measurement Methods 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000007787 solid Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 229920005610 lignin Polymers 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 241001330002 Bambuseae Species 0.000 description 3
- 239000011425 bamboo Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 244000025254 Cannabis sativa Species 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 235000019750 Crude protein Nutrition 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000007833 carbon precursor Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 230000010261 cell growth Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 125000004356 hydroxy functional group Chemical group O* 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 150000002596 lactones Chemical group 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
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Abstract
Description
技术领域technical field
本发明属于功能材料领域,特别是涉及一种氨化—活化植物质活性炭的制备方法。The invention belongs to the field of functional materials, in particular to a method for preparing ammoniated-activated plant activated carbon.
背景技术Background technique
活性炭作为一种常见的吸附剂,被广泛地应用于气相和液相中有害物质的吸附和去除。其吸附污染物质的能力主要源于发达的孔径结构和丰富的官能团(羧基、内酯基、酚羟基等酸性官能团和碱性官能团)。近年来,为了满足不断扩大的市场需求和消费者对更高效活性炭的要求,生产者常通过改性等方法来提高其物理化学性质和吸附性能。很多研究证明,植物质活性炭具有品质高、性能好等优点。所以,植物质原料在活性炭制备领域得到了大量的推广、应用。在植物质活性炭传统制备方法中,大多是将炭先驱体粉碎后直接浸渍、活化,导致活化剂浸渍不充分,利用率低下,浸渍时间长,活化温度高,活性炭比表面积低,官能团数量少等缺陷。针对传统方法存在的不足,提出将植物质原料氨化处理的制备方法。As a common adsorbent, activated carbon is widely used in the adsorption and removal of harmful substances in gas and liquid phases. Its ability to adsorb pollutants is mainly due to the well-developed pore structure and abundant functional groups (acidic and basic functional groups such as carboxyl, lactone, and phenolic hydroxyl groups). In recent years, in order to meet the ever-expanding market demand and consumers' requirements for more efficient activated carbon, producers often improve its physical and chemical properties and adsorption performance through modification and other methods. Many studies have proved that plant-based activated carbon has the advantages of high quality and good performance. Therefore, plant-based raw materials have been widely promoted and applied in the field of activated carbon preparation. In the traditional preparation methods of plant-based activated carbon, most of the carbon precursors are pulverized and directly impregnated and activated, resulting in insufficient impregnation of the activator, low utilization rate, long impregnation time, high activation temperature, low specific surface area of activated carbon, and small number of functional groups. defect. Aiming at the deficiencies of the traditional method, a preparation method of ammoniating plant material is proposed.
经检索,氨化—活化法制备植物质活性炭的工艺目前是一个技术空白。After searching, the process of preparing plant-based activated carbon by ammoniation-activation method is currently a technical blank.
发明内容Contents of the invention
本发明克服传统方法制备活性炭的不足之处,提供一种氨化-活化植物质活性炭的工艺方法。此方法在制备活性炭过程中先将植物质原料进行氨化处理,然后进行炭化活化。此方法制备的活性炭具有较高的比表面积和发达的表面官能团。The invention overcomes the shortcomings of the traditional method for preparing activated carbon, and provides a process method for ammoniating and activating plant-based activated carbon. In this method, in the process of preparing activated carbon, the plant matter raw material is firstly subjected to ammonification treatment, and then activated by carbonization. Activated carbon prepared by this method has a high specific surface area and developed surface functional groups.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
一种氨化—活化植物质活性炭的制备方法,包括以下步骤:A method for preparing ammoniated-activated plant matter activated carbon, comprising the following steps:
(1)采用尿素、碳酸氢铵或氨水等氨化试剂对植物质原料进行氨化处理,得到氨化后的原料;(1) using ammonification reagents such as urea, ammonium bicarbonate or ammonia water to carry out ammoniation treatment on plant matter raw materials to obtain the raw materials after ammoniation;
(2)将步骤(1)中氨化后的原料与活化剂混匀,在20~30℃浸渍2~12h,所述氨化后的原料与活化剂的质量比为1:0.5~2.0;(2) mix the raw material after ammoniation in step (1) with the activator, soak at 20-30°C for 2-12 hours, the mass ratio of the raw material after ammoniation to the activator is 1:0.5-2.0;
(3)浸渍后的原料在300~800℃下炭化活化30~60min,得活性炭;(3) Carbonize and activate the impregnated raw materials at 300-800°C for 30-60 minutes to obtain activated carbon;
(4)将活性炭洗涤、干燥,即得产品。(4) Wash and dry the activated carbon to obtain the product.
在植物质原料进行氨化处理前,对植物质原料进行预处理,预处理方法为:将植物质原料洗涤、晾干、粉碎至20~40目;进行预处理的好处是:为了使氨化处理的过程更加充分,氨化试剂与植物质原料反应接触面积更大,以便减少氨化时间,提高效率。Before the plant material raw material is subjected to ammoniation treatment, the plant material raw material is pretreated. The pretreatment method is: wash the plant material raw material, dry it, and crush it to 20-40 meshes; the advantage of pretreatment is: in order to make the ammoniated material The treatment process is more sufficient, and the reaction contact area between the ammoniation reagent and the plant material is larger, so as to reduce the ammoniation time and improve the efficiency.
步骤(1)中,所述的植物质原料为芦苇、芦竹或大叶荻的一种或多种混合,经过试验验证,上述三种植物质原料芦苇、芦竹或大叶荻采用氨化—活化处理后效果最好,具有较高的比表面积和发达的官能团。In step (1), the plant material raw material is one or more mixtures of reed, reed bamboo or big-leaf grass. It has been verified by experiments that the above three plant material raw materials of reed, reed bamboo or big-leaf grass are ammoniated— The effect is the best after activation treatment, with higher specific surface area and developed functional groups.
步骤(1)中,当氨化试剂为尿素或碳酸氢铵时,氨化处理的具体方法是:将植物质原料按照尿素或碳酸氢铵与植物质原料的质量比为0.03~0.08:1与尿素或碳酸氢铵混合,加水溶解,密封,在90~100℃保持1~6h,优选温度为100℃。In step (1), when the ammoniation reagent is urea or ammonium bicarbonate, the specific method of ammoniation treatment is: the mass ratio of urea or ammonium bicarbonate to the plant material is 0.03-0.08:1 and Mix urea or ammonium bicarbonate, add water to dissolve, seal, and keep at 90-100°C for 1-6 hours, preferably at 100°C.
经过实验论证与分析,得到尿素或碳酸氢铵与植物质原料的质量比为0.03~0.08:1时,氨化的效果和效率都是最好的,比值较高时,不仅浪费氨化试剂、污染环境,而且后续洗涤时也会造成麻烦;比值较低时,氨化作用没有得到充分的体现,活性炭没有得到较高的比表面积和发达的官能团。Through experimental demonstration and analysis, it is obtained that when the mass ratio of urea or ammonium bicarbonate to plant material is 0.03-0.08:1, the effect and efficiency of ammoniation are the best, and when the ratio is high, not only waste of ammoniation reagents, It will pollute the environment, and it will cause trouble during subsequent washing; when the ratio is low, the ammoniation effect has not been fully reflected, and the activated carbon has not obtained a high specific surface area and developed functional groups.
步骤(1)中,当氨化试剂为氨水时,氨化处理的具体方法是:将植物质原料按照氨水与植物质原料的质量比为0.01~0.05:1与氨水混合均匀,密封,在18~30℃保持5~14d,优选温度为25℃。优选的,氨水的质量浓度是3~15%。In step (1), when the ammoniation reagent is ammonia water, the specific method of ammoniation treatment is: mix the plant matter material with ammonia water according to the mass ratio of ammonia water to plant matter material at 0.01-0.05:1, seal it, and Keep at ~30°C for 5~14d, preferably at 25°C. Preferably, the mass concentration of ammonia water is 3-15%.
经过实验论证与分析,得到氨水与植物质原料的质量比为0.01~0.05:1时,氨化的效果和效率都是最好的,比值较高时,不仅浪费氨化试剂、污染环境,而且后续洗涤时也会造成麻烦;比值较低时,氨化作用没有得到充分的体现,活性炭没有得到较高的比表面积和发达的官能团。Through experimental demonstration and analysis, it is obtained that when the mass ratio of ammonia water to plant raw materials is 0.01-0.05:1, the effect and efficiency of ammoniation are the best. Subsequent washing will also cause trouble; when the ratio is low, the ammoniation effect has not been fully reflected, and the activated carbon has not obtained a high specific surface area and developed functional groups.
步骤(2)中,活化剂为磷酸溶液或氢氧化钾,所述磷酸溶液的质量分数为30~55%。In step (2), the activator is phosphoric acid solution or potassium hydroxide, and the mass fraction of the phosphoric acid solution is 30-55%.
步骤(2)中,优选的,所述浸渍时间为2~8h。In step (2), preferably, the soaking time is 2-8 hours.
根据氨化后的植物质原料的情况浸渍2~8h,此浸渍时间能使氨化后的植物质原料充分活化,时间过短的话,浸渍不完全,浸渍效果不理想;时间过长的话,浪费时间、降低效率。According to the situation of the ammoniated plant material, soak for 2-8 hours. This soaking time can fully activate the ammoniated plant material. time and reduce efficiency.
步骤(3)中,优选的,所述温度为300~450℃,所述时间为30~60min。经过氨化处理后,可显著降低碳化温度和时间(未氨化的植物质活性炭制备方法的碳化温度为500~900℃,炭化时间为1~4h),经试验验证该碳化温度和时间能够满足活性炭的含碳量的标准。In step (3), preferably, the temperature is 300-450° C., and the time is 30-60 min. After ammoniation treatment, the carbonization temperature and time can be significantly reduced (the carbonization temperature of the non-ammoniated plant-based activated carbon preparation method is 500-900°C, and the carbonization time is 1-4h), and the carbonization temperature and time have been verified by experiments. The carbon content standard of activated carbon.
步骤(4)中,将活性炭洗涤至pH值稳定在7.0左右再进行干燥,原因是:活性炭洗涤至酸性或碱性的话,可能会影响活性炭作用环境的反应,比如活性炭洗涤至碱性的话,那么可能与活性炭作用环境中的酸性物质反应。In step (4), the activated carbon is washed until the pH value is stabilized at about 7.0 and then dried. The reason is: if the activated carbon is washed to acidic or alkaline, it may affect the reaction of the active carbon environment. For example, if the activated carbon is washed to alkaline, then May react with acids in the environment in which activated carbon is used.
氨化对于植物质原料,可以破坏木质素和多糖之间的化学键结合,使纤维素,半纤维素与木质素分离,将不溶的木质素变为较易溶的羟基木质素,结晶纤维素变成无定形纤维素,引起细胞膨胀,使得植物质原料结构变得疏松;并且,在氨化过程中植物质原料中粗蛋白的含量显著提高,能够提高氨基官能团数量。在植物质活性炭制备的过程中,将植物质原料进行氨化处理,能够有效的增强浸渍效果,提高活性炭的比表面积,增加活性炭官能团的数量。For plant materials, ammoniation can destroy the chemical bonds between lignin and polysaccharides, separate cellulose and hemicellulose from lignin, change insoluble lignin into more soluble hydroxy lignin, and crystalline cellulose into Forming amorphous cellulose, causing cell expansion, making the structure of the plant material material loose; moreover, the content of crude protein in the plant material material is significantly increased during the ammoniation process, which can increase the number of amino functional groups. In the process of preparing plant-based activated carbon, ammoniating plant-based raw materials can effectively enhance the impregnation effect, increase the specific surface area of activated carbon, and increase the number of functional groups of activated carbon.
本发明与传统的制备方法相比有以下优点:Compared with traditional preparation methods, the present invention has the following advantages:
(1)原料使用秸秆等植物质原料,具有分布广泛,成本低廉的优点。(1) Plant materials such as straws are used as raw materials, which have the advantages of wide distribution and low cost.
(2)氨化试剂用量小,对环境造成的污染小。(2) The amount of ammoniation reagent is small, and the pollution to the environment is small.
(3)由于氨化作用,活化剂使用量减少,活化温度降低,节约成本,降低能耗,减少污染。(3) Due to the ammonification, the usage of activator is reduced, the activation temperature is lowered, the cost is saved, the energy consumption is reduced, and the pollution is reduced.
(4)生产成本低,生产工艺简单,所制得的活性炭相对于传统方法具有较高比表面积和较丰富的官能团。(4) The production cost is low, the production process is simple, and the prepared activated carbon has a higher specific surface area and richer functional groups than traditional methods.
(5)经过大量实验与分析,本发明的制备方法得到的活性炭吸附效果比普通的方法制备得到的活性炭的吸附效果更好。(5) Through a large number of experiments and analysis, the adsorption effect of the activated carbon obtained by the preparation method of the present invention is better than that of the activated carbon prepared by the common method.
具体实施方式detailed description
下面结合实施例对本发明进一步说明。Below in conjunction with embodiment the present invention is further described.
实施例1Example 1
将芦苇洗涤、晾干、粉碎至40目;注入相当于芦苇干物质重量质量浓度为3%的氨水与其混匀,密封,在25℃下保持7d进行氨化处理;将氨化后的芦苇粉末和45wt.%磷酸溶液按质量比1:1室温浸渍5h;浸渍物转入坩埚内置于马弗炉中,300℃下炭化活化40min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。所得活性炭较传统方法对照例1制备的活性炭比表面积提高20%,总官能团数量提高46%。Wash, dry, and crush the reeds to 40 meshes; inject ammonia water with a weight concentration of 3% of the dry matter of the reeds, mix it evenly, seal it, and keep it at 25°C for 7 days for ammoniation treatment; the ammoniated reed powder and 45wt.% phosphoric acid solution in a mass ratio of 1:1 and impregnated at room temperature for 5 hours; the impregnated material was transferred to a crucible and placed in a muffle furnace, carbonized and activated at 300°C for 40 minutes, and naturally cooled to room temperature; the obtained activated carbon was washed with deionized water to pH 7 or so, solid-liquid separation, drying. Compared with the activated carbon prepared by the traditional method of Comparative Example 1, the specific surface area of the obtained activated carbon is increased by 20%, and the total functional group quantity is increased by 46%.
对照例1Comparative example 1
将芦苇洗涤、晾干、粉碎至40目,将芦苇粉末和45wt.%磷酸溶液按质量比1:2浸渍10h;浸渍物转入坩埚内置于马弗炉中,500℃下炭化活化60min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。The reeds were washed, dried, and crushed to 40 mesh, and the reed powder and 45wt.% phosphoric acid solution were impregnated for 10 hours at a mass ratio of 1:2; Cool to room temperature; wash the obtained activated carbon with deionized water until the pH is about 7, separate solid and liquid, and dry.
实施例2Example 2
将芦苇洗涤、晾干、粉碎至40目;取相当于芦苇干物质重量7%的尿素,每10g芦苇干物质重量加2ml水溶解,尿素水溶液与芦苇粉末混匀,密封,在100℃下保持2h,进行氨化处理;将氨化后的芦苇粉末和氢氧化钾按质量比1:2在30℃浸渍2h;浸渍物转入镍坩埚内置于马弗炉中,650℃下炭化活化60min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。其比表面积较传统方法对照例2提高15%,表面官能团数量提高了50%。Wash the reeds, dry them, and crush them to 40 meshes; take urea equivalent to 7% of the weight of the dry matter of the reeds, add 2ml of water to dissolve the weight of the dry matter of the reeds per 10g, mix the aqueous urea solution with the reed powder, seal it, and keep it at 100°C 2h, carry out ammoniation treatment; soak the ammoniated reed powder and potassium hydroxide at a mass ratio of 1:2 at 30°C for 2h; transfer the impregnated material into a nickel crucible and put it in a muffle furnace, and carbonize and activate it at 650°C for 60min. Naturally cool to room temperature; wash the obtained activated carbon with deionized water until the pH is about 7, separate solid and liquid, and dry. Its specific surface area is increased by 15% compared with the traditional method Comparative Example 2, and the number of surface functional groups is increased by 50%.
对照例2Comparative example 2
将芦苇洗涤、晾干、粉碎至40目,将芦苇粉末和氢氧化钾按质量比1:2浸渍8h;浸渍物转入坩埚内置于马弗炉中,900℃下炭化活化120min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。The reeds were washed, dried, and crushed to 40 mesh, and the reed powder and potassium hydroxide were impregnated for 8 hours at a mass ratio of 1:2; the impregnated material was transferred into a crucible and placed in a muffle furnace, carbonized and activated at 900°C for 120 minutes, and cooled naturally to room temperature; wash the obtained activated carbon with deionized water until the pH is about 7, separate solid and liquid, and dry.
实施例3Example 3
将芦苇洗涤、晾干、粉碎至40目;取芦苇粉末干物质重量5%的碳酸氢铵,每10g芦苇粉末干物质重量加2ml水溶解,碳酸氢铵水溶液与芦苇粉末混匀,密封,在100℃下保持4h,进行氨化处理;将氨化后芦苇粉末和45wt.%磷酸溶液按质量比1:1.5在20℃浸渍8h;浸渍物转入坩埚内置于马弗炉中,400℃下炭化活化60min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。其比表面积较传统方法对照例3提高了15%,官能团数量提高18%。Wash the reeds, dry them, and crush them to 40 meshes; take 5% ammonium bicarbonate of reed powder dry matter weight, add 2ml water for every 10g reed powder dry matter weight, mix the ammonium bicarbonate aqueous solution with the reed powder, seal, Keep at 100°C for 4h, carry out ammoniation treatment; soak the ammoniated reed powder and 45wt.% phosphoric acid solution at a mass ratio of 1:1.5 at 20°C for 8h; Carbonize and activate for 60 minutes, cool naturally to room temperature; wash the obtained activated carbon with deionized water until the pH is about 7, separate solid and liquid, and dry. The specific surface area is increased by 15% and the number of functional groups is increased by 18% compared with the traditional method of Comparative Example 3.
对照例3Comparative example 3
将芦苇洗涤、晾干、粉碎至40目,将芦苇粉末和45wt.%磷酸溶液按质量比1:1.5浸渍8h;浸渍物转入坩埚内置于马弗炉中,650℃下炭化活化90min,自然冷却至室温;将所得活性炭用去离子水洗涤至pH为7左右,固液分离、烘干。The reeds were washed, dried, and crushed to 40 mesh, and the reed powder and 45wt.% phosphoric acid solution were impregnated for 8 hours at a mass ratio of 1:1.5; Cool to room temperature; wash the obtained activated carbon with deionized water until the pH is about 7, separate solid and liquid, and dry.
表1:活性炭比表面积,孔径参数以及官能团数量。Table 1: Specific surface area of activated carbon, pore size parameters and number of functional groups.
经试验,芦竹、大叶荻获得同样好的效果。After testing, reed bamboo and Dayedi obtained the same good effect.
实施例4Example 4
利用实施例1和对比例1制得的活性炭应用在生活污水、化工废水和制药废水中,三种污水经过活性炭吸附前后的实验结果见表2。The activated carbon prepared in Example 1 and Comparative Example 1 was used in domestic sewage, chemical wastewater and pharmaceutical wastewater. The experimental results of the three kinds of sewage before and after activated carbon adsorption are shown in Table 2.
表2实施例1和对比例1的活性炭吸附效果The activated carbon adsorption effect of table 2 embodiment 1 and comparative example 1
废水中的残留有机物、残留悬浮物等通过活性炭的过滤、吸附实现污染物与水体的分离,表2可直观的看出采用实施例1的方法制备得到的活性炭的吸附效果明显优于对比例1的活性炭的吸附效果。The residual organic matter and residual suspended matter in the waste water are separated from the water body through the filtration and adsorption of activated carbon. It can be seen from Table 2 that the adsorption effect of the activated carbon prepared by the method of Example 1 is significantly better than that of Comparative Example 1. The adsorption effect of activated carbon.
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