CN115041137B - Preparation and application of a recyclable humic acid biomass carbon material - Google Patents
Preparation and application of a recyclable humic acid biomass carbon material Download PDFInfo
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- 239000004021 humic acid Substances 0.000 title claims abstract description 115
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 title claims abstract description 114
- 239000002028 Biomass Substances 0.000 title claims abstract description 51
- 239000003575 carbonaceous material Substances 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims abstract description 54
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 48
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 40
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims abstract description 36
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 35
- 229910000029 sodium carbonate Inorganic materials 0.000 claims abstract description 27
- 239000012190 activator Substances 0.000 claims abstract description 23
- 238000011282 treatment Methods 0.000 claims abstract description 22
- XMEVHPAGJVLHIG-FMZCEJRJSA-N chembl454950 Chemical compound [Cl-].C1=CC=C2[C@](O)(C)[C@H]3C[C@H]4[C@H]([NH+](C)C)C(O)=C(C(N)=O)C(=O)[C@@]4(O)C(O)=C3C(=O)C2=C1O XMEVHPAGJVLHIG-FMZCEJRJSA-N 0.000 claims abstract description 20
- FDZZZRQASAIRJF-UHFFFAOYSA-M malachite green Chemical compound [Cl-].C1=CC(N(C)C)=CC=C1C(C=1C=CC=CC=1)=C1C=CC(=[N+](C)C)C=C1 FDZZZRQASAIRJF-UHFFFAOYSA-M 0.000 claims abstract description 20
- 229940107698 malachite green Drugs 0.000 claims abstract description 20
- 229960004989 tetracycline hydrochloride Drugs 0.000 claims abstract description 20
- 239000007864 aqueous solution Substances 0.000 claims abstract description 18
- 239000002131 composite material Substances 0.000 claims abstract description 18
- 239000002253 acid Substances 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract description 4
- 238000005554 pickling Methods 0.000 claims abstract description 3
- 238000002156 mixing Methods 0.000 claims abstract 5
- 238000000034 method Methods 0.000 claims description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 238000005406 washing Methods 0.000 claims description 14
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000003242 anti bacterial agent Substances 0.000 claims description 7
- 229940088710 antibiotic agent Drugs 0.000 claims description 7
- 239000000975 dye Substances 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 238000009210 therapy by ultrasound Methods 0.000 claims description 7
- 230000007935 neutral effect Effects 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
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- 238000001914 filtration Methods 0.000 claims description 2
- 231100000719 pollutant Toxicity 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims 3
- 238000000227 grinding Methods 0.000 claims 2
- 230000003213 activating effect Effects 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 29
- 239000011148 porous material Substances 0.000 abstract description 9
- 238000002791 soaking Methods 0.000 abstract description 3
- 230000001172 regenerating effect Effects 0.000 abstract 1
- PUKLDDOGISCFCP-JSQCKWNTSA-N 21-Deoxycortisone Chemical compound C1CC2=CC(=O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@@](C(=O)C)(O)[C@@]1(C)CC2=O PUKLDDOGISCFCP-JSQCKWNTSA-N 0.000 description 8
- FCYKAQOGGFGCMD-UHFFFAOYSA-N Fulvic acid Natural products O1C2=CC(O)=C(O)C(C(O)=O)=C2C(=O)C2=C1CC(C)(O)OC2 FCYKAQOGGFGCMD-UHFFFAOYSA-N 0.000 description 8
- 239000002509 fulvic acid Substances 0.000 description 8
- 229940095100 fulvic acid Drugs 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 6
- 230000004913 activation Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
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- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 238000007781 pre-processing Methods 0.000 description 4
- 238000003763 carbonization Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 2
- 244000144974 aquaculture Species 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- JLDCNMJPBBKAHH-UHFFFAOYSA-N sodium;(4-aminophenyl)sulfonyl-pyrimidin-2-ylazanide Chemical compound [Na+].C1=CC(N)=CC=C1S(=O)(=O)[N-]C1=NC=CC=N1 JLDCNMJPBBKAHH-UHFFFAOYSA-N 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000002604 ultrasonography Methods 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 108010077805 Bacterial Proteins Proteins 0.000 description 1
- 241001000394 Diaphania hyalinata Species 0.000 description 1
- 206010028400 Mutagenic effect Diseases 0.000 description 1
- 241000907663 Siproeta stelenes Species 0.000 description 1
- 239000004098 Tetracycline Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
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- 239000003610 charcoal Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
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- 230000018109 developmental process Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 231100000243 mutagenic effect Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
- 231100000175 potential carcinogenicity Toxicity 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 231100000378 teratogenic Toxicity 0.000 description 1
- 230000003390 teratogenic effect Effects 0.000 description 1
- 229960002180 tetracycline Drugs 0.000 description 1
- 229930101283 tetracycline Natural products 0.000 description 1
- 235000019364 tetracycline Nutrition 0.000 description 1
- 150000003522 tetracyclines Chemical class 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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Abstract
Description
技术领域technical field
本发明涉及有机废水处理技术领域,具体涉及一种可循环使用的腐殖酸生物质碳材料的制备及应用。The invention relates to the technical field of organic wastewater treatment, in particular to the preparation and application of a recyclable humic acid biomass carbon material.
背景技术Background technique
近年来,由于社会的快速发展,水污染已经成为一个日益严重的问题,染料和抗生素是废水污染的主要来源之一。对于废水中有机染料和抗生素的吸附降解已成为研究热点。处理水污染的常用方法包括化学絮凝、膜过滤、反渗透、离子交换、吸附及电化学过程等,其中吸附法具有操作简单、成本低、效率高的优点,成为了一种流行的废水处理方法。In recent years, due to the rapid development of society, water pollution has become an increasingly serious problem, and dyes and antibiotics are one of the main sources of wastewater pollution. The adsorption and degradation of organic dyes and antibiotics in wastewater has become a research hotspot. Common methods for treating water pollution include chemical flocculation, membrane filtration, reverse osmosis, ion exchange, adsorption, and electrochemical processes, etc. Among them, the adsorption method has the advantages of simple operation, low cost, and high efficiency, and has become a popular wastewater treatment method. .
孔雀石绿曾被广泛用于预防和治疗各类水产动物的水霉病、鳃霉病和小瓜虫等疾病,同时也用作丝绸、皮革和纸张的染料,但是孔雀石绿具有潜在的致癌、致畸、致突变的作用,无公害水产养殖领域国家明令禁止添加。Malachite green has been widely used to prevent and treat diseases such as saprolegniasis, gill mold and melon worms of various aquatic animals. It is also used as a dye for silk, leather and paper, but malachite green has potential carcinogenicity. , teratogenic and mutagenic effects, and the state explicitly prohibits adding it in the field of pollution-free aquaculture.
四环类抗生素是一种广谱抗生素,能够抑制细菌蛋白质的合成,被广泛应用与医药行业、畜牧业和水产养殖业,但四环类抗生素很难被完全降解,其降解中间产物往往具有很大的毒性,且普遍残留会造成抗药性菌群的富集及抗性基因的产生。在采用生物质碳吸附处理盐酸四环素时,往往出现吸附量低、团聚、分离困难等技术问题,导致该方法在吸附盐酸四环素中的应用受阻。Tetracyclic antibiotics are broad-spectrum antibiotics that can inhibit the synthesis of bacterial proteins and are widely used in the pharmaceutical industry, animal husbandry and aquaculture. However, tetracyclic antibiotics are difficult to be completely degraded, and their degradation intermediates often have very Large toxicity, and the general residue will cause the enrichment of drug-resistant bacteria and the production of resistance genes. When using biomass carbon adsorption to treat tetracycline hydrochloride, there are often technical problems such as low adsorption capacity, agglomeration, and separation difficulties, which hinder the application of this method in the adsorption of tetracycline hydrochloride.
腐殖酸具有较强的离子交换能力、吸附能力和脱除杂质的能力,因此广泛应用于废水处理领域,其可以作为阳离子染料脱色剂处理阳离子印染废水。现有技术中有直接使用腐殖酸对孔雀石绿及盐酸四环素进行吸附降解的,但是降解效率不高,且稳定性较差。已有文献报道采用黄腐酸经高温碳化后,采用氢氧化钠为活化剂,高温活化制备的生物质碳,比表面积达到2922m2/g,对于亮绿和磺胺嘧啶钠盐达到吸附量分别为2250mg/g和941mg/g。但是该方法制备的生物质碳用于处理孔雀石绿和盐酸四环素时的吸附性能较差,基于此,需要进一步改进,制备出对孔雀石绿和盐酸四环素具有优异吸附性能的腐殖酸生物质碳材料。Humic acid has strong ion exchange capacity, adsorption capacity and ability to remove impurities, so it is widely used in the field of wastewater treatment. It can be used as a cationic dye decolorizer to treat cationic printing and dyeing wastewater. In the prior art, humic acid is directly used to adsorb and degrade malachite green and tetracycline hydrochloride, but the degradation efficiency is not high and the stability is poor. It has been reported in the literature that after high-temperature carbonization of fulvic acid and sodium hydroxide as an activator, the biomass carbon prepared by high-temperature activation has a specific surface area of 2922m 2 /g, and the adsorption capacity of bright green and sulfadiazine sodium salt is respectively 2250mg/g and 941mg/g. However, the biomass carbon prepared by this method has poor adsorption performance when used to treat malachite green and tetracycline hydrochloride. Based on this, further improvement is needed to prepare humic acid biomass with excellent adsorption performance for malachite green and tetracycline hydrochloride. carbon material.
发明内容Contents of the invention
本发明目的在于提供一种可循环使用的腐殖酸生物质碳材料的制备方法。The purpose of the present invention is to provide a method for preparing a recyclable humic acid biomass carbon material.
本发明另一目的在于提供上述腐殖酸生物质碳材料的应用。Another object of the present invention is to provide the application of the humic acid biomass carbon material.
本发明目的通过如下技术方案实现:The object of the invention is achieved through the following technical solutions:
一种可循环使用的腐殖酸生物质碳材料的制备方法,其特征在于:包括碳材料的制备和再生处理,所述碳材料制备是将腐殖酸加入碳酸钠水溶液中,超声处理,在处理后的腐殖酸中加入双氧水混合,进行第一次高温处理,得到腐殖酸碳,腐殖酸碳经氢氧化钾和氢氧化钠作为复合活化剂处理,然后进行第二次高温处理,再进行酸洗、干燥,所述腐殖酸中黑腐酸质量占比为85%以上。A kind of preparation method of recyclable humic acid biomass carbon material, it is characterized in that: comprise the preparation of carbon material and regeneration treatment, described carbon material preparation is that humic acid is added in sodium carbonate aqueous solution, ultrasonic treatment, in The treated humic acid is mixed with hydrogen peroxide, and the first high-temperature treatment is carried out to obtain humic acid carbon. The humic acid carbon is treated with potassium hydroxide and sodium hydroxide as a composite activator, and then the second high-temperature treatment is carried out. Pickling and drying are then carried out, and the mass ratio of black humic acid in the humic acid is more than 85%.
进一步,上述碳酸钠水溶液的浓度为0.6-1mmol/L,超声处理的功率为60-100W。Further, the concentration of the above sodium carbonate aqueous solution is 0.6-1mmol/L, and the power of the ultrasonic treatment is 60-100W.
黑腐酸的分子量较大,活性较低,直接进行高温碳化,再进行活化,制备的生物碳的理化性能较差,整体吸附性能不理想。Black humic acid has a large molecular weight and low activity. If it is directly carbonized at high temperature and then activated, the physical and chemical properties of the prepared biochar are poor, and the overall adsorption performance is not ideal.
本发明采用碳酸钠结合超声进行预处理,通过超声活化碳酸钠,去除少量的黑腐酸,达到松动黑腐酸的稳固结构的作用,再加入双氧水,通过双氧水的氧化性,在黑腐酸结构松动的基础上进一步断裂黑腐酸的分子链,在第一次高温处理过程中,碳酸钠作为活化剂对经过双氧水氧化处理后的腐殖酸起到了活化造孔的作用,增加了碳材料表面的活性基团,随后采用氢氧化钾和氢氧化钠,在第一次活化造孔的基础上进一步调节了对腐殖酸碳的活化程度,并调节了其表面官能团的变化趋势,从而制备出对孔雀石绿和盐酸四环素具有高效吸附性能,且吸附稳定性优异的生物质碳材料。The present invention uses sodium carbonate combined with ultrasound for pretreatment, activates sodium carbonate through ultrasound, removes a small amount of black humic acid, and achieves the effect of loosening the stable structure of black humic acid, and then adds hydrogen peroxide, through the oxidation of hydrogen peroxide, in the structure of black humic acid On the basis of loosening, the molecular chain of black humic acid is further broken. In the first high-temperature treatment process, sodium carbonate acts as an activator to activate pore-forming effect on humic acid after hydrogen peroxide oxidation treatment, increasing the carbon material surface. The active group of the active group, followed by potassium hydroxide and sodium hydroxide, on the basis of the first activation of pore-forming, further adjusted the activation degree of humic acid carbon, and adjusted the change trend of its surface functional groups, thus preparing A biomass carbon material with high adsorption performance for malachite green and tetracycline hydrochloride and excellent adsorption stability.
优选的,上述碳酸钠水溶液的浓度为0.8mmol/L,超声处理的功率为80W。Preferably, the concentration of the above-mentioned sodium carbonate aqueous solution is 0.8mmol/L, and the power of the ultrasonic treatment is 80W.
进一步,上述双氧水的质量分数为20%,腐殖酸、碳酸钠水溶液和双氧水的用量关系为10g:15-20mL:4-5mL。Further, the mass fraction of the above-mentioned hydrogen peroxide is 20%, and the dosage relationship of humic acid, sodium carbonate aqueous solution and hydrogen peroxide is 10g: 15-20mL: 4-5mL.
进一步,上述第一次高温处理具体是预处理后的腐殖酸置于氮气保护下,以2-3℃/min升温至550-600℃,保温40-50min,得腐殖酸碳。Furthermore, the above first high temperature treatment is specifically to place the pretreated humic acid under nitrogen protection, raise the temperature to 550-600°C at 2-3°C/min, and keep it warm for 40-50min to obtain humic acid carbon.
进一步,上述第二次高温处理将腐殖酸碳与复合活化剂按照质量比为1:2-3混合研磨,然后置于管式炉中,按照6-8℃/min升温至600-650℃,保温60min;保温结束后,经盐酸洗涤,再用去离子水洗涤至中性。Further, in the above second high temperature treatment, the humic acid carbon and the composite activator are mixed and ground according to the mass ratio of 1:2-3, and then placed in a tube furnace, and the temperature is raised to 600-650°C at 6-8°C/min , keep warm for 60min; after the keep warm, wash with hydrochloric acid, then wash with deionized water until neutral.
进一步,上述复合活化剂中氢氧化钾和氢氧化钠质量比为1:1。Further, the mass ratio of potassium hydroxide and sodium hydroxide in the above composite activator is 1:1.
在制备过程中尝试采用氢氧化钠作为活化剂进行活化,虽然能提高生物质碳材料的比表面积和孔容积等物理性能,但是制备出来的生物质碳对于孔雀石绿和盐酸四环素的吸附性较差,而采用氢氧化钠和氢氧化钾复合活化制备的生物质碳材料,对于孔雀石绿和盐酸四环素的吸附性能具有显著的提升。In the preparation process, sodium hydroxide was used as an activator for activation. Although the specific surface area and pore volume of the biomass carbon material can be improved, the adsorption of the prepared biomass carbon to malachite green and tetracycline hydrochloride is relatively low. Poor, while the biomass carbon material prepared by the combined activation of sodium hydroxide and potassium hydroxide has a significant improvement in the adsorption performance of malachite green and tetracycline hydrochloride.
一种腐殖酸生物质碳材料的制备方法,其特征在于,按如下步骤进行:A kind of preparation method of humic acid biomass carbon material is characterized in that, carries out as follows:
步骤1:预处理Step 1: Preprocessing
在粉末中加入浓度为0.6-1mmol/L的碳酸钠水溶液,在功率为60-100W下超声处理40-60min,过滤后在固体组分中加入质量分数为20%的双氧水搅拌混合,所述腐殖酸中黑腐酸占比为85%,腐殖酸、碳酸钠水溶液和双氧水的用量比为10g:15-20mL:4-5mL;Add a sodium carbonate aqueous solution with a concentration of 0.6-1mmol/L to the powder, and ultrasonically treat it for 40-60min at a power of 60-100W. The proportion of black humic acid in humic acid is 85%, and the dosage ratio of humic acid, sodium carbonate aqueous solution and hydrogen peroxide is 10g: 15-20mL: 4-5mL;
步骤2:第一次高温Step 2: First High Temperature
将预处理后的腐殖酸置于管式炉中,在氮气保护下,以2-3℃/min升温至550-600℃,保温40-50min,得腐殖酸碳;Put the pretreated humic acid in a tube furnace, and under the protection of nitrogen, raise the temperature to 550-600°C at 2-3°C/min, and keep it warm for 40-50min to obtain humic acid carbon;
步骤3:第二次高温Step 3: Second High Temperature
将腐殖酸碳与复合活化剂按照质量比为1:2-3混合研磨,然后置于管式炉中,按照6-8℃/min升温至600-650℃,保温60min;保温结束后,经盐酸洗涤,再用去离子水洗涤至中性,复合活化剂是KOH和NaOH按照质量比为1:1组成。The humic acid carbon and the composite activator are mixed and ground according to the mass ratio of 1:2-3, then placed in a tube furnace, heated to 600-650°C at 6-8°C/min, and kept for 60 minutes; after the heat preservation is completed, After washing with hydrochloric acid, and then washing with deionized water until neutral, the composite activator is composed of KOH and NaOH in a mass ratio of 1:1.
所述再生处理,是将上述腐殖酸生物质炭吸附污染物完成后,从废水中进行离心分离,烘干后置于管式炉中,以2-3℃/min升温至550-600℃,保温40-50min。The regeneration treatment is to centrifuge the above-mentioned humic acid biomass charcoal from the waste water after the pollutants are adsorbed, put it in a tube furnace after drying, and raise the temperature to 550-600°C at 2-3°C/min , keep warm for 40-50min.
上述腐殖酸生物质碳材料的应用,用于吸附有机染料和抗生素。The application of the above-mentioned humic acid biomass carbon material is used to adsorb organic dyes and antibiotics.
具体的,上述腐殖酸生物质碳材料用于吸附孔雀石绿和盐酸四环素。Specifically, the humic acid biomass carbon material is used to adsorb malachite green and tetracycline hydrochloride.
本发明具有如下技术效果:The present invention has following technical effect:
本发明制备的腐殖酸生物质碳材料具有优异理化性质,比表面积达到2376m2/g,孔容积达到2.27cm3/g,表面具有丰富的活性基团,对于孔雀石绿和盐酸四环素吸附量达到1059.4mg/g和872.3mg/g,在循环使用5次后,腐殖酸生物质碳材料对于孔雀石绿和盐酸四环素的去除率依然达到69.7%和58.6%,具有优异的循环稳定性。The humic acid biomass carbon material prepared by the invention has excellent physical and chemical properties, the specific surface area reaches 2376m 2 /g, the pore volume reaches 2.27cm 3 /g, the surface has abundant active groups, and the adsorption capacity for malachite green and tetracycline hydrochloride Reaching 1059.4mg/g and 872.3mg/g, after 5 times of recycling, the removal rate of humic acid biomass carbon material for malachite green and tetracycline hydrochloride still reached 69.7% and 58.6%, which has excellent cycle stability.
附图说明Description of drawings
图1:本发明中腐殖酸原料、碳化后的腐殖酸碳和腐殖酸生物质碳材料成品的扫描电镜图。Fig. 1: scanning electron micrograph of humic acid raw material, carbonized humic acid carbon and humic acid biomass carbon material finished product in the present invention.
具体实施方式Detailed ways
下面通过实施例对本发明进行具体的描述,有必要在此指出的是,以下实施例只用于对本发明进行进一步说明,不能理解为对本发明保护范围的限制,该领域的技术人员可以根据上述本发明内容对本发明作出一些非本质的改进和调整。The present invention is specifically described by the following examples. It is necessary to point out that the following examples are only used to further illustrate the present invention, and cannot be interpreted as limiting the protection scope of the present invention. Those skilled in the art can according to the above-mentioned description SUMMARY OF THE INVENTION Some non-essential improvements and adjustments are made to the present invention.
按照文献“Preparation of biomass carbon material based on fulvic acidand its application in dye and antibiotic treatments,Xu Qiao等”中记载的方案制备黄腐酸生物质碳比表面积为2250m2/g,孔容积为1.8cm3/g,在pH为3时,对磺胺嘧啶钠盐最大吸附量为941mg/g,在pH为9时对亮绿的最大吸附量为2250mg/g,但是将该黄腐酸生物质碳用于吸附孔雀石绿和盐酸四环素时,吸附性能不高,仅为388.4mg/g和363.5mg/g,且循环使用5个周期后,对孔雀石绿和盐酸四环素去除率仅仅为第一次的31.4%和27.9%。According to the protocol recorded in the document "Preparation of biomass carbon material based on fulvic acid and its application in dye and antibiotic treatments, Xu Qiao, etc.", the specific surface area of fulvic acid biomass carbon is 2250m 2 /g, and the pore volume is 1.8cm 3 / g, when the pH is 3, the maximum adsorption capacity for sulfadiazine sodium salt is 941 mg/g, and the maximum adsorption capacity for bright green is 2250 mg/g when the pH is 9, but the fulvic acid biomass carbon is used for adsorption For malachite green and tetracycline hydrochloride, the adsorption performance is not high, only 388.4mg/g and 363.5mg/g, and after 5 cycles of recycling, the removal rate of malachite green and tetracycline hydrochloride is only 31.4% of the first time and 27.9%.
实施例1Example 1
一种腐殖酸生物质碳材料的制备方法,按如下步骤进行:A preparation method of humic acid biomass carbon material, carried out as follows:
步骤1:预处理Step 1: Preprocessing
在粉末中加入浓度为0.8mmol/L的碳酸钠水溶液,在功率为80W下超声处理60min,过滤后在固体组分中加入质量分数为20%的双氧水搅拌混合,所述腐殖酸中黑腐酸占比为85%,腐殖酸、碳酸钠水溶液和双氧水的用量比为10g:20mL:5mL;Add a sodium carbonate aqueous solution with a concentration of 0.8mmol/L to the powder, and ultrasonically treat it for 60min at a power of 80W. The proportion of acid is 85%, and the dosage ratio of humic acid, sodium carbonate aqueous solution and hydrogen peroxide is 10g: 20mL: 5mL;
步骤2:第一次高温Step 2: First High Temperature
将预处理后的腐殖酸置于管式炉中,在氮气保护下,以2℃/min升温至600℃,保温40min,得腐殖酸碳;Put the pretreated humic acid in a tube furnace, and under the protection of nitrogen, raise the temperature to 600°C at 2°C/min and keep it warm for 40min to obtain humic acid carbon;
步骤3:第二次高温Step 3: Second High Temperature
将腐殖酸碳与复合活化剂按照质量比为1:2混合研磨,然后置于管式炉中,按照8℃/min升温至650℃,保温60min;保温结束后,经质量分数为10%的盐酸洗涤,再用去离子水洗涤至中性,复合活化剂是KOH和NaOH按照质量比为1:1组成。The humic acid carbon and the composite activator are mixed and ground according to the mass ratio of 1:2, and then placed in a tube furnace, heated to 650°C at 8°C/min, and kept for 60min; Hydrochloric acid washing, and then washing with deionized water to neutrality, the composite activator is composed of KOH and NaOH according to the mass ratio of 1:1.
实施例2Example 2
一种腐殖酸生物质碳材料的制备方法,按如下步骤进行:A preparation method of humic acid biomass carbon material, carried out as follows:
步骤1:预处理Step 1: Preprocessing
在粉末中加入浓度为1mmol/L的碳酸钠水溶液,在功率为60W下超声处理40min,过滤后在固体组分中加入质量分数为20%的双氧水搅拌混合,所述腐殖酸中黑腐酸占比为85%,腐殖酸、碳酸钠水溶液和双氧水的用量比为10g:15mL:4mL;Add a sodium carbonate aqueous solution with a concentration of 1mmol/L to the powder, and ultrasonically treat it for 40min at a power of 60W. After filtering, add hydrogen peroxide with a mass fraction of 20% in the solid component and stir and mix. Among the humic acids, black humic acid The proportion is 85%, and the dosage ratio of humic acid, sodium carbonate aqueous solution and hydrogen peroxide is 10g: 15mL: 4mL;
步骤2:第一次高温Step 2: First High Temperature
将预处理后的腐殖酸置于管式炉中,在氮气保护下,以3℃/min升温至550℃,保温50min,得腐殖酸碳;Put the pretreated humic acid in a tube furnace, and under the protection of nitrogen, raise the temperature to 550°C at 3°C/min and keep it warm for 50min to obtain humic acid carbon;
步骤3:第二次高温Step 3: Second High Temperature
将腐殖酸碳与复合活化剂按照质量比为1:3混合研磨,然后置于管式炉中,按照6℃/min升温至600℃,保温60min;保温结束后,经质量分数为10%的盐酸洗涤,再用去离子水洗涤至中性,复合活化剂是KOH和NaOH按照质量比为1:1组成。Mix and grind the humic acid carbon and the composite activator according to the mass ratio of 1:3, then place it in a tube furnace, raise the temperature to 600°C at 6°C/min, and keep it warm for 60 minutes; Hydrochloric acid washing, and then washing with deionized water to neutrality, the composite activator is composed of KOH and NaOH according to the mass ratio of 1:1.
实施例3Example 3
一种腐殖酸生物质碳材料的制备方法,按如下步骤进行:A preparation method of humic acid biomass carbon material, carried out as follows:
步骤1:预处理Step 1: Preprocessing
在粉末中加入浓度为0.6mmol/L的碳酸钠水溶液,在功率为100W下超声处理50min,过滤后在固体组分中加入质量分数为20%的双氧水搅拌混合,所述腐殖酸中黑腐酸占比为85%,腐殖酸、碳酸钠水溶液和双氧水的用量比为10g:16mL:4mL;Add a sodium carbonate aqueous solution with a concentration of 0.6mmol/L to the powder, and ultrasonically treat it for 50min at a power of 100W. The proportion of acid is 85%, and the dosage ratio of humic acid, sodium carbonate aqueous solution and hydrogen peroxide is 10g: 16mL: 4mL;
步骤2:第一次高温Step 2: First High Temperature
将预处理后的腐殖酸置于管式炉中,在氮气保护下,以2℃/min升温至580℃,保温45min,得腐殖酸碳;Put the pretreated humic acid in a tube furnace, and under the protection of nitrogen, raise the temperature to 580°C at 2°C/min and keep it warm for 45min to obtain humic acid carbon;
步骤3:第二次高温Step 3: Second High Temperature
将腐殖酸碳与复合活化剂按照质量比为1:2.5混合研磨,然后置于管式炉中,按照7℃/min升温至620℃,保温60min;保温结束后,经质量分数为10%的盐酸洗涤,再用去离子水洗涤至中性,复合活化剂是KOH和NaOH按照质量比为1:1组成。Mix and grind the humic acid carbon and the composite activator according to the mass ratio of 1:2.5, then place it in a tube furnace, raise the temperature to 620°C at 7°C/min, and keep it warm for 60 minutes; Hydrochloric acid washing, and then washing with deionized water to neutrality, the composite activator is composed of KOH and NaOH according to the mass ratio of 1:1.
本发明各实施例制备的腐殖酸生物质碳对于孔雀石绿和盐酸四环素的吸附性能,以及循环稳定性如表1所示。The humic acid biomass carbon prepared by each embodiment of the present invention has the adsorption performance and cycle stability of malachite green and tetracycline hydrochloride as shown in Table 1.
表1:Table 1:
本发明制备的腐殖酸生物质碳对于孔雀石绿和盐酸四环素具有优异的吸附性能,第一次吸附时去除率分别达到90.7%和88.2%,经5次循环吸附使用后,依然能保持在58.4%和50.5%以上,具有优异的循环稳定性。The humic acid biomass carbon prepared by the present invention has excellent adsorption performance for malachite green and tetracycline hydrochloride, and the removal rate reaches 90.7% and 88.2% respectively during the first adsorption, and can still be maintained at 58.4% and above 50.5%, with excellent cycle stability.
对比例1Comparative example 1
与实施例1不同的是,将实施例1中的腐殖酸浸泡碳酸钠后,再加入双氧水,进行第一次高温处理,采用活化剂为NaOH,其余步骤与实施例1相同。The difference from Example 1 is that after the humic acid in Example 1 is soaked in sodium carbonate, hydrogen peroxide is added to carry out the first high-temperature treatment, and the activator is NaOH, and the rest of the steps are the same as in Example 1.
对比例2Comparative example 2
与实施例1不同的是,在进行第一次高温处理后,采用活化剂为NaOH,然后在相同的参数下进行二次高温处理,其余步骤与实施例1相同。The difference from Example 1 is that after the first high-temperature treatment, the activator is NaOH, and then a second high-temperature treatment is performed under the same parameters, and the rest of the steps are the same as in Example 1.
对比例3Comparative example 3
与实施例1不同的是,将实施例1中的腐殖酸在碳酸钠溶液中,通过在外光照处理后,直接进行高温处理,其余步骤与实施例1相同。The difference from Example 1 is that the humic acid in Example 1 is treated in sodium carbonate solution, and then directly subjected to high temperature treatment after external light treatment, and the rest of the steps are the same as in Example 1.
对比例4Comparative example 4
采用黄腐酸占比为90%的腐殖酸作为原料,按照本发明方法制备。Humic acid with a proportion of fulvic acid of 90% is used as a raw material and prepared according to the method of the invention.
各对比例制备的生物质碳对于孔雀石绿和盐酸四环素的吸附性能如表2所示。The adsorption properties of the biomass carbon prepared in each comparative example for malachite green and tetracycline hydrochloride are shown in Table 2.
表2:Table 2:
由于对比例1中采用分子量较大的黑腐酸为原料,单独碳酸钠浸泡腐殖酸对于腐殖酸碳化前结构基本没有任何改变,仅仅是进行碳化时参与造孔,再加入双氧水,对于结构稳固的黑腐酸的氧化作用较弱,黑腐酸的活性较低,制备的生物质碳比表面积和孔容积均不高,对于孔雀石速率和盐酸四环素的吸附能力有限。而碳酸钠浸泡时结合超声处理后,腐殖酸中极少量的黑腐酸被降解,松动了黑腐酸稳固的整体结构,在高温碳化过程中,碳酸钠作为第一道活化剂,同步活化造孔,在后续采用复合碱进行二次造孔,制备的生物质碳比表面积和孔容积等均有显著提高,且表面官能团也发生了变化,使其对于孔雀石绿和运算四环素的吸附性能得到一定的提高。而在本发明的基础上,将以黑腐酸为主的腐殖酸更换为以分子量较小的黄腐酸为主的腐殖酸,在紫外光下采用碳酸钠浸泡,黄腐酸的降解程度不可控,导致其原始结构被破坏,在后续加入双氧水时,双氧水的强氧化性再一次破坏黄腐酸内部结构,导致最终制备的生物质碳比表面积和孔容积均呈下降趋势,吸附性能极差,在循环吸附过程中,吸附性能也衰减严重。Since black humic acid with a relatively large molecular weight was used as raw material in Comparative Example 1, soaking humic acid in sodium carbonate alone did not change the structure of humic acid before carbonization. The oxidation of stable black humic acid is weak, the activity of black humic acid is low, the specific surface area and pore volume of the prepared biomass carbon are not high, and the adsorption capacity for malachite rate and tetracycline hydrochloride is limited. However, after soaking in sodium carbonate combined with ultrasonic treatment, a very small amount of black humic acid in humic acid is degraded, loosening the solid overall structure of black humic acid. During the high-temperature carbonization process, sodium carbonate is used as the first activator to activate simultaneously Pore making, followed by secondary pore making with compound alkali, the specific surface area and pore volume of the prepared biomass carbon have been significantly improved, and the surface functional groups have also changed, making it more effective for the adsorption of malachite green and tetracycline. Get a certain improvement. And on the basis of the present invention, the humic acid based on black humic acid is replaced by the humic acid based on fulvic acid with a smaller molecular weight, soaked in sodium carbonate under ultraviolet light, the degradation of fulvic acid The degree is uncontrollable, leading to the destruction of its original structure. When hydrogen peroxide is added later, the strong oxidation of hydrogen peroxide destroys the internal structure of fulvic acid again, resulting in a downward trend in the specific surface area and pore volume of the final prepared biomass carbon. Extremely poor, in the process of cyclic adsorption, the adsorption performance also decays seriously.
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