CN104984734A - Production method for hydrothermal bamboo based biomass carbon adsorption material catalyzed by inorganic strong acid - Google Patents
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- 235000017166 Bambusa arundinacea Nutrition 0.000 title claims abstract description 63
- 235000017491 Bambusa tulda Nutrition 0.000 title claims abstract description 63
- 241001330002 Bambuseae Species 0.000 title claims abstract description 63
- 235000015334 Phyllostachys viridis Nutrition 0.000 title claims abstract description 63
- 239000011425 bamboo Substances 0.000 title claims abstract description 63
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 29
- 239000000463 material Substances 0.000 title claims abstract description 17
- 239000002253 acid Substances 0.000 title claims abstract description 16
- 239000002028 Biomass Substances 0.000 title claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 9
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 9
- 239000003610 charcoal Substances 0.000 claims abstract description 18
- 239000000843 powder Substances 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 239000003513 alkali Substances 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- 230000007935 neutral effect Effects 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 150000007529 inorganic bases Chemical class 0.000 claims description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 3
- 239000005977 Ethylene Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 150000007513 acids Chemical class 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 5
- 125000002091 cationic group Chemical group 0.000 abstract description 4
- 239000000975 dye Substances 0.000 abstract description 4
- 239000003463 adsorbent Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000002378 acidificating effect Effects 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000001027 hydrothermal synthesis Methods 0.000 abstract 1
- 238000009700 powder processing Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 11
- 229960000907 methylthioninium chloride Drugs 0.000 description 11
- 238000003763 carbonization Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000004042 decolorization Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000010675 chips/crisps Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003933 environmental pollution control Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 235000021190 leftovers Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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Abstract
本发明公开了一种无机强酸催化水热竹基生物质炭吸附材料的生产方法,其步骤包括:将竹粉加工剩余物粉碎成60-80目竹粉,再对竹粉在强酸性条件下进行水热反应制备水热竹炭;将上述得到的水热竹炭用无机碱活化后即得到活化水热竹炭吸附材料。本发明工艺简单、原料成本低、吸附量大。本方法制得的吸附材料可以应用于阳离子染料的吸附治理,并具有良好的处理效果。本发明不仅实现了竹材加工剩余物资源的回收利用,并且得到了廉价、高效的新型吸附剂,促进环保事业的发展。
The invention discloses a production method of an inorganic strong acid catalyzed hydrothermal bamboo-based biomass carbon adsorption material. The steps include: crushing the bamboo powder processing residue into 60-80 mesh bamboo powder, and then treating the bamboo powder under strong acidic conditions. The hydrothermal reaction is carried out to prepare the hydrothermal bamboo charcoal; the activated hydrothermal bamboo charcoal adsorption material is obtained after the hydrothermal bamboo charcoal obtained above is activated with an inorganic alkali. The invention has the advantages of simple process, low raw material cost and large adsorption capacity. The adsorption material prepared by the method can be applied to the adsorption and treatment of cationic dyes, and has good treatment effect. The invention not only realizes the recycling and utilization of bamboo processing residue resources, but also obtains a cheap and efficient novel adsorbent, and promotes the development of environmental protection.
Description
技术领域technical field
本发明属于生物质炭吸附材料制备以及环境污染治理领域,特别涉及一种以竹粉为主要材料进行水热炭化制备生物质吸附材料的生产方法,具体是无机强酸催化水热竹基生物质炭吸附材料的生产方法。The invention belongs to the field of preparation of biomass charcoal adsorption materials and environmental pollution control, in particular to a production method of using bamboo powder as the main material to carry out hydrothermal carbonization to prepare biomass adsorption materials, specifically inorganic strong acid catalyzed hydrothermal bamboo-based biomass charcoal Methods of production of adsorbent materials.
背景技术Background technique
全国第八次森林资源清查统计显示,我国竹林面积有601万公顷,竹林面积、竹材蓄积、竹制品产量和出口量均居世界第一,竹加工技术和竹产品创新能力处于世界先进水平。但是,目前我国竹材资源的利用率偏低,一次利用率为20%-50%,每年有大量的竹材加工剩余物如竹屑、锯末、边角料等,以及1180万吨以上尚未利用的杂竹和小径竹。因此,急需开发清洁高效的农林废弃物资源化利用技术。Statistics from the Eighth National Forest Resources Inventory show that my country's bamboo forest area is 6.01 million hectares, and the bamboo forest area, bamboo stock, bamboo product output and export volume all rank first in the world, and bamboo processing technology and bamboo product innovation capabilities are at the world's advanced level. However, at present, the utilization rate of bamboo resources in my country is on the low side, and the primary utilization rate is 20%-50%. Trail bamboo. Therefore, there is an urgent need to develop clean and efficient resource utilization technologies for agricultural and forestry waste.
发明内容Contents of the invention
本发明的目的在于提供一种吸附性能良好的无机强酸催化水热竹基生物质炭吸附材料的生产方法。The object of the present invention is to provide a production method of inorganic strong acid catalyzed hydrothermal bamboo-based biomass carbon adsorption material with good adsorption performance.
解决上述技术问题所采用的技术方案是:The technical scheme adopted to solve the above-mentioned technical problems is:
一种无机强酸催化水热竹基生物质炭吸附材料的生产方法,按下列步骤进行:A kind of production method of inorganic strong acid catalyzed hydrothermal bamboo-based biomass carbon adsorption material is carried out according to the following steps:
(1)将包括竹屑、竹片、边角料、竹丝在内的原料粉碎成60-80目竹粉;(1) raw materials including bamboo chips, bamboo slices, scraps, bamboo silk are pulverized into 60-80 order bamboo powder;
(2)水热竹炭制备:将60重量份的60-80目竹粉和6-24重量份无机强酸置于200-300重量份的水中,在室温下搅拌混合均匀后置于带聚四氟乙烯内衬的不锈钢反应釜中,然后在180-240℃条件下反应6-24小时、自然冷却、抽滤、洗涤至中性后烘干,即得到水热竹炭;(2) Preparation of hydrothermal bamboo charcoal: 60 parts by weight of 60-80 mesh bamboo powder and 6-24 parts by weight of inorganic strong acid are placed in 200-300 parts by weight of water, stirred and mixed at room temperature In a stainless steel reaction kettle lined with ethylene, react at 180-240°C for 6-24 hours, cool naturally, filter with suction, wash until neutral and then dry to obtain hydrothermal bamboo charcoal;
(3)活化水热竹炭制备:将步骤(2)得到的水热竹炭与2.5-6重量份无机碱和200-300重量份水混合,室温搅拌0.5-3h后,抽滤、洗涤至中性后烘干。(3) Preparation of activated hydrothermal bamboo charcoal: mix the hydrothermal bamboo charcoal obtained in step (2) with 2.5-6 parts by weight of inorganic alkali and 200-300 parts by weight of water, stir at room temperature for 0.5-3h, then suction filter and wash until neutral Then dry.
所述无机强酸催化水热竹基生物质炭吸附材料的生产方法,步骤(2)中所说的无机强酸为浓盐酸或浓硫酸中任一种或两种强酸的混合物。The production method of the described inorganic strong acid catalyzed hydrothermal bamboo-based biomass carbon adsorption material, the inorganic strong acid mentioned in the step (2) is any one of concentrated hydrochloric acid or concentrated sulfuric acid or a mixture of two strong acids.
所述无机强酸催化水热竹基生物质炭吸附材料的生产方法,步骤(3)中所述的无机碱为氢氧化钠、氢氧化钾任一种或两种无机碱的混合物。In the production method of the inorganic strong acid catalyzed hydrothermal bamboo-based biomass carbon adsorption material, the inorganic base described in step (3) is either sodium hydroxide, potassium hydroxide or a mixture of two inorganic bases.
本发明采用无机强酸作为水热炭化的催化剂,使竹粉炭化程度变大,炭化产物密度变小。制取的竹基生物质炭吸附材料比对应的无催化剂制备的竹基生物质炭对阳离子染料亚甲基蓝的吸附能力明显提高,对阳离子染料亚甲基蓝的吸附容量可以达到540mg/g以上,对高浓度的400mg/L亚甲基蓝,固液比为0.8g/L时,脱色率(去除率)可以达99.8%以上,而对应的无催化剂制备的竹基生物质炭对亚甲基蓝的饱和吸附容量仅为288mg/g。将作为竹材加工剩余物、环境污染物改性成吸附率高的水热竹炭吸附材料,对阳离子染料具有良好的吸附性能,有利于应用到工业废水的处理等领域,且变废为宝,极大地提高了竹粉的附加值。The invention adopts strong inorganic acid as the catalyst of hydrothermal carbonization, so that the degree of carbonization of bamboo powder is increased and the density of carbonization products is reduced. Compared with the corresponding bamboo-based biochar prepared without catalyst, the prepared bamboo-based biochar adsorption material has a significantly higher adsorption capacity for the cationic dye methylene blue, and the adsorption capacity for the cationic dye methylene blue can reach more than 540mg/g. 400mg/L methylene blue, when the solid-to-liquid ratio is 0.8g/L, the decolorization rate (removal rate) can reach more than 99.8%, while the corresponding bamboo-based biochar prepared without catalyst has a saturated adsorption capacity of methylene blue only 288mg/g . Modification of bamboo processing residues and environmental pollutants into hydrothermal bamboo charcoal adsorption materials with high adsorption rate has good adsorption performance for cationic dyes, which is conducive to application in industrial wastewater treatment and other fields, and turns waste into treasure. Greatly increased the added value of bamboo powder.
附图说明Description of drawings
图1是本发明实施例1所得的样品对亚甲基蓝的等温吸附线图。Fig. 1 is the isotherm adsorption line graph of the sample obtained in Example 1 of the present invention to methylene blue.
图2是本发明实施例1所得的样品对亚甲基蓝的脱色率图。Fig. 2 is a graph of the decolorization rate of methylene blue by the sample obtained in Example 1 of the present invention.
具体实施方式Detailed ways
以下结合具体实施例,对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific embodiments.
表1实施例1-8原料配比(重量份)Table 1 Embodiment 1-8 raw material proportioning (weight part)
实施例1(对照上表中对应实施例1与重量份配比值),按如下按下列步骤进行制备:Embodiment 1 (corresponding embodiment 1 and the proportioning value by weight in contrasting table above), prepare as follows according to the following steps:
(1)将竹屑、竹片、边角料、竹丝等粉碎成60-80目;(1) Grinding bamboo chips, bamboo chips, leftovers, bamboo silk, etc. into 60-80 meshes;
(2)水热竹炭制备:将60重量份的60-80目竹粉和21重量份浓度为37%浓盐酸置于220重量份的水中,在室温下搅拌混合均匀后置于带聚四氟乙烯内衬的不锈钢反应釜中,然后在200℃条件下反应15小时、自然冷却、抽滤、洗涤至中性后烘干,即得到水热竹炭;(2) Preparation of hydrothermal bamboo charcoal: the 60-80 mesh bamboo powder of 60 parts by weight and the concentration of 21 parts by weight of 37% concentrated hydrochloric acid are placed in 220 parts by weight of water, stirred and mixed evenly at room temperature and then placed in a polytetrafluoroethylene In a stainless steel reaction kettle lined with ethylene, react at 200°C for 15 hours, cool naturally, filter with suction, wash until neutral, and then dry to obtain hydrothermal bamboo charcoal;
(3)活化水热竹炭制备:将步骤(2)得到的水热竹炭与3.6重量份氢氧化钠和240重量份水混合,室温搅拌2h后、抽滤、洗涤至中性后烘干。(3) Preparation of activated hydrothermal bamboo charcoal: mix the hydrothermal bamboo charcoal obtained in step (2) with 3.6 parts by weight of sodium hydroxide and 240 parts by weight of water, stir at room temperature for 2 hours, suction filter, wash until neutral, and then dry.
需说明的是实施例1为最佳实施例,其余实施例2-8均各对照表中对应实施例的原料和配比值,按实施例1相同方法制得。It should be noted that embodiment 1 is the best embodiment, and all the other embodiments 2-8 are made by the same method as embodiment 1 according to the raw materials and proportioning values of the corresponding embodiments in each comparison table.
现以实施例1所得样品为例,对亚甲基蓝吸附情况见图1。图1是本发明实施例1所得样品在室温下吸附亚甲基蓝的量,在平衡时,以吸附容量对平衡浓度作图,得到的等温吸附线,图中的吸附容量表示每克吸附剂吸附亚甲基蓝的量。图2是本发明实施例1所得样品在室温下对亚甲基蓝的脱色率图,亚甲基蓝的初始浓度为400毫克/升、体积为50毫升。Now taking the sample obtained in Example 1 as an example, the adsorption of methylene blue is shown in Figure 1. Fig. 1 is the amount of methylene blue adsorbed by the sample obtained in Example 1 of the present invention at room temperature. When in equilibrium, the adsorption capacity is plotted against the equilibrium concentration, and the isotherm adsorption line obtained. The adsorption capacity in the figure represents the adsorption capacity of methylene blue per gram of adsorbent. quantity. Fig. 2 is a diagram of the decolorization rate of the sample obtained in Example 1 of the present invention to methylene blue at room temperature, the initial concentration of methylene blue is 400 mg/L, and the volume is 50 ml.
本发明以竹粉为原料将原作废弃物处理的锯竹屑、竹片、边角料、竹丝等粉碎成60-80目粉状物,既有利于堆放,又可使反应更充分,效果更好。The present invention uses bamboo powder as a raw material to crush sawn bamboo chips, bamboo slices, scraps, bamboo shreds, etc. from the original waste into 60-80 mesh powder, which is not only beneficial to stacking, but also enables more sufficient reaction and better effect .
应当理解的是,对本领域普通技术人员来说,可以根据上述说明加以改进或变换,而所有这些改进和变换都应属于本发明所附权利要求的保护范围。It should be understood that those skilled in the art can make improvements or changes based on the above description, and all these improvements and changes should belong to the protection scope of the appended claims of the present invention.
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CN105733034A (en) * | 2016-02-18 | 2016-07-06 | 合肥市再德高分子材料有限公司 | High-performance natural rubber/butadiene styrene rubber composite material |
CN105935581A (en) * | 2016-01-11 | 2016-09-14 | 浙江科技学院 | Inorganic acid catalysis hydrothermal method for preparation of bamboo biochar |
CN106207179A (en) * | 2016-07-07 | 2016-12-07 | 陕西科技大学 | The method that a kind of KOH activation pomelo peel prepares sodium-ion battery negative material |
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CN105733034A (en) * | 2016-02-18 | 2016-07-06 | 合肥市再德高分子材料有限公司 | High-performance natural rubber/butadiene styrene rubber composite material |
CN106207179A (en) * | 2016-07-07 | 2016-12-07 | 陕西科技大学 | The method that a kind of KOH activation pomelo peel prepares sodium-ion battery negative material |
CN107200385A (en) * | 2017-07-18 | 2017-09-26 | 甘琦 | A kind of method that iron carbon or Fenton sludge prepare porous light electrolysis particle in utilization waste water treatment process |
CN108262028A (en) * | 2018-01-19 | 2018-07-10 | 浙江农林大学 | A kind of preparation method of maleic anhydride modification hydro-thermal bamboo Charcoal Adsorption agent |
CN108479713A (en) * | 2018-04-10 | 2018-09-04 | 浙江农林大学 | A kind of aminocarboxylic acid type hydro-thermal bamboo charcoal synthetic method |
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Application publication date: 20151021 |