CN106006638A - Preparation method of high-penetration microporous granular active carbon - Google Patents
Preparation method of high-penetration microporous granular active carbon Download PDFInfo
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 87
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 229910052799 carbon Inorganic materials 0.000 title 1
- 210000002268 wool Anatomy 0.000 claims abstract description 67
- 239000000835 fiber Substances 0.000 claims abstract description 60
- 239000002699 waste material Substances 0.000 claims abstract description 44
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 20
- 230000000149 penetrating effect Effects 0.000 claims abstract description 19
- 239000003599 detergent Substances 0.000 claims abstract description 10
- 238000009826 distribution Methods 0.000 claims abstract description 9
- 238000009656 pre-carbonization Methods 0.000 claims abstract description 7
- 210000004243 sweat Anatomy 0.000 claims abstract description 6
- 238000003763 carbonization Methods 0.000 claims abstract description 4
- 239000002657 fibrous material Substances 0.000 claims abstract description 4
- 230000004913 activation Effects 0.000 claims abstract description 3
- 239000012535 impurity Substances 0.000 claims abstract description 3
- 210000000085 cashmere Anatomy 0.000 claims description 37
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 23
- 229910052757 nitrogen Inorganic materials 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 238000001994 activation Methods 0.000 claims description 9
- 239000012190 activator Substances 0.000 claims description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 8
- 238000000746 purification Methods 0.000 claims description 6
- 238000012545 processing Methods 0.000 claims description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical group [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 4
- 238000005238 degreasing Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims 3
- 229910000027 potassium carbonate Inorganic materials 0.000 claims 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims 2
- 235000015320 potassium carbonate Nutrition 0.000 claims 1
- 235000011118 potassium hydroxide Nutrition 0.000 claims 1
- 235000017550 sodium carbonate Nutrition 0.000 claims 1
- 235000011121 sodium hydroxide Nutrition 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000012958 reprocessing Methods 0.000 abstract description 2
- 239000011800 void material Substances 0.000 abstract description 2
- 229920000049 Carbon (fiber) Polymers 0.000 abstract 1
- 210000004209 hair Anatomy 0.000 description 38
- 230000008569 process Effects 0.000 description 8
- 239000010453 quartz Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000004753 textile Substances 0.000 description 7
- 239000002253 acid Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000005096 rolling process Methods 0.000 description 5
- 238000001878 scanning electron micrograph Methods 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 4
- 239000004519 grease Substances 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 238000010306 acid treatment Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000282836 Camelus dromedarius Species 0.000 description 2
- 241000287828 Gallus gallus Species 0.000 description 2
- 241000283973 Oryctolagus cuniculus Species 0.000 description 2
- 241001416177 Vicugna pacos Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- BFPYWIDHMRZLRN-UHFFFAOYSA-N 17alpha-ethynyl estradiol Natural products OC1=CC=C2C3CCC(C)(C(CC4)(O)C#C)C4C3CCC2=C1 BFPYWIDHMRZLRN-UHFFFAOYSA-N 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241000283707 Capra Species 0.000 description 1
- BFPYWIDHMRZLRN-SLHNCBLASA-N Ethinyl estradiol Chemical compound OC1=CC=C2[C@H]3CC[C@](C)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 BFPYWIDHMRZLRN-SLHNCBLASA-N 0.000 description 1
- 102000011782 Keratins Human genes 0.000 description 1
- 108010076876 Keratins Proteins 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005262 decarbonization Methods 0.000 description 1
- 230000035617 depilation Effects 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229960002568 ethinylestradiol Drugs 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 235000021190 leftovers Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/14—Pore volume
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明涉及一种高贯穿多微孔颗粒活性炭的制备方法,属于废料的回收或再加工技术领域。将废弃毛纤维置于硫酸溶液中处理后,轧酸并烘焙炭化,除杂,然后中和,加入非离子洗涤剂去除脂汗,最后洗净烘干,获得净毛纤维,将该净毛纤维进行预炭化和活化即得活性碳纤维。将发明应用于不可纺毛纤维或废弃毛纤维料的回收再利用制备活性炭,具有很高的比表面积,使用过程中相容性较高,吸附能力好,且空隙体积分布均匀等优点。
The invention relates to a preparation method of highly penetrating microporous granular activated carbon, which belongs to the technical field of waste recycling or reprocessing. After the waste wool fiber is treated in sulfuric acid solution, it is acid-rolled and baked for carbonization, impurities are removed, then neutralized, non-ionic detergent is added to remove fat and sweat, and finally washed and dried to obtain a clean wool fiber. Activated carbon fibers are obtained by pre-carbonization and activation. Applying the invention to the recovery and reuse of non-spinnable wool fibers or waste wool fiber materials to prepare activated carbon has the advantages of high specific surface area, high compatibility during use, good adsorption capacity, and uniform void volume distribution.
Description
技术领域 technical field
本发明涉及一种高贯穿多微孔颗粒活性炭的制备方法,属于废料的回收或再加工技术领域。 The invention relates to a preparation method of highly penetrating microporous granular activated carbon, which belongs to the technical field of waste recycling or reprocessing.
背景技术 Background technique
废弃纤维资源量巨大,处理不当不仅会造成环境污染,而且会增加处理成本,浪费资源。采用适当方法对废弃纺织纤维进行再加工不仅符合我国有关法律法规的要求,而且具有废物利用、资源回收的合理性。废弃毛纤维包括不可纺毛纤维(如猪毛、人发、鸡毛、羊毛或兔毛下脚料、骆驼毛、羊驼毛、羊绒针毛等)和废弃毛纤维料(如纺织厂的毛料回丝,回毛,布边,废毛纱边角料、旧的毛料服装、旧毛衣等)。第82届国际毛纺织组织年会上公布的最新数据显示,2013/2014年度全球仅羊毛产量预期为110万吨净毛,从这也可反映出废弃毛纤维资源量巨大。因此,如何合理处置或再利用废弃毛纤维资源是当前面临的重要课题。 The amount of waste fiber resources is huge, and improper disposal will not only cause environmental pollution, but also increase processing costs and waste resources. Using appropriate methods to reprocess waste textile fibers not only meets the requirements of relevant laws and regulations in our country, but also has the rationality of waste utilization and resource recovery. Waste wool fibers include non-spinnable wool fibers (such as pig hair, human hair, chicken hair, wool or rabbit fur scraps, camel hair, alpaca wool, cashmere needle hair, etc.) , back wool, selvage, waste wool yarn scraps, old wool clothing, old sweaters, etc.). According to the latest data released at the 82nd Annual Conference of the International Wool Textile Organization, the global wool production in 2013/2014 is expected to be 1.1 million tons of net wool, which also reflects the huge amount of waste wool fiber resources. Therefore, how to properly dispose or reuse waste wool fiber resources is an important issue currently facing.
在废弃毛纤维资源利用方面,主要有两个利用方向:一是采用开松、清洗、筛选、后直接利用或经纺织加工,形成可用纺织品的物理再利用方法,如中国专利CN102167418B公开了利用以废弃羊毛纤维为填料的吸附反应器去除污水中的炔雌醇污染物;二是清洗、溶解,形成角蛋白液体提纯利用或再生纺丝、纺织加工,形成纺织品或粉碎、炭化制成吸附类物质的化学物理方法,如中国专利CN 102161485 B利用废弃羊毛制备管状结构活性炭,但该专利存在的缺点在于管状结构容易爆裂成碎片,外壁活化微孔的贯穿性较差,导致活性炭比表面积较小,吸附能力较差;此外该专利仅利用水清洗废弃羊毛,无法将羊毛表明的脂、汉等去除,不利于活化微孔的产生,从而影响活性炭的比表面积的提高。羊绒针毛产生于山羊脱毛工序,直径分布范围较宽,粗细分布不匀,较粗的纤维可达170μm,且纤维截面既有实心结构,也有孔状结构,是废弃毛纤维中的一种典型代表,对这一废弃材料的应用少见报道。 Regarding the utilization of waste wool fiber resources, there are mainly two utilization directions: one is to adopt the method of opening, cleaning, screening, direct utilization or textile processing to form usable textiles, such as Chinese patent CN102167418B discloses the utilization of The adsorption reactor with waste wool fiber as filler removes ethinyl estradiol pollutants in sewage; the second is cleaning and dissolving to form keratin liquid purification and utilization or regeneration spinning and textile processing to form textiles or crush and carbonize to make adsorption substances The chemical and physical method, such as Chinese patent CN 102161485 B, uses waste wool to prepare tubular activated carbon, but the disadvantages of this patent are that the tubular structure is easy to burst into pieces, and the penetrability of activated micropores on the outer wall is poor, resulting in a small specific surface area of activated carbon. The adsorption capacity is poor; in addition, this patent only uses water to wash the waste wool, which cannot remove the fat and impurities in the wool, which is not conducive to the generation of activated micropores, thereby affecting the improvement of the specific surface area of the activated carbon. Cashmere needle hair is produced in the depilation process of goats. It has a wide range of diameter distribution and uneven thickness distribution. The thicker fibers can reach 170 μm, and the fiber cross-section has both solid and porous structures. It is a typical waste wool fiber. Representatives, there are few reports on the application of this waste material.
基于此,做出本申请。 Based on this, this application is made.
发明内容 Contents of the invention
本发明要解决的技术问题是提供一种利用羊绒针毛纤维制备高贯穿多微孔颗粒活性炭的方法,在减轻环境对废弃物处理压力的同时,获得高贯穿多微孔颗粒活性炭,变废为宝,符合资源的最大化利用原则。 The technical problem to be solved by the present invention is to provide a method for preparing highly penetrating microporous granular activated carbon by using cashmere needle hair fiber, which can obtain high penetrating microporous granular activated carbon while reducing the environmental pressure on waste treatment, and turn waste into Treasure, in line with the principle of maximizing the utilization of resources.
本发明采用如下技术路线: The present invention adopts following technical route:
一种利用羊绒针毛纤维制备高贯穿多微孔活性炭的方法,包括如下步骤: A kind of method utilizing cashmere needle wool fiber to prepare highly penetrating microporous activated carbon, comprises the steps:
步骤一、羊绒针毛纤维预处理阶段,即将废弃毛纤维置于2.5%-5.0%的硫酸溶液中处理,轧酸后在100℃-115℃之间烘焙炭化,再利用碎炭机除去植物性草杂,然后中和,加入非离子洗涤剂去除废弃毛纤维的脂汗,最后用35-55℃热水洗净后烘干,获得净羊绒针毛纤维; Step 1. The pretreatment stage of cashmere needle wool fiber, that is, the waste wool fiber is treated in 2.5%-5.0% sulfuric acid solution, and after acid rolling, it is baked and carbonized at 100°C-115°C, and then the vegetable is removed by a charcoal crusher. Weeds, then neutralized, adding non-ionic detergent to remove the grease and sweat of waste wool fibers, and finally washing with hot water at 35-55°C and drying to obtain clean cashmere needle wool fibers;
步骤二、羊绒针毛纤维预炭化阶段,即利用轧刀将净羊绒针毛纤维切成5mm-15mm短毛,在氮气保护下置于石英管式马弗炉内,通氮气30min后,升温至200℃-255℃之间,预炭化处理30min至90min,冷却至室温后取出,即获得不同结构形态的预炭化产物; Step 2, the pre-carbonization stage of cashmere needle hair fibers, that is, use a calender to cut the clean cashmere needle hair fibers into 5mm-15mm short hairs, place them in a quartz tubular muffle furnace under nitrogen protection, and heat up to Between 200°C and 255°C, pre-carbonize for 30 minutes to 90 minutes, take it out after cooling to room temperature, and obtain pre-carbonized products with different structures;
步骤三、预炭化产物炭化-活化阶段,即将预碳化产物与活化剂按照质量比以一定比例混合,在氮气保护下置于石英管式马弗炉,通氮气30min后,升温至500℃-900℃之间,再保温60min至150min,冷却至室温取出,用80℃热水清洗至清洗液pH 值为5.8-7.5之间,过滤烘干后即得以羊绒针毛纤维为原料的活性炭。 Step 3, the carbonization-activation stage of the pre-carbonized product, that is, the pre-carbonized product and the activator are mixed in a certain proportion according to the mass ratio, placed in a quartz tubular muffle furnace under the protection of nitrogen, and after 30 minutes of nitrogen gas, the temperature is raised to 500°C-900°C ℃, then keep warm for 60 to 150 minutes, cool to room temperature, take out, wash with 80 ℃ hot water until the pH value of the cleaning solution is between 5.8 and 7.5, filter and dry to obtain activated carbon made of cashmere needle wool fiber.
其中,所述步骤一中羊绒针毛纤维为废弃毛纤维的典型代表,可将其它不可纺毛纤维(如猪毛、人发、鸡毛、羊毛或兔毛下脚料、骆驼毛、羊驼毛等)和废弃毛纤维料(如纺织厂的毛料回丝,回毛,布边,废毛纱边角料、旧的毛料服装、旧毛衣等)顶替羊绒针毛纤维进行贯穿多微孔颗粒活性炭的制备;羊绒针毛纤维预处理阶段的预处理工艺流程为:含草废弃毛纤维→浸、轧酸→烘焙→除炭→中和→去脂→烘干→废弃净毛;非离子洗涤剂是指Lissapol TN 450、Teric N10、Antarox C0630及FK-9502型非离子洗涤剂中的一种;去脂洗涤过程工艺控制为:浓度0.5%至2%之间,浴比1:15-55,温度45℃-60℃,洗涤次数2次,洗涤时间分布为10min、5min; Wherein, the cashmere needle wool fiber in the step 1 is a typical representative of waste wool fiber, and other non-spinnable wool fibers (such as pig hair, human hair, chicken hair, wool or rabbit hair leftovers, camel hair, alpaca hair, etc. ) and waste wool fiber materials (such as wool back silk, wool back, selvage, waste wool yarn scraps, old woolen clothing, old sweaters, etc.) in the textile mill to replace cashmere needle wool fibers for the preparation of penetrating microporous granular activated carbon; cashmere The pretreatment process of the guard hair fiber pretreatment stage is: grass-containing waste wool fiber→soaking, acid rolling→baking→decarbonization→neutralization→degreasing→drying→discarding and cleaning wool; non-ionic detergent refers to Lissapol TN 450, one of Teric N10, Antarox C0630 and FK-9502 non-ionic detergents; the process control of the degreasing washing process is: the concentration is between 0.5% and 2%, the liquor ratio is 1:15-55, and the temperature is 45°C- 60°C, washing times 2 times, washing time distribution is 10min, 5min;
所述步骤二中升温速率为5-15℃/min; The heating rate in the step 2 is 5-15°C/min;
所述步骤三中预碳化产物与活化剂的混合质量比应小于2;升温速率为5-15℃/min;活化剂是指K2CO3、Na2CO3、Li2CO3、H3PO4 、KOH、NaOH、KOH- K2CO3、NaOH- Na2CO3中的一种。 The mixing mass ratio of the pre-carbonized product and the activator in the step 3 should be less than 2; the heating rate is 5-15°C/min; the activator refers to K 2 CO 3 , Na 2 CO 3 , Li 2 CO 3 , H 3 One of PO 4 , KOH, NaOH, KOH- K 2 CO 3 , NaOH- Na 2 CO 3 .
本发明的有益效果是: The beneficial effects of the present invention are:
本发明利用预处理工序很好地去除了废弃毛纤维的表面的脂、汉,利于预炭化、炭化-活化过程微孔结构的形成;再者通过对预炭化、炭化-活化过程控制,使废弃毛纤维颗粒活性炭具有高度贯穿、活化微孔明显、且稳定的网络状结构,极大地提高了活性炭的比表面积,增强了吸附能力,将作为高效吸附剂应用在重金属、有机染料、有害化学物质处理、水及甲醛等有害气体净化等领域,这一方面减少了处理废弃毛纤维带来的环境污染,又降低了废弃羊毛的处理成本,同时将废弃资源变废为宝,丰富了废弃资源处理利用的途径。 The present invention utilizes the pretreatment process to remove the fat and moisture on the surface of the waste wool fiber well, which is beneficial to the formation of the microporous structure in the pre-carbonization and carbonization-activation process; moreover, by controlling the pre-carbonization and carbonization-activation process, the waste Wool fiber granular activated carbon has a highly penetrating, activated micropore, and stable network structure, which greatly increases the specific surface area of activated carbon and enhances the adsorption capacity. It will be used as an efficient adsorbent in the treatment of heavy metals, organic dyes, and harmful chemicals. Purification of harmful gases such as , water and formaldehyde, etc. On the one hand, it reduces the environmental pollution caused by the treatment of waste wool fibers, and reduces the cost of waste wool treatment. At the same time, it turns waste resources into treasures and enriches the treatment and utilization of waste resources. way.
本申请通过对预炭化、预炭化-活化过程控制,以羊绒针毛纤维为原料,可以制备获得高贯穿多微孔颗粒活性炭,还可将羊绒针毛制备高贯穿多微孔颗粒活性炭的方法与工艺应用到其他废弃毛纤维的处理与应用中,这有利于减轻环境对废弃物处理压力,并为废弃毛纤维的合理利用提供更多有效途径,从而提高产品利用附加值。 This application controls the process of pre-carbonization, pre-carbonization-activation, and uses cashmere needle hair fiber as raw material to prepare highly penetrating microporous granular activated carbon, and can also prepare high penetrating microporous granular activated carbon from cashmere needle hair. The process is applied to the treatment and application of other waste wool fibers, which will help reduce the pressure on the environment for waste disposal, and provide more effective ways for the rational use of waste wool fibers, thereby increasing the added value of product utilization.
附图说明 Description of drawings
图1为本发明的加工流程示意图; Fig. 1 is a schematic diagram of the processing flow of the present invention;
图2为本申请中废弃羊绒针毛预处理前的状态示意图; Fig. 2 is a schematic diagram of the state before the pretreatment of discarded cashmere needle hair in the present application;
图3为本申请中废弃羊绒针毛预处理后的状态示意图; Fig. 3 is the state schematic diagram after the pretreatment of discarded cashmere needle hair in the present application;
图4为本申请第一种实施状态下中炭化-活化后废弃羊绒针毛颗粒活性炭扫描电镜图; Fig. 4 is the scanning electron micrograph of discarded cashmere needle hair granular activated carbon after carbonization-activation under the first implementation state of the present application;
图5为图4中A部位的局部放大图; Fig. 5 is a partially enlarged view of part A in Fig. 4;
图6为本申请第二种实施状态下中炭化-活化后废弃羊绒针毛颗粒活性炭扫描电镜图; Fig. 6 is a scanning electron micrograph of activated carbon of discarded cashmere needle hair particles after carbonization-activation in the second implementation state of the present application;
图7为图6中B部位的局部放大图; Fig. 7 is a partially enlarged view of part B in Fig. 6;
图8为本申请第三种实施状态下中炭化-活化后废弃羊绒针毛颗粒活性炭扫描电镜图; Fig. 8 is a scanning electron micrograph of activated carbon of discarded cashmere needle hair particles after carbonization-activation in the third implementation state of the present application;
图9为图8中C部位的局部放大图。 FIG. 9 is a partially enlarged view of part C in FIG. 8 .
具体实施方式 detailed description
以废弃毛纤维资料中羊绒针毛为例,结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。 Taking cashmere needle hair in waste wool fiber materials as an example, the present invention is further described in conjunction with specific examples. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
实施例1 Example 1
本实施例的处理工艺可参考图1所示,将废弃羊绒针毛纤维置于3.0%的硫酸溶液中硫酸处理,轧酸后在110℃烘焙炭化,再利用碎炭机除去植物性草杂,然后中和,加入Teric N10非离子洗涤剂(浓度1.5%,浴比1:35,温度50℃,洗涤次数两次,两次洗涤时间分布为10min、5min)去除羊绒针毛纤维的脂汗,最后用40℃热水洗净后烘干,获得净羊绒针毛纤维,对比图2和图3可以看出,净化处理后的纤维毛色光亮整洁,且亮泽度高;然后利用轧刀将净羊绒针毛纤维切成15mm短毛,在氮气保护下置于石英管式马弗炉内,通氮气30min后,以15℃/min升温至255℃,预炭化处理30min,冷却至室温,后取出获得预炭化产物;再将预碳化产物与Na2CO3活化剂按照质量比以1:1一定比例混合,在氮气保护下置于石英管式马弗炉,通氮气30min后,以5℃/min升温至500℃,再保温100min,冷却至室温取出,用80℃热水清洗至清洗液pH值为6.8左右,过滤烘干后即得以羊绒针毛纤维为原料的活性炭。 The treatment process of this embodiment can be referred to as shown in Figure 1. The waste cashmere needle hair fiber is placed in a 3.0% sulfuric acid solution for sulfuric acid treatment. After acid rolling, it is baked and carbonized at 110°C, and then the plant weeds are removed by a charcoal crusher. Then neutralize, add Teric N10 non-ionic detergent (concentration 1.5%, bath ratio 1:35, temperature 50°C, wash twice, the time distribution of the two washes is 10min, 5min) to remove the grease and sweat of cashmere needle wool fibers, and finally Wash with hot water at 40°C and dry to obtain clean cashmere needle wool fibers. Comparing Figure 2 and Figure 3, it can be seen that the fiber wool after purification treatment is bright and tidy, and has high gloss; The guard hair fiber is cut into short hairs of 15 mm, placed in a quartz tubular muffle furnace under the protection of nitrogen, and then heated to 255°C at 15°C/min for 30 minutes, pre-carbonized for 30 minutes, cooled to room temperature, and then taken out to obtain Pre-carbonized product; then mix the pre-carbonized product with Na 2 CO 3 activator at a certain ratio of 1:1 according to the mass ratio, and place it in a quartz tubular muffle furnace under the protection of nitrogen gas. Raise the temperature to 500°C, keep it warm for 100 minutes, cool to room temperature, take it out, wash with 80°C hot water until the pH of the cleaning solution is about 6.8, filter and dry to obtain activated carbon made of cashmere needle wool fiber.
图4和图5是采用本实施例所述的方法制备羊绒针毛颗粒活性炭在不同放大倍数下的电镜扫描图,可以观察到部分具有活性微孔的羊绒针毛颗粒活性炭,但是活化效果不够充分,且活化微孔较小。根据测定其BET 比表面积为370.04m2·g-1,平均孔隙体积为0.138cm3·g-1。 Figure 4 and Figure 5 are scanning electron microscope images of cashmere needle hair granular activated carbon prepared by the method described in this example under different magnifications, and it can be observed that some cashmere needle hair granular activated carbon with active micropores, but the activation effect is not sufficient , and the activated pores are smaller. According to the measurement, its BET specific surface area is 370.04m 2 ·g -1 , and the average pore volume is 0.138cm 3 ·g -1 .
实施例2 Example 2
本实施例的处理工艺可参考图1所示,将废弃羊绒针毛纤维置于3.5%的硫酸溶液中硫酸处理,轧酸后在105℃烘焙炭化,再利用碎炭机除去植物性草杂,然后中和,加入Lissapol TN 450非离子洗涤剂(浓度1%,浴比1:50,温度55℃,洗涤次数两次,两次洗涤时间分布为10min、5min)去除羊绒针毛纤维的脂汗,最后用40℃热水洗净后烘干,获得净羊绒针毛纤维,对比图2和图3可以看出,净化处理后的纤维毛色光亮整洁,且亮泽度高;然后利用轧刀将净羊绒针毛纤维切成10mm短毛,在氮气保护下置于石英管式马弗炉内,通氮气30min后,以5℃/min升温至250℃,预炭化处理60min,冷却至室温,后取出获得预炭化产物;再将预碳化产物与K2CO3活化剂按照质量比以4:2混合,在氮气保护下置于石英管式马弗炉,通氮气30min后,以5℃/min升温至500℃,再保温150min,冷却至室温取出,用80℃热水清洗至清洗液pH 值为6.2左右,过滤烘干后即得以羊绒针毛纤维为原料的活性炭。 The treatment process of this embodiment can be referred to as shown in Figure 1. The waste cashmere needle hair fiber is placed in 3.5% sulfuric acid solution for sulfuric acid treatment, and after acid rolling, it is baked and carbonized at 105°C, and then the plant weeds are removed by a charcoal crusher. Then neutralize, add Lissapol TN 450 non-ionic detergent (concentration 1%, bath ratio 1:50, temperature 55°C, wash twice, the time distribution of the two washes is 10min, 5min) to remove the grease and sweat of cashmere needle wool fiber, Finally, wash it with hot water at 40°C and dry it to obtain clean cashmere needle wool fiber. Comparing Figure 2 and Figure 3, it can be seen that the fiber wool color after purification treatment is bright and tidy, and has high gloss; Cashmere needle hair fibers are cut into short hairs of 10 mm, placed in a quartz tubular muffle furnace under the protection of nitrogen, and then heated to 250°C at 5°C/min for 30 minutes, pre-carbonized for 60 minutes, cooled to room temperature, and then taken out Obtain the pre-carbonized product; then mix the pre-carbonized product with the K 2 CO 3 activator at a mass ratio of 4:2, place it in a quartz tubular muffle furnace under the protection of nitrogen, and raise the temperature at 5°C/min after blowing nitrogen for 30 minutes To 500°C, keep warm for 150 minutes, cool to room temperature, take out, wash with 80°C hot water until the pH of the cleaning solution is about 6.2, filter and dry to obtain activated carbon made of cashmere needle wool fiber.
图6和图7是采用本实施例所述的方法制备羊绒针毛颗粒活性炭在不同放大倍数下的电镜扫描图,可观察到形成了内部具有大量活化微孔的颗粒活性炭,外部被完成炭化的鳞片结构层等外皮层包裹,这一定程度上影响了活性炭的吸附效果,不过外部包裹层部分位置开始出现活化微孔结构。根据测定其BET比表面积为526.54m2·g-1,平均孔隙体积为0. 201cm3·g-1。 Fig. 6 and Fig. 7 are the scanning electron micrographs of cashmere needle hair granular activated carbon prepared by the method described in this example under different magnifications. It can be observed that granular activated carbon with a large number of activated micropores is formed inside, and the carbonized exterior is completed. The scale structure layer and other skin layers are wrapped, which affects the adsorption effect of activated carbon to a certain extent, but the activated microporous structure begins to appear in some parts of the outer wrapping layer. According to the measurement, its BET specific surface area is 526.54m 2 ·g -1 , and the average pore volume is 0. 201cm 3 ·g -1 .
实施例3 Example 3
本实施例的处理工艺可参考图1所示,将废弃羊绒针毛纤维置于3.5%的硫酸溶液中硫酸处理,轧酸后在105℃烘焙炭化,再利用碎炭机除去植物性草杂,然后中和,加入Lissapol TN 450非离子洗涤剂(浓度1%,浴比1:50,温度55℃,洗涤次数两次,两次洗涤时间分布为10min、5min)去除羊绒针毛纤维的脂汗,最后用40℃热水洗净后烘干,获得废弃净毛纤维,对比图2和图3可以看出,净化处理后的纤维毛色光亮整洁,且亮泽度高;然后利用轧刀将净羊绒针毛纤维切成5mm短毛,在氮气保护下置于石英管式马弗炉内,通氮气30min后,以10℃/min升温至240℃,预炭化处理60min,冷却至室温,后取出获得预炭化产物;再将预碳化产物与Na2CO3-NaOH复合活化剂按照质量比以4:2混合,在氮气保护下置于石英管式马弗炉,通氮气30min后,以5℃/min升温至600℃,再保温120min,冷却至室温取出,用80℃热水清洗至清洗液pH 值为6.0左右,过滤烘干后即得以羊绒针毛纤维为原料的活性炭。 The treatment process of this embodiment can be referred to as shown in Figure 1. The waste cashmere needle hair fiber is placed in 3.5% sulfuric acid solution for sulfuric acid treatment, and after acid rolling, it is baked and carbonized at 105°C, and then the plant weeds are removed by a charcoal crusher. Then neutralize, add Lissapol TN 450 non-ionic detergent (concentration 1%, bath ratio 1:50, temperature 55°C, wash twice, the time distribution of the two washes is 10min, 5min) to remove the grease and sweat of cashmere needle wool fiber, Finally, wash it with hot water at 40°C and dry it to obtain the waste net wool fiber. Comparing Figure 2 and Figure 3, it can be seen that the fiber wool color after purification treatment is bright and tidy, and has a high gloss; The guard hair fiber is cut into short hairs of 5 mm, placed in a quartz tubular muffle furnace under the protection of nitrogen, and after 30 minutes of blowing nitrogen, the temperature is raised to 240°C at 10°C/min, pre-carbonized for 60 minutes, cooled to room temperature, and then taken out to obtain Pre-carbonized product; then mix the pre-carbonized product with Na 2 CO 3 -NaOH composite activator at a mass ratio of 4:2, place it in a quartz tubular muffle furnace under the protection of nitrogen, and pass nitrogen for 30 minutes, then set the temperature at 5°C/ The temperature was raised to 600°C for 1 minute, and then kept for 120 minutes, cooled to room temperature, taken out, washed with 80°C hot water until the pH value of the cleaning solution was about 6.0, filtered and dried to obtain activated carbon made of cashmere needle wool fiber.
图8和图9是采用本实施例所述的方法制备羊绒针毛颗粒活性炭在不同放大倍数下的电镜扫描图,可观察到形成了大量活化微孔的颗粒活性炭,大颗粒的活性炭分解成较多小粒径的颗粒活性炭,且羊毛鳞片层等外皮层在炭化后获得了较多的活化微孔结构,这有助于增加活性炭的比表面积。根据测定其BET比表面积为736.9m2·g-1,平均孔隙体积为0. 291cm3·g-1。 Fig. 8 and Fig. 9 are the scanning electron micrographs of cashmere needle hair granular activated carbon prepared by the method described in this embodiment under different magnifications. It can be observed that a large amount of granular activated carbon with activated micropores is formed, and the activated carbon of large particles is decomposed into relatively large particles. There are many granular activated carbons with small particle sizes, and the skin layers such as the wool scale layer have obtained more activated microporous structures after carbonization, which helps to increase the specific surface area of activated carbon. According to the measurement, its BET specific surface area is 736.9m 2 ·g -1 , and the average pore volume is 0. 291cm 3 ·g -1 .
从上述制备过程可以看出,在实施例3的状态下制备效果最佳。该方案下所制备的活性炭具有很高的比表面积,使用过程中相容性较高,吸附能力好,且空隙体积分布均匀。 As can be seen from the above preparation process, the preparation effect is the best in the state of Example 3. The activated carbon prepared under this scheme has a high specific surface area, high compatibility during use, good adsorption capacity, and uniform void volume distribution.
以上内容是结合本发明创造的优选实施方式对所提供技术方案所作的进一步详细说明,不能认定本发明创造具体实施只局限于上述这些说明,对于本发明创造所属技术领域的普通技术人员来说,在不脱离本发明创造构思的前提下,还可以做出若干简单推演或替换,都应当视为属于本发明创造的保护范围。 The above content is a further detailed description of the technical solutions provided in conjunction with the preferred embodiments of the present invention. It cannot be determined that the specific implementation of the present invention is only limited to the above descriptions. For those of ordinary skill in the technical field of the present invention, On the premise of not departing from the inventive concept of the present invention, some simple deduction or replacement can also be made, which should be regarded as belonging to the protection scope of the present invention.
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