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CN106635104A - Method for preparing high-performance compound machine-made charcoal - Google Patents

Method for preparing high-performance compound machine-made charcoal Download PDF

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Publication number
CN106635104A
CN106635104A CN201611037588.3A CN201611037588A CN106635104A CN 106635104 A CN106635104 A CN 106635104A CN 201611037588 A CN201611037588 A CN 201611037588A CN 106635104 A CN106635104 A CN 106635104A
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preparation
biomass
charcoal
carbon
lignite
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马文会
杨兴卫
魏奎先
陈正杰
伍继君
谢克强
刘大春
杨斌
王�华
戴永年
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Kunming University of Science and Technology
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    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
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Abstract

本发明涉及一种高性能复合机制炭的制备方法,属于资源综合利用技术领域。首先将含水率为5%以下的生物质原料、褐煤分别破碎至粒度小于1cm的颗粒;将得到的生物质原料颗粒热解得到生物炭;将生物炭、褐煤、粘结剂、助燃剂、水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;将得到的带有中心孔的炭棒以30~200℃/min的升温速率升温至400~700℃炭化1~12h,冷却后得到复合机制炭。该制备过程是以来源丰富、价格低廉、可再生且易于粉碎的生物质以及价格低廉的褐煤为碳源,具有大规模生产价格低、收率高、热值高、孔隙率高、广受市场欢迎的复合机制炭的潜能。The invention relates to a preparation method of high-performance composite machine-made carbon, which belongs to the technical field of resource comprehensive utilization. First, the biomass raw material and lignite with a moisture content of less than 5% are broken into particles with a particle size of less than 1cm; the obtained biomass raw material particles are pyrolyzed to obtain biochar; Mix evenly to obtain a mixed material, press the mixed material into a carbon rod with a central hole; heat the obtained carbon rod with a central hole at a heating rate of 30-200 °C/min to 400-700 °C for 1-12 hours, After cooling, a composite mechanism carbon is obtained. The preparation process uses abundant, low-cost, renewable and easily crushed biomass and low-cost lignite as carbon sources. It has the advantages of low mass production price, high yield, high calorific value, and high porosity. Welcome to the potential of composite mechanism charcoal.

Description

一种高性能复合机制炭的制备方法A kind of preparation method of high-performance composite machine-made carbon

技术领域technical field

本发明涉及一种高性能复合机制炭的制备方法,属于资源综合利用技术领域。The invention relates to a preparation method of high-performance composite machine-made carbon, which belongs to the technical field of resource comprehensive utilization.

背景技术Background technique

长期以来,木炭一直被广泛地用作生活燃料,木炭是将木材在缺氧的条件下燃烧或热解而制取的,生产木炭需要消耗大量的森林资源,严重破坏了生态环境,我国森林覆盖面积不到国土的10%,森林的形成需要一定的生长周期,大量的森林砍伐不符合保护生态环境、创建低炭社会、发展循环经济的要求;传统木炭的生产方法为将木材放入炉窑之中热解进行土窑制炭工艺具有密封性差、生产周期长、产量低、成本高等缺点,且热解过程中的烟气直接排放,不仅浪费资源还造成了环境污染,近年来,随着国家环保要求的提高,土窑制炭被淘汰将是大势所趋;For a long time, charcoal has been widely used as living fuel. Charcoal is produced by burning or pyrolyzing wood under anoxic conditions. The production of charcoal requires a large amount of forest resources, which seriously damages the ecological environment. my country's forest coverage The area is less than 10% of the country's land. The formation of forests requires a certain growth cycle. A large number of deforestation does not meet the requirements of protecting the ecological environment, creating a low-carbon society, and developing a circular economy; the traditional production method of charcoal is to put wood into kilns The earth kiln charcoal making process of medium pyrolysis has the disadvantages of poor sealing, long production cycle, low output, high cost, etc., and the flue gas in the pyrolysis process is directly discharged, which not only wastes resources but also causes environmental pollution. In recent years, with the With the improvement of national environmental protection requirements, it will be the general trend that earth kiln charcoal will be eliminated;

农林生物质原料是典型的可再生能源,其具有来源广泛,储量丰富,生长周期短等优点。地球上每年生产的生物质总量约为1400~1800亿吨,我国每年废弃的秸秆高达60亿多吨,资源化潜力巨大,且农林生物质原料热解所得生物质炭孔洞结构发达、易于燃烧。但农林生物质资源也存在其局限性,主要表现为:分布不集中,不易收集等,因此单独使用农林生物质为原料制备机制炭,从产量角度考虑远远无法满足日常生产生活对炭质燃料的需求;我国褐煤资源丰富,且价格低廉,但褐煤挥发成分高(>40%)、固定碳含量低、孔洞结构不发达,单独使用褐煤制备的机制炭燃烧效果不理想,这些缺点限制了褐煤的应用,以褐煤为原料,采用中低温干馏对褐煤进行炭化处理,脱去其中的大部分水分和挥发分,得到性能较好的褐煤半焦炭,并将其与生物质炭混合,可以扩大其应用范围。Agricultural and forestry biomass raw materials are typical renewable energy sources, which have the advantages of wide sources, abundant reserves, and short growth cycle. The total amount of biomass produced on the earth every year is about 140-180 billion tons, and the annual discarded straw in my country is as high as more than 6 billion tons, which has great resource potential, and the biochar obtained from the pyrolysis of agricultural and forestry biomass raw materials has a well-developed pore structure and is easy to burn . However, agricultural and forestry biomass resources also have their limitations. The main manifestations are: the distribution is not concentrated, and it is not easy to collect. my country's lignite resources are abundant and the price is low, but lignite has high volatile components (>40%), low fixed carbon content, and undeveloped pore structure, and the combustion effect of mechanism charcoal prepared by using lignite alone is not ideal. For the application of lignite, using lignite as raw material, medium and low temperature dry distillation is used to carbonize lignite, remove most of the water and volatile matter, and obtain lignite semi-coke with better performance, and mix it with biomass charcoal, which can expand its application range.

基于以上背景,本文提出了一种既克服了生物质炭产量小,又解决了褐煤固定碳含量低,孔隙结构不发达等问题的复合机制炭制备方法。本发明旨在充分利用可再生的农林生物质资源和价格低廉、储量丰富的褐煤,首先利用热解(干馏)技术对农林生物质原料进行加工,热解过程中的烟气得到充分利用,并将热解所产生的副产品生物质炭(配比较小)与储量十分丰富的褐煤(配比较大)混合后进行第二步炭化,炭化过程中烟气挥发去除,增加了复合机制炭的孔隙率,且烟气排入水池中被吸收,吸收了烟气的水分被循环用到复合机制炭配料环节。本发明制备的复合机制炭不仅解决了生物质炭和褐煤两者的局限性,而且资源得到循环利用,符合节能环保、绿色发展的要求。Based on the above background, this paper proposes a composite mechanism carbon preparation method that not only overcomes the low yield of biomass charcoal, but also solves the problems of low fixed carbon content of lignite and underdeveloped pore structure. The invention aims to make full use of renewable agricultural and forestry biomass resources and lignite with low price and abundant reserves. Firstly, the pyrolysis (dry distillation) technology is used to process the agricultural and forestry biomass raw materials, and the flue gas in the pyrolysis process is fully utilized, and The by-product biochar produced by pyrolysis (small ratio) is mixed with lignite with abundant reserves (large ratio) and then carbonized in the second step. During the carbonization process, the flue gas is volatilized and removed, which increases the porosity of the composite carbon. , and the flue gas is discharged into the pool to be absorbed, and the moisture absorbed by the flue gas is recycled to the carbon batching link of the composite mechanism. The composite machine-made charcoal prepared by the invention not only solves the limitations of both biomass charcoal and lignite, but also the resources are recycled, which meets the requirements of energy saving, environmental protection and green development.

发明内容Contents of the invention

针对上述现有技术存在的问题及不足,本发明提供一种高性能复合机制炭的制备方法。该制备过程是以来源丰富、价格低廉、可再生且易于粉碎的生物质以及价格低廉的褐煤为碳源,具有大规模生产价格低、收率高、热值高、孔隙率高、广受市场欢迎的复合机制炭的潜能。本发明通过以下技术方案实现。Aiming at the problems and deficiencies in the above-mentioned prior art, the present invention provides a method for preparing high-performance composite machine-made carbon. The preparation process uses abundant, low-cost, renewable and easily crushed biomass and low-cost lignite as carbon sources. It has the advantages of low mass production price, high yield, high calorific value, and high porosity. Welcome to the potential of composite mechanism charcoal. The present invention is realized through the following technical solutions.

一种高性能复合机制炭的制备方法,其具体步骤如下:A kind of preparation method of high-performance composite mechanism carbon, its specific steps are as follows:

(1)首先将含水率为5%以下的生物质原料、褐煤分别破碎至粒度小于1cm的颗粒;(1) Firstly, the biomass raw material and lignite with a moisture content of less than 5% are crushed to particles with a particle size of less than 1cm;

(2)将步骤(1)得到的生物质原料颗粒在温度为400℃~900℃下热解得到生物炭,将热解过程中产生的生物质气体进一步处理后用作燃气;(2) Pyrolyzing the biomass raw material particles obtained in step (1) at a temperature of 400°C to 900°C to obtain biochar, and further treating the biomass gas generated during the pyrolysis process as fuel;

(3)将质量百分比为10~40%的步骤(2)得到的生物炭、质量百分比为40~70%步骤(1)得到的褐煤、质量百分比为1~10%粘结剂、质量百分比1~10%为助燃剂、质量百分比为5~14%的水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;(3) The biochar obtained in the step (2) with a mass percentage of 10-40%, the lignite obtained in the step (1) with a mass percentage of 40-70%, the mass percentage of 1-10% binder, and the mass percentage of 1 ~10% is a combustion aid, and water with a mass percentage of 5~14% is mixed evenly to obtain a mixed material, and the mixed material is pressed into a carbon rod with a central hole;

(4)将步骤(3)得到的带有中心孔的炭棒以30~200℃/min的升温速率升温至400~700℃炭化1~12h,冷却后得到复合机制炭。(4) The carbon rod with a central hole obtained in step (3) is heated to 400-700°C for 1-12 hours at a heating rate of 30-200°C/min and carbonized for 1-12 hours, and the composite mechanism carbon is obtained after cooling.

所述步骤(1)中生物质原料为核桃壳、松子壳、椰子壳、玉米芯、甘蔗渣、糠醛渣、咖啡壳、花生壳中的一种或者几种任意比例混合物。The biomass raw material in the step (1) is one or a mixture of several of walnut shells, pine nut shells, coconut shells, corncobs, bagasse, furfural residue, coffee shells, and peanut shells in any proportion.

所述步骤(3)中粘结剂制备方法为:将含30wt%以上腐植酸的泥煤、褐煤或风化煤粉碎至粒径小于1mm,按照液固比为1~10:1ml/g加入到百分比浓度为5~30%的NaOH溶液中,在温度为80~120℃下搅拌20~40min制备得到粘结剂。The preparation method of the binder in the step (3) is: crush the peat, lignite or weathered coal containing more than 30wt% humic acid until the particle size is less than 1mm, and add it to the The binder is prepared by stirring in a NaOH solution with a percentage concentration of 5-30% at a temperature of 80-120° C. for 20-40 minutes.

所述步骤(3)得到的助燃剂为50~80wt%二氧化锰、15~30wt%三氧化二铝和5~20wt%碳酸钙混合物。The combustion accelerant obtained in the step (3) is a mixture of 50-80wt% manganese dioxide, 15-30wt% aluminum oxide and 5-20wt% calcium carbonate.

所述步骤(4)炭化过程产生的热解烟气将通过管道引入到蓄水池中被水吸收,蓄水池中的污水将循环利用于步骤(3)中作为混合物料的水。The pyrolysis flue gas produced during the carbonization process in the step (4) will be introduced into the reservoir through the pipeline to be absorbed by the water, and the sewage in the reservoir will be recycled and used as the water in the step (3) as the mixed material.

本发明的有益效果是:该机制炭的固定碳含量≥80%,灰分≤5%,热值≥35MJ/Kg,燃烧时最低温度大于或等于420℃;该机制炭中所用生物质原料和褐煤价格低廉,脱灰效果好,孔隙率高,本机制炭的制备过程中采用两步炭化,第一步炭化过程为生物质原料的热解(干馏)炭-气联产,热解烟气和副产品生物质炭均得到了充分利用;第二步为生物质炭(配比较小)、褐煤(配比较大)等混合物炭化,提高了褐煤的固定碳含量,且挥发分去除过程中产生的大量孔隙有利于机制炭的燃烧,此外,热解烟气排入水池中被吸收,吸收了烟气的水分被循环用到复合机制炭配料环节。本发明制备的复合机制炭不仅解决了生物质炭和褐煤两者的局限性,而且资源得到综合利用,符合绿色发展的要求。The beneficial effects of the present invention are: the fixed carbon content of the machine-made charcoal is ≥ 80%, the ash content is ≤ 5%, the calorific value is ≥ 35MJ/Kg, and the minimum temperature during combustion is greater than or equal to 420°C; the biomass raw material and lignite used in the machine-made charcoal The price is low, the deashing effect is good, and the porosity is high. The carbonization of this mechanism adopts two steps in the preparation process. The first carbonization process is the pyrolysis (dry distillation) of biomass raw materials. The by-product biomass charcoal has been fully utilized; the second step is the carbonization of mixtures of biomass charcoal (small proportion) and lignite (large proportion), which increases the fixed carbon content of lignite and produces a large amount of volatile matter during the removal process. Pores are conducive to the combustion of machine-made charcoal. In addition, the pyrolysis flue gas is discharged into the pool to be absorbed, and the moisture absorbed by the flue gas is recycled to the compound machine-made charcoal batching link. The composite machine-made charcoal prepared by the invention not only solves the limitations of both biomass charcoal and lignite, but also obtains comprehensive utilization of resources and meets the requirements of green development.

具体实施方式detailed description

下面结合具体实施方式,对本发明作进一步说明。The present invention will be further described below in combination with specific embodiments.

实施例1Example 1

该高性能复合机制炭的制备方法,其具体步骤如下:The preparation method of the high-performance composite mechanism carbon, its specific steps are as follows:

(1)首先将含水率为5%以下的生物质原料(质量比1:1:1:1的核桃壳、松子壳、椰子壳和玉米芯混合生物质原料)、褐煤分别破碎至粒度小于1cm的颗粒;(1) First, the biomass raw material with a moisture content of less than 5% (walnut shell, pine nut shell, coconut shell and corn cob mixed biomass raw material with a mass ratio of 1:1:1:1) and lignite are crushed to a particle size of less than 1cm particle;

(2)将步骤(1)得到的生物质原料颗粒在温度为400℃下热解3h得到生物炭,将热解过程中产生的生物质气体进一步处理后用作燃气;(2) The biomass raw material particles obtained in step (1) were pyrolyzed at a temperature of 400°C for 3 hours to obtain biochar, and the biomass gas generated during the pyrolysis process was further processed and used as fuel gas;

(3)将质量百分比为10%的步骤(2)得到的生物炭、质量百分比为70%步骤(1)得到的褐煤、质量百分比为10%粘结剂、质量百分比1%为助燃剂、质量百分比为9%的水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;粘结剂制备方法为:将含30wt%以上腐植酸的泥煤粉碎至粒径小于1mm,按照液固比为10:1ml/g加入到百分比浓度为5%的NaOH溶液中,在温度为80℃下搅拌20min制备得到粘结剂;助燃剂为50wt%二氧化锰、30wt%三氧化二铝和20wt%碳酸钙混合物;(3) The biochar obtained in the step (2) with a mass percentage of 10%, the lignite obtained in the step (1) with a mass percentage of 70%, a binder with a mass percentage of 10%, and a combustion aid with a mass percentage of 1%. 9% water is mixed evenly to obtain a mixed material, and the mixed material is pressed into a carbon rod with a central hole; the preparation method of the binder is: pulverize the peat containing more than 30wt% humic acid until the particle size is less than 1mm, according to The liquid-solid ratio is 10:1ml/g, add it to the NaOH solution with a percentage concentration of 5%, and stir at a temperature of 80°C for 20 minutes to prepare a binder; the combustion aid is 50wt% manganese dioxide, 30wt% aluminum oxide And 20wt% calcium carbonate mixture;

(4)将步骤(3)得到的带有中心孔的炭棒以200℃/min的升温速率升温至700℃炭化1h,冷却后得到复合机制炭;炭化过程产生的热解烟气将通过管道引入到蓄水池中被水吸收,蓄水池中的污水将循环利用于步骤(3)中作为混合物料的水。(4) Heat the carbon rod with a central hole obtained in step (3) to 700°C at a heating rate of 200°C/min for carbonization for 1 hour, and obtain a composite mechanism carbon after cooling; the pyrolysis flue gas generated during the carbonization process will pass through the pipeline Introduced into the storage tank to be absorbed by water, the sewage in the storage tank will be recycled to be used as the water of the mixed material in step (3).

结果表明,生物质炭化得率为32%;经检测,该复合机制炭的固定碳含量为83wt%,灰分含量为5wt%,热值为35MJ/Kg,燃烧时最高温度可以达到420℃。The results showed that the yield of biomass carbonization was 32%. After testing, the fixed carbon content of the composite mechanism carbon was 83wt%, the ash content was 5wt%, the calorific value was 35MJ/Kg, and the maximum temperature during combustion could reach 420°C.

实施例2Example 2

该高性能复合机制炭的制备方法,其具体步骤如下:The preparation method of the high-performance composite mechanism carbon, its specific steps are as follows:

(1)首先将含水率为5%以下的生物质原料(甘蔗渣)、褐煤分别破碎至粒度小于1cm的颗粒;(1) First, the biomass raw material (bagasse) and lignite with a moisture content of less than 5% are crushed to particles with a particle size of less than 1cm;

(2)将步骤(1)得到的生物质原料颗粒在温度为600℃下热解2.5 h得到生物炭,将热解过程中产生的生物质气体进一步处理后用作燃气;(2) The biomass raw material particles obtained in step (1) were pyrolyzed at a temperature of 600°C for 2.5 h to obtain biochar, and the biomass gas generated during the pyrolysis process was further processed and used as fuel gas;

(3)将质量百分比为30%的步骤(2)得到的生物炭、质量百分比为50%步骤(1)得到的褐煤、质量百分比为5%粘结剂、质量百分比10%为助燃剂、质量百分比为5%的水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;粘结剂制备方法为:将含30wt%以上腐植酸的褐煤粉碎至粒径小于1mm,按照液固比为1:1ml/g加入到百分比浓度为20%的NaOH溶液中,在温度为80℃下搅拌20min制备得到粘结剂;助燃剂为60wt%二氧化锰、20wt%三氧化二铝和20wt%碳酸钙混合物;(3) The biochar obtained in the step (2) with a mass percentage of 30%, the lignite obtained in the step (1) with a mass percentage of 50%, the binder with a mass percentage of 5%, and the combustion improver with a mass percentage of 10% 5% water is mixed evenly to obtain a mixed material, and the mixed material is pressed into a carbon rod with a central hole; the preparation method of the binder is: pulverize the lignite containing more than 30wt% humic acid until the particle size is less than 1mm, according to the liquid A solid ratio of 1:1ml/g was added to a NaOH solution with a percentage concentration of 20%, and the binder was prepared by stirring at a temperature of 80°C for 20 minutes; the combustion aid was 60wt% manganese dioxide, 20wt% aluminum oxide and 20wt% calcium carbonate mixture;

(4)将步骤(3)得到的带有中心孔的炭棒以100℃/min的升温速率升温至500℃炭化8h,冷却后得到复合机制炭;炭化过程产生的热解烟气将通过管道引入到蓄水池中被水吸收,蓄水池中的污水将循环利用于步骤(3)中作为混合物料的水。(4) Heat the carbon rod with a central hole obtained in step (3) to 500°C for 8 hours at a heating rate of 100°C/min, and then obtain composite mechanism carbon after cooling; the pyrolysis flue gas generated during the carbonization process will pass through the pipeline Introduced into the storage tank to be absorbed by water, the sewage in the storage tank will be recycled to be used as the water of the mixed material in step (3).

结果表明,生物质炭化得率为28%;经检测,该复合机制炭的固定碳含量为81wt%,灰分含量为4wt%,热值为39MJ/Kg,燃烧时最高温度可以达到440℃。The results show that the yield of biomass carbonization is 28%. After testing, the fixed carbon content of the composite mechanism carbon is 81wt%, the ash content is 4wt%, the calorific value is 39MJ/Kg, and the maximum temperature can reach 440°C during combustion.

实施例3Example 3

该高性能复合机制炭的制备方法,其具体步骤如下:The preparation method of the high-performance composite mechanism carbon, its specific steps are as follows:

(1)首先将含水率为5%以下的生物质原料(质量比为1:1:1的糠醛渣、咖啡壳和花生壳混合生物质料)、褐煤分别破碎至粒度小于1cm的颗粒;(1) First, the biomass raw material with a moisture content of less than 5% (furfural residue with a mass ratio of 1:1:1, coffee husk and peanut husk mixed biomass) and lignite are respectively crushed to particles with a particle size of less than 1cm;

(2)将步骤(1)得到的生物质原料颗粒在温度为900℃下热解1.5h得到生物炭,将热解过程中产生的生物质气体进一步处理后用作燃气;(2) The biomass raw material particles obtained in step (1) were pyrolyzed at a temperature of 900°C for 1.5 hours to obtain biochar, and the biomass gas generated during the pyrolysis process was further processed and used as fuel gas;

(3)将质量百分比为40%的步骤(2)得到的生物炭、质量百分比为40%步骤(1)得到的褐煤、质量百分比为1%粘结剂、质量百分比5%为助燃剂、质量百分比为14%的水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;粘结剂制备方法为:将含30wt%以上腐植酸的风化煤粉碎至粒径小于1mm,按照液固比为5:1ml/g加入到百分比浓度为30%的NaOH溶液中,在温度为100℃下搅拌30min制备得到粘结剂;助燃剂为80wt%二氧化锰、15wt%三氧化二铝和5wt%碳酸钙混合物;(3) The biochar obtained in the step (2) with a mass percentage of 40%, the lignite obtained in the step (1) with a mass percentage of 40%, the mass percentage of 1% binder, the mass percentage of 5% as a combustion aid, and the mass percentage 14% water is mixed evenly to obtain a mixed material, and the mixed material is pressed into a carbon rod with a central hole; the binder preparation method is: pulverize the weathered coal containing more than 30wt% humic acid to a particle size of less than 1mm, according to The liquid-solid ratio is 5:1ml/g, add it to the NaOH solution with a percentage concentration of 30%, and stir at a temperature of 100°C for 30 minutes to prepare a binder; the combustion aid is 80wt% manganese dioxide, 15wt% aluminum oxide And 5wt% calcium carbonate mixture;

(4)将步骤(3)得到的带有中心孔的炭棒以30℃/min的升温速率升温至400℃炭化12h,冷却后得到复合机制炭;炭化过程产生的热解烟气将通过管道引入到蓄水池中被水吸收,蓄水池中的污水将循环利用于步骤(3)中作为混合物料的水。(4) Heat the carbon rod with a central hole obtained in step (3) to 400°C at a heating rate of 30°C/min for carbonization for 12 hours, and obtain a composite mechanism carbon after cooling; the pyrolysis flue gas generated during the carbonization process will pass through the pipeline Introduced into the storage tank to be absorbed by water, the sewage in the storage tank will be recycled to be used as the water of the mixed material in step (3).

结果表明,生物质炭化得率为25%;经检测,该复合机制炭的固定碳含量为86wt%,灰分含量为3.5wt%,挥发分含量为10%,热值为37MJ/Kg,燃烧时最高温度可以达到430℃。The results show that the yield of biomass carbonization is 25%. After testing, the fixed carbon content of the composite mechanism carbon is 86wt%, the ash content is 3.5wt%, the volatile matter content is 10%, and the calorific value is 37MJ/Kg. The highest temperature can reach 430°C.

实施例4Example 4

该高性能复合机制炭的制备方法,其具体步骤如下:The preparation method of the high-performance composite mechanism carbon, its specific steps are as follows:

(1)首先将含水率为5%以下的生物质原料(花生壳)、褐煤分别破碎至粒度小于1cm的颗粒;(1) First, the biomass raw material (peanut shell) and lignite with a moisture content of less than 5% are crushed to particles with a particle size of less than 1cm;

(2)将步骤(1)得到的生物质原料颗粒在温度为800℃下热解2h得到生物炭,将热解过程中产生的生物质气体进一步处理后用作燃气;(2) Biomass raw material particles obtained in step (1) were pyrolyzed at 800°C for 2 hours to obtain biochar, and the biomass gas generated during the pyrolysis process was further processed and used as fuel gas;

(3)将质量百分比为35%的步骤(2)得到的生物炭、质量百分比为50%步骤(1)得到的褐煤、质量百分比为1%粘结剂、质量百分比6%为助燃剂、质量百分比为8%的水混合均匀得到混合物料,将混合物料压制成带有中心孔的炭棒;粘结剂制备方法为:将含30wt%以上腐植酸的风化煤粉碎至粒径小于1mm,按照液固比为5:1 ml/g加入到百分比浓度为20%的NaOH溶液中,在温度为120℃下搅拌40min制备得到粘结剂;助燃剂为65wt%二氧化锰、20wt%三氧化二铝和15wt%碳酸钙混合物;(3) The biochar obtained in the step (2) with a mass percentage of 35%, the lignite obtained in the step (1) with a mass percentage of 50%, the mass percentage of 1% binder, the mass percentage of 6% as a combustion aid, and the mass percentage 8% water is mixed evenly to obtain a mixed material, and the mixed material is pressed into a carbon rod with a central hole; the binder preparation method is: pulverize the weathered coal containing more than 30wt% humic acid until the particle size is less than 1mm, according to A liquid-solid ratio of 5:1 ml/g was added to a NaOH solution with a percentage concentration of 20%, and the binder was prepared by stirring at a temperature of 120°C for 40 minutes; the combustion promoter was 65wt% manganese dioxide, 20wt% di Aluminum and 15wt% calcium carbonate mixture;

(4)将步骤(3)得到的带有中心孔的炭棒以120℃/min的升温速率升温至600℃炭化10h,冷却后得到复合机制炭;炭化过程产生的热解烟气将通过管道引入到蓄水池中被水吸收,蓄水池中的污水将循环利用于步骤(3)中作为混合物料的水。(4) Heat the carbon rod with a central hole obtained in step (3) to 600°C at a heating rate of 120°C/min for carbonization for 10 hours, and obtain composite carbon after cooling; the pyrolysis flue gas generated during the carbonization process will pass through the pipeline Introduced into the storage tank to be absorbed by water, the sewage in the storage tank will be recycled to be used as the water of the mixed material in step (3).

以上对本发明的具体实施方式作了详细说明,但是本发明并不限于上述实施方式,在本领域普通技术人员所具备的知识范围内,还可以在不脱离本发明宗旨的前提下作出各种变化。The specific embodiments of the present invention have been described in detail above, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the gist of the present invention within the scope of knowledge possessed by those of ordinary skill in the art .

Claims (5)

1. a kind of preparation method of high-performance compounding machine charcoal processing, it is characterised in that comprise the following steps that:
(1)First biomass material that moisture content is less than 5%, brown coal are crushed to into respectively particle of the granularity less than 1cm;
(2)By step(1)The biomass raw material particle for obtaining pyrolysis in the case where temperature is for 400 DEG C~900 DEG C obtains charcoal, by heat The biomass gas produced in solution preocess are used as combustion gas after further processing;
(3)By mass percent be 10~40% the step of(2)The charcoal that obtains, mass percent are 40~70% steps(1) The brown coal that obtain, mass percent be 1~10% binding agent, mass percent 1~10% be combustion adjuvant, mass percent be 5~ 14% water is well mixed and obtains mixed material, and mixed material is pressed into into the carbon rod with centre bore;
(4)By step(3)The carbon rod with centre bore for obtaining is warming up to 400~700 with the heating rate of 30~200 DEG C/min DEG C charing 1~12h, compounding machine charcoal processing is obtained after cooling.
2. the preparation method of high-performance compounding machine charcoal processing according to claim 1, it is characterised in that:The step(1)In Biomass material be walnut shell, pine nut shell, cocoanut shell, corncob, bagasse, furfural dregs, coffee shell, peanut shell in one kind or Several arbitrary proportion mixtures of person.
3. the preparation method of high-performance compounding machine charcoal processing according to claim 1, it is characterised in that:The step(3)In Binding agent preparation method is:Mud coal containing more than 30wt% humic acids, brown coal or weathered coal are crushed to into particle diameter and are less than 1mm, according to Liquid-solid ratio is 1~10:1ml/g is added in the NaOH solution that percent concentration is 5~30%, is stirred in the case where temperature is for 80~120 DEG C Mix 20~40min and prepare binding agent.
4. the preparation method of high-performance compounding machine charcoal processing according to claim 1, it is characterised in that:The step(3) The combustion adjuvant for arriving is 50~80wt% manganese dioxide, 15~30wt% alundum (Al2O3)s and 5~20wt% calcium carbonate mixtures.
5. the preparation method of high-performance compounding machine charcoal processing according to claim 1, it is characterised in that:The step(4)Charcoal The pyrolysis smoke that change process is produced will be incorporated in cistern by pipeline and will be only absorbed by the water, and the sewage in cistern will be recycled In step(3)The middle water as mixed material.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107603686A (en) * 2017-10-16 2018-01-19 吴刚 A kind of preparation method of high heating value fragrant machine-made carbon
CN108373928A (en) * 2018-01-11 2018-08-07 定南县洪宇竹木再生制品厂 A kind of coal quality machine-made carbon preparation method
CN108384595A (en) * 2018-01-11 2018-08-10 定南县洪宇竹木再生制品厂 A kind of pecan shell machine-made carbon
CN108720074A (en) * 2018-06-19 2018-11-02 重庆霏洋环保科技股份有限公司 A kind of preparation method of fruit tree shredded tobacco for water pipes charcoal
CN115672943A (en) * 2022-11-07 2023-02-03 昆明理工大学 A kind of preparation method of stable mineral modified biochar material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101195418B1 (en) * 2012-08-08 2012-10-30 한국에너지기술연구원 Method for preparation of high caloric hybrid coal coated with carbon derived from biomass using two-step drying process and high caloric hybrid coal prepared thereby
CN103194245A (en) * 2013-04-07 2013-07-10 昆明理工大学 Preparation method of biomass carbon coal
CN103450915A (en) * 2013-09-07 2013-12-18 鞍钢股份有限公司 Method for manufacturing biomass semicoke for metallurgy

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101195418B1 (en) * 2012-08-08 2012-10-30 한국에너지기술연구원 Method for preparation of high caloric hybrid coal coated with carbon derived from biomass using two-step drying process and high caloric hybrid coal prepared thereby
CN103194245A (en) * 2013-04-07 2013-07-10 昆明理工大学 Preparation method of biomass carbon coal
CN103450915A (en) * 2013-09-07 2013-12-18 鞍钢股份有限公司 Method for manufacturing biomass semicoke for metallurgy

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
李东光: "《工业和民用合成燃料配方与制备》", 31 May 2012, 中国纺织工业社 *
李文哲: "《生物质能源工程》", 31 January 2013, 中国农业出版社 *
煤炭部煤炭科学院北京所: "腐植酸类粘合剂煤球的概况", 《腐植酸类粘合剂煤球的概况 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107603686A (en) * 2017-10-16 2018-01-19 吴刚 A kind of preparation method of high heating value fragrant machine-made carbon
CN108373928A (en) * 2018-01-11 2018-08-07 定南县洪宇竹木再生制品厂 A kind of coal quality machine-made carbon preparation method
CN108384595A (en) * 2018-01-11 2018-08-10 定南县洪宇竹木再生制品厂 A kind of pecan shell machine-made carbon
CN108720074A (en) * 2018-06-19 2018-11-02 重庆霏洋环保科技股份有限公司 A kind of preparation method of fruit tree shredded tobacco for water pipes charcoal
CN115672943A (en) * 2022-11-07 2023-02-03 昆明理工大学 A kind of preparation method of stable mineral modified biochar material

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Application publication date: 20170510