CN1644650A - Combined process for dry distillation of coal and production of carbon black by plasma cracking - Google Patents
Combined process for dry distillation of coal and production of carbon black by plasma cracking Download PDFInfo
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Abstract
本发明煤干馏与等离子裂解制碳黑的组合工艺,属于煤化工、等离子化工与碳黑生产领域,其特征在于煤经过干馏过程生成焦碳、半焦,及含有大量含碳挥发性物质的干馏气,含有挥发性含碳物质的干馏气直接进入等离子反应器,与等离子体作用生成碳黑和氢气等产品,构成煤干馏与等离子裂解制碳黑的组合工艺。本发明是解决现有工艺能量利用率低下,生产碳黑原料紧缺的问题。该组合工艺具有:能量利用效率高,流程短,节省设备投资,生产成本低,经济效益显著,环境污染小等特点。The combined process of coal dry distillation and plasma cracking to produce carbon black according to the invention belongs to the field of coal chemical industry, plasma chemical industry and carbon black production, and is characterized in that coal generates coke and semi-coke through the dry distillation process, and dry distillation containing a large amount of carbon-containing volatile substances The dry distillation gas containing volatile carbon-containing substances directly enters the plasma reactor, and reacts with the plasma to generate carbon black and hydrogen and other products, forming a combined process of coal dry distillation and plasma cracking to produce carbon black. The invention solves the problems of low utilization rate of energy in the existing process and shortage of raw materials for producing carbon black. The combination process has the characteristics of high energy utilization efficiency, short process, saving equipment investment, low production cost, significant economic benefits, and little environmental pollution.
Description
技术领域technical field
本发明煤干馏与等离子裂解制碳黑的组合工艺,涉及一种煤干馏与等离子裂解生产碳黑的组合工艺,属于煤化工、等离子化工与碳黑生产领域。The invention relates to a combined process for producing carbon black by coal dry distillation and plasma cracking, which relates to a combined process for producing carbon black by coal dry distillation and plasma cracking, and belongs to the fields of coal chemical industry, plasma chemical industry and carbon black production.
技术背景technical background
炭黑和煤干馏的主要产品(包括冶金焦、铸造焦、铁合金焦、煤气和煤焦油),是现代国民经济中不可缺少的化工原料,在许多基础工业部门发挥着极其重要的作用。Carbon black and the main products of coal dry distillation (including metallurgical coke, foundry coke, ferroalloy coke, gas and coal tar) are indispensable chemical raw materials in the modern national economy and play an extremely important role in many basic industrial sectors.
炭黑原料油按来源分为三类:一是澄清油(DC),就是粗柴油流态催化裂化(FCC)生产汽油时产生的;二是乙烯焦油(ET),是石脑油和粗柴油蒸汽裂解生产乙烯过程中产生的;三是煤焦油及其馏分油(CT),包括杂酚油和蒽油等,是煤转化过程中产生的。欧洲和美国的炭黑油以DC为主,尤其是美国95%以上为DC。我国是以煤焦油和乙烯焦油为主。Carbon black raw material oil is divided into three categories according to the source: one is clarified oil (DC), which is produced when gasoline is produced by fluid catalytic cracking (FCC) of gas oil; the other is ethylene tar (ET), which is naphtha and gas oil Produced in the process of steam cracking to produce ethylene; the third is coal tar and its fractions (CT), including creosote oil and anthracene oil, etc., which are produced in the process of coal conversion. The carbon black oil in Europe and the United States is mainly DC, especially in the United States, more than 95% is DC. my country is mainly coal tar and ethylene tar.
我国炭黑2003年消费量超过100万吨,已突破了规划2005年的预测,接近于2010年需求量的水平,橡胶等工业对碳黑的需求强劲,碳黑处于供不应求的状态。我国2003年乙烯表观消费量达600多万吨,估算所产生的总的乙烯焦油量应在150~200万吨,而实际上全部乙烯焦油的30%~50%可供炭黑生产,其余全部作为燃料,乙烯焦油短缺是现实问题。去年我国焦炭产量16000多万吨,估算可提供的煤焦油为350万吨,实际上相当一部分焦油在还没有从干馏气中冷却析出时就已经随干馏气白白烧掉,既浪费资源又污染环境,此外煤焦油还有一部分用于生产萘等化工产品,真正用于生产碳黑的煤焦油同样是短缺的。my country's carbon black consumption in 2003 exceeded 1 million tons, which exceeded the forecast for 2005 and was close to the level of demand in 2010. The demand for carbon black in rubber and other industries is strong, and carbon black is in short supply. my country's apparent consumption of ethylene in 2003 reached more than 6 million tons, and the estimated total ethylene tar produced should be 1.5 to 2 million tons. In fact, 30% to 50% of all ethylene tar can be used for carbon black production, and the rest All used as fuel, the shortage of ethylene tar is a real problem. Last year, my country's coke output was more than 160 million tons, and the available coal tar was estimated to be 3.5 million tons. In fact, a considerable part of the tar was burned with the retort gas before it was cooled and precipitated from the retort gas, which wastes resources and pollutes the environment. , In addition, some coal tar is used to produce naphthalene and other chemical products, and the coal tar actually used to produce carbon black is also in short supply.
由于以上原因炭黑原料油长期是卖方市场,且碳黑生产的主要成本是原料油,占碳黑总成本的70%~80%。可以说谁拥有了原料,谁就在炭黑生产中立于不败之地。另一方面,煤干馏气合理利用率严重不足,大量的干馏气被浪费。Due to the above reasons, carbon black raw material oil has long been a seller's market, and the main cost of carbon black production is raw material oil, which accounts for 70% to 80% of the total cost of carbon black. It can be said that whoever has the raw materials will be invincible in the production of carbon black. On the other hand, the reasonable utilization rate of coal dry distillation gas is seriously insufficient, and a large amount of dry distillation gas is wasted.
碳黑的传统制造工艺有炉法、槽法、热裂解法,等离子裂解法碳黑生产新工艺尽管碳黑质量好,污染小,但存在耗电比常规工艺高,热效率低的问题。The traditional manufacturing process of carbon black includes furnace method, tank method, thermal cracking method, and plasma cracking method. Although the new carbon black production process has good quality and low pollution, it has the problems of higher power consumption and lower thermal efficiency than conventional processes.
在煤干馏工艺中,自干馏室导出的干馏气含有CO、H2、CH4、挥发性含碳物质,经过冷却、处理,得到煤气和煤焦油;在碳黑生产工艺中,将煤焦油首先预热,再送入碳黑反应炉中,发生反应生成碳黑。在此过程中干馏气先被冷却后被加热,能量重复浪费,同时需要冷却和加热设备。干馏气中挥发性含碳物质在冷却加热过程中易发生二次反应生成焦油渣和硬碳,形成资源浪费和环境污染。In the coal dry distillation process, the dry distillation gas derived from the dry distillation chamber contains CO, H 2 , CH 4 , and volatile carbon-containing substances. After cooling and processing, coal gas and coal tar are obtained; in the carbon black production process, the coal tar is first Preheating, and then into the carbon black reaction furnace, the reaction occurs to generate carbon black. In this process, the retort gas is first cooled and then heated, and the energy is repeatedly wasted, and cooling and heating equipment are required at the same time. The volatile carbon-containing substances in the retort gas are prone to secondary reactions during the cooling and heating process to form tar residue and hard carbon, resulting in waste of resources and environmental pollution.
发明内容Contents of the invention
本发明煤干馏与等离子裂解制碳黑的组合工艺的目的是:解决目前碳黑生产原料短缺,煤干馏气利用率低下;煤干馏工艺与等离子裂解法生产碳黑工艺能量利用效率低的问题,并提供一种煤干馏与等离子裂解组合制碳黑的组合工艺。The purpose of the combined process of coal dry distillation and plasma cracking to produce carbon black of the present invention is: to solve the shortage of raw materials for carbon black production at present, the low utilization rate of coal dry distillation gas; the problem of low energy utilization efficiency of coal dry distillation process and plasma cracking process for producing carbon black, Also provided is a combined process for producing carbon black by combining coal dry distillation and plasma cracking.
本发明煤干馏与等离子裂解制碳黑的组合工艺其特征在于:煤经过干馏生成焦碳、半焦产品,同时生成含有挥发性含碳物质的干馏气直接进入等离子反应器,与等离子体作用生成碳黑、氢气和其他副产品,实质上就是一种将煤干馏生产半焦、焦碳工艺和等离子裂解制碳黑工艺进行组合的工艺。The combined process of coal dry distillation and plasma cracking to produce carbon black in the present invention is characterized in that: coal is dry-distilled to generate coke and semi-coke products, and at the same time, dry distillation gas containing volatile carbon-containing substances is directly entered into the plasma reactor, and generated by the interaction with the plasma Carbon black, hydrogen and other by-products are essentially a process that combines coal dry distillation to produce semi-coke, coke process and plasma cracking process to produce carbon black.
煤干馏与等离子裂解制碳黑的组合工艺,该工艺包含以下具体步骤:A combined process of coal dry distillation and plasma cracking to produce carbon black, the process includes the following specific steps:
I.将泥炭或褐煤或烟煤或他们的混合物输入干馏系统,煤在干馏系统中受热500~900℃,发生以热解为主的反应,生成焦炭、半焦等低挥发分含碳固体物质和含有挥发性含碳物质的干馏气;I. Put peat or lignite or bituminous coal or their mixture into the retort system, the coal is heated at 500-900°C in the retort system, and a pyrolysis-based reaction occurs to generate coke, semi-coke and other low-volatile carbon-containing solid substances and Retort gas containing volatile carbonaceous substances;
II.含有挥发性含碳物质的干馏气进入等离子反应器中,含有挥发性含碳物质的干馏气和等离子体作用,体系温度上升至1500℃~3000℃,反应在常压下进行,干馏气裂解为碳黑和富氢气体。根据使用的等离子发生器的工作气体是H2、Ar、O2、N2、H2O、空气等气体不同,产物除碳黑和氢气外,还有少量的CO、N2、CO2、CnHm、NH3等气体;II. The dry distillation gas containing volatile carbon-containing substances enters the plasma reactor, the dry distillation gas containing volatile carbon-containing substances interacts with the plasma, the temperature of the system rises to 1500 ° C ~ 3000 ° C, the reaction is carried out under normal pressure, and the dry distillation gas Cracked into carbon black and hydrogen-rich gas. Depending on the working gas of the plasma generator used is H 2 , Ar, O 2 , N 2 , H 2 O, air and other gases, the products include carbon black and hydrogen, and a small amount of CO, N 2 , CO 2 , C n H m , NH 3 and other gases;
III.碳黑和富氢气体进入分离系统,分离出碳黑和气体混合物,收集碳黑造粒包装成为产品。气体混合物可作以下处理:(1)直接作为燃气、还原气、合成气使用;(2)燃气发电供应等离子系统和整套工艺系统使用;(3)混合气进一步分离出H2、C2H2等气体作为产品气。III. Carbon black and hydrogen-rich gas enter the separation system, and the mixture of carbon black and gas is separated, and the carbon black is collected, granulated and packaged to become a product. The gas mixture can be processed as follows: (1) directly used as fuel gas, reducing gas, and synthesis gas; (2) gas-fired power generation supply plasma system and the entire process system; (3) further separation of H 2 , C 2 H 2 from the mixed gas And other gas as product gas.
上述等离子裂解制碳黑工艺中使用的等离子体由气体放电方法产生。The plasma used in the process of producing carbon black by plasma cracking is generated by a gas discharge method.
本发明通过实施以上技术方案,可取得如下优点和积极效果:The present invention can obtain the following advantages and positive effects by implementing the above technical solutions:
1.煤干馏气的热量被充分利用,大大提高了煤干馏与等离子裂解制碳黑两套工艺的能量利用效率。综合能耗低于传统的油炉法、接触法、热解裂解法及等离子裂解制碳黑生产工艺;2.缩短了两套工艺流程,节省了部分设备投资;3.为干馏气的利用开辟了新途径;4.拓宽了碳黑生产原料的来源,大大降低了碳黑的生产成本,经济效益显著;5.碳黑收获率高,可达90%以上,节约原料;6.等离子体加热功率,等离子发生器工作气体等参数调节极为简单,可分别控制碳黑的某个特性或多个特性,生产出适合各种用途要求的碳黑材料;7.减少了煤干馏和碳黑生产过程中的环境污染;8.副产品氢气、乙炔具有很高的经济价值。1. The heat of coal dry distillation gas is fully utilized, which greatly improves the energy utilization efficiency of the two processes of coal dry distillation and plasma cracking to carbon black. The comprehensive energy consumption is lower than the traditional oil furnace method, contact method, pyrolysis cracking method and plasma cracking carbon black production process; 2. Shorten the two sets of technological processes and save some equipment investment; 3. Open up for the utilization of retort gas 4. Broaden the source of raw materials for carbon black production, greatly reducing the production cost of carbon black, with remarkable economic benefits; 5. The yield of carbon black is high, up to 90%, saving raw materials; 6. Plasma heating Power, plasma generator working gas and other parameters are very simple to adjust, and one or more characteristics of carbon black can be controlled separately to produce carbon black materials suitable for various purposes; 7. Reduce the production process of coal dry distillation and carbon black 8. The by-products hydrogen and acetylene have high economic value.
具体实施方式Detailed ways
实施方式1Embodiment 1
气肥煤、肥煤、焦煤、瘦煤的混合煤加入干馏室,火道内燃烧产生煤干馏所需要的热量,由炉墙传入。火道加热用燃料由等离子碳黑生产系统的气相副产物提供,煤料在干馏室内发生干燥、裂解生成半焦、焦碳,析出含挥发性含碳物质的干馏气。干馏气送入等离子碳黑反应器,和含有高活性粒子的等离子体作用,体系温度上升至1800℃,干馏气瞬间裂解生成碳黑和氢气等副产物。带有碳黑的烟气在反应器底部喷水降温,经过旋风分离器、袋滤器捕集碳黑,收集下来的碳黑经过输送、筛分、造粒后包装。袋滤器分离出的富氢气体,部分供给干馏工艺加热使用;部分发电供等离子系统和整个工艺系统使用;部分富氢气体经过分离得到纯的氢气、乙炔等产品,少量氢气作为等离子发生器工作气。The mixed coal of gas fat coal, fat coal, coking coal and lean coal is added into the carbonization chamber, and the heat required for coal carbonization is generated by burning in the fire channel, which is introduced from the furnace wall. Fuel for heating the flue is provided by the gas phase by-products of the plasma carbon black production system. The coal material is dried and cracked in the retort chamber to generate semi-coke and coke, and the retort gas containing volatile carbon-containing substances is precipitated. The retort gas is sent into the plasma carbon black reactor, and interacts with the plasma containing highly active particles. The temperature of the system rises to 1800°C, and the retort gas is instantly cracked to generate by-products such as carbon black and hydrogen. The flue gas with carbon black is sprayed with water at the bottom of the reactor to cool down, and the carbon black is collected by a cyclone separator and a bag filter. The collected carbon black is transported, screened, granulated and then packaged. Part of the hydrogen-rich gas separated by the bag filter is supplied to the dry distillation process for heating; part of the power generation is used for the plasma system and the entire process system; part of the hydrogen-rich gas is separated to obtain pure hydrogen, acetylene and other products, and a small amount of hydrogen is used as the working gas of the plasma generator .
实施方式2Embodiment 2
褐煤与固体热载体(热半焦)在干馏反应器内混合,煤料被迅速加热,发生快速裂解,在干馏反应器后段完成干馏并析出。固体热载体送入提升管以热烟气并流加热,进入旋风分离器,烟气排除,半焦进入半焦槽。部分半焦作为产品;部分半焦返回干馏反应器循环使用。含有挥发性含碳物质的干馏气送入等离子裂解工艺系统,在等离子裂解反应器中,部分等离子化形成等离子体,反应器平均温度上升至2800℃,挥发性含碳物质瞬间发生裂解生成碳黑和富氢副产物,高温含碳黑烟气在换热器中预热干馏工艺加热所需的空气和富氢气体,然后以急冷水冷却含碳黑烟气,经过滤袋器捕集碳黑,碳黑进入粉状碳黑贮罐,然后湿法造粒,产品包装。富氢气体部分供给干馏工艺加热使用,部分发电供等离子系统和整个工艺系统使用。或部分富氢气体经过分离得到纯的氢气、乙炔等产品。Lignite and solid heat carrier (hot semi-coke) are mixed in the dry distillation reactor, the coal material is heated rapidly, rapid cracking occurs, and dry distillation and precipitation are completed in the rear section of the dry distillation reactor. The solid heat carrier is sent into the riser to be heated by the co-current flow of hot flue gas, then enters the cyclone separator, the flue gas is discharged, and the semi-coke enters the semi-coke tank. Part of the semi-coke is used as a product; part of the semi-coke is returned to the dry distillation reactor for recycling. The retort gas containing volatile carbon-containing substances is sent to the plasma cracking process system. In the plasma cracking reactor, part of the plasma is formed to form plasma. The average temperature of the reactor rises to 2800°C, and the volatile carbon-containing substances are cracked instantly to form carbon black. And hydrogen-rich by-products, high-temperature soot-containing flue gas is preheated in the heat exchanger to heat the air and hydrogen-rich gas required by the carbonization process, and then the soot-containing flue gas is cooled by quenching water, and the carbon black is captured by the filter bag , the carbon black enters the powdered carbon black storage tank, then wet granulation, product packaging. Part of the hydrogen-rich gas is used for heating in the dry distillation process, and part of the power is used for the plasma system and the entire process system. Or part of the hydrogen-rich gas is separated to obtain pure hydrogen, acetylene and other products.
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