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CN116606678A - Method of Deashing Raw Coal Using Deep Eutectic Solvent - Google Patents

Method of Deashing Raw Coal Using Deep Eutectic Solvent Download PDF

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CN116606678A
CN116606678A CN202310599330.6A CN202310599330A CN116606678A CN 116606678 A CN116606678 A CN 116606678A CN 202310599330 A CN202310599330 A CN 202310599330A CN 116606678 A CN116606678 A CN 116606678A
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eutectic solvent
coal
raw coal
deashing
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CN116606678B (en
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易兰
刘宏博
吴晓琴
陈佳玲
郭立
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Wuhan University of Science and Technology WHUST
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/08Drying or removing water
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/22Impregnation or immersion of a fuel component or a fuel as a whole

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Abstract

本发明涉及一种采用低共熔溶剂对原煤进行脱灰的方法,在技术方案中首先将氢键受体和氢键供体按一定摩尔比加热混合,制备出低共熔溶剂,之后将原煤与制备的低共熔溶剂按一定质量比混合,进行脱灰过程,最后利用低共熔溶剂易溶于水的特性,使用去离子水将处理后的煤洗涤干净。根据本发明可以减少原煤灰分9‑18%,且所述技术方案操作简单,成本低廉,对人体和环境无危害。The invention relates to a method for deashing raw coal with a deep eutectic solvent. In the technical scheme, firstly, the hydrogen bond acceptor and the hydrogen bond donor are heated and mixed according to a certain molar ratio to prepare a deep eutectic solvent, and then the raw coal is It is mixed with the prepared deep eutectic solvent according to a certain mass ratio, and the deashing process is carried out. Finally, the treated coal is washed with deionized water by utilizing the property of the deep eutectic solvent that it is easily soluble in water. According to the invention, the ash content of raw coal can be reduced by 9-18%, and the technical scheme is simple to operate, low in cost, and harmless to human body and environment.

Description

采用低共熔溶剂对原煤进行脱灰的方法Method of Deashing Raw Coal Using Deep Eutectic Solvent

技术领域technical field

本发明涉及煤化工工艺技术领域,具体涉及采用低共熔溶剂处理原煤的方法,能够减少原煤中的灰分含量用于制备低灰分煤和洁净煤。The invention relates to the technical field of coal chemical industry, in particular to a method for treating raw coal with a deep eutectic solvent, which can reduce the ash content in the raw coal for preparing low-ash coal and clean coal.

背景技术Background technique

目前,煤炭作为世界主要能源之一,面对日益贫瘠的石油资源,如何高效利用煤炭资源成为热点问题。在我国,颗粒污染物已逐渐成为城市大气污染的首要污染物,而电厂中的煤燃烧则是其污染的主要来源之一。煤在燃烧的过程中煤的灰分会变成细小的颗粒物,这些颗粒物表面富集了重金属元素,排入空气后会对人体和环境造成巨大的危害,并且煤的灰分会抑制燃烧热的传递,从而降低热效率,导致煤的利用率大大降低。因而煤在利用前进行脱灰过程显得尤为重要。At present, coal is one of the main energy sources in the world. In the face of increasingly poor oil resources, how to efficiently utilize coal resources has become a hot issue. In my country, particulate pollutants have gradually become the primary pollutant of urban air pollution, and coal combustion in power plants is one of the main sources of pollution. During the combustion of coal, the ash content of coal will turn into fine particles. The surface of these particles is enriched with heavy metal elements, which will cause great harm to the human body and the environment after being discharged into the air, and the ash content of coal will inhibit the transfer of combustion heat. Thereby reducing thermal efficiency, resulting in greatly reduced utilization of coal. Therefore, it is particularly important to carry out the deashing process of coal before utilization.

目前,正在研究的一些脱灰方法主要为物理法和化学法。煤的物理脱灰方法主要有磁力分选法、静电分选法和浮选法等,是基于煤中矿物质性质以及部分煤炭的物理性质所决定。煤的化学脱灰方法主要有酸法和碱法,将煤中的有机成分与化学物质反应,使矿物质有效脱除,进而达到降低灰分的目的。但现有的技术所需成本高,操作复杂,所使用的化学试剂多对人体和环境有危害,并且对仪器设备具有一定的腐蚀性。Currently, some deashing methods being studied are mainly physical and chemical. The physical deashing methods of coal mainly include magnetic separation method, electrostatic separation method and flotation method, etc., which are determined based on the properties of minerals in coal and the physical properties of some coal. The chemical deashing methods of coal mainly include acid method and alkali method, which react the organic components in coal with chemical substances to effectively remove minerals, and then achieve the purpose of reducing ash content. However, the existing technology requires high cost and complicated operation, and most of the chemical reagents used are harmful to the human body and the environment, and are corrosive to instruments and equipment.

因此,提供一种低成本绿色环保的原煤脱灰方法,对提高煤炭资源利用率有重大意义。Therefore, providing a low-cost, green and environment-friendly raw coal deashing method is of great significance for improving the utilization rate of coal resources.

发明内容Contents of the invention

有鉴于此,本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,有效脱除了原煤中的灰分,降低生产成本,减少对环境的危害,提高煤的品质,具有良好的经济效益。In view of this, the present invention provides a method for deashing raw coal using a deep eutectic solvent, which effectively removes ash in raw coal, reduces production costs, reduces environmental hazards, improves coal quality, and has good economic benefits.

为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:

采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The method for deashing raw coal by using a deep eutectic solvent comprises the following steps:

(1)将原煤进行自然风干12-24h后,将原煤粉碎,得煤粉;(1) After the raw coal is naturally air-dried for 12-24 hours, the raw coal is crushed to obtain coal powder;

(2)取氢键受体和氢键供体试剂按一定摩尔比混合,加热升温,持续搅拌,制备低共熔溶剂;(2) Mix hydrogen bond acceptor and hydrogen bond donor reagents in a certain molar ratio, heat up, and continue stirring to prepare a deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,按比例加入所述步骤(2)得到的低共熔溶剂中,加热升温并持续搅拌后,趁热抽滤,并用去离子水进行洗涤,对所得煤粉进行干燥处理。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2) in proportion, heat up and keep stirring, then suction filter while it is hot, and wash with deionized water , drying the obtained coal powder.

优选的,所述步骤(1)中的原煤粉碎粒径为100-300μm,小粒径增加原煤与试剂的接触面积,提升处理效率和处理效果。Preferably, the pulverized raw coal in the step (1) has a particle size of 100-300 μm, and a small particle size increases the contact area between the raw coal and the reagent, improving the processing efficiency and effect.

优选的,所述步骤(2)中加热升温温度为70-90℃,直到固体全部融化,溶剂为透明状。Preferably, the heating temperature in the step (2) is 70-90° C. until all the solids are melted and the solvent is transparent.

优选的,所述步骤(3)中煤粉与低共熔溶剂的质量比为1:2。Preferably, the mass ratio of coal powder to deep eutectic solvent in the step (3) is 1:2.

优选的,所述步骤(3)中加热升温温度为50-180℃,搅拌反应3-5h。Preferably, in the step (3), the heating temperature is 50-180° C., and the reaction is stirred for 3-5 hours.

优选的,所述步骤(3)中用去离子水进行洗涤,直到滤液为中性,以保证低共熔溶剂被完全去除。Preferably, the step (3) is washed with deionized water until the filtrate is neutral, so as to ensure that the deep eutectic solvent is completely removed.

优选的,所述步骤(3)中的干燥温度为50-90℃,干燥时间为20-24小时。Preferably, the drying temperature in the step (3) is 50-90° C., and the drying time is 20-24 hours.

经由上述技术方案,与现有的技术对比,本发明的技术方案中使用氢键受体和氢键供体制备低共熔溶剂后再对原煤进行脱灰处理,并利用低共熔溶剂的亲水性将处理的煤与溶剂分离,从而达到煤炭的降灰提质的目的。其成本低廉、绿色环保、方法工艺简单,实现了良好的经济实用效益。Through the above technical solution, compared with the existing technology, the technical solution of the present invention uses the hydrogen bond acceptor and the hydrogen bond donor to prepare the deep eutectic solvent and then deashes the raw coal, and utilizes the affinity of the deep eutectic solvent to The water-based method separates the treated coal from the solvent, so as to achieve the purpose of reducing ash and improving the quality of coal. The method has the advantages of low cost, environmental protection, simple method and process, and realizes good economic and practical benefits.

具体实施方案specific implementation plan

下面对本发明实施例中的技术方案进行清楚地、完整地描述。所描述的实施例仅为本发明的部分实施例,并非全部的实施例。基于本发明中的实施例。其他人员在未作出创造性发展前提下所做出的所有其它实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention are clearly and completely described below. The described embodiments are only some, not all, embodiments of the present invention. Based on the examples in the present invention. All other embodiments made by other people on the premise of no creative development fall within the protection scope of the present invention.

实施例1Example 1

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将脯氨酸和对甲苯磺酸按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix proline and p-toluenesulfonic acid at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至50℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 50°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到9.39%。After testing the ash before and after treatment, the ash removal rate reached 9.39%.

实施例2Example 2

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将乙酰胺和对甲苯磺酸按1:3的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix acetamide and p-toluenesulfonic acid at a molar ratio of 1:3, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至50℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 50°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到9.92%。After testing the ash before and after treatment, the ash removal rate reached 9.92%.

实施例3Example 3

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将乙酰胺和戊二酸按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix acetamide and glutaric acid at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至50℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 50°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到9.00%。After testing the ash before and after treatment, the ash removal rate reached 9.00%.

实施例4Example 4

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将氯化胆碱和对甲苯磺酸按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix choline chloride and p-toluenesulfonic acid at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至50℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 50°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到11.65%。After testing the ash before and after treatment, the ash removal rate reached 11.65%.

实施例5Example 5

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将氯化胆碱和尿素按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix choline chloride and urea at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至150℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 150°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到11.09%。After testing the ash before and after treatment, the ash removal rate reached 11.09%.

实施例6Example 6

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将氯化胆碱和乙二醇按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix choline chloride and ethylene glycol at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至150℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 150°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到18.12%。After testing the ash before and after treatment, the ash removal rate reached 18.12%.

实施例7Example 7

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将氯化胆碱和对甲苯磺酸按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix choline chloride and p-toluenesulfonic acid at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至150℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 150°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到15.97%。After testing the ash before and after treatment, the ash removal rate reached 15.97%.

实施例8Example 8

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将四丁基氯化铵和对甲苯磺酸按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix tetrabutylammonium chloride and p-toluenesulfonic acid at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至150℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 150°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到16.26%。After testing the ash before and after treatment, the ash removal rate reached 16.26%.

实施例9Example 9

本发明提供了采用低共熔溶剂对原煤进行脱灰的方法,包括以下步骤:The invention provides a method for deashing raw coal using a deep eutectic solvent, comprising the following steps:

(1)将原煤进行自然风干18h后,将原煤粉碎至粒径为200μm,得煤粉;(1) After natural air-drying the raw coal for 18 hours, crush the raw coal to a particle size of 200 μm to obtain coal powder;

(2)将氯化胆碱和丙三醇按1:2的摩尔比混合,混合后加热升温至80℃,持续搅拌至无固体残留,完成低共熔溶剂的制备;(2) Mix choline chloride and glycerol at a molar ratio of 1:2, heat up to 80°C after mixing, and continue stirring until no solid remains, and complete the preparation of the deep eutectic solvent;

(3)将所述步骤(1)得到的煤粉,加入所述步骤(2)得到的低共熔溶剂中,二者质量比为1:2,加热升温至150℃,并持续搅拌3h后,趁热抽滤,并用去离子水洗涤,将所得煤粉置于干燥箱中70℃干燥12h。(3) Add the coal powder obtained in the step (1) into the deep eutectic solvent obtained in the step (2), the mass ratio of the two is 1:2, heat up to 150°C, and continue stirring for 3 hours , suction filtered while it was hot, and washed with deionized water, and the obtained coal powder was dried in a drying oven at 70° C. for 12 hours.

测试处理前后的灰分,灰分去除率达到17.15%。After testing the ash before and after treatment, the ash removal rate reached 17.15%.

实施例1-11的不同条件以及相关数据参照表1The different conditions of embodiment 1-11 and relevant data refer to table 1

表1 实施例1-11相关条件和数据Table 1 Relevant conditions and data of Examples 1-11

实施例Example 氢键受体(HBA)Hydrogen bond acceptor (HBA) 氢键供体(HBD)Hydrogen Bond Donor (HBD) HBA与HBD的质量比Mass ratio of HBA to HBD 低共熔溶剂与煤的质量比Mass ratio of deep eutectic solvent to coal 反应温度temperature reflex 脱灰率Deashing rate 实施例1Example 1 脯氨酸proline 对甲苯磺酸p-Toluenesulfonic acid 1:21:2 1:21:2 50℃50℃ 9.39%9.39% 实施例2Example 2 乙酰胺Acetamide 对甲苯磺酸p-Toluenesulfonic acid 1:31:3 1:21:2 50℃50℃ 9.92%9.92% 实施例3Example 3 乙酰胺Acetamide 戊二酸glutaric acid 1:21:2 1:21:2 50℃50℃ 9.00%9.00% 实施例4Example 4 氯化胆碱Choline chloride 对甲苯磺酸p-Toluenesulfonic acid 1:21:2 1:21:2 50℃50℃ 11.65%11.65% 实施例5Example 5 氯化胆碱Choline chloride 尿素urea 1:21:2 1:21:2 150℃150°C 11.09%11.09% 实施例6Example 6 氯化胆碱Choline chloride 乙二醇ethylene glycol 1:21:2 1:21:2 150℃150°C 18.12%18.12% 实施例7Example 7 氯化胆碱Choline chloride 对甲苯磺酸p-Toluenesulfonic acid 1:21:2 1:21:2 150℃150°C 15.97%15.97% 实施例8Example 8 四丁基氯化铵Tetrabutylammonium chloride 对甲苯磺酸p-Toluenesulfonic acid 1:21:2 1:21:2 150℃150°C 16.26%16.26% 实施例9Example 9 氯化胆碱Choline chloride 丙三醇Glycerol 1:21:2 1:21:2 150℃150°C 17.15%17.15%

根据表1数据可知,按照本发明提供的处理方法对原煤进行脱灰处理,能够脱除煤中9.00%-18.12%的灰分。According to the data in Table 1, it can be known that the deashing treatment of raw coal according to the treatment method provided by the present invention can remove 9.00%-18.12% of ash in the coal.

根据实施例1-4和实施例5-9的数据对比可知,高温条件下,低共熔溶剂对煤的脱硫效果更好。According to the data comparison of Examples 1-4 and Examples 5-9, it can be seen that under high temperature conditions, the deep eutectic solvent has a better desulfurization effect on coal.

经由上述具体实施方案的测试,本发明的技术方案所使用的氢键受体和氢键供体试剂较为常见,成本低廉,无毒无污染,且具有较好的脱灰效果。Through the tests of the above specific embodiments, the hydrogen bond acceptor and hydrogen bond donor reagents used in the technical solution of the present invention are relatively common, low in cost, non-toxic and pollution-free, and have a good deashing effect.

本说明书中各个实施例侧重点主要在于低共熔溶剂中氢键受体和氢键供体的选取和混合比例不同,以及低共熔溶剂与原煤混合温度不同,由于不同煤样的结构和组成不同,低共熔溶剂对不同煤的脱灰效果有较大差异,因此各个实施例之间相同相似部分互相参考即可。The focus of each embodiment in this specification is mainly on the selection and mixing ratio of hydrogen bond acceptors and hydrogen bond donors in the deep eutectic solvent, and the different mixing temperatures of the deep eutectic solvent and raw coal. Due to the structure and composition of different coal samples Different, the deashing effect of deep eutectic solvents on different coals is quite different, so the same and similar parts in each embodiment can be referred to each other.

应当理解的是,对公开的上述实施例说明,仅仅用于示例性的说明。对本领域的专业技术人员来说,能够对上述实施例进行多种修改、等同替换、改进等,本文中所定义的一般原理能够在不偏离本技术方案的精神和范围的情况下,出现于其它实施例之中。因此上述实施例不会构成对本发明的限制,其限制范围应为符合与本技术方案所公开的原理和创新点相一致的最宽范围。It should be understood that the descriptions of the above disclosed embodiments are only for exemplary description. For those skilled in the art, various modifications, equivalent replacements, improvements, etc. can be made to the above-mentioned embodiments, and the general principles defined herein can appear in other embodiments without departing from the spirit and scope of the technical solution. Among the examples. Therefore, the above-mentioned embodiments will not constitute a limitation to the present invention, and the scope of limitation should be the widest range consistent with the principles and innovations disclosed in the technical solution.

Claims (7)

1. The method for deashing raw coal by adopting the eutectic solvent is characterized by comprising the following steps of:
(1) Natural air-drying raw coal for 12-24h, and crushing the raw coal to obtain coal dust;
(2) Mixing a hydrogen bond acceptor and a hydrogen bond donor reagent according to a certain molar ratio, heating to raise the temperature, and continuously stirring to prepare a eutectic solvent;
(3) And (3) adding the pulverized coal obtained in the step (1) into the eutectic solvent obtained in the step (2) in proportion, heating, continuously stirring, filtering while the pulverized coal is hot, washing the pulverized coal with deionized water, and drying the obtained pulverized coal.
2. The method for deashing raw coal using a eutectic solvent according to claim 1, wherein the crushed raw coal in the step (1) has a particle size of 100-300 μm.
3. The method for deashing raw coal using a eutectic solvent according to claim 1, wherein the heating temperature in the step (2) is 70-90 ℃ until the solid is completely melted, and the solvent is transparent.
4. The method for deashing raw coal using a eutectic solvent according to claim 1, wherein the mass ratio of pulverized coal to the eutectic solvent in the step (3) is 1:2.
5. The method for deashing raw coal using a eutectic solvent according to claim 1, wherein the heating temperature in the step (3) is 50-180 ℃, and the reaction is stirred for 3-5 hours.
6. The method for deashing raw coal using eutectic solvents according to claim 1, wherein the step (3) is performed with deionized water until the filtrate is neutral.
7. The method for deashing raw coal using a eutectic solvent according to claim 1, wherein the drying temperature in the step (3) is 50-90 ℃ and the drying time is 20-24 hours.
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Citations (2)

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Publication number Priority date Publication date Assignee Title
US4119524A (en) * 1976-06-01 1978-10-10 Kerr-Mcgee Corporation Coal deashing process having improved solvent recovery techniques
CN103923680A (en) * 2014-04-30 2014-07-16 安徽工业大学 Method for increasing yield of pyrolytic tar of lignite and improving quality of pyrolytic tar of lignite through pretreating lignite by using acidic ionic liquid

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4119524A (en) * 1976-06-01 1978-10-10 Kerr-Mcgee Corporation Coal deashing process having improved solvent recovery techniques
CN103923680A (en) * 2014-04-30 2014-07-16 安徽工业大学 Method for increasing yield of pyrolytic tar of lignite and improving quality of pyrolytic tar of lignite through pretreating lignite by using acidic ionic liquid

Non-Patent Citations (1)

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Title
ANKUR DWIVEDI等: "《Investigations of coal beneficiation by using choline chloride and urea-based deep eutectic solvent》", 《INTERNATIONAL JOURNAL OF COAL PREPARATION AND UTILIZATION》, 11 March 2022 (2022-03-11), pages 423 - 435 *

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