CN108636615A - A kind of Fine Coal Flotation collecting agent preparation method - Google Patents
A kind of Fine Coal Flotation collecting agent preparation method Download PDFInfo
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- CN108636615A CN108636615A CN201810350190.8A CN201810350190A CN108636615A CN 108636615 A CN108636615 A CN 108636615A CN 201810350190 A CN201810350190 A CN 201810350190A CN 108636615 A CN108636615 A CN 108636615A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/018—Mixtures of inorganic and organic compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
- B03D2203/04—Non-sulfide ores
- B03D2203/08—Coal ores, fly ash or soot
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Abstract
Description
技术领域technical field
本发明涉及一种煤浮选药剂技术领域,特别是一种细粒煤浮选捕收剂制备方法。The invention relates to the technical field of coal flotation agents, in particular to a method for preparing fine coal flotation collectors.
背景技术Background technique
煤炭作为我国最主要的化石能源,在未来相当长的时间内,其在一次能源消费结构中的主导地位不会改变。煤炭是有机和无机材料的混合物,因此在使用前需要分选。随着国民经济的高速发展,能源需求量不断增加,中、高变质程度的煤被大量开采,储量日益减少,然而,储量大,易获取的低阶煤和氧化煤由于难以有效的分选,没有得到很好的利用。Coal is the most important fossil energy in my country, and its dominant position in the primary energy consumption structure will not change for a long time in the future. Coal is a mixture of organic and inorganic materials and therefore needs to be sorted before use. With the rapid development of the national economy, the demand for energy continues to increase, and coals with medium and high metamorphic degrees are mined in large quantities, and their reserves are decreasing day by day. Not well utilized.
煤炭高效分选技术是实现煤炭资源清洁高效利用的重要前提。其中,浮选是目前分选小于0.5mm煤炭最成熟、最有效的方法,并广泛用于工业生产。在浮选中,使用浮选机分离细粒煤(<0.5mm)。一般而言,煤具有天然的疏水性,但这种疏水程度不足以有效地浮选,通常需要非极性烃类油如柴油和煤油作为捕收剂以进一步提高煤颗粒的可浮性。High-efficiency coal sorting technology is an important prerequisite for realizing clean and efficient utilization of coal resources. Among them, flotation is currently the most mature and effective method for sorting coal smaller than 0.5mm, and is widely used in industrial production. In flotation, fine coal (<0.5mm) is separated using a flotation machine. In general, coal is naturally hydrophobic, but this degree of hydrophobicity is not sufficient for effective flotation, and non-polar hydrocarbon oils such as diesel and kerosene are usually required as collectors to further improve the floatability of coal particles.
然而,对于低阶煤和氧化煤等难浮煤而言,其表面往往含有大量的含氧官能团,亲水性强,可浮性差,采用常规的油性药剂(柴油、煤油等)很难进行有效地浮选,且选择性差。为解决该技术难题,目前的研究主要集中于研制高效的浮选药剂或者药剂组合方法,表面改性等以提高难浮煤表面的疏水性和选择性。具体包括在浮选过程中添加各种表面活性剂,磨矿预处理、加热加压预处理、微波或者超声波预处理、高剪切调浆等技术手段。虽然上述手段可改善难浮煤的浮选效果,但是表面改性的成本较高,难以工业化。其次,目前的研究主要关注于减少煤表面的含氧官能团数量,提高其疏水性,从而改善其浮选效果。但是,难浮煤泥浮选过程中泡沫稳定性差,泡沫携带的固体量少,导致其精煤产品产率低的问题未得到足够重视。因此,开发一种提高煤泥浮选回收效果的新型药剂的制备方法,将会为改善煤泥的浮选回收效果提供新的思路。However, for difficult-to-float coals such as low-rank coal and oxidized coal, the surface often contains a large number of oxygen-containing functional groups, which are highly hydrophilic and poor in floatability. Ground flotation, and poor selectivity. In order to solve this technical problem, the current research is mainly focused on the development of efficient flotation reagents or reagent combination methods, surface modification, etc. to improve the hydrophobicity and selectivity of the difficult-to-float coal surface. Specifically, it includes adding various surfactants during the flotation process, ore grinding pretreatment, heating and pressure pretreatment, microwave or ultrasonic pretreatment, high-shear pulping and other technical means. Although the above means can improve the flotation effect of difficult-to-float coal, the cost of surface modification is high and it is difficult to industrialize. Secondly, current research mainly focuses on reducing the number of oxygen-containing functional groups on the coal surface and increasing its hydrophobicity, thereby improving its flotation effect. However, in the flotation process of difficult-to-float slime, the foam stability is poor, and the amount of solids carried by the foam is small, resulting in low yield of clean coal products, which has not been paid enough attention. Therefore, the development of a preparation method for a new agent that improves the flotation recovery effect of coal slime will provide a new idea for improving the flotation recovery effect of coal slime.
发明内容Contents of the invention
本发明的目的是要提供一种细粒煤浮选捕收剂制备方法,解决非极性烃类油在煤泥浮选回收精煤浮选回收效果差的问题。The purpose of the present invention is to provide a fine-grained coal flotation collector preparation method to solve the problem of poor recovery effect of non-polar hydrocarbon oil in coal slime flotation recovery clean coal flotation recovery.
本发明的目的是这样实现的:浮选捕收剂制备方法,步骤如下:The object of the present invention is achieved like this: the preparation method of flotation collector, step is as follows:
(1)制备蜡烛灰:在4个蜡烛火焰顶部倒置250ml的烧杯以使火焰不完全燃烧,烟灰附着在烧杯内壁,直至烧杯内壁有一层蜡烛灰,制备完成,收集备用;(1) Preparation of candle ashes: Invert 250ml beakers on the top of the 4 candle flames so that the flames do not burn completely, and the soot adheres to the inner wall of the beaker until there is a layer of candle ashes on the inner wall of the beaker. After the preparation is completed, collect it for later use;
(2)将步骤(1)制备的蜡烛灰取1g,加入120-180ml的非极性烃类油中,混匀后静置24-48h;即获得浮选捕收剂。(2) Take 1 g of the candle ash prepared in step (1), add it to 120-180 ml of non-polar hydrocarbon oil, mix it and let it stand for 24-48 hours; the flotation collector is obtained.
所述的非极性烃类油包括:煤油、改性煤油、柴油、燃料油、天然气冷凝油或正十二烷中的任意一种。The non-polar hydrocarbon oil includes: any one of kerosene, modified kerosene, diesel oil, fuel oil, natural gas condensate oil or n-dodecane.
有益效果,由于采用了上述方案,通过在非极性烃类油中添加一种由蜡烛不完全燃烧而制备的蜡烛灰,在浮选过程中有助于矿物表面水化膜的破裂和油滴的分散,从而明显改善煤泥的浮选回收效果。Beneficial effect, due to the above scheme, by adding a kind of candle ashes prepared by incomplete combustion of candles in non-polar hydrocarbon oils, it helps the rupture of the hydration film on the mineral surface and oil droplets during the flotation process Dispersion, thereby significantly improving the flotation recovery effect of coal slime.
解决了非极性烃类油在煤泥浮选回收精煤效果差的问题,达到了本发明的目的。The problem of poor recovery of clean coal by non-polar hydrocarbon oil in coal slime flotation is solved, and the object of the invention is achieved.
优点:细粒煤浮选药剂制备方法,用以精煤提质,浮选捕收剂较传统的非极性烃类油捕收剂在浮选过程中有助于矿物表面水化膜的破裂和油滴的分散,提高煤粒疏水性,从而明显改善煤泥的浮选回收效果。Advantages: The preparation method of fine coal flotation agent is used to improve the quality of clean coal. Compared with the traditional non-polar hydrocarbon oil collector, the flotation collector helps to break the hydration film on the mineral surface during the flotation process And the dispersion of oil droplets, improve the hydrophobicity of coal particles, thereby significantly improving the flotation recovery effect of coal slime.
附图说明Description of drawings
图1为本发明的蜡烛灰制备的设备示意图。Figure 1 is a schematic diagram of equipment for preparing candle ash of the present invention.
图2为本发明的浮选捕收剂制备流程图。Fig. 2 is a flow chart of the preparation of the flotation collector of the present invention.
图3为本发明的浮选工艺流程图。Fig. 3 is the flow chart of the flotation process of the present invention.
具体实施方式Detailed ways
图2中,浮选捕收剂制备流程图,方法步骤如下:In Fig. 2, the flow chart of preparation of flotation collector, method steps are as follows:
(1)制备蜡烛灰:在4个蜡烛火焰顶部倒置250ml的烧杯以使火焰不完全燃烧,烟灰附着在烧杯内壁,直至烧杯内壁有一层蜡烛灰,制备完成,收集备用;(如图1所示);(1) Preparation of candle ashes: Invert 250ml beakers at the top of 4 candle flames so that the flames do not burn completely, and the soot adheres to the inner wall of the beaker until there is a layer of candle ashes on the inner wall of the beaker. After the preparation is completed, collect it for later use; (as shown in Figure 1 );
(2)将步骤(1)制备的蜡烛灰取1g,加入120-180ml的非极性烃类油中,混匀后静置24-48h;即获得浮选捕收剂。(2) Take 1 g of the candle ash prepared in step (1), add it into 120-180 ml of non-polar hydrocarbon oil, mix it and let it stand for 24-48 hours; the flotation collector is obtained.
所述的非极性烃类油包括:煤油、改性煤油、柴油、燃料油、天然气冷凝油或正十二烷中的任意一种。The non-polar hydrocarbon oil includes: any one of kerosene, modified kerosene, diesel oil, fuel oil, natural gas condensate oil or n-dodecane.
下面结合附图来具体描述本发明的优选实施例,其中,附图构成本申请的一部分,并于本发明的实施例一起用于阐释本发明的原理。Preferred embodiments of the present invention will be specifically described below in conjunction with the accompanying drawings, wherein the accompanying drawings constitute a part of the application and are used together with the embodiments of the present invention to explain the principles of the present invention.
实施例1:煤泥浮选药剂,非极性烃类油捕收剂的原料按固液比为:蜡烛灰1g,非极性烃类油120-180ml;混匀后静置24-48h;即获得浮选捕收剂。Embodiment 1: Coal slime flotation agent, the raw material of nonpolar hydrocarbon oil collector is as follows according to solid-liquid ratio: candle ash 1g, nonpolar hydrocarbon oil 120-180ml; Stand still 24-48h after mixing; That is to obtain the flotation collector.
所述的非极性烃类油包括:煤油、改性煤油、柴油、燃料油、天然气冷凝油或正十二烷中的任意一种。The non-polar hydrocarbon oil includes: any one of kerosene, modified kerosene, diesel oil, fuel oil, natural gas condensate oil or n-dodecane.
如图3所示,本发明的具体浮选工艺流程,步骤如下:As shown in Figure 3, the concrete flotation process flow of the present invention, the steps are as follows:
1、将粒度在0.5mm以下的细粒煤泥(原料)加入浮选槽中,加入自来水调浆,搅拌1-3min。1. Add fine-grained coal slime (raw material) with a particle size below 0.5 mm into the flotation tank, add tap water to adjust the slurry, and stir for 1-3 minutes.
2、在步骤1的矿浆中加入捕收剂,搅拌1-3min。2. Add collector to the slurry in step 1, and stir for 1-3 minutes.
3、在步骤2的矿浆中加入起泡剂,搅拌0.5-1min。3. Add foaming agent to the slurry in step 2, and stir for 0.5-1min.
4、在步骤3的矿浆中充入气泡进行浮选;浮选时间为3-5min,分别收集泡沫浮出的颗粒和矿浆中停留的颗粒,作为最终的精煤、尾煤产品。4. Fill the pulp in step 3 with air bubbles for flotation; the flotation time is 3-5 minutes, and the particles floating out of the foam and the particles staying in the pulp are collected separately as the final clean coal and tailings products.
5、所述步骤1中的细粒煤泥为神东大柳塔选煤厂长焰煤;所述步骤1中的水为自来水,或者为去离子水,或者为生产系统的循环水。5. The fine-grained coal slime in the step 1 is long flame coal of Shendong Daliuta Coal Preparation Plant; the water in the step 1 is tap water, or deionized water, or circulating water of the production system.
6、所述步骤2中的捕收剂为本发明制备的捕收剂与单纯的非极性烃类油对比,用量分别为5000、7000、9000g/t干煤泥。6. The collector in the step 2 is compared with the collector prepared by the present invention and pure non-polar hydrocarbon oil, and the dosage is 5000, 7000, 9000 g/t dry coal slime respectively.
7、所述步骤3中的起泡剂为仲辛醇,用量为150g/t。7. The foaming agent in the step 3 is 2-octanol, and the dosage is 150 g/t.
8、所述步骤2中的矿浆的固体质量浓度为60g/L。8. The solid mass concentration of the pulp in the step 2 is 60g/L.
9、所述步骤7中,在不同药剂用量时,捕收剂较非极性烃类油相比,精煤产率分别增加0.99%,3.09%,3.43%,精煤灰分分别降低2.09%,3.63%,2.91%。9. In the step 7, when the dosage of different agents is different, compared with the non-polar hydrocarbon oil, the yield of clean coal increases by 0.99%, 3.09%, and 3.43%, respectively, and the ash content of clean coal decreases by 2.09%. 3.63%, 2.91%.
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| CN113351376A (en) * | 2021-05-28 | 2021-09-07 | 中国矿业大学 | Gasified slag flotation collector and preparation method thereof |
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