CN114133966B - Method for preparing low-rank coal water slurry with good slurry property based on particle size distribution model - Google Patents
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- 239000003245 coal Substances 0.000 title claims abstract description 97
- 239000002245 particle Substances 0.000 title claims abstract description 81
- 239000002002 slurry Substances 0.000 title claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 51
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000000843 powder Substances 0.000 claims abstract description 31
- 239000000654 additive Substances 0.000 claims abstract description 22
- 239000002994 raw material Substances 0.000 claims abstract description 19
- 239000002131 composite material Substances 0.000 claims abstract description 16
- 238000000498 ball milling Methods 0.000 claims abstract description 14
- 230000000996 additive effect Effects 0.000 claims abstract description 10
- 239000002270 dispersing agent Substances 0.000 claims abstract description 4
- 229920005610 lignin Polymers 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 4
- 125000001624 naphthyl group Chemical group 0.000 claims 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 abstract description 6
- 238000010586 diagram Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/326—Coal-water suspensions
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Abstract
本发明公开了基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法,方法步骤如下:S1:对煤原料进行粗磨,得煤粉A;S2:以S1中的煤粉A为原料,进行球磨,得煤粉B;S3:构建水煤浆的粒度分布模型,并根据粒度分布模型确定煤粉A和煤粉B的配比;S4:将S3中确定的配比的煤粉A和煤粉B与添加剂、水混合制浆,得高浓度水煤浆;其中水煤浆包含如下重量份计的原料:复合煤粉60‑80份、水25‑35份、添加剂0.1‑0.2份;复合煤粉由煤粉A和煤粉B按2‑5:1比例组成;所述添加剂为萘系添加剂、木质素系添加剂、分散剂GSH中的一种或几种;所述复合煤粉的D10粒径为3‑5μm、D50的粒径为40‑50μm。本发明制备的水煤浆具有更好的成浆性,且采用的粒度分布模型与实测值的误差更小。
The invention discloses a method for preparing a low-order coal-water slurry with good slurryability based on a particle size distribution model. The method steps are as follows: S1: coarsely grind the coal raw material to obtain coal powder A; S2: use the coal powder A in S1 As raw material, ball milling is carried out to obtain pulverized coal B; S3: Construct the particle size distribution model of coal-water slurry, and determine the proportion of pulverized coal A and pulverized coal B according to the particle size distribution model; Powder A and coal powder B are mixed with additives and water for slurrying to obtain high-concentration coal-water slurry; wherein the coal-water slurry contains the following raw materials in parts by weight: 60-80 parts of composite coal powder, 25-35 parts of water, and 0.1-35 parts of additives 0.2 part; the composite coal powder is composed of coal powder A and coal powder B in a ratio of 2-5:1; the additive is one or more of naphthalene-based additives, lignin-based additives, and dispersant GSH; the composite The D10 particle size of coal powder is 3-5μm, and the D50 particle size is 40-50μm. The coal-water slurry prepared by the invention has better slurry-forming properties, and the error between the adopted particle size distribution model and the measured value is smaller.
Description
技术领域technical field
本发明涉及水煤浆制备技术领域,尤其涉及基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法。The invention relates to the technical field of coal-water slurry preparation, in particular to a method for preparing low-order coal-water slurry with good slurryability based on a particle size distribution model.
背景技术Background technique
水煤浆作为代油燃料应该具有高浓度、易流动、稳定性好等性能,而对于低阶煤来说虽然资源比较丰富,但是具有成浆性较差的问题,且目前主要的粒度分布模型Rosin-Rammler模型、Gaudin-Schuhmann模型、Alfred模型等在低阶煤中的应用存在的误差较大,无法有效获得成浆效果好的水煤浆。As an oil substitute fuel, coal-water slurry should have high concentration, easy flow, and good stability. For low-rank coal, although the resources are relatively rich, it has the problem of poor slurryability, and the current main particle size distribution model The application of Rosin-Rammler model, Gaudin-Schuhmann model and Alfred model to low-rank coal has large errors, and it is impossible to effectively obtain CWS with good slurrying effect.
发明内容Contents of the invention
基于背景技术存在的技术问题,本发明提出了基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法,制备的水煤浆具有更好的成浆性,且采用的粒度分布模型与实测值的误差更小。Based on the technical problems existing in the background technology, the present invention proposes a method for preparing low-order coal-water slurry with good slurryability based on the particle size distribution model. The prepared coal-water slurry has better slurryability, and the particle size distribution model adopted The error with the measured value is smaller.
本发明提出的基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法,方法步骤如下:The method that the present invention proposes based on particle size distribution model prepares the low-order coal-water slurry with good slurryability, method step is as follows:
S1:对煤原料进行粗磨,得煤粉A;S1: Coarsely grind the coal raw material to obtain coal powder A;
S2:以S1中的煤粉A为原料,进行球磨,得煤粉B;S2: Using the pulverized coal A in S1 as a raw material, perform ball milling to obtain pulverized coal B;
S3:构建水煤浆的粒度分布模型,并根据粒度分布模型确定煤粉A和煤粉B的配比;S3: Construct the particle size distribution model of the coal-water slurry, and determine the ratio of pulverized coal A and pulverized coal B according to the particle size distribution model;
S4:将S3中确定的配比的煤粉A和煤粉B与添加剂、水混合制浆,得高浓度水煤浆。S4: Mix the pulverized coal A and pulverized coal B with additives and water in the ratio determined in S3 to make slurry to obtain a high-concentration coal-water slurry.
优选地,所述S1中煤原料为低阶煤。Preferably, the coal raw material in S1 is low-rank coal.
优选地,所述低阶煤为神木煤。Preferably, the low-rank coal is Shenmu coal.
优选地,所述S1中粗磨后的煤粉A的D50粒径为64-84μm。Preferably, the D50 particle size of the coarsely ground coal powder A in S1 is 64-84 μm.
优选地,所述S2中球磨时的转速为150-200r/min,球磨的时间为20-40min。Preferably, the rotating speed of ball milling in S2 is 150-200r/min, and the time of ball milling is 20-40min.
优选地,所述S2中球磨后煤粉B的D50粒径为5-15μm。Preferably, the D50 particle size of the pulverized coal B after ball milling in S2 is 5-15 μm.
优选地,所述S3中粒度分布模型为:Preferably, the particle size distribution model in the S3 is:
式中:x为某个粒度;y为小于粒度的颗粒含量;K为颗粒含量为K%时的粒度(K取值0、10、20.....80、90);n为模型参数;(K+10)%>x>K%。In the formula: x is a certain particle size; y is the particle content smaller than the particle size; K is the particle size when the particle content is K% (K takes the value of 0, 10, 20...80, 90); n is the model parameter ; (K+10)%>x>K%.
优选地,所述S4中的水煤浆包含如下重量份计的原料:Preferably, the coal water slurry in the S4 comprises the following raw materials in parts by weight:
复合煤粉60-80份、水25-35份、添加剂0.1-0.2份;60-80 parts of composite coal powder, 25-35 parts of water, 0.1-0.2 parts of additives;
其中所述复合煤粉由煤粉A和煤粉B按2-5:1比例组成。The composite pulverized coal is composed of pulverized coal A and pulverized coal B in a ratio of 2-5:1.
优选地,所述添加剂为萘系添加剂、木质素系添加剂、分散剂GSH中的一种或几种。Preferably, the additive is one or more of naphthalene-based additives, lignin-based additives, and dispersant GSH.
优选地,所述复合煤粉的D10粒径为3-5μm、D50的粒径为40-50μm。Preferably, the D10 particle size of the composite coal powder is 3-5 μm, and the D50 particle size is 40-50 μm.
本发明的有益技术效果:Beneficial technical effect of the present invention:
(1)本发明通过构建水煤浆的粒度分布模型,调节煤粉A和煤粉B的配比,当复合煤粉的D10粒径为3-5μm、D50的粒径为40-50μm时,获得的水煤浆的成浆性最好。(1) The present invention adjusts the proportioning of pulverized coal A and pulverized coal B by building the particle size distribution model of coal-water slurry, when the particle diameter of D10 of composite pulverized coal is 3-5 μ m, when the particle diameter of D50 is 40-50 μ m, The obtained coal water slurry has the best slurrying property.
(2)本发明构建的水煤浆粒度分布模型相比于现有的Rosin-Rammler模型、Gaudin-Schuhmann模型、Alfred模型来说,更贴近于实测值,误差更小,从而可以准确获取以低阶煤制备成浆性好的高浓度水煤浆的粒度分布。(2) Compared with the existing Rosin-Rammler model, Gaudin-Schuhmann model and Alfred model, the coal-water slurry particle size distribution model constructed by the present invention is closer to the measured value, and the error is smaller, so that it can be accurately obtained at a low The particle size distribution of high-concentration coal-water slurry prepared from rank coal with good slurryability.
附图说明Description of drawings
图1为采用本发明提出的粒度分布模型的分布图;Fig. 1 adopts the distribution diagram of the particle size distribution model that the present invention proposes;
图2为采用Rosin-Rammler模型的分布图;Figure 2 is a distribution diagram using the Rosin-Rammler model;
图3为采用Gaudin-Schuhmann模型的分布图;Figure 3 is a distribution diagram using the Gaudin-Schuhmann model;
图4为采用Alfred模型的分布图;Fig. 4 is a distribution diagram using the Alfred model;
具体实施方式Detailed ways
本发明中粗磨用的设备为SF-高速粉碎机(棒磨机),球磨用的设备为立式方形行星式球磨机。Among the present invention, the equipment used for coarse grinding is SF-high-speed pulverizer (rod mill), and the equipment used for ball milling is a vertical square planetary ball mill.
本发明中煤粉粒度的测定通过BT-2003激光粒度分析仪。In the present invention, the coal powder particle size is measured by a BT-2003 laser particle size analyzer.
水煤浆的粘度测定通过NXS-4C水煤浆粘度计。The viscosity of coal water slurry was measured by NXS-4C coal water slurry viscometer.
实施例1Example 1
本发明提出的基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法步骤如下:The method steps of preparing the low-rank coal-water slurry with good slurryability based on the particle size distribution model proposed by the present invention are as follows:
S1:对煤原料进行粗磨,得煤粉A;S1: Coarsely grind the coal raw material to obtain coal powder A;
S2:以S1中的煤粉A为原料,进行球磨,得煤粉B;S2: Using the pulverized coal A in S1 as a raw material, perform ball milling to obtain pulverized coal B;
S3:构建水煤浆的粒度分布模型,并根据粒度分布模型确定煤粉A和煤粉B的配比;S3: Construct the particle size distribution model of the coal-water slurry, and determine the ratio of pulverized coal A and pulverized coal B according to the particle size distribution model;
S4:将S3中确定的配比的煤粉A和煤粉B与添加剂、水混合制浆,得高浓度水煤浆。S4: Mix the pulverized coal A and pulverized coal B with additives and water in the ratio determined in S3 to make slurry to obtain a high-concentration coal-water slurry.
S1中煤原料为低阶的神木煤。The coal raw material in S1 is low-rank Shenmu coal.
S1中粗磨后的煤粉A的D50粒径为79.02μm。The D50 particle size of coarsely ground coal powder A in S1 is 79.02 μm.
S2中球磨的转速为150r/min,球磨的时间为30min。The rotation speed of the ball mill in S2 is 150r/min, and the time of the ball mill is 30min.
S2中球磨后煤粉B的D50粒径为13.58μm。The D50 particle size of pulverized coal B after ball milling in S2 is 13.58 μm.
S3中粒度分布模型为:The particle size distribution model in S3 is:
式中:x为某个粒度;y为小于粒度的颗粒含量;K为颗粒含量为K%时的粒度(K取值0、10、20.....80、90);n为模型参数;(K+10)%>x>K%。In the formula: x is a certain particle size; y is the particle content smaller than the particle size; K is the particle size when the particle content is K% (K takes the value of 0, 10, 20...80, 90); n is the model parameter ; (K+10)%>x>K%.
S4中的水煤浆包含如下重量份计的原料:复合煤粉70份、水30份、添加剂0.15份;其中所述复合煤粉由煤粉A和煤粉B按4:1比例组成。The coal-water slurry in S4 contains the following raw materials in parts by weight: 70 parts of composite coal powder, 30 parts of water, and 0.15 parts of additive; wherein the composite coal powder is composed of coal powder A and coal powder B at a ratio of 4:1.
添加剂为分散剂GSHAdditive is dispersant GSH
复合煤粉的D10粒径为4.052μm、D50的粒径为47.36μm。The D10 particle size of the composite coal powder is 4.052 μm, and the D50 particle size is 47.36 μm.
采用上述方法制备的水煤浆的最高成浆浓度为63%,表观粘度为1188.8mPa·s。The highest slurry concentration of the coal-water slurry prepared by the above method is 63%, and the apparent viscosity is 1188.8mPa·s.
实施例2Example 2
本发明提出的基于粒度分布模型制备成浆性好的低阶煤水煤浆的方法步骤如下:The method steps of preparing the low-rank coal-water slurry with good slurryability based on the particle size distribution model proposed by the present invention are as follows:
S1:对煤原料进行粗磨,得煤粉A;S1: Coarsely grind the coal raw material to obtain coal powder A;
S2:以S1中的煤粉A为原料,进行球磨,得煤粉B;S2: Using the pulverized coal A in S1 as a raw material, perform ball milling to obtain pulverized coal B;
S3:构建水煤浆的粒度分布模型,并根据粒度分布模型确定煤粉A和煤粉B的配比;S3: Construct the particle size distribution model of the coal-water slurry, and determine the ratio of pulverized coal A and pulverized coal B according to the particle size distribution model;
S4:将S3中确定的配比的煤粉A和煤粉B与添加剂、水混合制浆,得高浓度水煤浆。S4: Mix the pulverized coal A and pulverized coal B with additives and water in the ratio determined in S3 to make slurry to obtain a high-concentration coal-water slurry.
S1中煤原料为低阶的神木煤。The coal raw material in S1 is low-rank Shenmu coal.
S1中粗磨后的煤粉A的D50粒径为79.02μm。The D50 particle size of coarsely ground coal powder A in S1 is 79.02 μm.
S2中球磨的转速为200r/min,球磨的时间为30min。The rotational speed of the ball mill in S2 is 200r/min, and the time of the ball mill is 30min.
S2中球磨后的煤粉B的D50粒径为8.727μm。The D50 particle size of pulverized coal B after ball milling in S2 is 8.727 μm.
S3中粒度分布模型为:The particle size distribution model in S3 is:
式中:x为某个粒度;y为小于粒度的颗粒含量;K为颗粒含量为K%时的粒度(K取值0、10、20.....80、90);n为模型参数;(K+10)%>x>K%。In the formula: x is a certain particle size; y is the particle content smaller than the particle size; K is the particle size when the particle content is K% (K takes the value of 0, 10, 20...80, 90); n is the model parameter ; (K+10)%>x>K%.
S4中的水煤浆包含如下重量份计的原料:复合煤粉70份、水30份、添加剂0.15份;其中所述复合煤粉由煤粉A和煤粉B按4:1比例组成。The coal-water slurry in S4 contains the following raw materials in parts by weight: 70 parts of composite coal powder, 30 parts of water, and 0.15 parts of additive; wherein the composite coal powder is composed of coal powder A and coal powder B at a ratio of 4:1.
添加剂为萘系添加剂。The additive is a naphthalene-based additive.
复合煤粉的D10粒径为3.308μm、D50的粒径为48.24μm。The D10 particle size of the composite coal powder is 3.308 μm, and the D50 particle size is 48.24 μm.
采用上述方法制备的水煤浆的最高成浆浓度为64%,表观粘度为1305.2mPa·s。The highest slurry concentration of the coal-water slurry prepared by the above method is 64%, and the apparent viscosity is 1305.2mPa·s.
对比例comparative example
以目前最常用的粒度分布模型Rosin-Rammler、Gaudin-Schuhmann、Alfred模型为对比例,对其预测的粒度分布与实测的粒度分布于本发明提出的粒度分布模型进行对比,结果如图1-4所示。由图1-4可知,本发明提出的更贴近于实测值,误差更小,从而可以准确获取以低阶煤制备成浆性好的高浓度水煤浆的粒度分布。Taking the currently most commonly used particle size distribution models Rosin-Rammler, Gaudin-Schuhmann, and Alfred models as comparative examples, the predicted particle size distribution and the measured particle size distribution are compared with the particle size distribution model proposed by the present invention. The results are shown in Figures 1-4 shown. It can be seen from Figures 1-4 that the value proposed by the present invention is closer to the actual measured value, and the error is smaller, so that the particle size distribution of high-concentration coal-water slurry prepared with low-rank coal and good slurryability can be accurately obtained.
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