WO2017071025A1 - Preparation method and usage method of inhibitor for preventing spontaneous combustion of dry lignite - Google Patents

Preparation method and usage method of inhibitor for preventing spontaneous combustion of dry lignite Download PDF

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WO2017071025A1
WO2017071025A1 PCT/CN2015/098038 CN2015098038W WO2017071025A1 WO 2017071025 A1 WO2017071025 A1 WO 2017071025A1 CN 2015098038 W CN2015098038 W CN 2015098038W WO 2017071025 A1 WO2017071025 A1 WO 2017071025A1
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inhibitor
coal
spontaneous combustion
lignite
solution
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PCT/CN2015/098038
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French (fr)
Chinese (zh)
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吴国光
孟献梁
褚睿智
刘晖
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中国矿业大学
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00Fireproofing materials
    • C09K21/02Inorganic materials
    • C09K21/04Inorganic materials containing phosphorus

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  • the invention relates to a preparation method and a use method for preventing coal spontaneous combustion inhibitor, in particular to a preparation method and a use method for preventing a self-ignition of dry brown coal.
  • China's coal resources are abundant, and its output and consumption rank first in the world. It is a key driving resource for China's rapid economic development. In the process of coal production, transportation and storage, oxidative spontaneous combustion occurs frequently, and it is not easy to be discovered in the early stage of spontaneous combustion.
  • Lignite is a low-grade coal. Due to its high oxygen content, high porosity, high volatile content and strong reactivity, it is becoming the main coal in the field of clean coal utilization such as power generation, pyrolysis, gasification and liquefaction. Because of these characteristics, lignite has a high tendency to spontaneous combustion, and it is highly prone to oxidation in the air, eventually leading to spontaneous combustion.
  • fire prevention technology mainly includes water injection grouting, filling with inert gas, adding inhibitor, equalizing plugging, foam and colloidal fire prevention.
  • the above fire prevention technologies have their own characteristics. Among them, the use of inhibitors to prevent coal spontaneous combustion is a commonly used fire prevention technology. Generally speaking, the main inhibitory effect of inhibitors on coal is physical, and some chemical reactions occur at the same time. The reaction is low in cost, simple in operation and good in resistive effect, and is widely recognized and applied. Each of the inhibitors has its advantages and limitations, and its mechanism of action and effects are also different.
  • the object of the present invention is to provide a preparation method and a use method of a resisting agent for preventing spontaneous combustion of dry lignite, the inhibitor has the following effects: 1 obvious effect, long resistive life; 2 non-toxic and non-polluting, no harm to human health , does not damage the environment; 3 easy to produce, low cost of raw materials, easy to use; 4 pairs of equipment without corrosion.
  • the object of the present invention is achieved by the method for preparing the inhibitor of the present invention; the inhibitor comprises the component (A) and the component (B), and the specific steps are as follows:
  • component (A) is 60-80% by weight of primary inhibitor
  • component (B) is 20-40% by-product; uniformly mixing it into inhibitor powder
  • the inhibitor powder and water are sufficiently mixed to form a inhibitor solution in a ratio of 1-5:5 by weight.
  • the primary inhibitor is magnesium chloride.
  • the secondary inhibitor is obtained by mixing ammonium dihydrogen phosphate and ammonium polyphosphate in a mass ratio of 1:1 to 2.
  • the secondary retarding agent ammonium polyphosphate is obtained by synthesizing phosphoric acid and urea, and the controlled temperature during synthesis is not more than 80 ° C, and the synthesized gas is absorbed by the sodium hydroxide solution.
  • the molar ratio of phosphoric acid to urea is 8:9.
  • thermogravimetric analyzer confirmed that the coal water activation activation energy and the ignition activation energy were significantly improved, and the ignition point was increased to above 130 ° C, and the resistance effect was remarkable.
  • the inhibitor is economical, non-polluting, convenient to transport, and simple to use; at the same time, the spraying is simple and easy to operate.
  • the activation energy of the resistive coal sample in the water evaporation stage is 38.21kJ/mol, which is 25.4% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.97kJ/mol, which is better than the raw coal. 3.56kJ/mol is 183.4% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 132 ° C.
  • the inhibitor is harmless to the human body, and is less irritating to human skin and mucous membranes of the eyes. Therefore, the dusting agent is safe for the human body.
  • the inhibitor has low cost, is easy to use, and is easy to store.
  • the preparation method of the inhibitor of the present invention comprises the component (A) and the component (B); the specific steps are as follows:
  • component (A) is 60-80% by weight of primary inhibitor
  • component (B) is 20-40% by-product; uniformly mixing it into inhibitor powder
  • the inhibitor powder and water are sufficiently mixed to form a inhibitor solution in a ratio of 1-5:5 by weight.
  • the specific steps of the method of the invention are as follows: g gas sample/ml resistive solution according to mass to volume ratio, and a 1:0.1-2.0 ratio of the resistive solution is evenly sprayed on the surface of the coal sample.
  • the activation energy of the resistive coal sample after spraying the resistive solution is more than 25% higher than that of the original dry lignite.
  • the activation energy in the oxygen oxidation stage is more than 170% higher than that of the original dry lignite.
  • the critical temperature of lignite spontaneous combustion can be from the raw coal. Increasing to about 136 ° C at around 75 ° C, the resistance effect is significant.
  • the primary inhibitor is magnesium chloride.
  • the secondary inhibitor is obtained by mixing ammonium dihydrogen phosphate and ammonium polyphosphate in a mass ratio of 1:1 to 2.
  • the secondary retarding agent ammonium polyphosphate is obtained by synthesizing phosphoric acid and urea, and the controlled temperature during synthesis is not more than 80 ° C, and the synthesized gas is absorbed by the sodium hydroxide solution.
  • the molar ratio of phosphoric acid to urea is 8:9.
  • the invention relates to a resisting agent for preventing self-ignition of coal.
  • a resisting agent for preventing self-ignition of coal.
  • Component (A) is 60% of the primary inhibitor and component (B) is 40% by weight of the catalyst. Mix it evenly into a inhibitor powder;
  • the critical temperature of coal sample reached 79 °C, the cracking temperature reached 139 °C, and the resistive coal sample had a good resisting effect, which obviously delayed the evaporation process of water, and the water evaporation phase in the low temperature oxidation process prolonged.
  • the activation energy of the resistive coal sample in the water evaporation stage is 39.47kJ/mol, which is 29.5% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.84kJ/mol, which is -3.56kJ/ of the raw coal.
  • the mol is 179.7% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 140 ° C.
  • Sample preparation The lignite is stripped of the surface oxide layer, followed by rapid crushing, and a sufficient amount of coal sample having a particle size of 1 mm ⁇ particle size ⁇ 4 mm is sieved.
  • Component (A) is 70% of the main inhibitor, and component (B) is 30% by weight of the catalyst. Put it
  • the critical temperature of the coal sample reached 73 °C, and the cracking temperature reached 122 °C.
  • the resistive coal sample had a good resisting effect, which obviously delayed the evaporation process of water, and the water evaporation phase in the low temperature oxidation process prolonged.
  • the activation energy of the resistive coal sample in the water evaporation stage is 32.18kJ/mol, which is 5.6% higher than the original coal of 30.48kJ/mol; the activity in the oxygen oxidation stage
  • the chemical energy is 2.47kJ/mol, which is 169.4% higher than the original coal of -3.56kJ/mol. That is, the critical temperature of self-ignition of lignite that has been resisted is increased from 77 ° C to 132 ° C.
  • Sample preparation The lignite is stripped of the surface oxide layer, followed by rapid crushing, and a coal sample of a sufficient amount of particle size is sieved.
  • Component (A) is 80% by mass of the main inhibitor, and component (B) is 20% by weight of the catalyst. Mix it evenly into a inhibitor powder;
  • the critical temperature of the coal sample reached 84 ° C, the cracking temperature reached 100 ° C, and the resistance of the coal sample was blocked.
  • the activation energy of the resistive coal sample in the water evaporation stage is 42.15kJ/mol, which is 19.5% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.65kJ/mol, which is -3.56kJ/ of the raw coal.
  • the mol is 174.4% higher. That is, the critical temperature of self-ignition of lignite that has been resisted is increased from 72 ° C to 136 ° C.
  • the activation energy of the resistive coal sample in the water evaporation stage is 38.21kJ/mol, which is 25.4% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.97kJ/mol, which is -3.56kJ/ of the raw coal.
  • the mol is 183.4% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 130 ° C.

Abstract

Provided are a preparation method and a usage method of an inhibitor for preventing the spontaneous combustion of dry lignite, belonging to preparation methods and usage methods of an inhibitor for preventing the spontaneous combustion of coal. A component (A) of the inhibitor accounting for 60-80 wt% is a main inhibitor, and a component (B) of the inhibitor accounting for 20-40 wt% is a secondary inhibitor. The preparation method comprises: (1) preparing a sample; (2) preparing the secondary inhibitor at a certain temperature; (3) uniformly mixing to form an inhibitor powder; (4) weighing the inhibitor powder and water and thoroughly mixing same in a weight ratio of 1 : 1-8 to obtain an inhibitor solution; and (5) by the mass-volume ratio, uniformly spraying the inhibitor solution onto the surface of a coal sample in a ratio of 1 : 0.1-2.0. In a water evaporation stage, compared with raw dry lignite, the activation energy of the inhibited coal sample after being sprayed with the inhibitor solution is improved by 25% or more; in an oxygen absorbing oxidation stage, compared with the raw dry lignite, the activation energy is improved by 170% or more; the critical temperature for spontaneous combustion of the lignite can be increased to 136°C or more from about 75°C for the raw lignite, and thus the inhibition effect is significant. The inhibitor is economical, creates no pollution, is convenient to transport, simple to use and convenient to operate.

Description

一种防止干燥褐煤自燃的阻化剂的制备方法和使用方法Preparation method and use method of inhibitor for preventing dry lignite spontaneous combustion 技术领域Technical field
本发明涉及一种防止煤自燃阻化剂的制备方法和使用方法,特别是一种防止干燥褐煤自燃的阻化剂的制备方法和使用方法。The invention relates to a preparation method and a use method for preventing coal spontaneous combustion inhibitor, in particular to a preparation method and a use method for preventing a self-ignition of dry brown coal.
背景技术Background technique
我国的煤炭资源丰富,其产量和消耗量均居世界首位,是我国经济快速发展关键的动力基础资源。而在煤炭的生产、运输和储存过程中,氧化自燃发火现象时有发生,且自燃发火前期不容易被发现。China's coal resources are abundant, and its output and consumption rank first in the world. It is a key driving resource for China's rapid economic development. In the process of coal production, transportation and storage, oxidative spontaneous combustion occurs frequently, and it is not easy to be discovered in the early stage of spontaneous combustion.
我国已发现的煤炭中储量最大的就是褐煤,约占全国煤炭储量的17%。褐煤是低变质程度煤,因其氧含量高、孔隙度大、挥发分高和反应活性强等特点,正逐渐成为发电、热解、气化和液化等煤炭洁净利用领域的主要煤种。而正因为这些特点,褐煤自燃倾向性高,在空气中极易发生氧化,最终导致自燃发火。China's largest coal reserves have been found to be lignite, accounting for about 17% of the country's coal reserves. Lignite is a low-grade coal. Due to its high oxygen content, high porosity, high volatile content and strong reactivity, it is becoming the main coal in the field of clean coal utilization such as power generation, pyrolysis, gasification and liquefaction. Because of these characteristics, lignite has a high tendency to spontaneous combustion, and it is highly prone to oxidation in the air, eventually leading to spontaneous combustion.
目前,防灭火技术主要有注水灌浆、充入惰性气体、添加阻化剂、均压堵漏、泡沫和胶体防灭火等。以上的防灭火技术各有特点,其中利用阻化剂防治煤自燃,是当前常用的一种防灭火技术,一般来说,阻化剂对煤炭的主要阻化作用是物理作用,同时发生部分化学反应,该技术成本较低、操作简单且阻化效果较好,得到了广泛认可和应用。而每一种阻化剂都有它的优势和局限性,其作用机理和作用效果也不尽相同。At present, fire prevention technology mainly includes water injection grouting, filling with inert gas, adding inhibitor, equalizing plugging, foam and colloidal fire prevention. The above fire prevention technologies have their own characteristics. Among them, the use of inhibitors to prevent coal spontaneous combustion is a commonly used fire prevention technology. Generally speaking, the main inhibitory effect of inhibitors on coal is physical, and some chemical reactions occur at the same time. The reaction is low in cost, simple in operation and good in resistive effect, and is widely recognized and applied. Each of the inhibitors has its advantages and limitations, and its mechanism of action and effects are also different.
目前国内在选择阻化剂时存在盲目性,不能有效针对解决自身煤种自燃问题。At present, there is blindness in the selection of inhibitors in China, which cannot effectively solve the problem of self-ignition of coal types.
发明内容Summary of the invention
本发明的目的是要提供一种防止干燥褐煤自燃的阻化剂的制备方法和使用方法,该阻化剂具有:①作用效果明显,阻化寿命长;②无毒无污染,不危害人员健康,不破坏环境;③易生产,原料成本低,使用便捷;④对设备无腐蚀。The object of the present invention is to provide a preparation method and a use method of a resisting agent for preventing spontaneous combustion of dry lignite, the inhibitor has the following effects: 1 obvious effect, long resistive life; 2 non-toxic and non-polluting, no harm to human health , does not damage the environment; 3 easy to produce, low cost of raw materials, easy to use; 4 pairs of equipment without corrosion.
本发明的目的是这样实现的:本发明的阻化剂的制备方法;该阻化剂包含组分(A)和组分(B),具体步骤如下:The object of the present invention is achieved by the method for preparing the inhibitor of the present invention; the inhibitor comprises the component (A) and the component (B), and the specific steps are as follows:
(1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量1mm<粒度<4mm的煤样;(1) Sample preparation: the lignite is stripped of the surface oxide layer, followed by rapid crushing, and a sufficient amount of coal sample having a size of 1 mm < particle size < 4 mm is sieved;
(2)在三口烧瓶中加入磷酸,加热升温,边搅拌边加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) Add phosphoric acid to a three-necked flask, heat up, add a metered amount of urea (8:9 molar ratio with phosphoric acid) while stirring, and control the temperature not to exceed 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
(3)按质量计,组分(A)是占60-80wt%主阻化剂,组分(B)是占20-40%的副催化剂;将其均匀混合成阻化剂粉;(3) by mass, component (A) is 60-80% by weight of primary inhibitor, component (B) is 20-40% by-product; uniformly mixing it into inhibitor powder;
(4)取阻化剂粉和水按重量计1-5∶5的比例进行充分混合成阻化剂溶液。(4) The inhibitor powder and water are sufficiently mixed to form a inhibitor solution in a ratio of 1-5:5 by weight.
本发明的使用方法具体步骤:按质量体积比计,g煤样/ml阻化液,将1:0.1-2.0比例的阻化溶液均匀喷洒于煤样表面即可。Specific steps of the method of use of the present invention: g gas sample / ml resistive solution, a 1:0.1-2.0 ratio of the resistive solution is evenly sprayed on the surface of the coal sample.
所述的主阻化剂为氯化镁。 The primary inhibitor is magnesium chloride.
所述的副阻化剂为磷酸二氢铵和低聚磷酸铵,按质量百分比1:1-2混合而得。The secondary inhibitor is obtained by mixing ammonium dihydrogen phosphate and ammonium polyphosphate in a mass ratio of 1:1 to 2.
所述的副阻化剂低聚磷酸铵是由磷酸、尿素合成而得,合成时控制温度不得超过80℃,合成生成的气体由氢氧化钠溶液吸收。磷酸与尿素的摩尔比为8:9。The secondary retarding agent ammonium polyphosphate is obtained by synthesizing phosphoric acid and urea, and the controlled temperature during synthesis is not more than 80 ° C, and the synthesized gas is absorbed by the sodium hydroxide solution. The molar ratio of phosphoric acid to urea is 8:9.
有益效果,由于采用了上述方案,应用热重分析仪实验测定证实煤样失水活化能和着火活化能明显提高,着火点提高至130℃以上,阻化效果显著。阻化剂经济、无污染、运输方便、使用简单;同时喷洒简单,便于操作。The beneficial effects, due to the adoption of the above scheme, the experimental determination by the thermogravimetric analyzer confirmed that the coal water activation activation energy and the ignition activation energy were significantly improved, and the ignition point was increased to above 130 ° C, and the resistance effect was remarkable. The inhibitor is economical, non-polluting, convenient to transport, and simple to use; at the same time, the spraying is simple and easy to operate.
(1)阻化煤样在水分蒸发阶段的活化能为38.21kJ/mol,比原煤的30.48kJ/mol高出25.4%;在吸氧氧化阶段的活化能为2.97kJ/mol,比原煤的-3.56kJ/mol高出183.4%。即经过阻化的褐煤自燃临界温度由75℃提高到132℃。(1) The activation energy of the resistive coal sample in the water evaporation stage is 38.21kJ/mol, which is 25.4% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.97kJ/mol, which is better than the raw coal. 3.56kJ/mol is 183.4% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 132 ° C.
(2)该阻化剂对人体无害,对人体皮肤、眼睛的黏膜组织的刺激性也很小。因此,本降尘剂对人体安全。(2) The inhibitor is harmless to the human body, and is less irritating to human skin and mucous membranes of the eyes. Therefore, the dusting agent is safe for the human body.
(3)该阻化剂对设备几乎无腐蚀性。(3) The inhibitor is almost non-corrosive to the equipment.
(4)该阻化剂原料成本低,使用便捷,且易于保存。(4) The inhibitor has low cost, is easy to use, and is easy to store.
具体实施方式detailed description
本发明的阻化剂的制备方法,该阻化剂包含组分(A)和组分(B);具体步骤如下:The preparation method of the inhibitor of the present invention, the inhibitor comprises the component (A) and the component (B); the specific steps are as follows:
(1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量1mm<粒度<4mm的煤样;(1) Sample preparation: the lignite is stripped of the surface oxide layer, followed by rapid crushing, and a sufficient amount of coal sample having a size of 1 mm < particle size < 4 mm is sieved;
(2)在三口烧瓶中加入磷酸,加热升温,边搅拌边按摩尔比8:9加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) Adding phosphoric acid to a three-necked flask, heating and heating, adding a metered urea (8:9 molar ratio to phosphoric acid) with a molar ratio of 8:9 while stirring, and controlling the temperature not to exceed 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
(3)按质量计,组分(A)是占60-80wt%主阻化剂,组分(B)是占20-40%的副催化剂;将其均匀混合成阻化剂粉;(3) by mass, component (A) is 60-80% by weight of primary inhibitor, component (B) is 20-40% by-product; uniformly mixing it into inhibitor powder;
(4)取阻化剂粉和水按重量计1-5∶5的比例进行充分混合成阻化剂溶液。(4) The inhibitor powder and water are sufficiently mixed to form a inhibitor solution in a ratio of 1-5:5 by weight.
本发明使用方法具体步骤:按质量体积比计,g煤样/ml阻化液,将1:0.1-2.0比例的阻化溶液均匀喷洒于煤样表面即可。The specific steps of the method of the invention are as follows: g gas sample/ml resistive solution according to mass to volume ratio, and a 1:0.1-2.0 ratio of the resistive solution is evenly sprayed on the surface of the coal sample.
喷洒阻化溶液后的阻化煤样在水分蒸发阶段的活化能较原干燥褐煤提高25%以上,在吸氧氧化阶段的活化能较原干燥褐煤提高170%以上,褐煤自燃临界温度可由原煤的75℃左右提高到136℃以上,阻化效果显著。The activation energy of the resistive coal sample after spraying the resistive solution is more than 25% higher than that of the original dry lignite. The activation energy in the oxygen oxidation stage is more than 170% higher than that of the original dry lignite. The critical temperature of lignite spontaneous combustion can be from the raw coal. Increasing to about 136 ° C at around 75 ° C, the resistance effect is significant.
所述的主阻化剂为氯化镁。The primary inhibitor is magnesium chloride.
所述的副阻化剂为磷酸二氢铵和低聚磷酸铵,按质量百分比1:1-2混合而得。The secondary inhibitor is obtained by mixing ammonium dihydrogen phosphate and ammonium polyphosphate in a mass ratio of 1:1 to 2.
所述的副阻化剂低聚磷酸铵是由磷酸、尿素合成而得,合成时控制温度不得超过80℃,合成生成的气体由氢氧化钠溶液吸收。磷酸与尿素的摩尔比为8:9。The secondary retarding agent ammonium polyphosphate is obtained by synthesizing phosphoric acid and urea, and the controlled temperature during synthesis is not more than 80 ° C, and the synthesized gas is absorbed by the sodium hydroxide solution. The molar ratio of phosphoric acid to urea is 8:9.
本发明涉及一种防止煤炭自燃的阻化剂,在水中加入阻化剂配置成阻化溶液,按比例喷洒在煤堆上,便可以防止煤炭自燃。The invention relates to a resisting agent for preventing self-ignition of coal. When a resisting agent is added to the water to be arranged as a resistive solution, and sprayed on the coal pile in proportion, the coal can be prevented from spontaneous combustion.
实施例1:Example 1:
(1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量1mm<粒度 <4mm的煤样。(1) Sample preparation: the lignite is stripped of the surface oxide layer, followed by rapid crushing, and sieved out a sufficient amount of 1 mm<grain <4mm coal sample.
(2)在三口烧瓶中加入的磷酸,加热升温,边搅拌边加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) The phosphoric acid added to the three-necked flask is heated and heated, and the metered urea is added (with a molar ratio of 8:9 to the phosphoric acid) while stirring, and the controlled temperature is not more than 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
(3)按质量计,组分(A)是占60%主阻化剂,组分(B)是占40%的副催化剂。将其均匀混合成阻化剂粉;(3) Component (A) is 60% of the primary inhibitor and component (B) is 40% by weight of the catalyst. Mix it evenly into a inhibitor powder;
(4)取阻化剂粉和水按重量计2∶5的比例进行充分混合成阻化剂溶液;(4) taking the inhibitor powder and water in a ratio of 2:5 by weight to thoroughly mix into a resist agent solution;
(5)取煤样1克与阻化剂溶液0.3mL均匀混合;(5) 1 g of the coal sample and 0.3 mL of the inhibitor solution are uniformly mixed;
(6)应用热重分析仪,实验测定条件确定;(6) Applying a thermogravimetric analyzer, and determining experimental conditions;
(7)测定煤样起始温度为T0和失水结束点温度T1(7) determining the coal sample starting temperature is T 0 and the water loss end point temperature T 1 ;
(8)最后根据求解出的失水结束点温度和着火活化能的增加值。(8) Finally, based on the calculated dehydration end point temperature and the increase in ignition activation energy.
2、阻化效果2, resistance effect
煤样临界温度达到79℃,裂解温度达到139℃,阻化煤样发生了良好的阻化作用,明显地延迟了水分蒸发进程,低温氧化过程中的水分蒸发阶段时间延长。阻化煤样在水分蒸发阶段的活化能为39.47kJ/mol,比原煤的30.48kJ/mol高出29.5%;在吸氧氧化阶段的活化能为2.84kJ/mol,比原煤的-3.56kJ/mol高出179.7%。即经过阻化的褐煤自燃临界温度由75℃提高到140℃。The critical temperature of coal sample reached 79 °C, the cracking temperature reached 139 °C, and the resistive coal sample had a good resisting effect, which obviously delayed the evaporation process of water, and the water evaporation phase in the low temperature oxidation process prolonged. The activation energy of the resistive coal sample in the water evaporation stage is 39.47kJ/mol, which is 29.5% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.84kJ/mol, which is -3.56kJ/ of the raw coal. The mol is 179.7% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 140 ° C.
实施例2:Example 2:
(1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量粒度1mm<粒度<4mm的煤样。(1) Sample preparation: The lignite is stripped of the surface oxide layer, followed by rapid crushing, and a sufficient amount of coal sample having a particle size of 1 mm < particle size < 4 mm is sieved.
(2)在三口烧瓶中加入的磷酸,加热升温,边搅拌边加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) The phosphoric acid added to the three-necked flask is heated and heated, and the metered urea is added (with a molar ratio of 8:9 to the phosphoric acid) while stirring, and the controlled temperature is not more than 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
(3)按质量计,组分(A)是占70%主阻化剂,组分(B)是占30%的副催化剂。将其(3) Component (A) is 70% of the main inhibitor, and component (B) is 30% by weight of the catalyst. Put it
均匀混合成阻化剂粉;Evenly mixed into a inhibitor powder;
(4)取阻化剂粉和水按重量计4∶5的比例进行充分混合成阻化剂溶液;(4) taking the inhibitor powder and water in a ratio of 4:5 by weight to fully mix into a resist agent solution;
(5)取煤样1克与阻化剂溶液0.4mL均匀混合;(5) 1 g of the coal sample and 0.4 mL of the inhibitor solution are uniformly mixed;
(6)应用热重分析仪,实验测定条件确定;(6) Applying a thermogravimetric analyzer, and determining experimental conditions;
(7)测定煤样起始温度为T0和失水结束点温度T1(7) determining the coal sample starting temperature is T 0 and the water loss end point temperature T 1 ;
(8)最后根据求解出的失水结束点温度和着火活化能的增加值。(8) Finally, based on the calculated dehydration end point temperature and the increase in ignition activation energy.
2、阻化效果2, resistance effect
煤样临界温度达到73℃,裂解温度达到122℃,阻化煤样发生了良好的阻化作用,明显地延迟了水分蒸发进程,低温氧化过程中的水分蒸发阶段时间延长。阻化煤样在水分蒸发阶段的活化能为32.18kJ/mol,比原煤的30.48kJ/mol高出5.6%;在吸氧氧化阶段的活 化能为2.47kJ/mol,比原煤的-3.56kJ/mol高出169.4%。即经过阻化的褐煤自燃临界温度由77℃提高到132℃。The critical temperature of the coal sample reached 73 °C, and the cracking temperature reached 122 °C. The resistive coal sample had a good resisting effect, which obviously delayed the evaporation process of water, and the water evaporation phase in the low temperature oxidation process prolonged. The activation energy of the resistive coal sample in the water evaporation stage is 32.18kJ/mol, which is 5.6% higher than the original coal of 30.48kJ/mol; the activity in the oxygen oxidation stage The chemical energy is 2.47kJ/mol, which is 169.4% higher than the original coal of -3.56kJ/mol. That is, the critical temperature of self-ignition of lignite that has been resisted is increased from 77 ° C to 132 ° C.
实施例3:Example 3:
(1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量粒度的煤样。(1) Sample preparation: The lignite is stripped of the surface oxide layer, followed by rapid crushing, and a coal sample of a sufficient amount of particle size is sieved.
(2)在三口烧瓶中加入的磷酸,加热升温,边搅拌边加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) The phosphoric acid added to the three-necked flask is heated and heated, and the metered urea is added (with a molar ratio of 8:9 to the phosphoric acid) while stirring, and the controlled temperature is not more than 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
(3)按质量计,组分(A)是占80%主阻化剂,组分(B)是占20%的副催化剂。将其均匀混合成阻化剂粉;(3) Component (A) is 80% by mass of the main inhibitor, and component (B) is 20% by weight of the catalyst. Mix it evenly into a inhibitor powder;
(4)取阻化剂粉和水按重量计3∶5的比例进行充分混合成阻化剂溶液;(4) taking the inhibitor powder and water in a ratio of 3:5 by weight to fully mix into a resist agent solution;
(5)取煤样1克与阻化剂溶液0.5mL均匀混合;(5) 1 g of coal sample and 0.5 mL of the inhibitor solution are uniformly mixed;
(6)应用热重分析仪,实验测定条件确定;(6) Applying a thermogravimetric analyzer, and determining experimental conditions;
(7)测定煤样起始温度为T0和失水结束点温度T1(7) determining the coal sample starting temperature is T 0 and the water loss end point temperature T 1 ;
(8)最后根据求解出的失水结束点温度和着火活化能的增加值。(8) Finally, based on the calculated dehydration end point temperature and the increase in ignition activation energy.
2、阻化效果2, resistance effect
煤样临界温度达到84℃,裂解温度达到100℃,阻化煤样发生了阻化作用。阻化煤样在水分蒸发阶段的活化能为42.15kJ/mol,比原煤的30.48kJ/mol高出19.5%;在吸氧氧化阶段的活化能为2.65kJ/mol,比原煤的-3.56kJ/mol高出174.4%。即经过阻化的褐煤自燃临界温度由72℃提高到136℃。The critical temperature of the coal sample reached 84 ° C, the cracking temperature reached 100 ° C, and the resistance of the coal sample was blocked. The activation energy of the resistive coal sample in the water evaporation stage is 42.15kJ/mol, which is 19.5% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.65kJ/mol, which is -3.56kJ/ of the raw coal. The mol is 174.4% higher. That is, the critical temperature of self-ignition of lignite that has been resisted is increased from 72 ° C to 136 ° C.
实用例4:在高速搅拌的100kg水中添加25kg阻化剂缓慢搅拌均匀,配置成阻化溶液。将其溶液按50L:100kg均匀喷洒在小龙潭褐煤堆上,并完全混合。在煤堆堆储期间同时采用煤堆低温氧化温度及标志性气体浓度耦合测量装置监控煤堆内部温度和气体浓度变化情况,以判断煤堆是否存在自燃的可能性;煤堆可以放置百天而不发生自燃现象。Practical Example 4: 25 kg of a blocking agent was added to 100 kg of water which was stirred at a high speed, and the mixture was stirred slowly, and was set as a resistive solution. Spray the solution evenly on 50L:100kg on the Xiaolongtan lignite pile and mix thoroughly. During the coal storage and storage period, the coal pile low temperature oxidation temperature and the marker gas concentration coupling measuring device are used to monitor the internal temperature and gas concentration changes of the coal pile to determine whether the coal pile has the possibility of spontaneous combustion; the coal pile can be placed for one hundred days. No spontaneous combustion occurs.
阻化煤样在水分蒸发阶段的活化能为38.21kJ/mol,比原煤的30.48kJ/mol高出25.4%;在吸氧氧化阶段的活化能为2.97kJ/mol,比原煤的-3.56kJ/mol高出183.4%。即经过阻化的褐煤自燃临界温度由75℃提高到130℃。 The activation energy of the resistive coal sample in the water evaporation stage is 38.21kJ/mol, which is 25.4% higher than the original coal of 30.48kJ/mol; the activation energy in the oxygen oxidation stage is 2.97kJ/mol, which is -3.56kJ/ of the raw coal. The mol is 183.4% higher. That is, the self-ignition critical temperature of the lignified lignite is increased from 75 ° C to 130 ° C.

Claims (5)

  1. 一种防止干燥褐煤自燃的阻化剂的制备方法与使用方法,其特征是:阻化剂的制备方法,该阻化剂包含组分(A)和组分(B);具体步骤如下:A preparation method and a use method for preventing a self-ignition of dry brown coal, characterized in that: a preparation method of a inhibitor, the inhibitor comprises component (A) and component (B); the specific steps are as follows:
    (1)制样:将褐煤剥去表面氧化层,继而进行快速破碎,筛分出足够量1mm<粒度<4mm的煤样;(1) Sample preparation: the lignite is stripped of the surface oxide layer, followed by rapid crushing, and a sufficient amount of coal sample having a size of 1 mm < particle size < 4 mm is sieved;
    (2)在三口烧瓶中加入磷酸,加热升温,边搅拌边加入计量好的尿素(与磷酸摩尔比为8:9),控制温度不要超过80℃。待尿素全部溶解完后,将溶液进一步升温,经发泡、聚合、固化三个阶段可得到白色固体,即低聚磷酸铵。产生的气体经回流冷凝、水洗后用1.0mol/L的氢氧化钠溶液吸收;(2) Add phosphoric acid to a three-necked flask, heat up, add a metered amount of urea (8:9 molar ratio to phosphoric acid) with stirring, and control the temperature not to exceed 80 °C. After the urea is completely dissolved, the solution is further heated, and a white solid, that is, an ammonium polyphosphate, is obtained through three stages of foaming, polymerization, and solidification. The generated gas is condensed by reflux, washed with water and then absorbed with a 1.0 mol/L sodium hydroxide solution;
    (3)按质量计,组分(A)是占60-80wt%主阻化剂,组分(B)是占20-40%的副催化剂;将其均匀混合成阻化剂粉;(3) by mass, component (A) is 60-80% by weight of primary inhibitor, component (B) is 20-40% by-product; uniformly mixing it into inhibitor powder;
    (4)取阻化剂粉和水按重量计1-5∶5的比例进行充分混合成阻化剂溶液。(4) The inhibitor powder and water are sufficiently mixed to form a inhibitor solution in a ratio of 1-5:5 by weight.
  2. 根据权利要求1所述的一种防止干燥褐煤自燃的阻化剂的制备方法,其特征是:所述的主阻化剂为氯化镁。The method for preparing a resisting agent for preventing spontaneous combustion of dry lignite according to claim 1, wherein the primary inhibitor is magnesium chloride.
  3. 根据权利要求1所述的一种防止干燥褐煤自燃的阻化剂的制备方法,其特征是:所述的副阻化剂为磷酸二氢铵和低聚磷酸铵,按质量百分比1:1-2混合而得。The method for preparing a resisting agent for preventing spontaneous combustion of dry lignite according to claim 1, wherein the auxiliary inhibitor is ammonium dihydrogen phosphate and ammonium polyphosphate, and is 1:1 by mass. 2 mixed.
  4. 根据权利要求1所述的一种防止干燥褐煤自燃的阻化剂的制备方法,其特征是:所述的副阻化剂低聚磷酸铵是由磷酸、尿素合成而得,合成时控制温度不得超过80℃,合成生成的气体由氢氧化钠溶液吸收;磷酸与尿素的摩尔比为8:9。The method for preparing a resisting agent for preventing spontaneous combustion of dry lignite according to claim 1, wherein the auxiliary retarding agent ammonium polyphosphate is obtained by synthesizing phosphoric acid and urea, and the temperature is not controlled during the synthesis. Above 80 ° C, the synthetic gas is absorbed by the sodium hydroxide solution; the molar ratio of phosphoric acid to urea is 8:9.
  5. 一种防止干燥褐煤自燃的阻化剂的使用方法,其特征是:按质量体积比计,g煤样/ml阻化液,将1:(0.1-2.0)比例的阻化溶液均匀喷洒于煤样表面即可。 The invention discloses a method for using a resisting agent for preventing spontaneous combustion of dry lignite, characterized in that: in a mass-to-volume ratio, g coal sample/ml resisting solution, uniformly spraying a resisting solution of a ratio of 1: (0.1-2.0) on coal The surface can be.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114247343A (en) * 2021-12-21 2022-03-29 太原理工大学 Soluble slow-release temperature-sensitive inhibitor manufacturing control device and control system

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106644803A (en) * 2016-10-28 2017-05-10 内蒙古科技大学 Method for determining optimal fireproof critical moisture content in hydrated coal dewatering process
CN106948857A (en) * 2017-05-11 2017-07-14 宿州市金鼎安全技术股份有限公司 A kind of inorganic retardant of spontaneous combustionof coal and its application method
CN109957434B (en) * 2019-03-27 2021-08-10 中国矿业大学 Inhibitor for inhibiting spontaneous combustion in upgraded lignite stacking and storing process and preparation and use methods thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01119242A (en) * 1987-07-28 1989-05-11 Antonio Espejo Martinez Epidural space locator
CN101487399A (en) * 2008-07-29 2009-07-22 辽宁工程技术大学 Stopping agent for preventing coal self-ignition and its production and use method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101793160B (en) * 2010-01-29 2011-10-05 北京工业大学 Environment-friendly flame-retardant high-molecular gel inhibitor for preventing coal from spontaneously combusting of coal mine
CN101830670A (en) * 2010-05-07 2010-09-15 陆彪东 Flame-retardant pitch for underground tunnel road of coal mine and preparation method thereof
CN103306710B (en) * 2013-06-14 2015-10-28 陕煤集团神木张家峁矿业有限公司 A kind of compound retardant preventing spontaneous combustion of pulverized coal
CN103304846A (en) * 2013-06-14 2013-09-18 北京理工大学 Ammonium polyphosphate and aluminum hydroxide nano-composite and preparation method thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01119242A (en) * 1987-07-28 1989-05-11 Antonio Espejo Martinez Epidural space locator
CN101487399A (en) * 2008-07-29 2009-07-22 辽宁工程技术大学 Stopping agent for preventing coal self-ignition and its production and use method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
HU , BINGCHENG ET AL.: "The Synthesis of Ammonium Low-Polysphate and Application in the Extinguishing Agent", EXPLOSIVE MATERIALS, vol. 6, no. 30, 31 December 2001 (2001-12-31), pages 31, ISSN: 1001-8352 *
ZHANG, WENYU ET AL.: "Experimental Study on Inhibition of Lignite Oxidation and Spontaneous Combustion by Composite Inhibitor", ENERGY TECHNOLOGY AND MANAGEMENT, vol. 40, no. 1, 28 February 2015 (2015-02-28), pages 132, ISSN: 1672-9943 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114247343A (en) * 2021-12-21 2022-03-29 太原理工大学 Soluble slow-release temperature-sensitive inhibitor manufacturing control device and control system
CN114247343B (en) * 2021-12-21 2024-03-01 太原理工大学 Control device and control system for manufacturing soluble slow-release temperature-sensitive inhibitor

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