CN115078458A - A method for precise determination of coal low temperature oxidation microcalorimetry based on phase transition reference - Google Patents

A method for precise determination of coal low temperature oxidation microcalorimetry based on phase transition reference Download PDF

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CN115078458A
CN115078458A CN202210844975.7A CN202210844975A CN115078458A CN 115078458 A CN115078458 A CN 115078458A CN 202210844975 A CN202210844975 A CN 202210844975A CN 115078458 A CN115078458 A CN 115078458A
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CN115078458B (en
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辛海会
张鹏程
竹永健
刘金虎
石长坤
李文科
舒通
梁玉柱
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Chongxin County Baiguangou Coal Industry Co ltd
Xuzhou Mining Business Group Co ltd
China University of Mining and Technology CUMT
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Chongxin County Baiguangou Coal Industry Co ltd
Xuzhou Mining Business Group Co ltd
China University of Mining and Technology CUMT
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Abstract

本发明公开了一种基于相变参比的煤低温氧化微量热精准测定方法,首先测定某一特定相变温度的有机相变材料在升温过程中的热流变化,再根据测量方式为恒温热效应或者升温热效应设定升温程序,将该有机相变材料作为参比以煤样作为样品进行测试,基于此得到恒温或升温过程中煤低温氧化的完整量热峰及其相变参比放热量,通过减去相变材料完整量热峰的值,即可精准得到所设定的恒温或升温过程中煤低温氧化的放热量;经过该方法测定的煤低温氧化的产热量以单独的相变材料作为参比基线,突破了使用微量热分析仪直接测定煤低温氧化放热量时无法得到完整放热峰的局限性,有效避免了基线误差所带来的影响,实现煤样低温氧化放热全过程和分阶段的精准测量。

Figure 202210844975

The invention discloses an accurate measurement method of low temperature oxidation microcalorimetry of coal based on phase change reference. First, the heat flow change of an organic phase change material with a specific phase change temperature during the heating process is measured, and then according to the measurement method, constant temperature thermal effect or The heating program is set for the heating effect, and the organic phase change material is used as a reference and the coal sample is used as the sample for testing. By subtracting the value of the complete calorimetric peak of the phase change material, the heat release of the coal low temperature oxidation during the set constant temperature or heating process can be accurately obtained; the heat production of the low temperature oxidation of coal measured by this method is taken as the phase change material alone. The reference baseline breaks through the limitation that a complete exothermic peak cannot be obtained when using a microcalorimeter to directly measure the exothermic heat of coal low-temperature oxidation, effectively avoids the influence of the baseline error, and realizes the whole process of low-temperature oxidation exothermic of coal samples. Accurate measurement in stages.

Figure 202210844975

Description

一种基于相变参比的煤低温氧化微量热精准测定方法A method for precise determination of coal low temperature oxidation microcalorimetry based on phase transition reference

技术领域technical field

本发明涉及一种测定煤低温氧化产热的方法,具体为一种基于相变参比的煤低温氧化微量热精准测定方法,属于煤低温氧化产热测定技术领域。The invention relates to a method for measuring the heat production by low temperature oxidation of coal, in particular to a method for accurate measurement of the microcalorimetry of coal low temperature oxidation based on phase transition reference, and belongs to the technical field of low temperature oxidation heat production measurement of coal.

背景技术Background technique

煤自燃是矿井开采过程中存在的主要灾害之一,它不仅烧毁大量煤炭资源,造成巨大的经济损失,而且会产生大量有毒有害气体,对矿工的生命安全造成了极大的威胁。采空区是最易于发生煤自燃的危险区域,其存在大量裂隙和漏风通道,在一定条件下煤炭逐渐发生低温氧化产热,而采空区三带中的自燃带由于氧化产生的热量不能够及时散失掉,发生煤自燃的可能性大大增加。Coal spontaneous combustion is one of the main disasters in the process of mine mining. It not only burns a large amount of coal resources and causes huge economic losses, but also produces a large amount of toxic and harmful gases, posing a great threat to the safety of miners. The mined-out area is the most prone to coal spontaneous combustion dangerous area. There are a lot of cracks and air leakage channels. Under certain conditions, the coal gradually undergoes low-temperature oxidation to generate heat, while the spontaneous combustion zone in the three-zone of the mined-out area cannot be heated due to oxidation. If it is lost in time, the possibility of spontaneous combustion of coal is greatly increased.

对于煤炭低温氧化许多科学家做了研究,然而大多数研究停留在煤炭产气特性、官能团变化、动力学参数测定、热解产物分析等方面,对于煤炭低温氧化的产热特性研究涉及较少,已知的测定方法主要是TG-DSC法,即热重-差热法,但该方法扫描精度不足,升温速率较快,使用的煤样量较少(一般约为10mg),难以体现煤样在井下大量赋存且呈破碎堆积状态下的氧化产热特性。另外现有的微量热分析仪同样利用差热补偿的原理,能够精准测定煤炭在低温氧化时的产热特性,灵敏度高,升温速率能够达到0.001℃/min,信号稳定性好,样品池体积大,能够容纳较多煤样量,与井下煤炭低温氧化的过程较为符合。但是在没有参比的情况下,现有使用该仪器测得的煤低温氧化热流变化曲线基线并不准确,使用该基线进行计算求解煤样热量变化时存在一定偏差,尤其是煤样在较低温度下氧化放热时,无法显示出煤样的完整量热峰,连续放热的情况下更加难以测定;目前也有研究在样品池放入煤样并通入氧气,且采用相同质量的煤样通氮气作为参比,但是由于作为参比的煤样在惰性气体氛围下升温发生化学变化仍然会产生热效应,这部分热效应对测试结果也会产生影响;而且,当前的热测量方法并不能有效地测量煤样在某一设定温度变化范围内低温氧化的产热量,进而导致无法对煤样在特定温度变化区间内的低温氧化产热情况进行后续分析,因此,如何提供一种方法,在基于微量热分析仪进行测量的情况下,不仅能实现准确测定煤样低温氧化产热特性,而且还能对测量煤样设定温度变化范围内完整放热峰进行低温氧化产热量测定,从而为后续对煤样的分析提供精准的数据,是本行业的研究方向之一。Many scientists have done research on the low temperature oxidation of coal, but most of the research stays in the aspects of coal gas production characteristics, functional group changes, kinetic parameter determination, pyrolysis product analysis, etc. The known determination method is mainly TG-DSC method, that is, thermogravimetric-differential thermal method, but this method has insufficient scanning accuracy, fast heating rate, and uses a small amount of coal sample (generally about 10 mg), which is difficult to reflect the coal sample. Oxidative heat production characteristics in the state of broken accumulation and large occurrences in wells. In addition, the existing microcalorimeter also uses the principle of differential thermal compensation, which can accurately measure the heat production characteristics of coal during low temperature oxidation. It has high sensitivity, the heating rate can reach 0.001 °C/min, the signal stability is good, and the sample cell volume is large. , which can accommodate more coal samples, which is more in line with the low-temperature oxidation process of underground coal. However, in the absence of a reference, the existing baseline of the coal low temperature oxidation heat flow change curve measured by this instrument is not accurate, and there is a certain deviation when using this baseline to calculate and solve the heat change of the coal sample, especially when the coal sample is at a lower temperature When oxidizing and exothermic at high temperature, the complete calorimetric peak of the coal sample cannot be displayed, and it is more difficult to measure in the case of continuous exothermicity. At present, there are also studies in which coal samples are placed in the sample pool and oxygen is introduced, and coal samples of the same quality are used. Nitrogen gas is used as a reference, but because the coal sample used as a reference is heated up in an inert gas atmosphere and chemical changes will still produce thermal effects, this part of the thermal effect will also have an impact on the test results; moreover, the current thermal measurement methods are not effective. Measure the heat production of low-temperature oxidation of coal samples within a certain temperature range, which makes it impossible to carry out subsequent analysis on the low-temperature oxidation heat production of coal samples in a specific temperature range. Therefore, how to provide a method based on When the microcalorimeter is used for measurement, it can not only accurately measure the low-temperature oxidation heat production characteristics of coal samples, but also measure the complete exothermic peaks within the set temperature variation range of the measured coal samples. The analysis of coal samples to provide accurate data is one of the research directions of the industry.

发明内容SUMMARY OF THE INVENTION

针对上述现有技术存在的问题,本发明提供一种基于相变参比的煤低温氧化微量热精准测定方法,不仅能实现准确测定煤样低温氧化产热特性,而且还能对测量煤样设定温度变化范围内进完整放热峰行低温氧化产热量测定,从而为后续对煤样的分析提供精准的数据。In view of the problems existing in the above-mentioned prior art, the present invention provides a method for accurate determination of low temperature oxidation microcalorimetry of coal based on phase transition reference, which can not only accurately measure the low temperature oxidation heat production characteristics of coal samples, but also set the The complete exothermic peak is measured within a certain temperature range for low temperature oxidation heat production, thereby providing accurate data for subsequent analysis of coal samples.

为了实现上述目的,本发明采用的技术方案是:基于相变参比的煤低温氧化微量热精准测定方法,具体步骤为:In order to achieve the above purpose, the technical solution adopted in the present invention is: a method for accurate determination of low temperature oxidation microcalorimetry of coal based on phase transition reference, the specific steps are:

步骤一、先选择原煤煤样,然后设定原煤煤样的温度变化区间,后续在该温度变化区间内测量其低温氧化产热量,根据设定的温度变化区间选择相变温度与该温度区间相适应的有机相变材料,接着确定后续煤样测量试验时的加热条件,所述加热条件为恒温热效应或者升温热效应,根据加热条件在微量热分析仪内选定对应的升温程序;Step 1: First select the raw coal sample, then set the temperature change interval of the raw coal sample, then measure its low-temperature oxidation heat production within the temperature change interval, and select the phase transition temperature corresponding to the temperature interval according to the set temperature change interval. The adapted organic phase change material, and then determine the heating conditions during the subsequent coal sample measurement test, the heating conditions are constant temperature thermal effect or heating thermal effect, and a corresponding heating program is selected in the microcalorimeter according to the heating conditions;

步骤二、向样品池不加入物质并持续通入纯氧气,参比池加入步骤一选定的有机相变材料并通入纯氮气,根据步骤一确定的加热条件,利用微量热分析仪采用设定的升温程序测定得到有机相变材料的热流随温度的变化曲线;Step 2: No substance is added to the sample cell and pure oxygen is continuously fed. The organic phase change material selected in Step 1 is added to the reference cell and pure nitrogen is fed into the reference cell. The change curve of the heat flow of the organic phase change material with the temperature is obtained by the determined heating program;

步骤三、向样品池加入步骤一选定的原煤煤样并持续通入纯氧气,参比池加入有机相变材料并通入纯氮气,选择与步骤二相同的加热条件,利用微量热分析仪采用设定的升温程序测定得到有机相变材料作为参比的原煤热流随温度的变化曲线;Step 3: Add the raw coal sample selected in step 1 to the sample pool and continuously feed pure oxygen, add organic phase change material to the reference pool and feed pure nitrogen gas, select the same heating conditions as step 2, and use a microcalorimeter analyzer. The change curve of raw coal heat flow with temperature with organic phase change material as a reference is obtained by using the set heating program;

步骤四、向样品池加入所需测量的原煤煤样并持续通入纯氧气,参比池不加入物质并通入纯氮气,选择与步骤二相同的加热条件,利用微量热分析仪采用设定的升温程序测定得到原煤的热流随温度的变化曲线;Step 4. Add the raw coal sample to be measured into the sample pool and continuously feed pure oxygen. The reference pool does not add substances and feeds pure nitrogen. Select the same heating conditions as step 2, and use the microcalorimeter to set the The curve of the heat flow of the raw coal with the temperature was obtained by measuring the heating program;

步骤五、将步骤二得到的有机相变材料热流变化曲线、步骤三得到的有机相变材料作为参比的原煤热流变化曲线以及步骤四得到原煤的热流变化曲线,按照步骤一选定的温度变化区间分别进行计算得到三者在该温度变化区间内的热量变化的具体数值分别为Q1、Q2和Q3 J/g;其中Q3即为传统测量方法得到的原煤在所选温度范围内的氧化放热量;将Q2值与Q1值做差,即为精准测定原煤在所选温度变化区间内的实际氧化放热量。Step 5. Use the organic phase change material heat flow change curve obtained in step 2, the organic phase change material obtained in step 3 as a reference heat flow change curve of raw coal, and the heat flow change curve of raw coal obtained in step 4, according to the temperature change selected in step 1. The specific values of the three heat changes in the temperature change range are respectively Q 1 , Q 2 and Q 3 J/g; among them Q 3 is the raw coal obtained by the traditional measurement method within the selected temperature range. The difference between the Q 2 value and the Q 1 value is to accurately measure the actual oxidation heat release of the raw coal in the selected temperature change interval.

进一步,所述有机相变材料的相变温度在30℃~200℃,有机相变材料包括相变温度为165℃的甘露醇、相变温度为116℃的赤藓糖醇、相变温度在30℃~200℃的多种相变石蜡;根据温度变化区间选定有机相变材料由上述单一物质或多种不同相变温度的物质复配形成,其中单一相变材料能够实现煤低温氧化分阶段热量的测量,多种有机相变材料复配能够实现煤低温氧化全过程热量的测量。Further, the phase transition temperature of the organic phase change material is between 30°C and 200°C, and the organic phase change material includes mannitol with a phase transition temperature of 165°C, erythritol with a phase transition temperature of 116°C, and a phase transition temperature of 116°C. A variety of phase change paraffin waxes from 30°C to 200°C; organic phase change materials are selected according to the temperature change interval and are formed from the above single substance or a variety of substances with different phase change temperatures, wherein a single phase change material can realize the low temperature oxidation of coal. The measurement of stage heat and the combination of various organic phase change materials can realize the measurement of heat in the whole process of low temperature oxidation of coal.

进一步,所述恒温热效应的升温程序为:首先在30℃下恒温保持1h,然后由30℃升温至选定有机相变材料的相变温度,升温速率为0.1℃/min、0.2℃/min、0.5℃/min、1℃/min其中一种,然后在该温度下恒温保持2h。采用这种参数能保证恒温热效应稳定进行,进一步保证后续试验测量的数据精度。Further, the heating procedure of the constant temperature thermal effect is as follows: firstly, the temperature is kept constant at 30 °C for 1 h, and then the temperature is increased from 30 °C to the phase change temperature of the selected organic phase change material, and the heating rate is 0.1 °C/min, 0.2 °C/min, One of 0.5°C/min and 1°C/min, and then kept at this temperature for 2h at a constant temperature. Adopting this parameter can ensure the stable heating effect of constant temperature, and further ensure the data accuracy of subsequent test measurements.

进一步,所述升温热效应的升温程序为:对于n种有机相变材料复配的相变参比,首先由室温以5℃/min的升温速率快速升温至(T1-x1)℃,然后由(T1-x1)℃升温至(Tn+xn)℃,升温速率为0.1℃/min、0.2℃/min、0.5℃/min、1℃/min其中一种,所述T1为n种有机相变材料中相变温度最小的有机相变材料对应的相变温度值,Tn为n种有机相变材料中相变温度最大的有机相变材料对应的相变温度值,x1和xn分别为相变温度最小的有机相变材料和相变温度最大的有机相变材料各自相变峰半峰宽的温度变化数值。采用这种参数能保证升温热效应进行的温度变化区间能覆盖复配相变材料所有的相变峰,进一步保证后续试验测量的数据精度。Further, the heating program of the heating effect is as follows: for the phase change reference compounded by n kinds of organic phase change materials, firstly, the temperature is rapidly raised from room temperature to (T 1 -x 1 )° C. at a heating rate of 5° C./min, and then From (T 1 -x 1 )°C to (T n +x n )°C, the temperature rise rate is one of 0.1°C/min, 0.2°C/min, 0.5°C/min, 1 °C/min, the T1 is the phase transition temperature value corresponding to the organic phase change material with the smallest phase transition temperature among the n organic phase change materials, T n is the phase transition temperature value corresponding to the organic phase change material with the largest phase transition temperature among the n organic phase change materials, x 1 and x n are the temperature change values of the half-peak widths of the respective phase transition peaks of the organic phase change material with the smallest phase transition temperature and the organic phase change material with the largest phase transition temperature, respectively. The use of this parameter can ensure that the temperature change interval of the heating effect can cover all the phase change peaks of the composite phase change material, and further ensure the data accuracy of subsequent test measurements.

进一步,所述原煤煤样用量为1~2g,所述有机相变材料用量为1~8g,原煤煤样与有机相变材料的用量比为1:1、1:2、1:4其中一种;所述用量比的选择方法为:当需要测量的温度区间最大值小于85℃时,原煤煤样与有机相变材料的用量比为1:1;当需要测量的温度区间最大值位于(85,Tcpt]℃时,原煤煤样与有机相变材料的用量比为1:2;当需要测量的温度区间最大值大于Tcpt℃时,原煤煤样与有机相变材料的用量比为1:4,所述Tcpt为原煤煤样的交叉点温度数值。采用这种用量比能保证煤样量热峰能够尽可能地被相变材料量热峰覆盖,从而进一步保证后续试验测量的数据精度。Further, the dosage of the raw coal sample is 1-2 g, the dosage of the organic phase change material is 1-8 g, and the dosage ratio of the raw coal sample and the organic phase change material is one of 1:1, 1:2, and 1:4. The method for selecting the dosage ratio is: when the maximum temperature interval to be measured is less than 85°C, the dosage ratio of the raw coal sample to the organic phase change material is 1:1; when the maximum temperature interval to be measured is located at ( 85,T cpt ] ℃, the dosage ratio of raw coal sample and organic phase change material is 1:2; when the maximum temperature interval to be measured is greater than T cpt ℃, the dosage ratio of raw coal sample and organic phase change material is: 1:4, the T cpt is the temperature value of the intersection point of the raw coal sample. Using this dosage ratio can ensure that the calorimetric peak of the coal sample can be covered by the calorimetric peak of the phase change material as much as possible, thereby further ensuring the subsequent test measurement data precision.

进一步,所述氮气和氧气的气体流速保持一致,均为50~100mL/min其中任一数值,气体流速由质量流量计控制。Further, the gas flow rates of the nitrogen gas and the oxygen gas are kept the same, which is any value between 50 and 100 mL/min, and the gas flow rates are controlled by a mass flow meter.

与现有技术相比,本发明基于相变参比的煤低温氧化微量热精准测定方法,针对本领域内无法准确测量煤样低温氧化过程中某一设定温度变化范围煤样产热情况以及微量热分析仪测试基线变化导致无法显示出完整放热峰,致使测定其产热出现偏差的缺陷,提供了一种基于相变参比的煤低温氧化微量热精准测定方法,首先测定了某一相变温度的有机相变材料或复合有机相变材料在升温过程中的热流变化,再根据测量方式为恒温热效应或者升温热效应设定升温程序,将该有机相变材料作为参比以煤样作为样品进行测试,对两条曲线计算并相减精准得到煤样低温氧化过程中某一温度范围内的产热总量。经过该方法测定的煤低温氧化的产热量以单独的相变材料作为参比基线,突破了使用微量热分析仪直接测定煤低温氧化放热量时无法得到完整放热峰的局限性,能够显示出煤样氧化的完整放热峰,有效的避免了使用微量热分析仪实测时非完整放热峰热流曲线基线误差所带来的影响;并且可以针对煤样在不同温度范围的产热量选取该相变温度内的单一有机相变材料或复合有机相变材料,实现煤样低温氧化放热全过程和分阶段的测量,同时还能对煤样恒温氧化的放热水平进行准确评估,对于评价煤样的氧化能力、预测煤自然发火特征具有重要理论价值;该方法操作简便,测量精准且偏差极小,为后续研究煤低温氧化产热以及煤自燃方面尤其是煤样低温氧化产热的连续特性研究提供数据支撑。Compared with the prior art, the present invention is based on the phase-change reference-based method for accurate determination of microcalorimetry of coal low-temperature oxidation, aiming at the inability to accurately measure the heat production of coal samples in a set temperature change range during the low-temperature oxidation process of coal samples in the art and The change of the test baseline of the microcalorimeter analyzer leads to the defect that the complete exothermic peak cannot be displayed, resulting in the deviation of the determination of its heat production. An accurate measurement method of the low temperature oxidation microcalorimetry of coal based on the phase change reference is provided. The heat flow change of the organic phase change material or composite organic phase change material at the phase change temperature during the heating process, and then set the heating program for the constant temperature thermal effect or the heating thermal effect according to the measurement method, and the organic phase change material is used as a reference. The samples are tested, and the two curves are calculated and subtracted to accurately obtain the total heat production in a certain temperature range during the low-temperature oxidation of coal samples. The heat production of coal low-temperature oxidation determined by this method uses a separate phase change material as a reference baseline, which breaks through the limitation that a complete exothermic peak cannot be obtained when using a microcalorimeter to directly measure the heat of coal low-temperature oxidation. The complete exothermic peak of coal sample oxidation can effectively avoid the influence of the baseline error of the heat flow curve of the incomplete exothermic peak measured by the microcalorimeter; and the phase can be selected according to the heat production of coal samples in different temperature ranges. The single organic phase change material or composite organic phase change material in the variable temperature can realize the whole process and stage measurement of the low temperature oxidation heat release of coal samples, and can also accurately evaluate the heat release level of the constant temperature oxidation of coal samples. It has important theoretical value in predicting the oxidative capacity of coal samples and predicting the spontaneous combustion characteristics of coal; this method is easy to operate, accurate in measurement and has minimal deviation. The research provides data support.

附图说明Description of drawings

图1为本发明的整体实施流程图;Fig. 1 is the overall implementation flow chart of the present invention;

图2为本发明升温热效应对应程序的温度区间选择示意图;Fig. 2 is the temperature range selection schematic diagram of the program corresponding to the heating effect of the present invention;

图3为实施例1中相变温度为80℃相变石蜡热流曲线及计算范围;Fig. 3 is the heat flow curve and calculation range of the phase change paraffin wax when the phase transition temperature is 80°C in Example 1;

图4为实施例1中相变温度为80℃相变石蜡作为参比的硫磺沟长焰煤热流曲线及计算范围;Fig. 4 is the heat flow curve and the calculation range of the sulfur ditch long-flame coal with the phase change temperature of 80°C as the reference in Example 1;

图5为实施例1中硫磺沟长焰煤热流曲线及计算范围;Fig. 5 is sulfur ditch long flame coal heat flow curve and calculation range in embodiment 1;

图6为实施例2中相变温度为120℃相变石蜡热流曲线及计算范围;Fig. 6 is the heat flow curve and the calculation range of the phase change paraffin wax when the phase transition temperature is 120°C in Example 2;

图7为实施例2中相变温度为120℃相变石蜡作为参比的东露天气煤热流曲线及计算范围;Fig. 7 is the heat flow curve and calculation range of the open-air coal in Example 2 where the phase transition temperature is 120°C and the phase transition paraffin is used as a reference;

图8为实施例2中东露天气煤热流曲线及计算范围。Fig. 8 is the heat flow curve and calculation range of coal in the open air in the middle of Example 2.

具体实施方式Detailed ways

下面将对本发明作进一步说明。The present invention will be further described below.

实施例1:具体步骤为:Embodiment 1: Concrete steps are:

步骤一、先选择硫磺沟长焰煤作为原煤煤样,然后选定原煤煤样的温度变化区间为48℃到83℃,后续在该温度变化区间内测量其低温氧化产热量,根据设定的温度变化区间选择相变温度为80℃的相变石蜡2g待用,取硫磺沟长焰煤煤样2g待用,接着确定后续煤样测量试验时的加热条件为升温热效应,其对应的升温程序为:首先由室温以5℃/min的升温速率快速升温至48℃,然后由48℃以0.1℃/min的速率升温至115℃;Step 1. First select Sushuanggou long-flame coal as the raw coal sample, and then select the temperature change range of the raw coal sample to be 48°C to 83°C, and then measure its low-temperature oxidation heat production within this temperature range. In the temperature change interval, 2 g of phase-change paraffin with a phase transition temperature of 80°C was selected for use, and 2 g of sulfuric ditch long-flame coal sample was taken for use. Then, the heating condition in the subsequent coal sample measurement test was determined as the heating effect, and the corresponding heating program It is: firstly from room temperature to 48°C at a heating rate of 5°C/min, and then from 48°C to 115°C at a rate of 0.1°C/min;

步骤二、向样品池不加入物质并持续通入纯氧气,参比池加入步骤一中相变温度为80℃的相变石蜡1g并通入纯氮气,二者速率均为50mL/min,根据步骤一确定的的加热条件,利用微量热分析仪采用对应的升温程序测定得到该相变石蜡的热流随温度的变化曲线,如图3所示;Step 2. No substance is added to the sample cell and pure oxygen is continuously fed. In the reference cell, 1 g of phase-change paraffin with a phase transition temperature of 80°C in step 1 is added and pure nitrogen is fed. Both rates are 50 mL/min. The heating conditions determined in step 1 are measured by a microcalorimeter using a corresponding heating program to obtain the heat flow curve of the phase change paraffin as a function of temperature, as shown in Figure 3;

步骤三、向样品池加入步骤一选定的硫磺沟长焰煤煤样1g并持续通入纯氧气,参比池加入步骤一中相变温度为80℃的相变石蜡1g并通入纯氮气,二者速率均为50mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用设定的升温程序测定得到该相变石蜡作为参比的硫磺沟长焰煤热流随温度的变化曲线,如图4所示;Step 3: Add 1 g of the sulfur ditch long-flame coal sample selected in step 1 to the sample pool and continuously inject pure oxygen. Add 1 g of phase change paraffin with a phase transition temperature of 80°C in the reference pool and inject pure nitrogen into the reference pool. , the rate of both is 50mL/min, select the same heating conditions as step 2, and use the microcalorimeter to measure the temperature change of the long-flame coal with the phase change paraffin as a reference. curve, as shown in Figure 4;

步骤四、向样品池加入所需测量的硫磺沟长焰煤煤样1g并持续通入纯氧气,参比池不加入物质并通入纯氮气,二者速率均为50mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用对应的升温程序测定得到硫磺沟长焰煤的热流随温度的变化曲线,如图5所示;Step 4. Add 1 g of the sulfur ditch long-flame coal sample to be measured into the sample pool and continuously feed pure oxygen. The reference pool does not add substances and feeds pure nitrogen. The rate of both is 50mL/min. 2. Under the same heating conditions, use a microcalorimeter to measure the change curve of the heat flow with temperature of the long-flame coal in the Sushuanggou, as shown in Figure 5;

步骤五、将步骤二得到的相变石蜡热流变化曲线、步骤三得到的相变石蜡作为参比的硫磺沟长焰煤热流变化曲线以及步骤四得到的硫磺沟长焰煤热流变化曲线,按照步骤一选定的48℃到83℃的温度变化区间分别进行计算,得到三者在该温度变化区间内的热量变化的具体数值;其中图5计算热效应变化数值即为传统测量方法得到的原煤在所选温度范围内的氧化放热量(即升温热效应);将图4计算热效应变化数值减去图3热效应变化数值即为本发明精准测定原煤在所选温度变化区间内的实际氧化放热量(即升温热效应)。Step 5, take the phase change paraffin heat flow change curve obtained in step 2, the phase change paraffin obtained in step 3 as the reference heat flow change curve of sulfur ditch long flame coal and the heat flow change curve of sulfur ditch long flame coal obtained in step 4, according to the steps A selected temperature change interval of 48°C to 83°C is calculated separately, and the specific value of the heat change of the three in this temperature change interval is obtained; among them, the heat effect change value calculated in Fig. 5 is the raw coal obtained by the traditional measurement method. Oxidation heat release (i.e. heating effect) within the selected temperature range; subtracting the thermal effect change value calculated in Figure 4 from the thermal effect change value in Figure 3 is the present invention to accurately measure the actual oxidation heat release (i.e. heating effect) of raw coal in the selected temperature change interval Thermal effect).

实施例2:具体步骤为:Embodiment 2: Concrete steps are:

步骤一、先选择东露天气煤作为原煤煤样,然后选定原煤煤样的温度变化区间为90℃到128℃,后续在该温度变化区间内测量其低温氧化产热量,根据设定的温度变化区间选择相变温度为120℃的相变石蜡4g待用,取东露天气煤煤样2g待用,接着确定后续煤样测量试验时的加热条件为升温热效应,其对应的升温程序为:首先由室温以5℃/min的升温速率快速升温至90℃,然后由90℃以0.2℃/min的速率升温至150℃;Step 1. First select the Donglu weather coal as the raw coal sample, and then select the temperature range of the raw coal sample to be 90°C to 128°C, and then measure its low-temperature oxidation heat production within the temperature range, according to the set temperature. In the change interval, 4g of phase change paraffin with a phase transition temperature of 120°C was selected for use, and 2g of coal sample from Donglu weather was used for use. Then, the heating condition in the subsequent coal sample measurement test was determined as the heating effect, and the corresponding heating program was: First, the temperature is rapidly heated from room temperature to 90°C at a rate of 5°C/min, and then from 90°C to 150°C at a rate of 0.2°C/min;

步骤二、向样品池不加入物质并持续通入纯氧气,参比池加入步骤一中相变温度为120℃的相变石蜡2g并通入纯氮气,二者速率均为80mL/min,根据步骤一确定的的加热条件,利用微量热分析仪采用对应的升温程序测定得到该相变石蜡的热流随温度的变化曲线,如图6所示;Step 2: No substance is added to the sample cell and pure oxygen is continuously fed. The reference cell is added with 2g of phase change paraffin with a phase transition temperature of 120°C in step 1 and pure nitrogen gas is fed into the reference cell. The rate of both is 80mL/min. The heating conditions determined in step 1 are measured by a microcalorimeter using a corresponding heating program to obtain the heat flow curve of the phase change paraffin as a function of temperature, as shown in Figure 6;

步骤三、向样品池加入步骤一选定的东露天气煤煤样1g并持续通入纯氧气,参比池加入步骤一中相变温度为120℃的相变石蜡2g并通入纯氮气,二者速率均为80mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用设定的升温程序测定得到该相变石蜡作为参比的东露天气煤的热流随温度的变化曲线,如图7所示;Step 3: Add 1g of Donglu weather coal sample selected in step 1 to the sample pool and continuously inject pure oxygen, add 2g of phase change paraffin with a phase transition temperature of 120°C in the reference pool and inject pure nitrogen gas into the reference pool, The rate of both is 80mL/min, and the same heating conditions as in step 2 are selected, and the heat flow curve of Donglu weather coal with the phase change paraffin as a reference is obtained by using a microcalorimeter and a set heating program to measure the change curve of heat flow with temperature. , as shown in Figure 7;

步骤四、向样品池加入所需测量的东露天气煤煤样1g并持续通入纯氧气,参比池不加入物质并通入纯氮气,二者速率均为80mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用对应的升温程序测定得到东露天气煤的热流随温度的变化曲线,如图8所示;Step 4. Add 1 g of the Donglu weather coal sample to be measured into the sample pool and continuously feed pure oxygen. The reference pool does not add substances and feeds pure nitrogen. The rate of both is 80mL/min. The selection is the same as that of step 2. Under the same heating conditions, the variation curve of heat flow with temperature of coal in the open weather was obtained by using a microcalorimeter and a corresponding heating program, as shown in Figure 8;

步骤五、将步骤二得到的相变石蜡热流变化曲线、步骤三得到的相变石蜡作为参比的东露天气煤热流变化曲线以及步骤四得到的东露天气煤热流变化曲线,按照步骤一选定的90℃到128℃的温度变化区间分别进行计算,得到三者在该温度变化区间内的热量变化的具体数值;其中图8计算热效应变化数值即为传统测量方法得到的原煤在所选温度范围内的氧化放热量(即升温热效应);将图7计算热效应变化数值减去图6热效应变化数值即为本发明精准测定原煤在所选温度变化区间内的实际氧化放热量(即升温热效应)。Step 5, take the phase change paraffin heat flow change curve obtained in step 2, the phase change paraffin obtained in step 3 as the reference heat flow change curve of Donglu weather coal and the heat flow change curve of Donglu weather coal obtained in step 4, select according to step one Calculate the temperature change interval between 90°C and 128°C, respectively, and obtain the specific value of the heat change of the three in this temperature change interval; among them, the heat effect change value calculated in Figure 8 is the raw coal obtained by the traditional measurement method at the selected temperature. Oxidation heat release within the range (i.e. heating effect); subtracting the thermal effect change value calculated in Figure 7 from the thermal effect change value in Figure 6 is the present invention to accurately measure the actual oxidation heat release (i.e. heating effect) of raw coal in the selected temperature change interval .

实施例3:具体步骤为:Embodiment 3: Concrete steps are:

步骤一、先选择胜利褐煤作为原煤煤样,然后选定原煤煤样的温度变化区间为75℃到85℃,后续在该温度变化区间内测量其低温氧化产热量,根据设定的温度变化区间选择相变温度为80℃的相变石蜡2g待用,取胜利褐煤煤样2g待用,接着确定后续煤样测量试验时的加热条件为恒温热效应,其对应的升温程序为:首先在30℃下恒温保持1h,然后由30℃以0.5℃/min的速率升温至80℃,然后在该温度下恒温保持2h;Step 1. First select Shengli lignite as the raw coal sample, and then select the temperature variation range of the raw coal sample to be 75°C to 85°C, and then measure its low-temperature oxidation heat production within this temperature variation range. According to the set temperature variation range Select 2 g of phase change paraffin with a phase transition temperature of 80 °C for use, and take 2 g of Shengli lignite sample for use. The temperature was kept at a constant temperature for 1 h, then the temperature was increased from 30 °C to 80 °C at a rate of 0.5 °C/min, and then the temperature was maintained at a constant temperature for 2 h;

步骤二、向样品池不加入物质并持续通入纯氧气,参比池加入步骤一中相变温度为80℃的相变石蜡1g并通入纯氮气,二者速率均为50mL/min,根据步骤一确定的加热条件,利用微量热分析仪采用对应的升温程序测定得到该相变石蜡的热流随温度的变化曲线;Step 2. No substance is added to the sample cell and pure oxygen is continuously fed. In the reference cell, 1 g of phase-change paraffin with a phase transition temperature of 80°C in step 1 is added and pure nitrogen is fed. Both rates are 50 mL/min. For the heating conditions determined in step 1, use a microcalorimeter to measure a curve of the heat flow of the phase change paraffin with temperature by using a corresponding heating program;

步骤三、向样品池加入步骤一选定的胜利褐煤煤样1g并持续通入纯氧气,参比池加入步骤一中相变温度为80℃的相变石蜡1g并通入纯氮气,二者速率均为50mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用设定的升温程序测定得到该相变石蜡作为参比的胜利褐煤的热流随温度的变化曲线;Step 3. Add 1 g of Shengli lignite sample selected in step 1 to the sample pool and continuously feed pure oxygen. Add 1 g of phase change paraffin with a phase change temperature of 80°C in the reference pool and feed pure nitrogen into the reference pool. The rate is all 50mL/min, and the same heating conditions as in step 2 are selected, and the heat flow curve of Shengli lignite with the phase change paraffin as a reference is obtained by using a microcalorimeter analyzer to measure the temperature rise program;

步骤四、向样品池加入所需测量的胜利褐煤煤样1g并持续通入纯氧气,参比池不加入物质并通入纯氮气,二者速率均为50mL/min,选择与步骤二相同的加热条件,利用微量热分析仪采用对应的升温程序测定得到胜利褐煤的热流随温度的变化曲线;Step 4. Add 1g of Shengli lignite sample to be measured into the sample pool and continue to feed pure oxygen. No substance is added to the reference pool and pure nitrogen is fed. Both rates are 50mL/min. Select the same as step 2. Heating conditions, the curve of the heat flow of Shengli lignite with temperature was obtained by using a microcalorimeter and a corresponding heating program to measure;

步骤五、将步骤二得到的相变石蜡热流变化曲线、步骤三得到的相变石蜡作为参比的胜利褐煤热流变化曲线以及步骤四得到的胜利褐煤热流变化曲线,按照步骤一选定的75℃到85℃的温度变化区间分别进行计算,得到三者在该温度变化区间内的热量变化的具体数值;其中胜利褐煤热流变化曲线计算得到的热效应变化数值即为传统测量方法得到的原煤在所选温度范围内的氧化放热量(即恒温热效应);将相变石蜡作为参比的胜利褐煤热流变化曲线计算得到的热效应变化数值减去相变石蜡热流变化曲线计算得到的热效应变化数值即为本发明精准测定原煤在所选温度变化区间内的实际氧化放热量(即恒温热效应)。Step 5. Use the phase change paraffin heat flow change curve obtained in step 2, the phase change paraffin obtained in step 3 as the reference Shengli lignite heat flow change curve and the Shengli lignite heat flow change curve obtained in step 4, according to the selected 75 ℃ in step 1. The temperature change interval to 85°C is calculated separately, and the specific value of the heat change of the three in the temperature change interval is obtained; among them, the heat effect change value calculated from the heat flow change curve of Shengli lignite is the raw coal obtained by the traditional measurement method. Oxidation heat release in the temperature range (that is, constant temperature thermal effect); the thermal effect change value calculated from the heat flow change curve of Shengli lignite with phase change paraffin as the reference minus the heat effect change value calculated from the phase change paraffin heat flow change curve is the present invention Accurately measure the actual oxidative heat release (ie constant temperature thermal effect) of raw coal in the selected temperature variation range.

实施例4:选择新桥无烟煤作为原煤煤样,测定其在75℃到175℃温度变化区间的低温氧化升温热效应规律特性;原煤煤样的用量为2g;选择的有机相变材料为相变温度为165℃的甘露醇、相变温度为116℃的赤藓糖醇与相变温度为95℃的相变石蜡按照质量比为1:1:1形成的混合物,用量为8g;本实施例中,T1为95℃,x1为20℃,Tn为165℃,xn为15℃;根据图2所示,则设定升温程序为:首先由室温以5℃/min的升温速率快速升温至75℃,然后由75℃以0.2℃/min的速率升温至180℃;后续测量实施过程与实施例1相同(测量过程中原煤煤样每次用量为1g,有机相变材料每次用量为4g),从而精准测定新桥无烟煤在75℃到175℃温度变化区间内的实际氧化放热量(即升温热效应)。Example 4: Xinqiao anthracite was selected as the raw coal sample, and its characteristics of the thermal effect of low temperature oxidation and heating in the temperature range of 75°C to 175°C were determined; the amount of raw coal sample was 2g; the selected organic phase change material was the phase change temperature It is a mixture of mannitol at 165°C, erythritol at a phase transition temperature of 116°C, and phase change paraffin at a phase transition temperature of 95°C in a mass ratio of 1:1:1, and the dosage is 8g; , T 1 is 95°C, x 1 is 20°C, Tn is 165°C, and xn is 15°C; as shown in Figure 2, the heating program is set as: firstly from room temperature at a heating rate of 5°C/min The temperature was raised to 75°C, and then increased from 75°C to 180°C at a rate of 0.2°C/min; the subsequent measurement implementation process was the same as that of Example 1 (the raw coal sample was 1 g each time during the measurement, and the organic phase change material was used each time. 4g), so as to accurately measure the actual oxidation heat release (ie heating effect) of Xinqiao anthracite in the temperature range of 75°C to 175°C.

实施例5:选择东露天气煤作为原煤煤样,测定其在110℃到120℃温度变化区间的低温氧化恒温热效应规律特性;原煤煤样的用量为3g;选择的有机相变材料为相变温度为116℃的赤藓糖醇,用量为6g;设定升温程序为:首先在30℃下恒温保持1h,然后由30℃以1℃/min的速率升温至116℃,然后在该温度下恒温保持2h;后续测量实施过程与实施例3相同(测量过程中原煤煤样每次用量为1.5g,有机相变材料每次用量为3g),从而精准测定东露天气煤110℃到120℃温度变化区间内的实际氧化放热量(即恒温热效应)。Example 5: The Donglu weather coal was selected as the raw coal sample, and its low-temperature oxidation constant temperature thermal effect law characteristics in the temperature range of 110°C to 120°C were determined; the amount of the raw coal sample was 3 g; the selected organic phase change material was phase change The temperature of erythritol is 116 °C, and the dosage is 6 g; the heating program is set as follows: first, keep constant temperature at 30 °C for 1 h, then increase the temperature from 30 °C to 116 °C at a rate of 1 °C/min, and then at this temperature The constant temperature was maintained for 2 hours; the subsequent measurement implementation process was the same as that of Example 3 (the amount of raw coal sample was 1.5g each time during the measurement process, and the amount of organic phase change material was 3g each time), so as to accurately determine the temperature of Donglu weather coal from 110 °C to 120 °C The actual oxidative heat release in the temperature range (ie constant temperature thermal effect).

上述五个实施例测量的结果如表1所示。The measurement results of the above five examples are shown in Table 1.

表1五个实施例的煤样低温氧化产热热效应具体参数:The specific parameters of the thermal effect of low temperature oxidation of coal samples in the five embodiments of table 1:

Figure BDA0003752286430000081
Figure BDA0003752286430000081

通过上述试验的数据及附图3至8可知,传统量热方法的量热数值在低温条件下测量精度较低,不能够显示出煤样氧化过程中的量热峰,难以实测出具体数值,本发明的方法在选定合适的相变温度的有机相变材料之后,能够精准测定煤样在低温氧化的过程中的实际热效应,将煤样在该过程中的热效应变化放大,显示出完整的放热峰并且能够针对热效应的方式测量出升温热效应或者恒温热效应,实现煤样热效应变化的分阶段或全过程精确测量。It can be seen from the data of the above test and accompanying drawings 3 to 8 that the calorimetric value of the traditional calorimetric method has a low measurement accuracy under low temperature conditions, and cannot show the calorimetric peak during the oxidation process of the coal sample, and it is difficult to measure the specific value. The method of the invention can accurately measure the actual thermal effect of the coal sample in the process of low-temperature oxidation after selecting an organic phase-change material with a suitable phase-transition temperature, amplify the thermal effect change of the coal sample in the process, and show a complete The exothermic peak can also measure the heating effect or the constant temperature heating effect according to the heating effect, so as to realize the accurate measurement of the thermal effect change of the coal sample in stages or in the whole process.

以上所述仅是本发明的优选实施方式,应当指出:对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only the preferred embodiment of the present invention, it should be pointed out that: for those skilled in the art, without departing from the principle of the present invention, several improvements and modifications can also be made, and these improvements and modifications are also It should be regarded as the protection scope of the present invention.

Claims (6)

1. A coal low-temperature oxidation micro-heat accurate determination method based on phase change reference is characterized by comprising the following specific steps:
firstly, selecting a raw coal sample, then setting a temperature change interval of the raw coal sample, subsequently measuring the low-temperature oxidation heat production quantity of the raw coal sample in the temperature change interval, selecting an organic phase change material with a phase change temperature corresponding to the temperature interval according to the set temperature change interval, then determining the heating condition of the subsequent coal sample during measurement test, wherein the heating condition is a constant-temperature heat effect or a heating-up heat effect, and selecting a corresponding heating-up program in a micro thermal analyzer according to the heating condition;
step two, adding no substance into the sample tank and continuously introducing pure oxygen, adding the organic phase change material selected in the step one into the reference tank and introducing pure nitrogen, and determining by using a trace thermal analyzer according to the heating condition determined in the step one and a set temperature rise program to obtain a change curve of the heat flow of the organic phase change material along with the temperature;
step three, adding the raw coal sample selected in the step one into a sample tank, continuously introducing pure oxygen, adding an organic phase change material into a reference tank, introducing pure nitrogen, selecting the heating condition same as that in the step two, and determining by using a trace thermal analyzer by adopting a set heating program to obtain a change curve of the heat flow of the raw coal as the reference, wherein the change curve of the heat flow of the raw coal is taken as the reference;
step four, adding a raw coal sample to be measured into a sample tank, continuously introducing pure oxygen, adding no substances into a reference tank, introducing pure nitrogen, selecting the heating condition same as that in the step two, and determining by using a trace thermal analyzer by adopting a set temperature-rising program to obtain a change curve of the heat flow of the raw coal along with the temperature;
step five, using the organic phase change material heat flow change curve obtained in the step two and the organic phase change material obtained in the step three as reference raw coal heat flowThe change curve and the heat flow change curve of the raw coal obtained in the fourth step are respectively calculated according to the temperature change interval selected in the first step, and the specific numerical values of the heat change of the raw coal, the heat flow change curve and the temperature change interval are respectively Q 1 、Q 2 And Q 3 J/g; wherein Q 3 Namely the oxidation heat release of the raw coal in the selected temperature range obtained by the traditional measuring method; will Q 2 Value and Q 1 And (4) making a difference, namely accurately measuring the actual oxidation heat release of the raw coal in the selected temperature change interval.
2. The coal low-temperature oxidation micro-calorimetry accurate determination method based on phase-change reference according to claim 1, wherein the phase-change temperature of the organic phase-change material is 30-200 ℃, the organic phase-change material comprises mannitol with a phase-change temperature of 165 ℃, erythritol with a phase-change temperature of 116 ℃, and a plurality of phase-change paraffins with a phase-change temperature of 30-200 ℃; the organic phase-change material is selected according to the temperature change interval and is formed by compounding the single substance or a plurality of substances with different phase-change temperatures.
3. The coal low-temperature oxidation micro-calorimetry accurate determination method based on phase-change reference according to claim 1, wherein the temperature rise program of the constant-temperature thermal effect is as follows: firstly keeping the temperature at 30 ℃ for 1h, then heating the temperature from 30 ℃ to the phase change temperature of the selected organic phase change material, wherein the heating rate is one of 0.1 ℃/min, 0.2 ℃/min, 0.5 ℃/min and 1 ℃/min, and then keeping the temperature at the constant temperature for 2 h.
4. The coal low-temperature oxidation micro-calorimetry accurate determination method based on phase change reference according to claim 1, wherein the temperature rise thermal effect is obtained by the following temperature rise program: for the phase change reference compounded by n organic phase change materials, the temperature is quickly raised from room temperature to (T) at the temperature rise rate of 5 ℃/min 1 -x 1 ) DEG C, then is prepared from (T) 1 -x 1 ) Raising the temperature to (T) n +x n ) The temperature rise rate is one of 0.1 ℃/min, 0.2 ℃/min, 0.5 ℃/min and 1 ℃/min, and the T is 1 Is n kinds of organicPhase change temperature value, T, corresponding to the organic phase change material with the minimum phase change temperature in the phase change material n The phase change temperature value, x, corresponding to the organic phase change material with the maximum phase change temperature in the n organic phase change materials 1 And x n The temperature change values are the half-peak widths of the phase change peak of the organic phase change material with the minimum phase change temperature and the phase change material with the maximum phase change temperature respectively.
5. The coal low-temperature oxidation micro-heat accurate determination method based on phase change reference as claimed in claim 1, wherein the raw coal sample is 1-2 g, the organic phase change material is 1-8 g, and the ratio of the raw coal sample to the organic phase change material is 1: 1. 1: 2. 1: 4, one of the compositions; the selection method of the dosage ratio comprises the following steps: when the maximum value of the temperature interval needing to be measured is less than 85 ℃, the usage ratio of the raw coal sample to the organic phase change material is 1: 1; when the maximum value of the temperature interval needing to be measured is positioned at (85, T) cpt ]At the time of DEG C, the dosage ratio of the raw coal sample to the organic phase-change material is 1: 2; when the maximum value of the temperature interval needing to be measured is more than T cpt At the time of DEG C, the dosage ratio of the raw coal sample to the organic phase-change material is 1: 4, said T cpt The cross point temperature value of the raw coal sample is shown.
6. The method for accurately measuring the coal low-temperature oxidation micro heat based on the phase change reference according to claim 1, wherein the gas flow rates of the nitrogen and the oxygen are kept consistent and are any value of 50-100 mL/min, and the gas flow rate is controlled by a mass flow meter.
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