JP2003215078A - Method of testing heat build-up of coal - Google Patents

Method of testing heat build-up of coal

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Publication number
JP2003215078A
JP2003215078A JP2002014399A JP2002014399A JP2003215078A JP 2003215078 A JP2003215078 A JP 2003215078A JP 2002014399 A JP2002014399 A JP 2002014399A JP 2002014399 A JP2002014399 A JP 2002014399A JP 2003215078 A JP2003215078 A JP 2003215078A
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JP
Japan
Prior art keywords
temperature
coal
container
sample
test
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2002014399A
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Japanese (ja)
Other versions
JP3939989B2 (en
Inventor
Kanji Matsudaira
寛司 松平
Masaru Nishimura
勝 西村
Masahito Fukuda
雅人 福田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kansai Coke and Chemicals Co Ltd
Original Assignee
Kansai Coke and Chemicals Co Ltd
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Priority to JP2002014399A priority Critical patent/JP3939989B2/en
Publication of JP2003215078A publication Critical patent/JP2003215078A/en
Application granted granted Critical
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method of testing heat build-up of coal by which the degree of temperature rise in each brand of coal layer can be evaluated in a short time. <P>SOLUTION: The temperature in a testing device system is held at a temperature T<SB>1</SB>corresponding to a test starting temperature T by preheating a heating machine (15) housing an insulation container (14). On the other hand, the surface moisture and holding moisture of a coal sample pulverized to a prescribed grain size or smaller are removed by drying the sample at a temperature T' under a vacuum by using a vacuum dryer (19) equipped with an evacuating means and a heating means while the sample is packed in an opened container (16). Subsequently, the temperature of the coal sample packed in the container (16) is adjusted to another temperature T<SB>2</SB>corresponding to the test starting temperature T. Then the sample is shifted to the insulation container (14) housed in the heating machine (15) and the atmosphere in the container (14) is replaced with an inert gas and, at the same time, the temperature of the sample is adjusted to the test starting temperature T. Thereafter, an oxidizing gas is supplied to the container (14) and the temperature or temperature change of the coal sample in the container (14) is tracked by means of a temperature data collecting device (12). <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、石炭の酸化による
石炭層内の温度上昇の程度を、銘柄ごとに短時間で評価
する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for evaluating the degree of temperature rise in a coal seam due to oxidation of coal for each brand in a short time.

【0002】[0002]

【従来の技術】〈石炭層の蓄熱と自然発火〉コークス製
造現場においては、ヤード(貯炭場)に各種銘柄の石炭
を野積みしておき、コークス製造に際しては、所定の配
合処方に従って必要な銘柄を選択し、コークス炉に装入
して乾留を行う。野積みされた石炭は、使用に供される
までに長期間貯蔵されることになるが、採掘後の石炭は
貯炭中に空気中の酸素により酸化されて発熱し、場合に
よっては発火に至ることもあるので、防災上の観点か
ら、銘柄間の発熱性の差を管理把握しておくことが必要
となる。ヤードに野積みされた石炭に限らず、空気と接
触する石炭層は、蓄熱、発火のおそれがある。
2. Description of the Related Art <Coal Layer Heat Storage and Spontaneous Ignition> At the coke manufacturing site, coal of various brands is piled up in the yard (coal storage yard). Is selected and charged into a coke oven for dry distillation. The coal loaded in the open field will be stored for a long time before it is used.However, the coal after mining will be oxidized by oxygen in the air during the coal storage to generate heat, which may lead to ignition. Therefore, from the perspective of disaster prevention, it is necessary to manage and understand the difference in heat generation between brands. Not only coal piled in the yard, but also coal layers that come into contact with air may accumulate heat or ignite.

【0003】「日本鉱業会誌/85 969(’69−
1)」(1969年)の15〜20頁には、「石炭の自
然発火初期現象と空気中の酸素濃度との関係」と題する
論文が掲載されており、(a) 酸素濃度と自然発火性との
関係、(b) 酸素消費量、CO 2 、CO発生量、CO/O
2 、CO2 /O2 と酸素濃度との関係、(c) 自然発火所
要日数と酸素濃度との関係などを調べている。
"Journal of the Japan Mining Industry / 85 969 ('69-
1) "(1969), pages 15-20," Coal
Relationship between the initial phenomenon of spontaneous ignition and oxygen concentration in air "
The paper is published, and (a) oxygen concentration and spontaneous combustion
Relationship, (b) oxygen consumption, CO 2 , CO generation rate, CO / O
2 , CO2 / O2 And the oxygen concentration, (c) spontaneous combustion
We are investigating the relationship between required days and oxygen concentration.

【0004】「技ダイ、昭和57年12月号」の13〜
22頁には、「貯炭の酸化昇温−石炭の自然発火に関す
る研究(その1)−」と題する論文が掲載されており、
酸化と蓄熱に関する現象としては、堆積圧密作用、酸化
発熱作用、熱伝導作用、通風作用、水分の蒸発と凝縮作
用、大気環境、石炭の性質(石炭化度、微細組織構造
等)が関係すること、酸化反応熱測定装置についての実
験(試料をマホービンに装入して、酸素ガスを通気した
ときの上昇温度の測定などにつき、基礎的な研究が示さ
れている。
13-in "Die, December 1982 issue"
On page 22, a paper entitled "Oxidation and temperature rise of coal storage-Study on spontaneous combustion of coal (1)-" is published.
Phenomena related to oxidation and heat storage are related to sedimentation consolidation, oxidation heat generation, heat conduction, ventilation, moisture evaporation and condensation, atmospheric environment, coal properties (coalification degree, microstructure, etc.) , Experiments on oxidation reaction heat measurement device (basic studies have been shown on measurement of elevated temperature when a sample is charged into a mahobin and oxygen gas is aerated.

【0005】「四国総合研究所研究期報 第54号」
(1989年)の48〜65頁には、「サイロ内に貯蔵
した石炭の昇温特性の評価」と題する論文が掲載されて
おり、石炭自然発火装置を用いる実験的手法や、コンピ
ュータを活用して数値計算を行うシミュレーション手法
により、石炭の昇温特性を評価している。
"Shikoku Research Institute Research Bulletin No. 54"
(1989), pp. 48-65, a paper entitled "Evaluation of temperature rising characteristics of coal stored in silo" is published, and experimental method using coal spontaneous ignition device and computer are utilized. The temperature rise characteristics of coal are evaluated by a simulation method in which numerical calculations are performed.

【0006】「日本エネルギー学会誌、第75巻第11
号(1996)」の963〜969頁には、「石炭の貯
蔵およびハンドリング技術」と題する総説が掲載されて
おり、その964〜965頁の「自然発熱」の項の図3
および図4には、自然発熱性測定装置と結果についての
例が示されている。
[Journal of the Japan Institute of Energy, Vol. 75, No. 11]
No. (1996), pages 963-969, provides a review entitled "Coal Storage and Handling Technology", which is illustrated in Figure 3 of the section "Spontaneous Heat Generation" on pages 964-965.
And FIG. 4 shows an example of the spontaneous heat generation measuring device and the result.

【0007】〈自然発火性の評価〉特開平11−344
456号公報には、微粉炭を充填する空間を有するケー
スと、該ケースの下端側に装着された加熱装置と、これ
らを収納する密閉容器と、該密閉容器内の雰囲気を加熱
するヒータとを具備した微粉炭の自然発火性評価装置が
示されている。
<Evaluation of spontaneous combustion> JP-A-11-344
Japanese Patent No. 456 discloses a case having a space filled with pulverized coal, a heating device mounted on the lower end side of the case, a closed container for housing these, and a heater for heating an atmosphere in the closed container. The provided pulverized coal self-ignitability evaluation apparatus is shown.

【0008】市販の自然発火評価装置(たとえば、株式
会社島津製作所製の「島津自然発火試験装置SIT−
2」)を用いて、発火性を測定することも可能である。
A commercially available spontaneous ignition evaluation device (for example, "Shimadzu spontaneous ignition test device SIT-manufactured by Shimadzu Corporation"
2 ”) can also be used to measure the ignitability.

【0009】「日立造船技報、第43巻第1号」(昭和
57年3月)」の13〜19頁には、市販の自然発火試
験装置(株式会社島津製作所製の「島津自然発火試験装
置SIT−1」)を用い、41種の石炭を対象に20〜
200℃の温度域での昇温特性について実験検討した結
果についての報告があり、酸素濃度の影響、石炭の粒径
の影響、炭種の影響、石炭の物性(O/C比、揮発分)
との関係などが示されている。
"Hitachi Zosen Giho, Vol. 43, No. 1," (March 1982), pp. 13 to 19 show commercially available spontaneous ignition test equipment ("Shimadzu spontaneous ignition test manufactured by Shimadzu Corporation"). Device SIT-1 ") and targeting 41 kinds of coal
There are reports on the results of experimental examinations regarding the temperature rise characteristics in the temperature range of 200 ° C., the influence of oxygen concentration, the influence of coal particle size, the influence of coal species, the physical properties of coal (O / C ratio, volatile matter).
The relationship with is shown.

【0010】[0010]

【発明が解決しようとする課題】石炭の酸化による石炭
層内の温度上昇の程度を銘柄ごとに短時間で評価する方
法としては、 ・石炭を5mm以下に粉砕して石炭と酸素との反応表面を
増加させることにより、温度上昇を速くする方法、 ・加速条件で温度上昇の程度を評価するために、石炭試
料を所定の温度にまで予熱しておく方法 が実際的であると考えられる。
As a method for evaluating the degree of temperature rise in the coal seam due to oxidation of coal for each brand in a short time, the reaction surface of coal and oxygen is obtained by crushing coal to 5 mm or less. It is considered that a method of increasing the temperature to increase the temperature rise, and a method of preheating the coal sample to a predetermined temperature in order to evaluate the degree of the temperature increase under acceleration conditions are practical.

【0011】しかしながら、石炭の銘柄によっては、石
炭の表面および付着水分のみならず、石炭に包蔵された
水分を有するものもあり、乾燥機で乾燥させる程度の条
件では、そのような石炭に包蔵された水分を取り除くこ
とは困難である。従って、石炭の発熱性の試験を行う場
合、この包蔵された水分が残ったままで評価すれば、温
度を上昇させるためのエネルギーが水分を温度上昇させ
る熱エネルギーにも使用されることで、温度上昇速度の
程度を短時間で評価する妨げとなる。
However, some brands of coal have not only the surface and the moisture content of the coal but also the moisture contained in the coal. Under the condition that they are dried by a dryer, they are enclosed in such coal. It is difficult to remove water. Therefore, when testing the exothermicity of coal, if the evaluation is made with the water contained therein remaining, the energy for raising the temperature is also used for the thermal energy for raising the temperature of the moisture, thereby increasing the temperature. This hinders the evaluation of the speed level in a short time.

【0012】〈発明の目的〉本発明は、このような背景
下において、各銘柄の石炭層内温度上昇の程度を短時間
で評価することのできる石炭の発熱性の試験方法を提供
することを目的とするものである。
<Object of the Invention> [0012] Under such a background, the present invention provides a test method for exothermicity of coal capable of evaluating the degree of temperature rise in the coal seam of each brand in a short time. It is intended.

【0013】[0013]

【課題を解決するための手段】本発明の石炭の発熱性の
試験方法は、石炭の酸化による石炭層内の温度上昇の程
度を、石炭の銘柄ごとに評価する方法であって、(イ)
ガス導入チューブ(9) およびガス排出チューブ(10)を付
設した断熱容器(14)を収容してある加熱機(15)を予熱し
て、試験装置系内の温度を試験開始温度Tに見合う温度
1 に保持しておくこと、(ロ)一方、所定の粒度以下
に粉砕した石炭試料を、開放容器(16)に装填した状態
で、真空手段と加熱手段とを備えた真空乾燥機(19)を用
いて真空下に温度T' で乾燥することにより、その石炭
試料の表面水分および包蔵水分を除去し、ついでその開
放容器(16)内の石炭試料を前記の試験開始温度Tに見合
う温度T2 にまで温度調節しておくこと、(ハ)水分が
除去されかつ温度調節された前記の石炭試料を、前記加
熱機(15)内の断熱容器(14)に移し替え、その断熱容器(1
4)内の雰囲気を不活性ガスに置換すると共に、試験開始
温度Tに温度調節してから、その断熱容器(14)内に酸化
性ガスを供給し、断熱容器(14)内の石炭試料の温度また
は温度変化を温度データ収集装置(12)により追跡するこ
とを特徴とするものである。
The method for testing the exothermicity of coal of the present invention is a method for evaluating the degree of temperature rise in a coal seam due to oxidation of coal for each brand of coal.
Preheating the heater (15) that houses the heat-insulating container (14) with the gas introduction tube (9) and the gas discharge tube (10), and adjusts the temperature in the test equipment system to a temperature that matches the test start temperature T. Hold at T 1 , (b) On the other hand, a vacuum dryer (19) equipped with a vacuum means and a heating means in a state where a coal sample crushed to a predetermined particle size or less is loaded in the open container (16). ) Is used to remove surface moisture and entrapped moisture of the coal sample under vacuum at a temperature T ′, and then the coal sample in the open container (16) is heated to a temperature corresponding to the test start temperature T. that it temperature adjusted until the T 2, (c) the coal sample moisture has been to and temperature control removed, transferred to a thermally insulated container (14) within said heater (15), the heat insulating container ( 1
The atmosphere in 4) is replaced with an inert gas, and the temperature is adjusted to the test start temperature T, and then an oxidizing gas is supplied into the heat insulating container (14) to remove the coal sample in the heat insulating container (14). It is characterized in that the temperature or temperature change is tracked by a temperature data collecting device (12).

【0014】[0014]

【発明の実施の形態】以下本発明を詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below.

【0015】本発明の試験方法にあっては、石炭の酸化
による石炭層内の温度上昇の程度を、石炭の銘柄ごとに
評価する。後述の実施例のように、貯炭中の石炭の蓄熱
性は銘柄によって大きく相違するので、各種銘柄につき
評価を行っておくことは、ヤードにおける野積み石炭
(銘柄ごとに山にしてある)の管理上有益である。
In the test method of the present invention, the degree of temperature rise in the coal seam due to oxidation of coal is evaluated for each brand of coal. As in the examples described below, the heat storage of coal in coal stocks varies greatly depending on the brand, so it is important to evaluate each type of brand when managing open-load coal in the yard (pile for each brand). Above is beneficial.

【0016】〈要件(イ)〉本発明においては、ガス導
入チューブ(9) およびガス排出チューブ(10)を付設した
断熱容器(14)を収容してある加熱機(15)を予熱して、試
験装置系内の温度を試験開始温度Tに見合う温度T1
保持しておく。
<Requirement (a)> In the present invention, a heater (15) containing a heat insulating container (14) provided with a gas introduction tube (9) and a gas discharge tube (10) is preheated, The temperature in the test apparatus system is kept at a temperature T 1 that matches the test starting temperature T.

【0017】ガス導入チューブ(9) は、窒素のような不
活性ガス、空気のような酸化性ガスを導入するためのも
のであるが、たとえば窒素用切替バルブ(1) 、空気用切
替バルブ(2) からの配管を合して、ガス供給共通チュー
ブとし、そのガス供給共通チューブに加熱用ヒーター
(3) を付設すると共に、それを断熱容器(14)内に導くよ
うに配管することが好ましい。
The gas introduction tube (9) is for introducing an inert gas such as nitrogen and an oxidizing gas such as air. For example, a nitrogen switching valve (1) and an air switching valve ( Combine the pipes from 2) to make a common tube for gas supply, and heat the heater for heating to the common tube for gas supply.
It is preferable to attach (3) and pipe so as to lead it into the heat insulating container (14).

【0018】ガス排出チューブ(10)は、断熱容器(14)内
に供給した不活性ガスや酸化性ガスを系外に排出するた
めの配管である。
The gas discharge tube (10) is a pipe for discharging the inert gas or oxidizing gas supplied into the heat insulating container (14) to the outside of the system.

【0019】加熱機(15)としては、加熱手段とファンと
を備えた通常の乾燥機を用いることができる。他のタイ
プの加熱機を用いることも可能である。
As the heater (15), an ordinary dryer equipped with a heating means and a fan can be used. It is also possible to use other types of heaters.

【0020】断熱容器(14)としては、断熱瓶のような断
熱性を有する容器が用いられる。その断熱容器(14)に
は、たとえば、ガス導入チューブ(9) 、ガス排出チュー
ブ(10)、石炭層内温度測定用手段(11)を挿通した密栓(1
3)を装着できるようにしておく。石炭層内温度測定用手
段(11)としては、たとえば熱電対を用いることができ
る。
As the heat insulating container (14), a container having a heat insulating property such as a heat insulating bottle is used. In the heat insulating container (14), for example, a gas inlet tube (9), a gas exhaust tube (10), and a tight stopper (1
3) Be prepared to wear. As the means (11) for measuring the temperature in the coal layer, for example, a thermocouple can be used.

【0021】そして、これらのガス導入チューブ(9) 、
ガス排出チューブ(10)、石炭層内温度測定用手段(11)、
密栓(13)、断熱容器(14)を含めて、加熱機(15)を予熱し
て、試験装置系内の温度を試験開始温度Tに見合う温度
1 に保持する。
And, these gas introduction tubes (9),
Gas discharge tube (10), means (11) for measuring the temperature in the coal bed,
The heater (15) including the tight stopper (13) and the heat insulating container (14) is preheated to maintain the temperature in the test apparatus system at the temperature T 1 corresponding to the test start temperature T.

【0022】〈要件(ロ)〉一方、本発明においては、
所定の粒度以下に粉砕した石炭試料を、開放容器(16)に
装填した状態で、真空手段と加熱手段とを備えた真空乾
燥機(19)を用いて真空下に温度T' で乾燥することによ
り、その石炭試料の表面水分および包蔵水分を除去し、
ついでその開放容器(16)内の石炭試料を前記の試験開始
温度Tに見合う温度T2 にまで温度調節しておく。
<Requirement (b)> On the other hand, in the present invention,
Drying a coal sample crushed to a predetermined particle size or less in an open container (16) under vacuum using a vacuum dryer (19) equipped with a vacuum means and a heating means at a temperature T '. Removes surface moisture and contained moisture of the coal sample,
Then, the temperature of the coal sample in the open container (16) is adjusted to a temperature T 2 corresponding to the test starting temperature T.

【0023】石炭試料としては、石炭を銘柄ごとに所定
の粒度以下に粉砕したものを用いる。所定の粒度とは、
石炭と酸化性ガスとの反応表面を増加させるために、た
とえば10mm篩下、殊に5mm篩下のものが適当である。
なお、試料中の微粉部分をカットする必要はないが、微
粉がガス導入チューブ(9) に詰まってガスの流れに支障
を来たすおそれがあるときは、試料粒子の最小径がその
ガス導入チューブ(9)の内径よりも小さくならないよう
にするなどして、試料粒子がガス導入チューブ(9) に詰
まらないような工夫を講じることができる(たとえば、
ガス導入チューブ(9) の内径が3mmであれば、試料粒子
を3mm篩上とするというように)。
As the coal sample, one obtained by crushing coal into a grain size not larger than a predetermined grain size is used. What is a predetermined grain size?
In order to increase the reaction surface between the coal and the oxidizing gas, for example, 10 mm sieve, especially 5 mm sieve is suitable.
Note that it is not necessary to cut the fine powder part in the sample, but if there is a risk that the fine powder will clog the gas introduction tube (9) and interfere with the gas flow, the minimum diameter of the sample particles is It is possible to take measures such that the sample particles do not get stuck in the gas introduction tube (9) by making it smaller than the inner diameter of 9) (for example,
If the inner diameter of the gas introduction tube (9) is 3 mm, the sample particles should be on the 3 mm sieve).

【0024】開放容器(16)としては、たとえば硬質ガラ
ス製パイプのようなものが用いられる。容器を開放容器
とするのは、石炭試料の表面水分および包蔵水分の除去
路を確保するためである。
As the open container (16), for example, a hard glass pipe is used. The reason why the container is an open container is to secure a removal path for surface moisture and contained moisture of the coal sample.

【0025】真空乾燥機(19)は、真空手段と加熱手段と
を備えた乾燥機である。加熱だけでは石炭試料の表面水
分は除去できても包蔵水分を除去することが難しいた
め、真空手段を併用することが必要である。
The vacuum dryer (19) is a dryer equipped with a vacuum means and a heating means. Even if the surface water of the coal sample can be removed only by heating, it is difficult to remove the contained water, so it is necessary to use a vacuum means together.

【0026】真空乾燥機(19)による真空度は、たとえば
系内が−700mmHg以下、殊に−750mmHg以下となる
ように設定する(なお、1mmHgは国際単位で表わせば
1.3×102 Paである)。真空下での乾燥温度T' は、真
空下において石炭試料の全水分を 0.5%以下、好ましく
は 0.1%以下にまで低減することができる温度、たとえ
ば100〜107℃程度、殊に100〜102℃程度に
設定することが望ましい。
The degree of vacuum by the vacuum dryer (19) is set, for example, so that the inside of the system is -700 mmHg or less, particularly -750 mmHg or less (1 mmHg is expressed in international units.
It is 1.3 × 10 2 Pa). The drying temperature T'in vacuum is a temperature at which the total water content of the coal sample can be reduced to 0.5% or less, preferably 0.1% or less under vacuum, for example, about 100 to 107 ° C, particularly 100 to 102 ° C. It is desirable to set it to a degree.

【0027】石炭試料の表面水分および包蔵水分を除去
した後は、開放容器(16)内の石炭試料を、先に述べた試
験開始温度Tに見合う温度T2 にまで温度調節してお
く。
After the surface moisture and the contained moisture of the coal sample are removed, the temperature of the coal sample in the open container (16) is adjusted to the temperature T 2 corresponding to the test starting temperature T described above.

【0028】〈要件(ハ)〉上記で準備が整ったので、
さらに本発明においては、水分が除去されかつ温度調節
された前記の石炭試料を、前記加熱機(15)内の断熱容器
(14)に移し替える。そして、その断熱容器(14)内の雰囲
気を不活性ガスに置換すると共に、試験開始温度Tに温
度調節してから、その断熱容器(14)内に酸化性ガスを供
給し、断熱容器(14)内の石炭試料の温度または温度変化
を温度データ収集装置(12)により追跡する。
<Requirement (C)> Since preparation is completed as described above,
Furthermore, in the present invention, the coal sample from which water has been removed and whose temperature has been adjusted is a heat insulating container in the heating machine (15).
Transfer to (14). Then, while replacing the atmosphere in the heat insulating container (14) with an inert gas and adjusting the temperature to the test start temperature T, an oxidizing gas is supplied into the heat insulating container (14) to The temperature or temperature change of the coal sample in () is tracked by the temperature data collector (12).

【0029】不活性ガスとしてはたとえば窒素ガスが用
いられ、酸化性ガスとしてはたとえば空気が用いられ
る。不活性ガス、酸化性ガスは、加熱機(15)内の断熱容
器(14)に供給する前に、加熱用ヒーター(3) で試験開始
温度Tに見合う温度にまで加熱しておくことが好まし
い。
Nitrogen gas is used as the inert gas, and air is used as the oxidizing gas. The inert gas and the oxidizing gas are preferably heated by the heating heater (3) to a temperature corresponding to the test starting temperature T before being supplied to the heat insulating container (14) in the heater (15). .

【0030】温度データ収集装置(12)においては、石炭
試料の温度を測定するか、石炭試料の試験開始温度Tか
らの温度差を測定する。
In the temperature data collecting device (12), the temperature of the coal sample is measured or the temperature difference from the test start temperature T of the coal sample is measured.

【0031】上述の試験開始温度Tは、50〜70℃の
範囲内の所定の温度(たとえば60℃)が適当である。
温度T1 および温度T2 は、実質的に試験開始温度Tと
同一にすることが望ましい。
As the above-mentioned test starting temperature T, a predetermined temperature within the range of 50 to 70 ° C. (eg 60 ° C.) is suitable.
It is desirable that the temperatures T 1 and T 2 be substantially the same as the test start temperature T.

【0032】〈その他〉開放容器(16)と断熱容器(14)と
は、各1セットによるシングルタイプとしてもよいが、
それらを複数セット設けることによってマルチシステム
とすることにより、試験を実施することもできる。
<Others> The open container (16) and the heat insulating container (14) may be of a single type each including one set,
It is also possible to carry out the test by providing them as a multi-system by providing a plurality of sets.

【0033】[0033]

【実施例】次に実施例をあげて本発明をさらに説明す
る。
EXAMPLES The present invention will be further described with reference to examples.

【0034】〈試験装置〉図1は、本発明の石炭の発熱
性の試験方法を実施するために用いる装置の一例を示し
た説明図である。
<Testing Apparatus> FIG. 1 is an explanatory view showing an example of an apparatus used for carrying out the method for testing the exothermicity of coal of the present invention.

【0035】(1) は窒素用切替バルブ、(2) は空気用切
替バルブ、(3) は加熱用ヒーター、(4) は制御信号線、
(5) はガス供給共通チューブ、(6) はチューブジョイン
ト、(7) は制御ユニットである。これらは、加熱機の外
部に配置してある。
(1) is a switching valve for nitrogen, (2) is a switching valve for air, (3) is a heater for heating, (4) is a control signal line,
(5) is a gas supply common tube, (6) is a tube joint, and (7) is a control unit. These are arranged outside the heater.

【0036】(8) は供給ガスの温度制御手段(制御用熱
電対)、(9) はガス導入チューブ(ガス供給共通チュー
ブ)、(10)はガス排出チューブ、(11)は石炭層内温度測
定用手段(熱電対)、(13)は密栓、(14)は断熱容器(断
熱瓶)である。これらは、加熱機(15)内に装備してある
(ただし、(8), (9), (10), (11)は、系外にも一部が出
ている)。(12)は温度データ収集装置である。
(8) is a temperature control means for the supply gas (control thermocouple), (9) is a gas introduction tube (gas supply common tube), (10) is a gas discharge tube, and (11) is a temperature in the coal bed. Measuring means (thermocouple), (13) is a sealed stopper, and (14) is a heat insulating container (heat insulating bottle). These are installed in the heater (15) (however, (8), (9), (10), (11) are partially out of the system). (12) is a temperature data collecting device.

【0037】(16)は開放容器(硬質ガラス製パイプ)、
(17)は水トラップ装置、(18)は真空ポンプ、(19)は真空
乾燥機である。開放容器(16)は、真空乾燥機(19)内に収
容してある。
(16) is an open container (a pipe made of hard glass),
(17) is a water trap device, (18) is a vacuum pump, and (19) is a vacuum dryer. The open container (16) is housed in the vacuum dryer (19).

【0038】〈測定手順〉測定手順は次の通りである。 1.5mm未満(5mm篩下)で3mm以上(3mm篩上)の大
きさに粉砕した各銘柄の石炭試料の約340g(乾燥基
準重量)を、内径40mmの開放容器(硬質ガラス製パイ
プ)(16)に均一に装填する。 2.真空ポンプ(18)により、真空乾燥機(19)内の圧力を
10mmHg(−750mmHg)まで負圧としながら、真空乾
燥機(19)内の温度をT' (100℃)まで上昇させる。 3.石炭試料の表面水分および包蔵水分を気化させ、水
トラップ装置(17)でその水分を捕獲、除去する。 4.上記操作を水トラップ装置(17)で捕獲する水分がな
くなるまで(石炭試料の全水分が 0.1%以下になるま
で)継続し、その後、真空乾燥機(19)を試験開始温度T
(60℃)に設定し、試料温度T2 をTに調節する。 5.上記4の真空乾燥機(19)を試験開始温度T(60
℃)に設定するタイミングと並行して、供給ガスの温度
制御手段(制御用熱電対)(8) 、ガス導入チューブ(ガ
ス供給共通チューブ)(9) 、ガス排出チューブ(10)、石
炭層内温度測定用手段(熱電対)(11)、密栓(13)および
断熱容器(断熱瓶)(14)を、加熱機(15)を用いて予熱
し、試験装置系内の温度T1 を試験開始温度T(60
℃)に保持する。 6.試料温度が試験開始温度Tに到達したところで、上
記4で準備した開放容器(硬質ガラス製パイプ)(16)を
真空乾燥機(19)から取り出して、その内部の試料を、加
熱機(15)から取り出した断熱容器(断熱瓶)(14)内に素
早く装填し、その断熱容器(断熱瓶)(14)に、供給ガス
の温度制御手段(制御用熱電対)(8) 、ガス導入チュー
ブ(ガス供給共通チューブ)(9) 、ガス排出チューブ(1
0)および石炭層内温度測定用手段(熱電対)(11)が挿通
された密栓(13)をする。 7.供給ガスの温度制御手段(制御用熱電対)(8) を制
御ユニット(7) に、石炭層内温度測定用手段(熱電対)
(11)を温度データ収集装置(12)に、ガス導入チューブ
(ガス供給共通チューブ)(9) をチューブジョイント
(6) に、それぞれつなぎ込む。 8.窒素用切替バルブ(1) を開き、窒素を供給する。こ
のとき、供給ガス温度が供給ガスの温度制御手段(制御
用熱電対)(8) で60℃になるように制御ユニット(7)
で調整する。 9.石炭層内温度測定用手段(熱電対)(11)の表示が試
験開始温度Tの60℃になった時点で窒素用切替バルブ
(1) を閉じ、空気用切替バルブ(2) を開いて酸化用の空
気を10〜100ml/minの範囲の速度(この実施例では
25ml/min)で供給する。なお、供給ガス温度が供給ガ
スの温度制御手段(制御用熱電対)(8)で60℃になる
ように制御ユニット(7) で調整する。 10.石炭を酸化させ始めた後は、加熱機(15)および供
給ガス温度は、一定の値(60℃)に保持する。 11.酸化用の空気を供給している間、石炭層内の温度
上昇の程度(温度または温度変化)を温度データ収集装
置(12)を用いて記録する。 12.約3時間酸化用の空気を導入すれば、温度上昇の
程度が確認できるので、その後、試験を完了する。
<Measurement Procedure> The measurement procedure is as follows. Approximately 340 g (dry basis weight) of each brand of coal sample crushed to a size of less than 1.5 mm (under 5 mm sieve) and over 3 mm (over 3 mm sieve), open container (hard glass pipe) with an inner diameter of 40 mm ( Evenly load 16). 2. The vacuum pump (18) raises the temperature in the vacuum dryer (19) to T ′ (100 ° C.) while keeping the pressure in the vacuum dryer (19) negative at 10 mmHg (−750 mmHg). 3. The surface water and the contained water of the coal sample are vaporized, and the water is trapped and removed by the water trap device (17). 4. The above operation is continued until there is no more water trapped in the water trap device (17) (until the total water content of the coal sample is 0.1% or less), and then the vacuum dryer (19) is set to the test start temperature T.
(60 ° C.) and the sample temperature T 2 is adjusted to T. 5. Test the vacuum dryer (19) of the above 4 at the test starting temperature T (60
In parallel with the timing of setting to (° C), the temperature control means of the supply gas (thermocouple for control) (8), gas introduction tube (gas supply common tube) (9), gas discharge tube (10), inside the coal bed Temperature measuring means (thermocouple) (11), sealed stopper (13) and heat insulation container (heat insulation bottle) (14) are preheated by using a heater (15), and the temperature T 1 in the test equipment system is tested. Temperature T (60
C)). 6. When the sample temperature reaches the test start temperature T, the open container (hard glass pipe) (16) prepared in 4 above is taken out of the vacuum dryer (19), and the sample inside is heated by a heater (15). The heat-insulated container (heat-insulated bottle) (14) taken out from the above was quickly loaded, and the heat-insulated container (heat-insulated bottle) (14) was supplied with the temperature control means (control thermocouple) (8) for the supply gas and the gas introduction tube ( Gas supply common tube) (9), gas discharge tube (1
0) and the means (thermocouple) for measuring the temperature in the coal bed (11) are inserted into the cap (13). 7. Supply gas temperature control means (control thermocouple) (8) to control unit (7), coal bed temperature measurement means (thermocouple)
(11) to the temperature data collector (12) and the gas inlet tube (common gas supply tube) (9) to the tube joint
Connect to (6) respectively. 8. Open the nitrogen switching valve (1) and supply nitrogen. At this time, the control unit (7) controls the temperature of the supply gas to 60 ° C. by the temperature control means (control thermocouple) (8) for the supply gas.
Adjust with. 9. Switching valve for nitrogen when the display of the means (thermocouple) for measuring the temperature in the coal bed (11) reaches the test start temperature T of 60 ° C.
(1) is closed, the air switching valve (2) is opened, and oxidizing air is supplied at a rate in the range of 10 to 100 ml / min (25 ml / min in this embodiment). The temperature of the supply gas is adjusted by the control unit (7) so that the temperature of the supply gas is 60 ° C. by the temperature control means (control thermocouple) (8). 10. After starting to oxidize the coal, the heater (15) and the feed gas temperature are kept constant (60 ° C). 11. While supplying the oxidizing air, the degree of temperature rise (temperature or temperature change) in the coal seam is recorded using the temperature data collector (12). 12. If air for oxidation is introduced for about 3 hours, the degree of temperature rise can be confirmed, and then the test is completed.

【0039】〈測定結果〉上述の測定手順に従い、産地
や全水分の異なる4銘柄の石炭について評価試験を行っ
た。結果を図2に示す。図2において、横軸は「空気用
切替バルブ(2) を開き酸化用の空気を供給開始してから
の経過時間」、縦軸は「温度データ収集装置(12)で1秒
間隔で収集した石炭層内の温度(熱電対(11))」であ
る。また、図2からの所定時間(200分、400分、
600分、660分)経過後の石炭層温度の読み取り値
を表1に示す。
<Measurement Results> In accordance with the above-mentioned measurement procedure, evaluation tests were carried out on four brands of coal having different origins and total water contents. The results are shown in Figure 2. In FIG. 2, the horizontal axis is “the elapsed time since the air switching valve (2) was opened and the supply of the oxidizing air was started”, and the vertical axis was the “temperature data collecting device (12) that collected data at 1 second intervals. The temperature in the coal seam (thermocouple (11)) ". In addition, the predetermined time (200 minutes, 400 minutes,
Table 1 shows the readings of the temperature of the coal bed after the elapse of 600 minutes and 660 minutes.

【0040】[0040]

【表1】 石炭の 全水分 石炭層温度(℃) 銘柄 (%) 初期設定 200分後 400分後 600分後 660分後 Coal A 24.6 60 73 87 95 98 Coal B 9.0 60 65 66 66 66 Coal C 9.0 60 61 62 62 62 Coal D 8.0 60 61 62 62 62 [Table 1]      Total moisture of coalCoal bed temperature (℃)   Brand (%) Initial setting 200 minutes later 400 minutes later 600 minutes later 660 minutes later   Coal A 24.6 60 73 87 95 98   Coal B 9.0 60 65 66 66 66   Coal C 9.0 60 61 62 62 62   Coal D 8.0 60 61 62 62 62

【0041】図2から、試験に供した4銘柄の中では、
Coal Aが一定温度状態(この場合60℃)に保った系か
らの温度上昇が著しく、発熱性の評価としては、「Coal
A<<Coal C<Coal B≦Coal D」の順に発熱しやすいと
いう結果となる。従って、Coal Aの銘柄の石炭を貯蔵す
るときは、その銘柄が発熱しやすいということに留意し
て、貯炭管理を行うべきであることがわかる。また、図
2から、最初の3時間弱で、各銘柄についての発熱性の
大小の傾向を知ることができることがわかる。
From FIG. 2, among the four brands used in the test,
The temperature rise from the system in which Coal A was kept at a constant temperature (60 ° C in this case) was remarkable, and the evaluation of exothermicity
The result is that heat is easily generated in the order of A << Coal C <Coal B ≦ Coal D. Therefore, when storing Coal A brand coal, it should be noted that coal storage management should be carried out while keeping in mind that the brand tends to generate heat. Further, it can be seen from FIG. 2 that it is possible to know the tendency of exothermicity of each brand in the first 3 hours or less.

【0042】[0042]

【発明の効果】本発明の試験方法によれば、各銘柄の石
炭の温度上昇の程度を短時間で評価することができる。
従って、石炭をヤード等に野積みしたときに自然発火を
起こす度合いを知ることができ、安全な貯炭管理が可能
になる。
According to the test method of the present invention, the degree of temperature rise of each brand of coal can be evaluated in a short time.
Therefore, it is possible to know the degree to which spontaneous combustion occurs when coal is loaded in the yard, etc., and safe coal stock management becomes possible.

【0043】また、試験中に石炭層内の急激な温度上昇
によって、石炭が発火した場合でも、空気用切替バルブ
(2) を閉じ、窒素用切替バルブ(1) を開くことで、窒息
消火できるので、すみやかな対応を図ることができる。
Further, even when coal is ignited by a rapid temperature rise in the coal bed during the test, the air switching valve is used.
By closing (2) and opening the nitrogen switching valve (1), it is possible to extinguish the suffocation, so a prompt response can be achieved.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の石炭の発熱性の試験方法を実施するた
めに用いる装置の一例を示した説明図である。
FIG. 1 is an explanatory view showing an example of an apparatus used for carrying out the method for testing the exothermicity of coal of the present invention.

【図2】実施例における4銘柄の石炭について評価試験
を行ったときの結果を示したグラフである。
FIG. 2 is a graph showing the results when an evaluation test was performed on four brands of coal in the examples.

【符号の説明】[Explanation of symbols]

(1) …窒素用切替バルブ、 (2) …空気用切替バルブ、 (3) …加熱用ヒーター、 (4) …制御信号線、 (5) …ガス供給共通チューブ、 (6) …チューブジョイント、 (7) …制御ユニット、 (8) …供給ガスの温度制御手段(制御用熱電対)、 (9) …ガス導入チューブ(ガス供給共通チューブ)、 (10)…ガス排出チューブ、 (11)…石炭層内温度測定用手段(熱電対)、 (12)…温度データ収集装置、 (13)…密栓、 (14)…断熱容器(断熱瓶)、 (15)…加熱機、 (16)…開放容器(硬質ガラス製パイプ)、 (17)…水トラップ装置、 (18)…真空ポンプ、 (19)…真空乾燥機 (1)… Switching valve for nitrogen, (2)… Air switching valve, (3)… Heating heater, (4)… Control signal line, (5)… Gas supply common tube, (6)… Tube joint, (7)… Control unit, (8) ... Supply gas temperature control means (control thermocouple), (9)… Gas introduction tube (gas supply common tube), (10)… Gas discharge tube, (11)… Means (thermocouple) for measuring the temperature in the coal bed, (12)… Temperature data collection device, (13) ... tight stopper, (14)… Insulation container (insulation bottle), (15)… Heating machine, (16)… Open container (hard glass pipe), (17) ... Water trap device, (18) ... vacuum pump, (19)… Vacuum dryer

───────────────────────────────────────────────────── フロントページの続き (72)発明者 福田 雅人 兵庫県尼崎市大浜町1丁目1番地 関西熱 化学株式会社研究開発センター内 Fターム(参考) 2G040 AA00 AB12 AB15 BA25 CA02 CB11 DA03 EA01 FA05    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Masato Fukuda             Kansai heat, 1-1 Ohama-cho, Amagasaki city, Hyogo prefecture             Chemical Research and Development Center F-term (reference) 2G040 AA00 AB12 AB15 BA25 CA02                       CB11 DA03 EA01 FA05

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】石炭の酸化による石炭層内の温度上昇の程
度を、石炭の銘柄ごとに評価する方法であって、 (イ)ガス導入チューブ(9) およびガス排出チューブ(1
0)を付設した断熱容器(14)を収容してある加熱機(15)を
予熱して、試験装置系内の温度を試験開始温度Tに見合
う温度T1 に保持しておくこと、 (ロ)一方、所定の粒度以下に粉砕した石炭試料を、開
放容器(16)に装填した状態で、真空手段と加熱手段とを
備えた真空乾燥機(19)を用いて真空下に温度T' で乾燥
することにより、その石炭試料の表面水分および包蔵水
分を除去し、ついでその開放容器(16)内の石炭試料を前
記の試験開始温度Tに見合う温度T2 にまで温度調節し
ておくこと、 (ハ)水分が除去されかつ温度調節された前記の石炭試
料を、前記加熱機(15)内の断熱容器(14)に移し替え、そ
の断熱容器(14)内の雰囲気を不活性ガスに置換すると共
に、試験開始温度Tに温度調節してから、その断熱容器
(14)内に酸化性ガスを供給し、断熱容器(14)内の石炭試
料の温度または温度変化を温度データ収集装置(12)によ
り追跡することを特徴とする石炭の発熱性の試験方法。
1. A method for evaluating the degree of temperature rise in a coal bed due to oxidation of coal for each brand of coal, comprising: (a) a gas introduction tube (9) and a gas discharge tube (1).
The heating device (15) accommodating the heat-insulating container (14) attached with (0) is preheated to keep the temperature in the test apparatus system at the temperature T 1 corresponding to the test start temperature T. ) On the other hand, a coal sample crushed to a predetermined particle size or less is loaded in an open container (16), and a vacuum dryer (19) equipped with a vacuum means and a heating means is used under vacuum at a temperature T ′. By drying, the surface water and the contained water of the coal sample are removed, and then the temperature of the coal sample in the open container (16) is adjusted to a temperature T 2 corresponding to the test start temperature T. (C) The coal sample from which water has been removed and whose temperature has been adjusted is transferred to the heat insulating container (14) in the heater (15), and the atmosphere in the heat insulating container (14) is replaced with an inert gas. In addition, after adjusting the temperature to the test start temperature T, the insulated container
A method for testing the exothermicity of coal, characterized in that an oxidizing gas is supplied into the (14) and the temperature or temperature change of the coal sample in the heat insulating container (14) is traced by a temperature data collecting device (12).
【請求項2】試験開始温度Tが50〜70℃の範囲内の
所定の温度であり、温度T1 および温度T2 が実質的に
試験開始温度Tであり、温度T' が真空下において石炭
試料の全水分を 0.5%以下にまで低減することができる
温度である請求項1記載の試験方法。
2. A test starting temperature T is a predetermined temperature within a range of 50 to 70 ° C., a temperature T 1 and a temperature T 2 are substantially a test starting temperature T, and a temperature T ′ is under vacuum. The test method according to claim 1, wherein the temperature is a temperature at which the total water content of the sample can be reduced to 0.5% or less.
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