JPH02263143A - Method of measuring volatile matter of coal - Google Patents
Method of measuring volatile matter of coalInfo
- Publication number
- JPH02263143A JPH02263143A JP8548889A JP8548889A JPH02263143A JP H02263143 A JPH02263143 A JP H02263143A JP 8548889 A JP8548889 A JP 8548889A JP 8548889 A JP8548889 A JP 8548889A JP H02263143 A JPH02263143 A JP H02263143A
- Authority
- JP
- Japan
- Prior art keywords
- coal
- heating
- temperature
- volatile matter
- value
- 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.)
- Pending
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Landscapes
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、コークス製造用原料石炭の品質評価として
重要な指標の一つである石炭の揮発分を簡易迅速にかつ
精度よく測定する方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a method for simply, quickly and accurately measuring the volatile content of coal, which is one of the important indicators for quality evaluation of raw material coal for coke production.
従来の技術
近年のコークス製造業におりる重要課題の一つは、品質
の安定化とコークス炉の効率的操業を同時に達成するこ
とである。このため、コークスの均一乾留と乾留熱量の
低減を目的とした燃焼管理の自動化の推進、石炭および
コークスの性状分析の自動化によるコークス炉装入炭の
品位調整の迅速化、安定化が進められている。BACKGROUND OF THE INVENTION One of the important issues facing the coke manufacturing industry in recent years is to simultaneously achieve stable quality and efficient coke oven operation. For this reason, progress has been made in promoting automation of combustion management for the purpose of uniform carbonization of coke and reducing the amount of heat of carbonization, and in speeding up and stabilizing the quality adjustment of coal charged in coke ovens by automating the property analysis of coal and coke. There is.
コークス製造用原料石炭の品質評価として重要な指標の
一つである揮発分の定量方法としては、JIS)188
12に規定された工業分析法がある。The method for quantifying volatile content, which is one of the important indicators for quality evaluation of coking coal for coke production, is JIS) 188.
There are industrial analytical methods specified in 12.
この方法は、試料的13を蓋付きのるつぼに入れ、空気
との接触を避(プるようにして900’Cの温度で7分
間加熱し、試料質量に対する加熱減量百分率を求め、こ
れから同時に定量した水分を減じて揮発分とする方法で
ある。In this method, sample 13 is placed in a crucible with a lid, heated at a temperature of 900'C for 7 minutes while avoiding contact with air, and the percentage loss on heating relative to the mass of the sample is determined, which is then simultaneously quantified. This method reduces the moisture content and converts it into volatile matter.
この外に、熱天秤による工業分析法も各種試みられてい
る。例えば、オタウエイ(Martyn Ottawa
y ; Fuel 、 61.p713−716198
2) 、Iルダ(John 、 P、 Elder
; [uel 、 62. p580−584゜198
3) 、線用ら(分析化学;34. 5.丁51−54
゜1985)の論文、特開昭61−19150号公報等
がある。In addition to this, various industrial analysis methods using thermobalances have also been attempted. For example, Martin Ottawa
y; Fuel, 61. p713-716198
2), John, P. Elder
; [uel, 62. p580-584゜198
3), Lines et al. (Analytical Chemistry; 34. 5. 51-54
1985), Japanese Patent Application Laid-open No. 19150/1983, etc.
これらの方法は、昇温時間、保持時間等で若干の差異が
あるが、基本的には次のような手順で実施される。Although these methods differ slightly in temperature raising time, holding time, etc., they are basically carried out according to the following procedure.
数m3〜数十IrIgの試料を容器に秤取り、熱天秤に
セットした後、窒素雰囲気下、100〜110℃の温度
に所定時間保持し、この時の試料質量に対する加熱原料
百分率を求めて水分とする。同じく窒素雰囲気下、90
0〜950’Cまで急速に昇温し、この温度に所定時間
保持し、試料質量に対する加熱減量百分率を求めて揮発
分とする。次に、酸素または空気雰囲気に切替え、恒量
になるまで温度900℃または815℃に保持し、試料
質量に対する恒量時残留分重量百分率を求めて灰分とす
る。After weighing a sample of several m3 to several tens of IrIg into a container and setting it on a thermobalance, it is held at a temperature of 100 to 110°C for a predetermined time in a nitrogen atmosphere, and the percentage of the heated raw material with respect to the sample mass at this time is determined to determine the moisture content. shall be. Similarly under nitrogen atmosphere, 90
The temperature is rapidly raised to 0 to 950'C, maintained at this temperature for a predetermined period of time, and the percentage loss on heating relative to the mass of the sample is determined to determine the volatile content. Next, the atmosphere is changed to oxygen or air, and the temperature is maintained at 900° C. or 815° C. until constant weight is reached, and the weight percentage of the residual component at constant weight with respect to the mass of the sample is determined to be the ash content.
しかしながら、前記JIS法においては、測定に時間盆
暮するとともに、自動化し難いというガ1点を有し、品
位調整へのフィードバックが不十分である。また、熱天
秤による方法においては、試料量が少なく、石炭のよう
な不均質物質ではサンプリング誤差が増大するおそれが
あるのみならず、サンプリングからの全自動化は現状で
は困難な状況にある。However, the above-mentioned JIS method has one drawback: it takes a long time to measure, is difficult to automate, and provides insufficient feedback for quality adjustment. Furthermore, in the method using a thermobalance, the amount of sample is small, and in the case of a heterogeneous material such as coal, there is a risk that the sampling error will increase, and it is currently difficult to fully automate the sampling process.
発明が解決しようとする課題
]−ラス製造用石炭の揮発分については、前記したとお
り、JIS法による測定を実施してタールおよびガス発
生量の推定、コークス炉装入炭の品位調整に使用してい
るが、測定に時間を要するとともに自動化が困難であり
、品位調整に対するフィードバックが不十分であり、ま
た熱天秤による方法は測定精度の問題と自動化し難いと
いう問題がある。[Problems to be Solved by the Invention] - As mentioned above, the volatile content of coal for lath manufacturing is measured according to the JIS method and used for estimating the amount of tar and gas generated and adjusting the quality of coal charged in a coke oven. However, measurement takes time and is difficult to automate, and feedback for quality adjustment is insufficient.Also, the method using a thermobalance has problems with measurement accuracy and is difficult to automate.
この発明は従来技術のこのような問題を解決し、石炭の
揮発分の測定の簡易迅速化と自動化がはかられる方法を
提案しようとするものである。The present invention aims to solve these problems of the prior art and propose a method that can simplify, speed up, and automate the measurement of volatile content in coal.
課題を解決するだめの手段
石炭の揮発分は石炭の乾留過程で石炭から逸散していく
水分以外の成分量を示すものである。石炭の乾留途中で
の熱分解ガスの発生状況を調査した結果では、揮発分の
構成要素は主にタール、C01CD2 、 H2,低級
炭化水素類であり、それぞれの発生極大温度は炭種によ
って異なるものの、低級炭化水素類は300〜500℃
、Co、 CO2は400〜50゜℃、タールは500
〜750℃、H2は700℃付近にそれぞれ存在し、大
略900℃で大部分のガスの発生は終了する。Means to Solve the Problem The volatile content of coal indicates the amount of components other than water that escape from the coal during the carbonization process. According to the results of investigating the generation of pyrolysis gas during the carbonization of coal, the volatile components are mainly tar, CO1CD2, H2, and lower hydrocarbons, and although the maximum temperature of each generation differs depending on the type of coal. , lower hydrocarbons: 300-500℃
, Co, CO2 is 400-50°C, tar is 500°C.
~750°C and H2 exist at around 700°C, and most of the gas generation ends at approximately 900°C.
したがって、コークス工業の指標として用いる揮発分に
相当する値は、少なくともH2の大部分の発生が終了す
る温度での測定が必要となる。Therefore, the value corresponding to the volatile content used as an indicator in the coke industry needs to be measured at a temperature at least at which most of the H2 generation ends.
しかし、この発明者が検討した結果、900℃以前、少
なくともタール発生、本体高分子部の分解の始まる大略
500℃以上の温度での加熱減量を求めることにより、
その温度から900℃までの間に発生する熱分解ガス量
と、その温度での残召分最との比率は、炭種によらずほ
ぼ一定であることを見い出した。However, as a result of the inventor's studies, by determining the heating loss at a temperature below 900°C, at least at a temperature of about 500°C or higher where tar generation and decomposition of the main polymer part begin,
It has been found that the ratio between the amount of pyrolysis gas generated from that temperature to 900° C. and the amount of residual carbon at that temperature is almost constant regardless of the type of coal.
すなわち、この発明は事前に乾燥処理した微粉炭を耐熱
ガラス容器にて一定量装入し秤量した後、500〜75
0℃の温度で少なくとも5分間以上加熱し、加熱後、再
度秤量して加熱減量を求め、この加熱減量値と予め求め
た所定温度における加熱減量値およびJIS法で測定さ
れる揮発分との関係式を用い、JIS法に換算した揮発
分値を求めることを要旨とするものである。That is, in this invention, after charging and weighing a certain amount of pulverized coal that has been dried in advance in a heat-resistant glass container,
Heating at a temperature of 0°C for at least 5 minutes, after heating, weighing again to determine the heating loss, and the relationship between this heating loss value, the heating loss value at a predetermined temperature determined in advance, and the volatile content measured by the JIS method. The gist of this method is to obtain the volatile content value converted to the JIS method using the formula.
作□ 用
耐熱ガラス容器は750℃の温度で使用可能なものであ
れば種類を問わず、硬質ガラス、石英ガラス等が使用で
きる。また、金属製でも使用することは可醜である。
“
石炭を加熱する方法としては、所定温度に加熱された環
状電気炉やメタルバスを用いることかでき、また赤外線
イメージ炉やマイクロ波加熱炉等を使用することもでき
る。Any type of heat-resistant glass container can be used as long as it can be used at a temperature of 750°C, such as hard glass or quartz glass. Also, it is ugly to use metal.
“As a method of heating the coal, it is possible to use an annular electric furnace or a metal bath heated to a predetermined temperature, and it is also possible to use an infrared image furnace, a microwave heating furnace, etc.
石炭の加熱温度を500〜750℃に限定したのは、タ
ール発生、石炭の高分子部分の分解の始まる温度が大略
500’Cであり、また750℃を超えると加熱速度が
250℃/minを超え、単位時間当りの発生揮発分量
が多くなりすぎ、試料の突沸現象が起り、再現性のある
加熱減量値が得られなくなるためである。The heating temperature of coal is limited to 500 to 750°C because the temperature at which tar generation and the decomposition of the polymeric part of coal begin is approximately 500'C, and when the temperature exceeds 750°C, the heating rate is reduced to 250°C/min. This is because the amount of volatile matter generated per unit time becomes too large, causing bumping of the sample and making it impossible to obtain a reproducible heating loss value.
また、この温度に到達後、5分間以上保持ずれば安定し
た値を得ることができるので、加熱保持時間は5分間以
上としたのである。Further, after reaching this temperature, a stable value can be obtained by holding the temperature for 5 minutes or more, so the heating holding time was set to 5 minutes or more.
加熱減量値を求めると、予め求めておいた下記(1)式
に示す所定温度における加熱減量値とJIS法で測定さ
れる揮発分との関係式により、JIS法揮発分に換算さ
れた揮発分を算出づる。When the heating loss value is calculated, the volatile content converted to the JIS method volatile content is determined by the relational expression between the heating loss value at a predetermined temperature shown in the following formula (1) calculated in advance and the volatile content measured by the JIS method. Calculate.
VMJ Is = (1−At ) VMt +100
At ・・(1)VMJ Is : JIS法揮発分に
換算された揮発分(%)
VMt :この発明方法により温度t ’Cで求めら
れる加熱減量値(%〉
At :温度t′Cでの換算係数
第1図は第1表に示す石炭を用い、この発明方法により
求めた各温度での加熱減量値とJIS法揮発分値の差の
各温度での残留分に苅する割合を示したものであるが、
500〜750’Cの間で炭種によらずほぼ一定の値を
示している。したがって、予めこの関係を求めておくこ
とにより、500〜750℃の加熱減量値を用いてJI
S法揮発分を簡単に求めることができるのである。VMJ Is = (1-At) VMt +100
At...(1) VMJ Is: Volatile content (%) converted to JIS method volatile content VMt: Heating loss value (%) determined at temperature t'C by the method of this invention At: Conversion at temperature t'C Coefficient Figure 1 shows the ratio of the difference between the heating loss value at each temperature determined by the method of this invention and the JIS method volatile content value to the residual content at each temperature using the coal shown in Table 1. In Although,
It shows a nearly constant value between 500 and 750'C regardless of the coal type. Therefore, by determining this relationship in advance, JI
The S method volatile content can be easily determined.
なお、第1図の関係は昇温速度が変化すればその絶対値
は変化するものの、比率が一定であることに変わりはな
く、特に昇温速度に左右されるものではない。Although the absolute value of the relationship shown in FIG. 1 changes as the temperature increase rate changes, the ratio remains constant and is not particularly influenced by the temperature increase rate.
実 施 例
実施例1
第1表に示す石炭を用い、60’Cに加熱された回転ド
ラム乾燥機により30分間乾燥した後、ダブルロールミ
ルで粗粉砕し、振動ディスクミルで250μm以下に微
粉砕し、ざらに107℃±10℃の乾燥機で1時間乾燥
して得た微粉炭を、内径10m、長さ120#の耐熱ガ
ラス製の細管内に高さ20.、装入密度o、”tg4で
充填し、温度550℃に設定された電気容量IKWのメ
タルバス中にステンレス製の保持容器を使用して150
#の深さまで浸漬し、加熱速度的100°Q/minで
加熱し、10分後に取出し、室温まで冷却後重量を測定
し、第1図の関係を用いてJIS法揮発分に換算された
揮発分を求めた。Examples Example 1 Using the coal shown in Table 1, it was dried for 30 minutes in a rotating drum dryer heated to 60'C, coarsely ground in a double roll mill, and finely ground to 250 μm or less in a vibrating disc mill. The pulverized coal obtained by drying it in a dryer at 107°C ± 10°C for 1 hour was placed in a heat-resistant glass tube with an inner diameter of 10m and a length of 120mm at a height of 20mm. , using a stainless steel holding container in a metal bath with a capacitance of IKW, packed with a charging density of o, "tg4, and set at a temperature of 550 °C.
#, heated at a heating rate of 100°Q/min, taken out after 10 minutes, cooled to room temperature, weighed, and converted to JIS volatile content using the relationship in Figure 1. I asked for a minute.
この計算により求めた揮発分とJIS法揮発分の関係を
第2図に示す。The relationship between the volatile content determined by this calculation and the JIS method volatile content is shown in FIG.
第2図より明らかなごとく、平均反射率0.68〜1.
22の広い範囲の炭化度の異なる石炭であるにもかかわ
らず、JIS法揮発分との差異は標準偏差で1.3%以
内と良好な一致を示した。As is clear from FIG. 2, the average reflectance is 0.68 to 1.
Despite the 22 coals having different carbonization degrees over a wide range, the difference from the JIS method volatile content was within 1.3% in terms of standard deviation, showing good agreement.
実施例2
コークス製造用原料として使用する配合炭2種について
、実施例1と同様の方法で揮発分を求めた結果を第2表
に示す。Example 2 Table 2 shows the results of determining the volatile content of two types of coal blends used as raw materials for coke production in the same manner as in Example 1.
第2表から明らかなごとく、配合炭においても単味炭と
同様に、本発明法により簡便にJIS法と同等の値を得
ることができた。As is clear from Table 2, the method of the present invention was able to easily obtain values equivalent to the JIS method for blended coal as well as for single coal.
実施例3
B、V、Blend炭(JIS法揮発分値26,2%)
を用い、実施例1と同様の方法(ただし加熱方法のみ電
気容量1にΔの赤外線イメージ炉を用いた)で、加熱温
度とその温度に到達後の加熱時間を変えて加熱減量値を
求め、第1図の関係を用いてJIS法揮発分に換算され
た揮発分を求めた結果を第3表に示す。Example 3 B, V, Blend charcoal (JIS method volatile content value 26.2%)
Using the same method as in Example 1 (however, only the heating method used an infrared image furnace with a capacitance of 1 and Δ), the heating loss value was determined by changing the heating temperature and the heating time after reaching that temperature. Table 3 shows the results of determining the volatile content converted to the JIS method volatile content using the relationship shown in FIG.
第3表より、加熱温度が750℃を超えると試料の突沸
が起りやずくなり、精度の良い測定値が得られず、また
加熱時間が5分未満でも精度良好な測定値が得られない
のに対し、加熱温度500〜750’C1加熱時間5分
間以上で精度の高い測定値が得られることが明らかであ
る。Table 3 shows that when the heating temperature exceeds 750°C, bumping of the sample tends to occur, making it difficult to obtain accurate measurement values, and even when the heating time is less than 5 minutes, accurate measurement values cannot be obtained. On the other hand, it is clear that highly accurate measured values can be obtained at a heating temperature of 500 to 750'C1 and a heating time of 5 minutes or more.
以下余白
表(%)
表(%)
発明の詳細
な説明したごとく、この発明方法によれば、コークス製
造用原料の品質評価として重要な指標である石炭の揮発
分を容易にかつ短時間に精度よく測定することができる
とともに、自動化も容易であるから、品位調整に対する
フィードバックが十分であり、コークス品質の安定化に
大きく貢献するものである。Margin table below (%) Table (%) As explained in detail, according to the method of this invention, the volatile content of coal, which is an important index for quality evaluation of raw materials for coke production, can be easily and quickly measured. Since it can be measured well and is easy to automate, it provides sufficient feedback for quality adjustment and greatly contributes to stabilizing coke quality.
第1図はこの発明方法により求めた各温度での加熱減量
値とJIS法で測定された揮発分との差の各温度での残
留分に対する割合を示す図、第2図はこの発明の実施例
における計算揮発分とJIS法で測定された揮発分との
関係を示す図である。
出願人 住友金属工業株式会社Figure 1 is a diagram showing the ratio of the difference between the heating loss value at each temperature determined by the method of this invention and the volatile content measured by the JIS method to the residual content at each temperature, and Figure 2 is a diagram showing the ratio of the difference between the heating loss value at each temperature determined by the method of this invention and the residual content at each temperature. It is a figure which shows the relationship between the calculated volatile content and the volatile content measured by JIS method in an example. Applicant: Sumitomo Metal Industries, Ltd.
Claims (1)
入し秤量した後、500〜750℃の温度で少なくとも
5分間以上加熱し、加熱後、再度秤量して加熱減量を求
め、この加熱減量値と予め求めた所定温度における加熱
減量値およびJIS法で測定される揮発分との関係式を
用い、JIS法に換算した揮発分値を求めることを特徴
とする石炭の揮発分測定方法。After charging a certain amount of pulverized coal that has been dried in advance into a heat-resistant glass container and weighing it, heat it at a temperature of 500 to 750°C for at least 5 minutes, and after heating, weigh it again to determine the loss on heating. A method for measuring the volatile content of coal, characterized in that the volatile content value converted to the JIS method is determined using a relational expression between the value, the heating loss value at a predetermined temperature determined in advance, and the volatile content measured by the JIS method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8548889A JPH02263143A (en) | 1989-04-03 | 1989-04-03 | Method of measuring volatile matter of coal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8548889A JPH02263143A (en) | 1989-04-03 | 1989-04-03 | Method of measuring volatile matter of coal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02263143A true JPH02263143A (en) | 1990-10-25 |
Family
ID=13860310
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8548889A Pending JPH02263143A (en) | 1989-04-03 | 1989-04-03 | Method of measuring volatile matter of coal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02263143A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2025127519A (en) * | 2024-02-21 | 2025-09-02 | 学校法人立命館 | Biochar analysis methods |
-
1989
- 1989-04-03 JP JP8548889A patent/JPH02263143A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2025127519A (en) * | 2024-02-21 | 2025-09-02 | 学校法人立命館 | Biochar analysis methods |
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