JPS5818400B2 - Coal gasification slag processing method - Google Patents
Coal gasification slag processing methodInfo
- Publication number
- JPS5818400B2 JPS5818400B2 JP16998180A JP16998180A JPS5818400B2 JP S5818400 B2 JPS5818400 B2 JP S5818400B2 JP 16998180 A JP16998180 A JP 16998180A JP 16998180 A JP16998180 A JP 16998180A JP S5818400 B2 JPS5818400 B2 JP S5818400B2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- coal
- coal gasification
- added
- sulfite
- 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.)
- Expired
Links
Description
【発明の詳細な説明】
この発明は、鉄浴ガス化炉で石炭をガス化する際発生す
るスラグを無害処理する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for harmlessly treating slag generated when coal is gasified in an iron bath gasifier.
鉄浴ガス化炉を用いて石炭をガス化する方法は、ガス化
反応に必要な熱を溶融鉄によって供給する方式で、石炭
をガス化剤(酸素、水蒸気等)と共に溶融状態に保たれ
た高温の溶融鉄浴中に吹込んでガス化する方法である。The method of gasifying coal using an iron bath gasifier is a method in which the heat necessary for the gasification reaction is supplied by molten iron, and the coal is kept in a molten state together with a gasifying agent (oxygen, steam, etc.). This method involves blowing into a high-temperature molten iron bath to gasify it.
この方法を実施するためのガス化装置としては、その一
例を第1図に示すごと(、炉側壁に排滓口1を有するガ
ス化炉2と、石炭およびガス化剤を吹込むランス、生成
ガス回収フード3から構成されており、予めガス化炉2
内に貯えられた溶融鉄浴(1300〜1500℃)4中
にランス5により石炭をガス化剤と共に吹込んでガス化
する装置が知られている。An example of a gasification apparatus for carrying out this method is shown in Fig. 1 (a gasification furnace 2 having a slag discharge port 1 on the side wall of the furnace, a lance for injecting coal and a gasification agent, It consists of a gas recovery hood 3, and the gasification furnace 2
An apparatus is known in which coal is gasified by blowing it together with a gasifying agent using a lance 5 into a molten iron bath (1,300 to 1,500°C) 4 stored in a molten iron bath (1300 to 1500°C).
このような鉄浴石炭ガス方式においては、ガス化の際溶
融鉄浴の表面にガスの生成に伴って石炭中の灰分に由来
するスラグ6が発生する。In such an iron bath coal gas system, slag 6 derived from the ash in the coal is generated on the surface of the molten iron bath during gasification as gas is generated.
この石炭ガス化スラグの成分は第1表に示すとおりであ
る。The components of this coal gasification slag are shown in Table 1.
すなわち、石炭ガス化の際溶融鉄浴は酸化発熱により昇
温するが、雰囲気としては還元性があり、石炭中のSは
FeS、CaS、MnS としてスラグ中に固定濃縮
される。That is, during coal gasification, the temperature of the molten iron bath rises due to heat generated by oxidation, but the atmosphere is reducing, and S in the coal is fixed and concentrated in the slag as FeS, CaS, and MnS.
このため、通常はCaOを大量投入してスラグによる脱
硫を行ない、スラグ量が増加すると定期的に排滓する。For this reason, usually a large amount of CaO is added to perform desulfurization using slag, and when the amount of slag increases, the slag is periodically discharged.
この排出スラグ中には8分が主にCaS 、FeS、
MnS として含まれており、空気および水と接触す
ると、2CaS+02+2H20→2Ca(OH) 2
+28・=(1)式CaS+(X−1)S→CaSx
・−−゛(2)式の反応により多硫化物が生成
し、この多硫化物が水に溶は黄色水の発生となる。This discharged slag contains mainly CaS, FeS,
Contained as MnS, when in contact with air and water, 2CaS+02+2H20→2Ca(OH)2
+28・=(1) Formula CaS+(X-1)S→CaSx
・---゛Polysulfide is produced by the reaction of formula (2), and when this polysulfide dissolves in water, yellow water is generated.
また、CaS+2H20→Ca(OH)2+2H2S
−−−−・−(3)式の反応により硫化水素が発生し
悪臭発生の原因となる。Also, CaS+2H20→Ca(OH)2+2H2S
-------Hydrogen sulfide is generated by the reaction of formula (3), which causes a bad odor.
ところで、石炭ガス化スラグは高炉滓等と同様河川等の
埋立て用あるいは道路用材料としてすぐれた特性をもち
、自然環境保護の上からも有力な資源であるため、有効
利用するためには前記黄色水や悪臭の問題を解決する必
要があり、また石炭ガス化を工業的規模で実施すること
になると当然その発生量は膨大なものとなるため、何等
かの有効な対策をこうじなければならない。By the way, coal gasification slag, like blast furnace slag, has excellent properties as a material for reclamation of rivers, roads, etc., and is a powerful resource from the standpoint of protecting the natural environment. Therefore, in order to use it effectively, it is necessary to It is necessary to solve the problem of yellow water and bad odor, and since the amount of gasification produced will naturally be enormous if coal gasification is carried out on an industrial scale, some effective countermeasure must be taken. .
: この発明は前記石炭ガス化スラグの有効利用をはか
るため、石炭ガス化スラグにCaSO3等の亜硫酸塩を
添加混合することにより、黄色水を防止すると共に硫化
水素ガスの悪臭をも解消し得る方法を提案するものであ
る。: In order to effectively utilize the coal gasification slag, this invention provides a method that prevents yellow water and also eliminates the bad odor of hydrogen sulfide gas by adding and mixing sulfites such as CaSO3 to the coal gasification slag. This is what we propose.
亜硫酸塩を石炭ガス化スラグ(以下スラグと略称する)
に添加混合する場合は、石炭ガス化炉から排滓されたス
ラグを目的用途に応じて適当な大きさに破砕した後必要
量の亜硫酸塩を添加混合する。Sulfite is converted into coal gasified slag (hereinafter abbreviated as slag)
When mixing with sulfite, the slag discharged from the coal gasifier is crushed into an appropriate size depending on the intended use, and then the necessary amount of sulfite is added and mixed.
この時、スラグ中のCaS は2 Ca S + 4
Ca5Oa + 3 H20→3 Ca S 203+
3 Ca (OH)’2 −・”−・(
4)式となりチオ塩酸に変る。At this time, CaS in the slag is 2 Ca S + 4
Ca5Oa + 3 H20→3 Ca S 203+
3 Ca (OH)'2 -・”-・(
4) The formula changes to thiohydrochloric acid.
この反応は前面1)、(3゜(3)式とは競争反応であ
るが、亜硫酸塩の共存下では(4)式の反応が支配的で
ある。This reaction is a competitive reaction with the front 1) and (3) equation (3), but in the presence of sulfite, the reaction of equation (4) is dominant.
亜硫酸塩としては、亜硫酸カルシウム (CaS03・2H20)が最適である。Calcium sulfite is a sulfite. (CaS03・2H20) is optimal.
CaSO3・2H20は最近の大気汚染防止による排煙
脱硫設備の副産物として大量かつ安価に入手できる。CaSO3.2H20 can be obtained in large quantities and at low cost as a byproduct of flue gas desulfurization equipment used to prevent recent air pollution.
亜硫酸塩のスラグへの必要添加量は、添加物の形態(液
状、粉末状等)、添加方法およびスラグの粒度、成分に
よって異なる。The amount of sulfite required to be added to the slag varies depending on the form of the additive (liquid, powder, etc.), the method of addition, the particle size of the slag, and the components.
第2図は黄色水の発生と亜硫酸カルシウム添加量との関
係を示す1実験結果である。Figure 2 shows the results of an experiment showing the relationship between the generation of yellow water and the amount of calcium sulfite added.
すなわち、第2表に示す成分を有するスラグをぶ粒径0
.5 mm以下に粉砕し、これに粉末状のCaSO3・
2H20を50%含有する液状物質を添加し約1昼夜放
置し、黄色水の発生状況を観察した。That is, if the slag containing the components shown in Table 2 has a particle size of 0,
.. Grind it to 5 mm or less and add powdered CaSO3 to it.
A liquid material containing 50% 2H20 was added and left to stand for about one day and night, and the generation of yellow water was observed.
黄色水の発生試験はスラグ100グに対して300rn
lの蒸留水を加え、ビーカーに水面のレベルを表示した
後、約10分間で100℃になるように加熱し、加熱開
始から60分間煮沸し、煮沸後室温まで冷却し、ビーカ
ーのもとの水位まで水を加えて水量を調節しr過後黄色
度指数を求め、CaSO3・2H20添加率に対してプ
ロットした。Yellow water generation test is 300rn for 100g of slag.
1 of distilled water and display the water level in the beaker, heat to 100℃ in about 10 minutes, boil for 60 minutes from the start of heating, cool to room temperature after boiling, and return to the bottom of the beaker. The amount of water was adjusted by adding water up to the water level, and the yellowness index was determined after filtration and plotted against the addition rate of CaSO3.2H20.
この場合、黄色度指数は吸光光度計を用い石英10Cr
/lセルを使用し波長350mmでの吸光度をいう。In this case, the yellowness index was determined using a spectrophotometer using quartz 10Cr.
It refers to the absorbance at a wavelength of 350 mm using a /l cell.
図から明らかなごとく、前記の試験では
Ca SOs・2H20を0.5%以上添加すれば黄色
水の発生はほぼ完全に防止できる。As is clear from the figure, in the above test, the generation of yellow water can be almost completely prevented by adding 0.5% or more of CaSOs.2H20.
しかし、この添加量は特に限定するものではなく、スラ
グの粒径やCaSの含有量に応じて、またスラク泪体の
強度が低下しない程度に加減して添加する。However, the amount added is not particularly limited, and is adjusted depending on the particle size of the slag and the content of CaS, and to the extent that the strength of the slag body does not decrease.
亜硫酸塩の添加混合方法としては、スラグの排滓後破砕
工程から目的用途に使用される工程までのいかなる工程
でもよいが、破砕時に粉状で添加するか、あるいは路盤
材等敷設後にスラリー状で散布する方法が実施し易い。Sulfite can be added and mixed in any process from the crushing process after the slag is discharged to the process where it is used for the intended purpose, but it can be added in powder form during crushing, or in slurry form after laying roadbed material, etc. The spraying method is easy to implement.
前記のように、この発明法によれば、亜硫酸塩、の添加
混合という極く簡単な方法で石炭ガス化スラグの有効利
用を可能とするもので、石炭ガスの開発のみならず、土
木建築関係その他にも寄与するところが大きい。As mentioned above, according to the method of this invention, it is possible to effectively utilize coal gasification slag by an extremely simple method of adding and mixing sulfite, and it is useful not only for the development of coal gas but also for civil engineering and construction. There are other major contributions as well.
次に、この発明の実施例について説明する。Next, embodiments of the invention will be described.
;実施例
前記第2表に示す成分を有するスラグを粉砕し、粒径5
mm以下の粒度な有するもの100fに亜硫酸カルシウ
ム(’CaSO3・2H2Q’)を0.251.0.5
り、2グ、各別に添加混合し、それぞれIB。Example: A slag having the components shown in Table 2 above was ground, and the particle size was 5.
Calcium sulfite ('CaSO3.2H2Q') is added to 100f of particles with a particle size of 0.251.0.5 mm or less.
Add and mix 2 grams of each separately, and mix each with IB.
2日、3日放置した後、黄色水の溶出試験を行なった。After leaving it for 2 or 3 days, a yellow water elution test was conducted.
溶出試験はスラグ対水を1:3の割合で混合して1時間
煮沸した後涙過し、その濾過液の吸光度を波長350m
mで測定した。In the elution test, slag to water was mixed at a ratio of 1:3, boiled for 1 hour, filtered, and the absorbance of the filtrate was measured at a wavelength of 350 m.
Measured in m.
その結果を第3表に示す。The results are shown in Table 3.
なお第3表中には比較のため蒸留水添加スラグについて
行なった溶出試験結果を併わせて示す。For comparison, Table 3 also shows the results of an elution test conducted on slag with distilled water added.
第3表の結果から明らかなごとく、亜硫酸カルシウムを
添加したスラグの場合は、蒸留水添加スラグに比し吸光
度は低い値を示し、黄色水の発生傾向は認められなかっ
た。As is clear from the results in Table 3, in the case of the slag to which calcium sulfite was added, the absorbance was lower than that of the slag to which distilled water was added, and no tendency to generate yellow water was observed.
また蒸留水添加スラグでは硫化水素に起因する悪臭が発
生したが、亜硫酸カルシウム添加スラグの場合は臭気は
認められなかった。In addition, while distilled water-added slag produced a bad odor due to hydrogen sulfide, no odor was observed in calcium sulfite-added slag.
第1図は鉄浴ガス化装置の一例を示す断面図、第2図は
この発明におけるCaSO3・2H20添加率と黄色度
指数との関係を示す図表であや。
1−・−・−排滓口、2・・・・・・ガス化炉、3・・
・・・−ガス回収フード、4・・−・・・溶融鉄浴、5
・・・・・・ランス、6・・・・・・スラグ。FIG. 1 is a cross-sectional view showing an example of an iron bath gasifier, and FIG. 2 is a chart showing the relationship between CaSO3.2H20 addition rate and yellowness index in this invention. 1-----Slag outlet, 2... Gasifier, 3...
...-Gas recovery hood, 4... Molten iron bath, 5
...Lance, 6...Slag.
Claims (1)
んでガス化する際発生するスラグに、亜硫酸塩を添加混
合することを特徴とする石炭ガス化スラグの処理方法。1. Blowing coal into a high-temperature molten iron bath together with a gasifying agent: A method for treating coal gasification slag, which is characterized by adding and mixing sulfite to the slag generated when the coal is poured into a hot molten iron bath and gasified.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16998180A JPS5818400B2 (en) | 1980-12-01 | 1980-12-01 | Coal gasification slag processing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16998180A JPS5818400B2 (en) | 1980-12-01 | 1980-12-01 | Coal gasification slag processing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5794091A JPS5794091A (en) | 1982-06-11 |
| JPS5818400B2 true JPS5818400B2 (en) | 1983-04-12 |
Family
ID=15896381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16998180A Expired JPS5818400B2 (en) | 1980-12-01 | 1980-12-01 | Coal gasification slag processing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5818400B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6514532B2 (en) * | 2015-03-17 | 2019-05-15 | 株式会社大林組 | Spraying prevention method |
-
1980
- 1980-12-01 JP JP16998180A patent/JPS5818400B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5794091A (en) | 1982-06-11 |
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