JPS5848600B2 - Cement clinker - Google Patents

Cement clinker

Info

Publication number
JPS5848600B2
JPS5848600B2 JP50108092A JP10809275A JPS5848600B2 JP S5848600 B2 JPS5848600 B2 JP S5848600B2 JP 50108092 A JP50108092 A JP 50108092A JP 10809275 A JP10809275 A JP 10809275A JP S5848600 B2 JPS5848600 B2 JP S5848600B2
Authority
JP
Japan
Prior art keywords
gas
cement clinker
desulfurization
clinker
cement
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
Application number
JP50108092A
Other languages
Japanese (ja)
Other versions
JPS5232001A (en
Inventor
成仁 高本
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP50108092A priority Critical patent/JPS5848600B2/en
Publication of JPS5232001A publication Critical patent/JPS5232001A/en
Publication of JPS5848600B2 publication Critical patent/JPS5848600B2/en
Expired legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Industrial Gases (AREA)

Description

【発明の詳細な説明】 この発明は、高温脱硫の方法に関する。[Detailed description of the invention] The present invention relates to a method of high temperature desulfurization.

現在エネルギー源の不足から燃料として石炭を主用する
ことが考えられている。
Currently, due to the lack of energy sources, it is being considered to mainly use coal as a fuel.

これを発電用燃料として用いる場合、低カロリーガス化
してガスタービンとスチームタービンを組合せた所謂複
合発電方式が最も有利とされている。
When using this as a fuel for power generation, it is considered most advantageous to convert it into a low-calorie gas and use a so-called combined power generation system in which a gas turbine and a steam turbine are combined.

石炭をガス化してガスタービンに導入する場合生戒粗ガ
スは精製しないと前記ガスタービンに支障を生ずるので
高温で脱硫を行ない、熱交換にもとづく損失を最小限に
とどめかつ湿式脱硫法などに見られるガスの体積損失を
なくすことが全発電効率を高める上で望ましい。
When coal is gasified and introduced into a gas turbine, raw gas must be purified, otherwise it will cause trouble to the gas turbine. Therefore, desulfurization is carried out at high temperatures to minimize losses due to heat exchange and to improve the wet desulfurization method. It is desirable to eliminate the volume loss of the gas that is generated in order to increase the overall power generation efficiency.

即ち石炭をガス化すると同時に生成ガスから効率よ《経
済的に硫黄分を除去するが重要な技術的課題の一つとな
っている。
That is, one of the important technical issues is to gasify coal and simultaneously remove the sulfur content from the produced gas efficiently and economically.

現在開発のすすめられている高温における脱硫の多くは
高圧反応塔間で脱硫剤粒子を循環使用し、それぞれの塔
で脱硫再生を行なう方法がとられている。
Most of the high-temperature desulfurization currently being developed uses a method in which desulfurization agent particles are circulated between high-pressure reaction towers and desulfurization regeneration is performed in each tower.

従来から考えられている脱硫剤としては酸化カルシュウ
ム、ドロマイト等があるが、これら脱硫剤を流動層、ま
たは移動層で使用する場合、高温において脱硫剤が焼結
するという問題又は逆に粉化するという問題が生じてい
る。
Conventionally considered desulfurizing agents include calcium oxide and dolomite, but when these desulfurizing agents are used in a fluidized bed or moving bed, there is a problem that the desulfurizing agents sinter at high temperatures or, conversely, become powder. This problem has arisen.

脱硫剤が焼結すると細孔面積の減少、流動化不能、偏流
など種々の問題を生ずる、一方粉化の場合は排ガスの脱
じん装置、脱硫剤の追加、補充、その後の工程における
それだけ負担になる工程が必要とされるという問題があ
る。
Sintering of the desulfurization agent causes various problems such as a decrease in pore area, inability to fluidize, and uneven flow.On the other hand, in the case of pulverization, it requires a dust removal device for exhaust gas, addition of desulfurization agent, replenishment, and subsequent processes. The problem is that it requires a different process.

またこれらの問題の解決が非常に困難である。Moreover, it is very difficult to solve these problems.

この発明は脱流、再生の二種の塔の必要なことや焼結等
につき問題を解決する手段を提案するものである。
This invention proposes a means to solve problems regarding the necessity of two types of columns for deflow and regeneration, sintering, etc.

セメントクリンカはセメントの原料であり、原料として
石炭、粘土、石をそれぞれ粉砕し微粉にしたものをよく
混合し小量の水を加え小塊とする方法、またはベーズン
中でよく混合させる湿式法、サスペンションプレヒータ
ーを使用する乾式法などによりよ《混合した原料をキル
ンに投入し1 600℃位で焼成するものである。
Cement clinker is a raw material for cement, and can be produced by grinding coal, clay, and stone into fine powder, mixing them well and adding a small amount of water to make small lumps, or by wet method, mixing well in a basin. The mixed raw materials are put into a kiln using a dry method using a suspension preheater and fired at about 1,600°C.

その高温粉粒塊を急冷装置で急冷し50〜80℃で排出
されるときは硬度の高い表面の粗いクリンカーが得られ
る。
When the high-temperature powder agglomerates are quenched in a quenching device and discharged at 50 to 80°C, a clinker with high hardness and a rough surface is obtained.

クリンカーの組成はアリット、ベリット、セリット等よ
りなる複雑な組成を有するガラス質の物質でかつ多孔質
のものである。
The clinker is a porous glassy substance with a complex composition consisting of alit, berit, cerit, and the like.

このクリンカーの水溶液は微アルカリ性を量する。This aqueous solution of clinker is slightly alkaline.

高温において硫化水素(H2S)や亜硫酸ガス(SO2
)等硫黄酸化物を捕捉し除去する性質を確認したがその
捕集反応過程については明確にすることができない。
At high temperatures, hydrogen sulfide (H2S) and sulfur dioxide gas (SO2
) has been confirmed to capture and remove sulfur oxides, but the capture reaction process cannot be clarified.

一例としての次にのべる実験結果はそのH2S捕集性能
を示すものである。
As an example, the following experimental results show its H2S trapping performance.

この特質はクリンカ一が多孔質で表面積が犬であること
と前記組或物中のCa(カルジューム)成分の化学反応
的働きによるものと推定されている。
This characteristic is presumed to be due to the fact that the clinker is porous and has a large surface area, and the chemical reaction of the Ca (calcium) component in the composition.

第1図は実験結果を示すものでセメントクリンカ5,9
rを固定層に充填し硫化水素ガス(H2S)を含む還元
性ガスを用いて脱流した結果を示す。
Figure 1 shows the experimental results for cement clinker 5,9
The results are shown in which a fixed bed was filled with r and deflowed using a reducing gas containing hydrogen sulfide gas (H2S).

ガス温度900℃にして充分脱硫の効果を収めることを
示すものである。
This shows that a sufficient desulfurization effect can be obtained at a gas temperature of 900°C.

この脱硫作用をさせたのちタリンカを取り出してみたが
全《焼結の現象はおこしていなかった。
After this desulfurization effect was applied, the tarinka was taken out, but no sintering phenomenon had occurred.

このセメントタリンカ粒子または細粒で固定床を形成さ
せまたは流動床を形成させて高温ガスを通すとき脱硫作
用がされ、石炭をガス化した生或ガスの精製にいちぢる
しい効果を収めるものである。
This cement tarinka particles or fine particles are used to form a fixed bed or a fluidized bed, and when high temperature gas is passed through it, a desulfurization effect is produced, which has a remarkable effect on the purification of raw gas produced by gasifying coal. It is.

この発明の実施により固定床(流動床においても同様)
を用いセメントタリンカ層を設け、石炭よりの生成ガス
を通すとき900℃の高温ガスは脱硫され同時にセメン
トクリンカ層はフィルターとして作用し除じんの効果を
あわせ奏するという結果が得られた。
By implementing this invention, fixed bed (same as fluidized bed)
A cement clinker layer was provided using a cement clinker layer, and when gas generated from coal was passed through, the high temperature gas at 900°C was desulfurized, and at the same time, the cement clinker layer acted as a filter and had the effect of removing dust.

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

第1図は硫化水素ガスを含む模擬ガスを用いセメントタ
リンカ固定層の脱硫効果を確認した実験結果を示す線図
である。
FIG. 1 is a diagram showing the results of an experiment in which the desulfurization effect of a cement tarinka fixed layer was confirmed using a simulated gas containing hydrogen sulfide gas.

Claims (1)

【特許請求の範囲】[Claims] 1 固定床または流動床の媒体としてセメントクリンカ
粒子を用いて高温ガスを脱硫することを特徴とするセメ
ントクリンカを用いる高温脱硫方法。
1. A high-temperature desulfurization method using cement clinker, characterized in that high-temperature gas is desulfurized using cement clinker particles as a fixed bed or fluidized bed medium.
JP50108092A 1975-09-08 1975-09-08 Cement clinker Expired JPS5848600B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50108092A JPS5848600B2 (en) 1975-09-08 1975-09-08 Cement clinker

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50108092A JPS5848600B2 (en) 1975-09-08 1975-09-08 Cement clinker

Publications (2)

Publication Number Publication Date
JPS5232001A JPS5232001A (en) 1977-03-10
JPS5848600B2 true JPS5848600B2 (en) 1983-10-29

Family

ID=14475655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50108092A Expired JPS5848600B2 (en) 1975-09-08 1975-09-08 Cement clinker

Country Status (1)

Country Link
JP (1) JPS5848600B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61202475A (en) * 1985-03-05 1986-09-08 Mitsubishi Electric Corp Solar battery array for space

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5496472A (en) * 1978-01-17 1979-07-30 Hitachi Plant Eng & Constr Co Ltd Removing method for harmful gas contained in city refuse incinerator waste gas
US4218878A (en) * 1978-04-28 1980-08-26 Westinghouse Electric Corp. Acceleration monitoring system for protecting gas turbine against damaging operation at resonant speeds
JPS56158249A (en) * 1980-05-09 1981-12-05 Kaou Kueekaa Kk Acidic gas capturing material in gas produced from mold
US4716027A (en) * 1986-07-25 1987-12-29 Passamaquoddy Tribe, A Sovereign Indian Tribe Recognized By The Government Of The United States Of America Method for simultaneously scrubbing cement kiln exhaust gas and producing useful by-products therefrom
US5100633A (en) * 1985-11-07 1992-03-31 Passamaquoddy Technology Limited Partnership Method for scrubbing pollutants from an exhaust gas stream
DE4330593A1 (en) * 1993-09-09 1995-03-16 Krupp Polysius Ag Process for cleaning flue gases
DE4401166A1 (en) * 1994-01-17 1995-07-20 Krupp Polysius Ag Process for cleaning flue gases

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61202475A (en) * 1985-03-05 1986-09-08 Mitsubishi Electric Corp Solar battery array for space

Also Published As

Publication number Publication date
JPS5232001A (en) 1977-03-10

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