JPS589761B2 - How to use the service - Google Patents

How to use the service

Info

Publication number
JPS589761B2
JPS589761B2 JP15828475A JP15828475A JPS589761B2 JP S589761 B2 JPS589761 B2 JP S589761B2 JP 15828475 A JP15828475 A JP 15828475A JP 15828475 A JP15828475 A JP 15828475A JP S589761 B2 JPS589761 B2 JP S589761B2
Authority
JP
Japan
Prior art keywords
oyster
rod
heating furnace
calcium nitrate
rotary
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
JP15828475A
Other languages
Japanese (ja)
Other versions
JPS5281095A (en
Inventor
伊東速水
清水克実
富永昇助
和賀克公
和泉憲明
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP15828475A priority Critical patent/JPS589761B2/en
Publication of JPS5281095A publication Critical patent/JPS5281095A/en
Publication of JPS589761B2 publication Critical patent/JPS589761B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/02Oxides or hydroxides
    • C01F11/04Oxides or hydroxides by thermal decomposition

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 本発明は廃棄処理を要する硝酸カルシウム成分及び湿式
脱硝処理で副生じた硝酸カルシウム塩の熱分解処理、更
に硝酸塩の熱分解によるNOxの製造方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a thermal decomposition treatment of calcium nitrate components that require disposal and calcium nitrate salts produced by-product in wet denitration treatment, and a method for producing NOx by thermal decomposition of nitrates.

ボイラー、燃焼炉又は仮焼炉等の排ガス中にはNOxガ
スを数百ppm含んでいてこれらNOxガスは極めて有
害であり、除去されねばならない。
Exhaust gas from boilers, combustion furnaces, calciners, etc. contains several hundred ppm of NOx gas, and these NOx gases are extremely harmful and must be removed.

この排ガス中のNOxガスの除去はアルカリ吸収液で吸
収する法(等モル法)又は排ガス中にオゾンを添加して
アルカリ性吸収液又は亜硫酸吸収液で吸収する法(オゾ
ン法)があるが、この場合副生成物として硝酸塩及び亜
硝酸塩が生起し、これら硝酸塩、亜硝酸塩は無害化処理
する必要がある。
There are two methods for removing NOx gas from exhaust gas: the method of absorbing it with an alkaline absorption liquid (equimolar method), or the method of adding ozone to the exhaust gas and absorbing it with an alkaline absorption liquid or sulfite absorption liquid (ozone method). In this case, nitrates and nitrites are produced as by-products, and these nitrates and nitrites must be treated to render them harmless.

本発明者等は既に硝酸塩を熱分解する方法を発明した。The inventors have already invented a method for thermally decomposing nitrates.

(特願昭50−106797号(特開昭52−3029
8号公報))。
(Patent Application No. 50-106797 (Japanese Patent Application No. 52-3029)
Publication No. 8)).

その要点は硝酸カルシウムとその熱分解生成物でもある
生石灰を適当比に混合して800°〜1200℃に熱分
解温度を維持して分解を行ない活性度のよい生石灰を連
続的に製造し、且つ高濃度のNOxガスを発生させると
ころにある。
The key point is to mix calcium nitrate and quicklime, which is a thermal decomposition product of calcium nitrate, in an appropriate ratio and maintain the thermal decomposition temperature between 800° and 1200°C to continuously produce quicklime with good activity. This is where a high concentration of NOx gas is generated.

しかしながら上記の方法では回転式連続加熱炉(以下単
に回転炉と略称)による連続的熱分解は可能であるが更
に長時間運転を続けると所謂リングが生成し、安定した
運転が困難になり、且つリングとして長時間熱処理され
ると生成した生石灰は活性度が低下して死石灰になる。
However, in the above method, continuous thermal decomposition using a rotary continuous heating furnace (hereinafter simply referred to as rotary furnace) is possible, but if the operation continues for a long time, so-called rings are formed, making stable operation difficult. When the ring is heat-treated for a long time, the generated quicklime loses its activity and becomes dead lime.

一般的に回転炉の運転にはリングの生成によるトラブル
の例は数多く存在する。
In general, there are many examples of troubles caused by the formation of rings in the operation of rotary furnaces.

これらの防止法には例えば重曹等の処理に鎖がよく使用
されている如く、硝酸塩の熱分解でもその効果は認めら
れるが、鎖にも融着して成長し、充分安定した長時間運
転が困難である。
For example, chains are often used to treat baking soda, etc., and thermal decomposition of nitrates is also effective, but the chains also fuse and grow, making it difficult to operate stably for long periods of time. Have difficulty.

更に第1図に示す如く、回転炉内の上部にクリアランス
を僅少にしたかきとり棒を設置するとかなり長時間にわ
たり安定した運転が可能となる。
Furthermore, as shown in FIG. 1, if a scraping rod with a small clearance is installed in the upper part of the rotary furnace, stable operation for a considerably long period of time becomes possible.

しかし約1000℃にもなる回転炉内ではかきとり棒の
たわみが短時間に起る。
However, in a rotary furnace where the temperature reaches about 1000° C., the scraping rod becomes deflected in a short period of time.

これを防止するためにかきとり棒の中に水を通すとたわ
みは防止され回転炉内壁に融着したものがかきとられリ
ングの成長が生じない。
To prevent this, by passing water through a scraping rod, the deflection is prevented and the material fused to the inner wall of the rotary furnace is scraped off, preventing ring growth.

しかしながらかきとり棒に通す水が持ち去る熱により、
回転炉の熱効率はかなり低下し、燃焼に要する燃料はそ
れだけ多くなる。
However, due to the heat carried away by the water passing through the scraping rod,
The thermal efficiency of rotary furnaces is significantly reduced and more fuel is required for combustion.

回転炉は装置が大型化するとシェルの放散熱は全体の所
要熱に対して10%程度まで低下していくが小型装置に
なるとシェル放散熱の割合が大きくなり40〜50%以
上にも達する。
As the size of the rotary furnace increases, the heat dissipated from the shell decreases to about 10% of the total required heat, but as the equipment becomes smaller, the proportion of heat dissipated from the shell increases and reaches 40 to 50% or more.

従ってかきとり棒の中を水冷することば熱効率の点から
は致命的であり、出口の排ガス中のNOx濃度は低下し
て次のNOxの無害化処理工程の規模が大きくなり効率
的でない。
Therefore, cooling the inside of the scraping rod with water is fatal from the point of view of thermal efficiency, and the NOx concentration in the exhaust gas at the outlet decreases, which increases the scale of the next NOx detoxification process, which is not efficient.

そこでかきとり棒の中を燃焼バーナーと並流に空気を定
量供給してかきとり棒の表面温度を700℃以下に保つ
、これは700℃を越える温度でかきとり棒を長時間さ
らにしておくとクリープ現象によりかきとり棒が変形す
るからである。
Therefore, a constant amount of air is supplied inside the scraping rod in parallel with the combustion burner to keep the surface temperature of the scraping rod below 700℃.This is because if the scraping rod is left at a temperature exceeding 700℃ for a long period of time, creep will occur. This is because the scraping rod is deformed.

かくて排出してくる空気をそのまま燃焼室に導入して燃
焼ガスの2次空気に充当して回転炉の熱効率を高め、従
って回転炉で分解するNOxガスをより高濃度にして且
つ予熱空気も燃焼バーナーの2次空気に使用すると回転
炉の燃焼バーナーとしてのぞましい拡散長炎を形成せし
め、回転炉内で完全燃焼することによって燃焼温度帯(
回転炉内の最高温度)が若干回転炉の中央部に寄り熱分
解に望ましい燃焼形式がとられることになる。
The air discharged in this way is directly introduced into the combustion chamber and used as secondary air for combustion gas, increasing the thermal efficiency of the rotary furnace, thereby increasing the concentration of NOx gas decomposed in the rotary furnace, and also using preheated air. When used as the secondary air of a combustion burner, it forms a long diffusion flame suitable for a rotary furnace combustion burner, and by completely burning in the rotary furnace, the combustion temperature range (
The maximum temperature inside the rotary furnace is slightly closer to the center of the rotary furnace, resulting in a combustion type desirable for thermal decomposition.

本発明によると硝酸カルシウムと生石灰との混合物を回
転炉で熱分解する場合にとりわけ顕著な効果を示す。
According to the present invention, a particularly remarkable effect is exhibited when a mixture of calcium nitrate and quicklime is thermally decomposed in a rotary furnace.

即ち高活性の良好で均質な生石灰が連続的に製造され、
且つ高濃度の窒素酸化物を生成せしめることが可能であ
る。
In other words, highly active and homogeneous quicklime is produced continuously,
Moreover, it is possible to generate nitrogen oxides at a high concentration.

次に本発明を実施例によって詳細説明する。Next, the present invention will be explained in detail by way of examples.

実施例 硝酸カルシウム:生石灰=1:4(重量比)の粉末混合
物を回転炉に連続供給して分解焼成ゾーンを900〜9
50℃にして直熱式ロータリーキルンで熱分解運転を行
った。
Example A powder mixture of calcium nitrate and quicklime = 1:4 (weight ratio) was continuously fed to a rotary furnace to form a decomposition and firing zone of 900 to 900.
Thermal decomposition operation was performed at 50° C. in a direct heating rotary kiln.

回転炉の運転条件 L/D=12L=1200、回転数3R、P、M 回転炉の傾斜3/100、滞留時間20分供給原料7.
5kg/Hr、燃料、プロパンガス排出生石灰の活性
度 85% (粗粒滴定法石膏石灰ハンドブック、技報堂版 P48
4による) 分解度 95%(キールダール法による全窒素分析値よ
り)運転結果を次の表に纏めた。
Rotary furnace operating conditions L/D=12L=1200, rotation speed 3R, P, M Rotary furnace inclination 3/100, residence time 20 minutes Feedstock7.
5kg/Hr, fuel, propane gas discharge Activity of quicklime 85% (Coarse particle titration method gypsum lime handbook, Gihodo edition P48
4) Decomposition degree: 95% (based on total nitrogen analysis value by Kieldahl method) The operation results are summarized in the following table.

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

第1図はかきとり棒を付着した回転炉の概略側面図、第
2図は回転炉に山形鋼と鎖を設けた概略説明図、第3図
Aは回転炉に山形鋼によるかきとり棒を付着した概略側
面図、同Bは断面図を示す。 1・・・・・・バーナー、2・・・・・・かきとり棒、
3・・・・・・回転炉、4・・・・・・回転炉のリング
ゾーン、5・・・・・・山形鋼、6・・・・・・鎖、7
・・・・・・山形鋼によるかきとり棒、8・・・・・・
熱分解試料、A・・・・・・空気導入、F1・・・・・
・入口フッド、F2・・・・・・出口フッド、C・・・
・・・CaO。
Figure 1 is a schematic side view of a rotary furnace with a scraping rod attached to it, Figure 2 is a schematic illustration of a rotary furnace equipped with angle iron and chains, and Figure 3A is a rotary furnace with a scraping rod made of angle iron attached. A schematic side view, and B shows a sectional view. 1... Burner, 2... Scraping stick,
3...Rotary furnace, 4...Ring zone of rotary furnace, 5...Angle iron, 6...Chain, 7
・・・・・・Scraping rod made of angle iron, 8・・・・・・
Pyrolysis sample, A...Air introduction, F1...
・Entrance hood, F2...Exit hood, C...
...CaO.

Claims (1)

【特許請求の範囲】[Claims] 1 硝酸カルシウム又は硝酸カルシウムを含む混合物を
回転式連続加熱炉で分解処理を行う方法において、回転
式加熱炉内上部に硝酸カルシウムを含む混合物の融着及
びリング発生防止用の棒状のカキトリ装置を取り付け、
カキトリ棒内に空気を定量供給してカキトリ棒表面の温
度を700℃以下に保って、カキトリ棒の熱による変形
を防止し、カキトリ棒から排出される加熱空気を回転式
連続加熱炉の燃焼用2次空気に充当し、回転式連続加熱
炉による熱分解に適わしい加熱バーナーの拡散長炎を形
成せしめて熱分解反応を円滑ならしめ、高活性の良好な
均質な生石灰を連続的に製造し、且つ高濃度の窒素酸化
物を生成させることを特徴とする硝酸塩を熱分解する方
法。
1 In a method of decomposing calcium nitrate or a mixture containing calcium nitrate in a rotary continuous heating furnace, a rod-shaped oyster device is attached to the upper part of the rotary heating furnace to prevent the mixture containing calcium nitrate from fusing and ring formation. ,
A fixed amount of air is supplied into the oyster rod to keep the surface temperature of the oyster rod below 700°C to prevent deformation of the oyster rod due to heat, and the heated air discharged from the oyster rod is used for combustion in a rotary continuous heating furnace. It is used as secondary air to form a long diffusion flame of a heating burner suitable for pyrolysis in a rotary continuous heating furnace to smooth the pyrolysis reaction and continuously produce homogeneous quicklime with high activity. , and a method for thermally decomposing nitrates, which is characterized by producing nitrogen oxides at a high concentration.
JP15828475A 1975-12-28 1975-12-28 How to use the service Expired JPS589761B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15828475A JPS589761B2 (en) 1975-12-28 1975-12-28 How to use the service

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15828475A JPS589761B2 (en) 1975-12-28 1975-12-28 How to use the service

Publications (2)

Publication Number Publication Date
JPS5281095A JPS5281095A (en) 1977-07-07
JPS589761B2 true JPS589761B2 (en) 1983-02-22

Family

ID=15668223

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15828475A Expired JPS589761B2 (en) 1975-12-28 1975-12-28 How to use the service

Country Status (1)

Country Link
JP (1) JPS589761B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61128060U (en) * 1985-01-31 1986-08-11
JPH0725119A (en) * 1993-07-09 1995-01-27 Nec Corp Thermal transfer ink ribbon

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61128060U (en) * 1985-01-31 1986-08-11
JPH0725119A (en) * 1993-07-09 1995-01-27 Nec Corp Thermal transfer ink ribbon

Also Published As

Publication number Publication date
JPS5281095A (en) 1977-07-07

Similar Documents

Publication Publication Date Title
US4080218A (en) Method of removal of nitrogen oxides, particularly for use in cement raw material burning installation
JPS622207B2 (en)
AU629834B2 (en) Method for lowering the content of oxides of nitrogen in flue gases
JPH03177785A (en) Method and device for re-utilizing poder dust for rotary kiln
US3838193A (en) Method of treating nitrogen oxide generating substances by combustion
ES2207047T3 (en) PROCEDURE FOR THE PREPARATION OF HETEROGENEAS PULVERULENT SUBSTANCES.
JPS589761B2 (en) How to use the service
US3940253A (en) Device for the purification of process waste gases
JPH10132241A (en) Method for disposing of waste liquid or exhaust gas
US2673141A (en) Process for rendering nitrous gases innocuous
US3795731A (en) Process for the combustion of ammonium sulfate
US6296820B1 (en) Method for the reduction of NOX emissions
US4263264A (en) Method of abating nitrogen oxides in combustion waste gases
CA2060457C (en) Method for burning halogenated hydrocarbon containing waste
JPS61282713A (en) Combustion furnace
JP2005522660A (en) Apparatus for purifying exhaust gas containing fluorine-containing compounds in a combustion furnace with a low nitrogen oxide emission level
Rutberg et al. Plasma furnace for treatment of solid toxic wastes
JPS6260159B2 (en)
JP2005030608A (en) Heating treatment installation with gas combustor
RU2116571C1 (en) Method of thermally neutralizing injurious substances in afterburner
US1213375A (en) Process of producing alkaline-earth-metal compounds.
JP3523999B2 (en) Production method of quicklime and calcined dolomite in rotary kiln using waste plastic
RU2151958C1 (en) Method for thermal decontamination of solid wastes
RU2147713C1 (en) Method of thermal reworking of solid wastes
DK143163B (en) PROCEDURE FOR COMPLETE OR PARTIAL NEUTRALIZATION OF THE SUBSEQUENTLY FUEL CONSUMPTION PRODUCED ACID COMBUSTION PRODUCTS AND THE USE OF THE PROCEDURE