JPS58190607A - Combustion with low nox performing desulfurization simultaneously - Google Patents

Combustion with low nox performing desulfurization simultaneously

Info

Publication number
JPS58190607A
JPS58190607A JP57071979A JP7197982A JPS58190607A JP S58190607 A JPS58190607 A JP S58190607A JP 57071979 A JP57071979 A JP 57071979A JP 7197982 A JP7197982 A JP 7197982A JP S58190607 A JPS58190607 A JP S58190607A
Authority
JP
Japan
Prior art keywords
combustion chamber
combustion
desulfurization
supplied
primary combustion
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
JP57071979A
Other languages
Japanese (ja)
Other versions
JPS6137522B2 (en
Inventor
Yoshitoshi Sekiguchi
善利 関口
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen Corp
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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP57071979A priority Critical patent/JPS58190607A/en
Publication of JPS58190607A publication Critical patent/JPS58190607A/en
Publication of JPS6137522B2 publication Critical patent/JPS6137522B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection

Abstract

PURPOSE:To make a low inclusion of NOx together with desulfurization by a method wherein desulfurization agent is supplied while a primary combustion region is applied as a reducing area and is kept at such a temperature as making the complete melting of ash. CONSTITUTION:A reducing combustion is performed in a primary combustion chamber 11 with an air ratio less than 1 and a temperature in the primary combustion chamber 11 is kept at a temperature higher than a point where the ash is melted and fluidized. Desulfurization agent 18 is supplied to the primary combustion chamber 11 from a desulfurization agent supplying nozzle 19 so as to perform the desulfurization process. The melted mixture C of the melted ash and the sulfide generated under the reaction between a sulfer compound and a alkaline substance in the primary combustion chamber 11 is taken out through the melted substance extraction port 20, and the primary combustion discharging gas D containing the non-combustioned substance is guided to a secondary combustion chamber 12 through the communication passage 13. At this secondary combustion chamber 12, a sufficient volume of secondary air 21 is supplied to make a complete oxidation and combustion of the non-combustion substance.

Description

【発明の詳細な説明】 本発明は、石炭等灰分、N分、5分を同時に多く含む燃
料を燃焼した際に発生する煤塵、NOx。
DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to soot and NOx generated when burning a fuel such as coal that simultaneously contains a large amount of ash, nitrogen, and carbon dioxide.

SOX等の自書物質を効果的に除去する脱硫を同時に行
表う低NOx燃焼法に胸するものである。
We are excited about the low NOx combustion method that simultaneously performs desulfurization and effectively removes self-reported substances such as SOX.

灰分り多い燃料の燃焼排ガスの脱硫法の1つとして、I
P内へlI接にアルカリ(多くは粉体で)を鋲給し、硫
酸塩あるいは亜硫酸塩として吸収する方法がある。しか
しながらこの方法では、炉内温度が高い場合に、 CaO+ Sw + 1/!Ox−一→Ca5O4−=
−(1)NaxO+ SOm +1/m0y−−−−→
Nas SOa  ・−・・・・(1)などの反応は起
ヤにくくなり%IIZ図に示すようにl・・01以上に
おいては脱硫率が低下する。一方、低NOx燃焼法の1
つとして空気二段燃焼法が知られている。すなわち簡2
図に示すように、火炉(1)内に上下方向の燃焼室建)
を形成し、そして燃焼室(2)の下部にII料(3)を
供給する燃料ノズル(4)を配設すると共に、この燃料
ノズル(4)の周りから一次空気に)を供給している。
I
There is a method of directly feeding an alkali (often in powder form) into P and absorbing it as sulfate or sulfite. However, in this method, when the temperature inside the furnace is high, CaO+ Sw + 1/! Ox-1→Ca5O4-=
−(1) NaxO+ SOm +1/m0y---→
Reactions such as Nas SOa (1) are difficult to occur, and as shown in the %IIZ diagram, the desulfurization rate decreases at l..01 or more. On the other hand, low NOx combustion method 1
One known method is the air two-stage combustion method. In other words, simple 2
As shown in the figure, vertical combustion chambers are built in the furnace (1).
A fuel nozzle (4) for supplying the II fuel (3) is arranged at the lower part of the combustion chamber (2), and primary air is supplied from around this fuel nozzle (4). .

そして、−火中気φ)の供給位曹の上方から二次空気(
6)を供給すると共に、前記燃料ノズル0)に対向させ
て、脱硫剤(υを供給する脱硫材供給ノズル俤〕を配設
している。(9月よ風箱を示す、かかる空気二段燃焼法
では、空気を分劃供給し、−火煙焼城囚では空気比が1
以下の還元燃焼となっている。このような還元雰囲気士
では、CaO+ H,S−→CaS + H*0−= 
(1m)NhO+ ToS   *  Nam5+ル0
・・・−(5)NhO十SO鵞+I C−> Na鵞s
 + sco・・・・・・α)など硫化物を作る反応が
主反応とな)、これらの反応によって生成した硫化物(
Na1S、CaS、FeSなど)は高温においても安定
である。そこで脱硫剤(1)を−次fIAtI8域に)
へ供給すれば、帥述の反応から脱硫率は高いものとなる
。しかしながら、従来の空気二段燃焼法にそのまま脱硫
剤(7)を供給したのでは、空気二段燃焼は、後流から
過剰の空気を供給して未燃分(還元物質)を完全に燃焼
酸化しており二次燃焼域む)は酸化雰囲気となっている
ために、−火煙焼滅(4)で生成した硫化物の大部分は
再び酸化され、捕捉しmsを、 CaS + s/z Ox  −→ CaO+ SOt
  −・・(Vl)NazS + 8/20!  −→
 NaO+50w  −−61)などの反応により放出
するため、従来の脱硫法とあまり差のない結果となって
いる。
Then, the secondary air (
6), and a desulfurizing agent (desulfurizing agent supply nozzle for supplying υ) is arranged opposite to the fuel nozzle 0). In the combustion method, air is supplied in portions;
The reduction combustion is shown below. In such a reducing atmosphere, CaO+ H,S-→CaS+H*0-=
(1m) NhO+ ToS * Nam5+ru0
...-(5) NhO 1 SO Go + I C-> Na Go s
The main reactions are reactions that produce sulfides such as + sco...
Na1S, CaS, FeS, etc.) are stable even at high temperatures. Therefore, the desulfurization agent (1) was added to the -th fIAtI8 region)
If it is supplied to , the desulfurization rate will be high due to the reaction described above. However, if the desulfurization agent (7) is supplied as is in the conventional two-stage air combustion method, the two-stage air combustion method will completely combust and oxidize the unburned matter (reduced substances) by supplying excess air from the downstream. Since the secondary combustion zone (in the secondary combustion zone) is an oxidizing atmosphere, most of the sulfides generated in the fire and smoke incineration (4) are oxidized again and captured, resulting in CaS + s/z. Ox −→ CaO+ SOt
-...(Vl)NazS + 8/20! −→
Because it is released by a reaction such as NaO+50w--61), the results are not much different from conventional desulfurization methods.

零斃朗は上記欠点をpH訣し得る脱硫を同時に行なう低
NOx燃m法を提供するものである。
Reiro provides a low NOx combustion method that simultaneously performs desulfurization and can eliminate the above-mentioned drawbacks.

すなわち本発明は、火炉に一次燃焼室と二次燃焼室とを
#Ij成し、−火煙焼室で空気比1以下の還元燃焼を行
なわせ、かつ−次燃焼室内の温度を灰分が熔融し線動化
する1度以上に保持し、この−火煙tla室内に脱硫材
であるアルカリを供給して脱硫を行なわせたのち、熔け
た灰分及びfIit貿化合物化合物カリの反応によって
生成し、2硫化物との熔融混合物を一次mm室から取)
出し1次に未燃分を含んだ一次燃焼排ガスを二次燃焼室
へ導き、この二次燃焼室で必要かつ十分な二次空気を供
給して未燃分を完全に鹸化・燃焼させる脱硫を同時に行
なう低NOx @ @法を提供するものである。かがる
方法によると、−次燃焼室内に生じる一次燃焼域を還元
域としつつ、且つ灰が完全に熔融するようなfmlfに
S特しつつ脱硫剤を供給することによって、F1a1g
を効果的に行なうことかでみる。また熔けた灰と硫化物
との混合物を一次m焼室がら抜−出した後、燃a#ガス
を二次燃tlb室に導き、ここで二次空気を供給し未燃
分を完全燃焼させる結果、再び酸化されるような逆反応
を防ぎ、大巾な脱硫率の向上をはかることができる。同
時に、熔けた灰−ζ接触した線部はAshに捕捉され、
蛭−一度を減少できる。tr:NOxの還元は高温はど
その効果は大きく、NOx抑制効果も大きいものとなる
That is, the present invention provides a furnace with a primary combustion chamber and a secondary combustion chamber, - performs reductive combustion at an air ratio of 1 or less in the smoke combustion chamber, and - lowers the temperature in the secondary combustion chamber so that the ash melts. After maintaining the temperature above 1 degree to make it linear, supplying alkali, which is a desulfurization agent, into the fire smoke chamber to perform desulfurization, it is produced by the reaction of the melted ash and the potassium compound, Take the molten mixture with disulfide from the primary mm chamber)
The primary combustion exhaust gas containing unburned matter is led to the secondary combustion chamber, where necessary and sufficient secondary air is supplied to completely saponify and burn the unburned matter for desulfurization. At the same time, it provides a low NOx @ @ method. According to the method, F1a1g is
Let's see if it can be done effectively. After extracting the mixture of melted ash and sulfide from the primary combustion chamber, the combustion a# gas is led to the secondary combustion chamber, where secondary air is supplied to completely burn the unburned matter. As a result, reverse reactions such as re-oxidation can be prevented, and the desulfurization rate can be greatly improved. At the same time, the line part that came into contact with the melted ash-ζ is captured by Ash,
Leech - can be reduced once. tr: The reduction of NOx is more effective at high temperatures, and the NOx suppression effect is also greater.

以下、本発明の一実施例を@8図、鉛4図に基づいて説
明する。鮎8図においてIQは火炉で、その内部には下
向きに傾斜した一次燃焼室(11)と、上向−で垂直の
二次燃焼室−とが形成され、さらに両燃焼室(2)四の
下端間に連通路(至)が形成されている。*記−火煙焼
室東の上端には、tlA#4(ロ)を供給する燃料ノズ
ルに)が下向きに傾斜させて配設してあ)、そして風箱
−を介して前記燃料ノズル四の8秒から一火中気翰を供
給すべく構成しである。
Hereinafter, one embodiment of the present invention will be described based on Figure @8 and Figure 4. In Figure Ayu 8, IQ is a furnace, and inside it there is a downwardly inclined primary combustion chamber (11) and an upwardly vertical secondary combustion chamber. A communication path (to) is formed between the lower ends. *Note: At the upper end of the east side of the fire and smoke combustion chamber, a fuel nozzle that supplies tlA #4 (b) is installed so as to be slanted downward, and the fuel nozzle 4 is connected to the fuel nozzle through a wind box. It is designed to supply Qihan from 8 seconds to 10 seconds.

さらに−次鰹焼室(ロ)の上端には脱硫剤(ト)を0(
給する脱硫剤供給ノズル(6)が設けられ、まtコ下端
には灰及び硫化物の溶融物抜出口(転)が設けられる。
Furthermore, 0 (
A desulfurizing agent supply nozzle (6) is provided to supply the desulfurizing agent, and a melt outlet for ash and sulfide is provided at the lower end of the shaft.

*記二次燃焼室(ロ)の下部には、二次空気(ロ)を供
給する二次空気ノズル四が設けられる。
*A secondary air nozzle 4 for supplying secondary air (b) is provided at the bottom of the secondary combustion chamber (b).

紡記−次S焼*軸で空気比1以下の還元燃焼を行なわせ
、かつ−次11焼室鵠内の温度を灰分が熔融し流動化す
る湿度以上に保持している。この−火煙焼室軸内に脱硫
材(アルカリ)−が脱硫材供給ノズル−から供給され、
脱硫が行なわれる。この−火煙焼室鋳において、熔けた
灰分及び硫黄化合物とアルカリの反応によって生成した
硫化物との熔融混合物0は、熔―物゛抜出ローを通して
取)出され、また未燃分を含んだ一火煙焼排ガスIは、
j!4路軸を通して二次燃焼室−に導びがれる。そして
この二次燃焼室韓で、必要かつ十分な二次空気−を供給
して未燃分を完全に酸化・燃焼させる。
Reductive combustion is carried out at an air ratio of 1 or less in the spinning and firing chamber, and the temperature in the firing chamber (11) is maintained above the humidity at which the ash melts and becomes fluid. Desulfurization material (alkali) is supplied into this fire and smoke combustion chamber shaft from the desulfurization material supply nozzle.
Desulfurization takes place. In this fire-and-smoke furnace casting, the molten mixture of ash and sulfides produced by the reaction of sulfur compounds with alkali is removed from the molten material through a extraction row, and contains unburned matter. Daichi fire smoke exhaust gas I is
j! It is led to the secondary combustion chamber through a four-way shaft. In this secondary combustion chamber, necessary and sufficient secondary air is supplied to completely oxidize and burn the unburned matter.

以上述べた本発明の脱硫を同時に行なう低動燃焼法によ
ると、−次燃焼室内に生じる一次燃焼域を還元域としつ
つ、且つ灰が完全に熔融するような温度に保持しつつ脱
硫剤を供給することによって、脱硫を効果的に行なうこ
とができる。また熔けr:駅と硫化物との混合物を一次
燃焼室から抜−出した優、燃m排ガスを二次燃焼室に導
き、ここで二次空気を供給し未燃分を完全燃焼させる結
果、再び酸化さ・れるような逆反応を防ぎ、大巾な脱硫
率の向上をはかることがで曇る。同時に、熔けた灰に接
触した煤塵はAshにl@捉され、謀塵濃度を減少でき
る。またNow O還元は高温はどその効果は大−<、
NOx抑制効果も大きいものとなる。1
According to the low dynamic combustion method of the present invention that simultaneously performs desulfurization as described above, the primary combustion zone generated in the secondary combustion chamber is used as the reduction zone, and the desulfurizing agent is supplied while maintaining the temperature at which the ash is completely melted. By doing so, desulfurization can be carried out effectively. In addition, the mixture of sulfide and sulfide is extracted from the primary combustion chamber, and the exhaust gas is led to the secondary combustion chamber, where secondary air is supplied and the unburned components are completely combusted. It prevents reverse reactions such as re-oxidation and greatly improves the desulfurization rate. At the same time, the soot dust that has come into contact with the melted ash is captured by the ash, and the dust concentration can be reduced. Also, Now O reduction is more effective at high temperatures.
The NOx suppression effect will also be great. 1

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

111図は炉内湿度と脱硫率oH係を示すグラフ図、@
意図は従来の一例を示す縦断面図、第8図は本発明の一
実施内を示す縦断面図、第4図は本発明と従来例との当
鳳比と脱硫率との11gkを比較ど(2)・一連通路、
榊・・・燃料、Ql−燃料ノズル、(至)・・・風箱、
仲−=−火中気、(至)・−・脱硫剤、(6)・・・脱
硫剤供給ノズル、(転)・・・溶融物抜出口、(2)・
−二次空気、@・・・二次空気ノズル 代理人 森本義弘 第1図 °°f    M ii。。、−4 炉内温度(0C) 第2図 〜 t: 第゛3図 4 (%)ホ蔚連 手続補正書(自船 1.事件の表示 昭和57 片持 許 願第  71979   月2、
発明の名称 脱硫を同時に行なう低NOx燃焼法 3補正をする者 事件との関係  特許出願人 名称 (511) El立造船株式会社4、代 理 人 氏名  (680g)弁理上前 本 義 弘5    
     の日付(発送日)昭和    年    月
    日 6補正により増加する発明の数 7、補正の対象 明細書の発明の詳細な説明の榴 明細台の特許請求の範囲の欄 8、補正の内容 別紙の通り 2、明細書の発明の詳細な説明の楠 0第2頁第7行目 rcao+82+1/20zJとあるt jcao +
502 +1/202 Jと訂正する。 O第2頁第19行目 「脱硫材供給ノズル」とあるを「脱硫剤供給ノズル」と
訂正する。 O第4頁第7行目、第6頁第4行目 「脱硫材」とあるを「脱硫剤」とU圧する。 2.1HI許錆求の範囲 1、 火炉に一火煙焼富と二次燃焼家とを構成し、−次
艦ImIMで空気比1以下の還元継続を行なわせ、かつ
−火煙焼富内の温度を灰分が熔融し流動化する温度以上
に保持し、この−火燃焼室内に脱硫lであるアルカリを
供給して脱硫を行なわせ友のち、熔けた灰分及び硫黄化
合物とアルカリの反15によって生成した硫化物との熔
融混合物を一次#!続室から取シ出し、次に未燃分を含
んだ一火煙焼紳ガスを二火煙**へ導き、とに行なう低
NOx燃焼法。
Figure 111 is a graph showing the relationship between furnace humidity and desulfurization rate oH, @
The intention is a vertical cross-sectional view showing an example of the conventional example, FIG. 8 is a vertical cross-sectional view showing one implementation of the present invention, and FIG. (2)・Series of passages,
Sakaki...fuel, Ql-fuel nozzle, (to)...wind box,
Medium = - Fire Medium, (To) -- Desulfurizing agent, (6) Desulfurizing agent supply nozzle, (Transfer)... Melt extraction port, (2)
-Secondary air, @...Secondary air nozzle agent Yoshihiro Morimoto Figure 1°°f M ii. . , -4 Temperature inside the furnace (0C) Figure 2~t: Figure 3 4 (%) Written amendment to the procedure (Own ship 1. Indication of the incident 1982 Cantilever Permit Application No. 71979, 2nd of May,
Name of the invention Low NOx combustion method that simultaneously performs desulfurization 3 Relationship with the amended case Name of patent applicant (511) El Ritsuzosen Co., Ltd. 4 Name of agent (680g) Patent attorney Yoshihiro Moto 5
date (shipment date) Showa year month/day 6. Number of inventions increased by the amendment 7. Claims column 8 of the detailed description of the invention in the specification subject to the amendment, content of the amendment as shown in the attached sheet. 2. Kusunoki 0, page 2, line 7 of the detailed description of the invention in the specification rcao+82+1/20zJ t jcao +
Correct it to 502 +1/202 J. On page 2, line 19, "desulfurizing agent supply nozzle" is corrected to "desulfurizing agent supply nozzle." Page 4, line 7, page 6, line 4, ``Desulfurizing agent'' is changed to ``Desulfurizing agent''. 2.1 Scope of HI Permissible Rubbing 1. Configure the furnace with a first fire, smoke, and secondary combustion chamber, - Continuous reduction with an air ratio of 1 or less in the next ship, ImIM, and - Temperature within the fire, smoke, and secondary combustion chamber. is maintained above the temperature at which the ash melts and becomes fluidized, and an alkali, which is desulfurization, is supplied into the combustion chamber to perform desulfurization. # Primary molten mixture with sulfide! A low NOx combustion method is carried out in which the gas is taken out from the continuation chamber, and then the first-flame combustion gas containing unburned components is led to the second-flame smoke**.

Claims (1)

【特許請求の範囲】 L 火炉に一次燃焼室と二次燃焼室とを構成し。 −火煙焼室で空気比1以下の還元燃焼を行なオ〕せ、か
つ−火燃焼室内のa!変を灰分が熔融し泳動化する湿度
以上に保持し、この−火燃焼室内に脱硫材であるアルカ
リを供給して脱硫を行なわせたのち、熔けた灰分及び硫
黄化合物とアルカリの反応によって生成した硫化物との
熔M!混合物を一次燃焼室から取り出し、次に未燃分を
含んだ一次燃焼排ガスを二次燃焼室へ導き、この二次燃
焼室で必要かつ十分な二次空気を供給して未燃分々完全
に酸化・燃焼させる脱硫を同時に行なう低NOx燃焼法
[Claims] L: A furnace includes a primary combustion chamber and a secondary combustion chamber. - Perform reduction combustion with an air ratio of 1 or less in the fire-smoke combustion chamber, and - a! in the fire-smoke combustion chamber. The sulfur compound is maintained at a humidity higher than that at which the ash melts and migrates, and an alkali, which is a desulfurization agent, is supplied into the combustion chamber to perform desulfurization. Melt M with sulfide! The mixture is taken out from the primary combustion chamber, and then the primary combustion exhaust gas containing unburned components is guided to the secondary combustion chamber, where the necessary and sufficient secondary air is supplied to completely remove the unburned components. A low NOx combustion method that simultaneously performs desulfurization through oxidation and combustion.
JP57071979A 1982-04-28 1982-04-28 Combustion with low nox performing desulfurization simultaneously Granted JPS58190607A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57071979A JPS58190607A (en) 1982-04-28 1982-04-28 Combustion with low nox performing desulfurization simultaneously

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57071979A JPS58190607A (en) 1982-04-28 1982-04-28 Combustion with low nox performing desulfurization simultaneously

Publications (2)

Publication Number Publication Date
JPS58190607A true JPS58190607A (en) 1983-11-07
JPS6137522B2 JPS6137522B2 (en) 1986-08-25

Family

ID=13476086

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57071979A Granted JPS58190607A (en) 1982-04-28 1982-04-28 Combustion with low nox performing desulfurization simultaneously

Country Status (1)

Country Link
JP (1) JPS58190607A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61208411A (en) * 1985-03-14 1986-09-16 Hitachi Zosen Corp Two-stage combustion method to suppress nox development with simultaneous desulphurization
WO1994020788A1 (en) * 1993-03-08 1994-09-15 Dykema Owen W COAL COMBUSTION PROCESS FOR SOx AND NOx CONTROL
EP0650018A2 (en) * 1993-10-20 1995-04-26 Florida Power Corporation Desulfurization of carbonaceous fuels

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61208411A (en) * 1985-03-14 1986-09-16 Hitachi Zosen Corp Two-stage combustion method to suppress nox development with simultaneous desulphurization
JPH044484B2 (en) * 1985-03-14 1992-01-28
WO1994020788A1 (en) * 1993-03-08 1994-09-15 Dykema Owen W COAL COMBUSTION PROCESS FOR SOx AND NOx CONTROL
EP0650018A2 (en) * 1993-10-20 1995-04-26 Florida Power Corporation Desulfurization of carbonaceous fuels
EP0650018A3 (en) * 1993-10-20 1995-09-27 Florida Power Corp Desulfurization of carbonaceous fuels.

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