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JPS5944513A - Nitrogen oxide suppressing operation of incinerator - Google Patents

Nitrogen oxide suppressing operation of incinerator

Info

Publication number
JPS5944513A
JPS5944513A JP57154087A JP15408782A JPS5944513A JP S5944513 A JPS5944513 A JP S5944513A JP 57154087 A JP57154087 A JP 57154087A JP 15408782 A JP15408782 A JP 15408782A JP S5944513 A JPS5944513 A JP S5944513A
Authority
JP
Japan
Prior art keywords
exhaust gas
incinerator
combustion
generation
nitrogen oxides
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
Application number
JP57154087A
Other languages
Japanese (ja)
Inventor
Eiroku Kamiyama
神山 栄六
Shinichiro Ando
真一郎 安藤
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 JP57154087A priority Critical patent/JPS5944513A/en
Publication of JPS5944513A publication Critical patent/JPS5944513A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/002Incineration of waste; Incinerator constructions; Details, accessories or control therefor characterised by their grates
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B7/00Combustion techniques; Other solid-fuel combustion apparatus
    • F23B7/002Combustion techniques; Other solid-fuel combustion apparatus characterised by gas flow arrangements
    • F23B7/007Combustion techniques; Other solid-fuel combustion apparatus characterised by gas flow arrangements with fluegas recirculation to combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/00001Exhaust gas recirculation

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)

Abstract

PURPOSE:To suppress the generation of nitrogen oxides by a method wherein the exhaust gas, which is discharged from the incinerator and cooled, is circulated and fed at positions higher than fire grates within the incinerator. CONSTITUTION:In nitrogen oxides suppressing operation, primary combustion air fed from the undersides of the fire grates 2 is throttled as few as possible in order to accelerate the gasification of the refuses onto the fire grates 2 and consequently suppress the generation of nitrogen oxides. In addition, a part of the exhaust gas cooled and dust-collected in blown into the incinerator 1 through exhaust gas blowing-in nozzles 3 by means of an exhaust gas circulating ventilator 10 in order to enable to accomplish slow and complete combustion under low oxygen concentration due to the effect of the direct cooling of combustion flame, mixing and stirring of combustion gas, resulting in enabling to control the exhaust gas temperature in a predetermined range and to effectively suppress the generation of nitrogen oxide.

Description

【発明の詳細な説明】 本発明は焼却fi O)窒素酸化物抑制運1z、法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for incinerating nitrogen oxides.

従来の焼却炉におい°Cは、炉出Elにおけるill・
気ガスffa1反をF9i定の111u囲内に調j≧わ
するため1こ、火格子の下側から送入する燃焼用−次空
気または冷却用空気の↓jUをi、’a jffil 
L/”Cいたが、空気の過剰送入1こより排気ガス中の
酸素濃度が高まり、窒素酸化物の発生S、(が多いとい
う問題があった。
In a conventional incinerator, °C is ill
In order to adjust the air gas ffa1 to within 111u of F9i, ↓jU of the combustion air or cooling air introduced from the bottom of the grate is i, 'a jffil.
However, there was a problem in that the oxygen concentration in the exhaust gas increased due to the excessive supply of air, and a large amount of nitrogen oxides were generated.

そこで、都市ごみ;φ゛ム却炉運転方法としC1燃焼−
次空気中へ冷却後の排気ガスを混入させ、火格子の下側
から送入ラーる方法が提案さイ[て°いるが、このよう
な方法では、窒素酸化物の発生を抑制する効果はあるも
のの、排気ガス中のA(%食成分(Hc l 。
Therefore, we decided to operate the municipal waste incinerator using C1 combustion.
A method has been proposed in which the cooled exhaust gas is mixed into the air and fed from the bottom of the grate, but this method is not effective in suppressing the generation of nitrogen oxides. Although there is A (% edible component (Hc l ) in exhaust gas.

:)Ox )により人格子等が倉n*するという問題が
あった。
:)Ox) caused the problem that the human lattice, etc. would be damaged.

本発明は上記従来の入点を解消するものであC)、炉出
1」1こおけるリド気ガス温度を所定の11包囲内に調
節でき、しかも商い窒素酸化物抑制効果を4」するもの
であI)ながら、火4′8子等を腐食さ・U′る恐れの
ない焼却炉の窒素酸、化物抑制運転法を得ることを・目
的とする。
The present invention solves the above-mentioned conventional problems, and C) allows the lid gas temperature at the furnace outlet to be adjusted to within a predetermined 11% range, and also achieves a nitrogen oxide suppression effect of 4". However, it is an object of the present invention to obtain a method of operating an incinerator that suppresses nitrogen acids and compounds without the risk of corroding or damaging the flames, etc.

と記目的を達するため、本発明のji17i却炉の窒素
L11Σ化物抑制運転法は、焼却炉から排出されかつ冷
却された十ノ1気ガスを、0■口記却炉内部の火格子よ
I)も上部に楯鍔1送入する構成である。
In order to achieve the purpose described above, the nitrogen L11Σ oxide suppression operation method of the ji17i incinerator of the present invention is to transfer the cooled gas discharged from the incinerator to the grate inside the incinerator. ) also has a structure in which one tatetsuba is inserted into the upper part.

かかるイIXI成によると、焼却炉内に循環送入さ9る
排気ガスによI)、燃焼火炎を直接冷却でき、しかも燃
焼ガスの混合・攪拌効果を高めて燃焼ガス中の未然分を
完全燃焼さぜることかできるので、炉出口1こおける排
気ガス温度を191定の範囲内に調ii:+できると共
に、窒素酸化物の発生を良好に抑制できる。まjコ、J
JI気カスを焼却ジノ1内部の火格子よI)も11部1
こ循17rf d<人するので、排気ガス中の6食成ヅ
Jによる人イ′ハ子等0月「・5食が発生ずること]j
ない、。
According to this IXI configuration, the combustion flame can be directly cooled by the exhaust gas circulated into the incinerator, and moreover, the mixing and stirring effect of the combustion gas is enhanced to completely remove unused components in the combustion gas. Since combustion can be carried out, the temperature of the exhaust gas at one outlet of the furnace can be adjusted within a constant range of 191, and the generation of nitrogen oxides can be suppressed well. Mako, J
Incineration of JI scum The grate inside Jino 1 I) also part 11 1
Circulation 17rf d<Since there are 6 meals in the exhaust gas, 5 meals will occur]j
do not have,.

以上、本:)lj II、lの一実hiij例についで
、N曲に基づい°C説明する。
That's it for the book:) lj II, I will explain one actual hiij example based on N songs.

C1Δ1図において、(])は例えば都?I C、/7
等の焼却炉であり、このヅρ゛6却〃−1(1)の内部
1こ(J1複数の火第1)子(21が設置1′3さイし
Cいると共に、この人Fifr子(2)よI〕も上部1
S側のe目J+’+ξta気ガス吹込みノズル(3)が
設置されごいる。(4)は1)ロ記;Jム動炉(1)内
へl+ii Iljごみ1ソ・を投入するtこめの投入
ホッパ、(旬はI30記;晶動炉(1)から(、小出さ
れたJ、IIIIスを冷却)−るガス冷却長1ζ1゛、
(6)は(りbえばごみビットから吸引したJjt!+
 Jj/l川−次菟気をIff ttL!h′ム却炉(
1)動炉給する押込送J’J’111..1−1(7)
はIU。
In the C1Δ1 diagram, (]) is, for example, capital? IC, /7
This is an incinerator, and inside this ヅρ゛6 〃-1(1) 1 (J1 plural fire first) child (21 is installed 1'3 times C), this person Fifr child. (2) Yo I] is also upper part 1
The e-th J+'+ξta air gas blowing nozzle (3) on the S side is installed. (4) is written in 1) B; t-loading hopper that throws 1 piece of garbage into the Jmu mower (1); gas cooling length 1ζ1゛,
(6) Jjt sucked from the garbage bit!+
Jj/l river - If ttL! h'mu furnace (
1) Force feeding J'J'111. .. 1-1(7)
is IU.

気集塵機、(8)は訪中jl’i’を訳1偵、(9)は
力)゛(欠、(III LL J〕1気ガス循v;1通
風(、,4である。
Air dust collector, (8) means visit to China jl'i', (9) means force) ゛(missing, (III LL J) 1 air gas circulation v; 1 ventilation (,, 4).

投入ホッパ(4)から焼却炉(1)内へ送゛り込まれた
ごみは、押込迭hL Q (+;Jにより火4’+l’
r子(2)の下側から送入される燃焼用訳気によつ°C
1火柘子(2)士で焼却される。燃焼排気ガスはガス冷
却装置1′:’i (!ilによI)約300°Cまで
冷却され、Ca(OH)z  I)末を添加さI’tて
1u気集塵機(7)で除JJ’lされIコ後、誘引j1
n風4ffa (8)及び煙突(9)を経由し゛C人気
中に放出される。Th2 j、、酸fし物抑制連+li
i< II!jは、火格子(2)の下側から送入するヅ
然焼用−次空気を神;方縁?)込み、火格子(2) J
:C2ごみのガス化を促進しC’4L累酸化物0)生成
を抑える。
The garbage sent into the incinerator (1) from the input hopper (4) is pushed into the incinerator (+;
Due to the combustion air introduced from the bottom of the cylinder (2) °C
Incinerated on 1st fire (2). The combustion exhaust gas is cooled to approximately 300°C by a gas cooling device 1':'i (!il), added with Ca(OH) powder, and removed by a 1u air dust collector (7). After being JJ'l, I was invited j1
It is released into the air via the n wind 4ffa (8) and the chimney (9). Th2 j,, acid famine suppression +li
i< II! J is the direction of air for firing that is introduced from the bottom of the grate (2). ) included, grate (2) J
:Promotes the gasification of C2 waste and suppresses the generation of C'4L accumulated oxides.

そし°C1冷却・除塵後の1j:2気ガス0)  !i
l:を排気力゛ス循j′8%tffll風tKA Ot
) +ごよりυ1°気ガス吹込みノズル(3)力・ら焼
却炉(1)内へ吹込み、火炎を冷却して炉出口Q)排気
ガス温度を1i1i定の範囲内に−11,1節すると同
111こ、カニ(モ)?:I、ガスを混合・j%ノ゛I
 L、 ’r完全燃焼さ一シ1′る。なお一時的には、
]J1気ガスの全部をか“2.動炉(1)内へ吹込むこ
とも(+きる。
Then °C1 after cooling and dust removal 1j: 2 gas 0)! i
l:Exhaust force circulates j'8%tffll windtKA Ot
) Air is blown into the incinerator (1) from the +υ1° gas blowing nozzle (3) to cool the flame and reduce the exhaust gas temperature to within the specified range -11,1. If you say the same 111, crab (mo)? :I, mix gas・j%ノ゛I
L, 'r Complete combustion. However, temporarily,
] It is also possible to blow all of the J1 gas into the furnace (1).

このように、送入排気ガスによる燃焼炎の直接冷却及び
焦り5′らガスの混合・17目下効果にJ: 11 、
低酸素一度士での19)るやかな完全燃焼をJ2G成で
きるυ〕で、炉出口1こ4.5りる(J+気ガスの?L
if度を)すl定範囲に調j71】でき、しかも第2図
実htit (:Oでホずまうに、屋累酸化物の発生を
効果的に抑制することができる。
In this way, due to the direct cooling of the combustion flame by the incoming exhaust gas and the mixing of the impatience gas and the 17 present effect, J: 11,
19) Smooth complete combustion can be achieved with low oxygen temperature υ], and 1 liter at the furnace outlet is 4.5 liters (J + ?L of gas)
The temperature (if) can be adjusted within a certain range, and the generation of accumulated oxides can be effectively suppressed as shown in FIG.

まtこ排気ガスケ焼却ル゛j(1)内部こり火格子(2
)よl)も上部に循環送入するので、火格子(2)等が
(jI気気ガス中x)S食成分によI)6食される恐れ
(40(い。なJjfl、1)2図はター1出口1こお
りる排気ガス111a ICI b; t+ r; o
o(jの時における一次?どシ1.比と窒素1t(−化
物(4月+2との関係の説明図で、Sδ(1li110
J窒、・)・ミ1俊化物濃度、(δ’j 1lil11
は一次空気比であり、一点鍾”J X、’4< (ロ)
は、従来方IJ、 lζ二J、マい゛Cヅ戸出出11部
二次々!気を多j、iEに送入し°c /、a r−リ
−!4 jjj L/た場合を力くし°Cいる1、 以上説明しtコように、本発明によれば、たと、動炉内
にl111Jζtjx人されるjノ1゛気ガスにま’l
 、jtl、’焼入炎を直接冷却でき、しかも燃焼ガス
の1J11台・(1シ、拌効果を几め゛C燃焼ガスをゆ
るやかに:、“「二仝燃1t!”f:Iさけることがで
きるので、炉出El lこおりる」)1゛気ガス温1y
:を所定の範ll−11円にXt1i1節し得るど其に
、51弓冒ljj化物の発生を良μ■゛に抑1jli 
シイする。よた、ノl(4;f、ガスを;、1ン、J、
11炉内部の火A・1”′l−1’ J″1)も上1S
l−に循1!、l送入゛Jるので、排気ガス中のに・)
食成力による火413子tj・のA”j IIIシかづ
1」生する恐れl;L lrい。
Exhaust gas incineration method (1) Internal fire grate (2)
) and l) are also circulated to the upper part, so there is a risk that the grate (2) etc. will be eaten by (jI x)S food components in the air gas (40 (I.na Jjfl, 1) Figure 2 shows the exhaust gas 111a flowing from the ter 1 outlet 111a ICI b; t+ r; o
This is an explanatory diagram of the relationship between the primary?
J nitrogen, ・)・Mi1 atomide concentration, (δ'j 1lil11
is the primary air ratio, and one point "JX,'4< (b)
Is the conventional IJ, lζ2J, and the 11 parts of the Mai Czudo, one after the other! Send the energy into the iE, °c/, a r-li-! According to the present invention, as explained above, if l111Jζtjx people are placed in the furnace, the gas is
, jtl, 'Can directly cool the quenching flame, and can reduce the amount of combustion gas by 1J11 units. Since the temperature of the gas coming out of the furnace is 1y,
: can be set to a predetermined range ll-11 yen, and the occurrence of 51 bow attack ljj monsters can be suppressed to a good μ■゛.
Shy. Yota, nol (4; f, gas;, 1 n, J,
11 The fire inside the furnace A・1"'l-1'J"1) is also upper 1S
Circulation 1 to l-! , l is injected into the exhaust gas.)
There is a risk that fire will occur due to the power of food production.

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

図面は本発明の一すこ71j1.lイタ)を力、し、第
1 r?J l、L焼却システムの肌1!lfi (?
lS成図、2132図(よ従来力Vミとσ〕1シ較1こ
おりる窒素識化物Jlll jlil効果の説明1スで
ある。 (1)°°゛焼ノズ1ノ炉、(2)・・・火、(テ)子
、(3)・・・j711公tガス1欠iΔIブノズル、
(5戸・・ガス冷却装置、叫・・・1)1気カスii+
“i D”i ij[1Ali4. <6 u 代理人   森 本 颯 弘 (オしさt%ζ1t6フWON
The drawings are part of the present invention 71j1. The first r? J l, L incineration system skin 1! lfi (?
lS diagram, Figure 2132 (conventional force Vmi and σ) is an explanation of the nitrogen chloride Jllll jlil effect that is 1 sq. ...Tuesday, (te)ko, (3)...j711 public t gas 1 lack iΔI nozzle,
(5 houses...gas cooling system, screaming...1) 1ki kasu ii+
“i D”i ij[1Ali4. <6 u Agent Hiroshi Morimoto (Oshisat%ζ1t6fu WON

Claims (1)

【特許請求の範囲】[Claims] 1、焼却炉からJul出されかつ冷却された排気ガスを
、06記焼却炉内部の火格子よ?)も上部に循環送入す
ることを+14.、徴とする焼却り1の窒素酸化物抑制
運転法。
1. Transfer the cooled exhaust gas discharged from the incinerator to the grate inside the incinerator. ) is also circulated to the upper part +14. , a nitrogen oxide suppression operation method for incineration 1.
JP57154087A 1982-09-03 1982-09-03 Nitrogen oxide suppressing operation of incinerator Pending JPS5944513A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57154087A JPS5944513A (en) 1982-09-03 1982-09-03 Nitrogen oxide suppressing operation of incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57154087A JPS5944513A (en) 1982-09-03 1982-09-03 Nitrogen oxide suppressing operation of incinerator

Publications (1)

Publication Number Publication Date
JPS5944513A true JPS5944513A (en) 1984-03-13

Family

ID=15576606

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57154087A Pending JPS5944513A (en) 1982-09-03 1982-09-03 Nitrogen oxide suppressing operation of incinerator

Country Status (1)

Country Link
JP (1) JPS5944513A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60251308A (en) * 1984-05-25 1985-12-12 Kubota Ltd Method of operating incinerator
JPS61204139U (en) * 1985-06-05 1986-12-23
EP0497089A2 (en) * 1991-02-01 1992-08-05 NOELL Abfall- und Energietechnik GmbH Temperature regulation method for incineration plants
EP0621448A1 (en) * 1993-04-20 1994-10-26 MARTIN GmbH für Umwelt- und Energietechnik Method for the combustion of fuels, particularly waste
WO1997004274A1 (en) * 1995-07-20 1997-02-06 Forschungszentrum Karlsruhe Gmbh Method of incinerating material
EP0846917A3 (en) * 1996-12-03 1999-06-09 MARTIN GmbH für Umwelt- und Energietechnik Process and apparatus for the production and use of a gas from waste products
US6138587A (en) * 1995-05-05 2000-10-31 Deutsche Babcock Anlagen Gmbh Process and furnace for burning refuse
WO2013147030A1 (en) * 2012-03-29 2013-10-03 日立造船株式会社 Combustion driving method in incinerator
WO2014132532A1 (en) * 2013-02-28 2014-09-04 日立造船株式会社 Recirculated exhaust gas supply control method for stoker furnace, and stoker furnace
JP2015169405A (en) * 2014-03-10 2015-09-28 日立造船株式会社 Angle variable type gas blowing-in device
EP3076076A1 (en) * 2015-03-30 2016-10-05 Martin GmbH für Umwelt- und Energietechnik Method for grate firings combustion management and grate firing
CN105008802B (en) * 2013-02-28 2016-11-30 日立造船株式会社 The EGR gas supply control method of grate furnace and grate furnace

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4823834U (en) * 1971-07-26 1973-03-19
JPS54120423A (en) * 1978-03-11 1979-09-19 Kubota Ltd Nox reducing method for incinerator exhaust gas

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4823834U (en) * 1971-07-26 1973-03-19
JPS54120423A (en) * 1978-03-11 1979-09-19 Kubota Ltd Nox reducing method for incinerator exhaust gas

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60251308A (en) * 1984-05-25 1985-12-12 Kubota Ltd Method of operating incinerator
JPS61204139U (en) * 1985-06-05 1986-12-23
EP0497089A2 (en) * 1991-02-01 1992-08-05 NOELL Abfall- und Energietechnik GmbH Temperature regulation method for incineration plants
EP0621448A1 (en) * 1993-04-20 1994-10-26 MARTIN GmbH für Umwelt- und Energietechnik Method for the combustion of fuels, particularly waste
US6138587A (en) * 1995-05-05 2000-10-31 Deutsche Babcock Anlagen Gmbh Process and furnace for burning refuse
WO1997004274A1 (en) * 1995-07-20 1997-02-06 Forschungszentrum Karlsruhe Gmbh Method of incinerating material
US6038988A (en) * 1995-07-20 2000-03-21 Forschungszentrum Kalsruhe Gmbh Waste incinerating method and apparatus with counter-current exhaust gas flow
EP0846917A3 (en) * 1996-12-03 1999-06-09 MARTIN GmbH für Umwelt- und Energietechnik Process and apparatus for the production and use of a gas from waste products
WO2013147030A1 (en) * 2012-03-29 2013-10-03 日立造船株式会社 Combustion driving method in incinerator
CN104334971A (en) * 2012-03-29 2015-02-04 日立造船株式会社 Combustion driving method in incinerator
JPWO2013147030A1 (en) * 2012-03-29 2015-12-14 日立造船株式会社 Combustion operation method in incinerator
CN104334971B (en) * 2012-03-29 2016-11-30 日立造船株式会社 The burning method of operation of incinerator
WO2014132532A1 (en) * 2013-02-28 2014-09-04 日立造船株式会社 Recirculated exhaust gas supply control method for stoker furnace, and stoker furnace
JP2014167353A (en) * 2013-02-28 2014-09-11 Hitachi Zosen Corp Stoker furnace recirculated exhaust gas supply control method and stoker furnace
CN105008802A (en) * 2013-02-28 2015-10-28 日立造船株式会社 Recirculated exhaust gas supply control method for stoker furnace, and stoker furnace
CN105008802B (en) * 2013-02-28 2016-11-30 日立造船株式会社 The EGR gas supply control method of grate furnace and grate furnace
JP2015169405A (en) * 2014-03-10 2015-09-28 日立造船株式会社 Angle variable type gas blowing-in device
EP3076076A1 (en) * 2015-03-30 2016-10-05 Martin GmbH für Umwelt- und Energietechnik Method for grate firings combustion management and grate firing
US10753604B2 (en) 2015-03-30 2020-08-25 Martin Gmbh Fuer Umwelt-Und Energietechnik Method for the combustion management in firing installations and firing installation

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