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JPS5844281B2 - Nenshiyouhouhou - Google Patents
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JPS5844281B2 - Nenshiyouhouhou - Google Patents

Nenshiyouhouhou

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Publication number
JPS5844281B2
JPS5844281B2 JP50122901A JP12290175A JPS5844281B2 JP S5844281 B2 JPS5844281 B2 JP S5844281B2 JP 50122901 A JP50122901 A JP 50122901A JP 12290175 A JP12290175 A JP 12290175A JP S5844281 B2 JPS5844281 B2 JP S5844281B2
Authority
JP
Japan
Prior art keywords
combustion
exhaust gas
moisture
water
fuel
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
JP50122901A
Other languages
Japanese (ja)
Other versions
JPS5248133A (en
Inventor
勝之 川口
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP50122901A priority Critical patent/JPS5844281B2/en
Publication of JPS5248133A publication Critical patent/JPS5248133A/en
Publication of JPS5844281B2 publication Critical patent/JPS5844281B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はクリーン燃料の燃焼を効率よく行なうために、
総合的なコントロールを行なう方法に関する。
[Detailed Description of the Invention] In order to efficiently burn clean fuel, the present invention
Concerning methods for comprehensive control.

クリーンエネルギーとして注目されているLNG(液化
天然ガス)、LPG(液化石油ガス)または水素は、硫
黄その他の腐食成分を含まないので、これらを燃料とす
る原動機や定置用燃焼装置においては、排ガス湿度を十
分低く設計して熱サイクルの効率を大きくすることが可
能である。
LNG (liquefied natural gas), LPG (liquefied petroleum gas), and hydrogen, which are attracting attention as clean energy, do not contain sulfur or other corrosive components, so in prime movers and stationary combustion equipment that use these as fuel, exhaust gas humidity can be reduced. It is possible to design the temperature to be sufficiently low to increase the efficiency of the thermal cycle.

しかし、これらの燃料はその排ガス中に多量の水分を含
むので(LNG約17容量饅、水素約34容量%)、排
ガス温度をあまり低く抑えると水分が凝縮して水となり
白煙が発生する。
However, since these fuels contain a large amount of moisture in their exhaust gas (LNG: about 17 volumes, hydrogen: about 34% by volume), if the exhaust gas temperature is kept too low, the moisture will condense and become water, producing white smoke.

筐た、この場合には排ガス温度が低いので排煙の浮力上
昇高さが小さくなり、排煙拡散の点からみても好筐しく
ない。
In this case, since the exhaust gas temperature is low, the buoyancy rise height of the flue gas is small, and the housing is not favorable from the viewpoint of exhaust smoke diffusion.

ところで近年、原動機の設置場所は種々の制約を受け、
立地条件によっては補給水あるいは機内用水の確保が困
難になりつつあり、将来の原動機の増加に伴い益々この
傾向に拍車をかけている。
However, in recent years, the installation location of the prime mover has been subject to various restrictions.
Depending on the location, it is becoming difficult to secure make-up water or on-board water, and this trend will only accelerate as the number of prime movers increases in the future.

筐たLNGや水素燃料の場合、クリーンエネルギーとは
いってもNOxを相当量に排出し、白煙と同時K N
Ox対策を取入れることが必須となる。
In the case of cased LNG and hydrogen fuel, although they are clean energy, they emit a considerable amount of NOx and produce white smoke and KN at the same time.
It is essential to take measures against Ox.

更に水素燃料の場合は輸送管および水素燃料機器類材料
の水素脆化、家庭用機器として使用する場合は特に爆発
範囲、燃焼速度が極めて大きいこと、および着火エネル
ギーが小なることが実用化の障害となってふ・す、これ
らを制御する技術の開発が要望されている。
Furthermore, in the case of hydrogen fuel, hydrogen embrittlement of transportation pipes and hydrogen fuel equipment materials, especially when used as household equipment, the explosion range, extremely high combustion speed, and low ignition energy are obstacles to practical application. Therefore, there is a demand for the development of technology to control these.

本発明者等は上記のような問題点を解決するために次の
ことを目的として研究を重ねた。
In order to solve the above-mentioned problems, the present inventors have carried out research aimed at the following.

1)排ガス温度を低く抑え、サイクルの熱回収率をよく
する。
1) Keep the exhaust gas temperature low and improve the heat recovery rate of the cycle.

2)排ガスの白煙化を防止する。2) Preventing exhaust gas from turning into white smoke.

3)新たなエネルギーを必要としない水分回収(遣水方
法) 4)排ガスのNOxの制御 5)燃え易い燃料の燃焼特注の制御(爆発範囲、燃焼速
度、着火エネルギーなど) 6)燃焼用機器類材料の水素脆化の防止 発明者は、クリーン燃料の場合よく燃焼管理筐たは処理
された排ガスは、そのま1酸素絶縁不活性ガスとして材
用できることに着目した。
3) Moisture recovery that does not require new energy (water supply method) 4) Control of NOx in exhaust gas 5) Customized control of combustion of easily flammable fuels (explosion range, combustion speed, ignition energy, etc.) 6) Combustion equipment materials Prevention of Hydrogen Embrittlement The inventor noticed that in the case of clean fuels, exhaust gas that has been treated in a combustion management chamber or treated can be directly used as an oxygen-insulating inert gas.

例えば水素燃焼の場合、理論燃焼排ガスはN2 とH2
0のみからなる。
For example, in the case of hydrogen combustion, the theoretical combustion exhaust gas is N2 and H2
Consists only of 0.

N20をINm″/Nm3とした場合。理論空気量は2
.38 Nms/Nm”、N2は1.88Nm″/Nm
3となるから排ガス中のN2とN20の合計は2.88
N m3/N m3となる。
When N20 is INm″/Nm3, the theoretical air amount is 2
.. 38 Nms/Nm", N2 is 1.88 Nm"/Nm
3, so the total of N2 and N20 in the exhaust gas is 2.88
N m3/N m3.

またLNGの場合、その排ガス中の成分は、大略N27
2%、H2O17優、CO28%、023条となる。
In the case of LNG, the components in the exhaust gas are approximately N27
2%, H2O 17%, CO28%, Article 023.

そこでまず1)水分回収装置を設置して排ガス中の水分
を回収すると同時に熱回収を行なうことを考えた。
Therefore, we first considered 1) installing a moisture recovery device to recover moisture from exhaust gas and at the same time recover heat.

次いで2)水分を除去した殆んど純粋なN2 ガスの一
部を燃料ガス中に循環させて流量を調節したり、回収水
の一部を高温燃焼領域に噴射して混合燃焼させることに
よりa)効果的な排ガス中のNOxの低減、b)燃焼器
機材の水素脆化の防止、C)燃え易い燃料の燃焼特性の
制御等、総合的なコントロールを行なうことを考えた。
2) by circulating a portion of the almost pure N2 gas from which moisture has been removed into the fuel gas to adjust the flow rate, or by injecting a portion of the recovered water into the high temperature combustion zone for mixed combustion; The idea was to perform comprehensive control such as a) effective reduction of NOx in exhaust gas, b) prevention of hydrogen embrittlement of combustor equipment, and c) control of the combustion characteristics of easily flammable fuel.

即ち、本発明はこのような水分回収と、それに伴う排ガ
ス中の有効な不活性ガスの純度を高め、これを再循環し
て公害成分の制御、並びに燃焼特性の制御を行なう総合
的な排ガス利用無公害燃焼とエネルギー回収との組合せ
システムに関し、燃焼して比較的多量の水を生成する燃
料を燃焼させる系において、該燃料の燃焼排ガス通過部
に水分回収装置を設置して水分を回収すると同時に、そ
の水分のうち一部釦よび前記水分回収装置の下流側の燃
焼排ガスの一部を前記燃料を燃焼させる燃焼室に再循環
することを特徴とする燃焼方法を骨子とするものである
That is, the present invention is a comprehensive exhaust gas utilization method that improves the purity of the effective inert gas in the exhaust gas through water recovery, and recirculates it to control polluting components and combustion characteristics. Regarding a system that combines pollution-free combustion and energy recovery, in a system that burns fuel that produces a relatively large amount of water, a moisture recovery device is installed in the combustion exhaust gas passage section of the fuel to recover moisture at the same time. The main feature of this combustion method is that part of the moisture in the combustion exhaust gas downstream of the moisture recovery device is recirculated to the combustion chamber where the fuel is combusted.

本発明を第1図にしたがって更に詳しく説明する。The present invention will be explained in more detail with reference to FIG.

各種燃焼器の燃焼室または炉1とその排ガス・ダクト系
2において、排ガス系に水分回収装置3を設置する。
A moisture recovery device 3 is installed in the exhaust gas system in the combustion chamber or furnace 1 of various combustors and its exhaust gas/duct system 2.

燃料供給管4から燃料を燃焼室IK送り燃焼させた後の
排ガスは排ガスダクト系2Fc入る。
After fuel is sent from the fuel supply pipe 4 to the combustion chamber IK and burned, the exhaust gas enters the exhaust gas duct system 2Fc.

排ガス系の水分回収装置3は空気式水冷器5と冷却系6
とに通じて作動していて、排ガスの露点よりも低い塩度
に保持された固体昔たは液体表面で結露させ、排ガス全
体は未飽和状態の′!!1排出させるようになっている
The exhaust gas system moisture recovery device 3 includes an air type water cooler 5 and a cooling system 6.
Condensation occurs on solid or liquid surfaces that are maintained at a salinity lower than the dew point of the exhaust gas, leaving the entire exhaust gas unsaturated. ! 1 is discharged.

水分回収装置を出た排ガスはライン7を経て煙突8より
外へ排出されるが、ライン7の途中で分岐管9をとり、
再循環送風機10訟よび流量制御弁11を経由して、排
ガスの一部を燃料供給管4に再循環させる。
The exhaust gas leaving the water recovery device is discharged outside from the chimney 8 through line 7, but a branch pipe 9 is taken in the middle of line 7.
A portion of the exhaust gas is recirculated to the fuel supply pipe 4 via the recirculation blower 10 and the flow control valve 11.

循環カス量は流量制御弁11によってコントロールされ
る。
The amount of circulating waste is controlled by a flow control valve 11.

また、この排ガスの一部を直接燃焼室に供給してもよい
Alternatively, a part of this exhaust gas may be directly supplied to the combustion chamber.

一方、水分回収装置3によって回収された排ガス中の凝
縮水分は暖房、風呂などの温水として利用できるが、一
部を回収水タンク12、流量制御弁13を経由して燃焼
室1に噴射して燃焼を制御することもできる。
On the other hand, the condensed moisture in the exhaust gas recovered by the moisture recovery device 3 can be used as hot water for heating, bathing, etc., but some of it is injected into the combustion chamber 1 via the recovered water tank 12 and the flow control valve 13. Combustion can also be controlled.

筐た水分回収装置3ど連結している空気式水冷却器5に
空気を通し、送風器14、空気予熱器15を経由して燃
料供給管4に送って燃焼用空気として使用する。
Air is passed through an air-type water cooler 5 connected to a water recovery device 3 in a housing, and is sent to a fuel supply pipe 4 via an air blower 14 and an air preheater 15 to be used as combustion air.

以上のような方法を採ることにより、次のような効果が
奏せられる。
By adopting the above method, the following effects can be achieved.

1)排ガス中の水分を水分回収装置により除去するため a、排ガスを低温となる昔で熱利用しても白煙が出ない
1) Moisture in the exhaust gas is removed by a moisture recovery device, so no white smoke is produced even if the exhaust gas is used for heat in the olden days when the temperature was low.

(熱効率大)b、殆んど純粋な水分を回収できる。(High thermal efficiency) b. Almost pure water can be recovered.

C0水分回収装置以後は水分による腐食、錆がない。There is no corrosion or rust due to moisture after the C0 moisture recovery device.

d、水分回収装置以後の排ガスはN2 ガスを主成分と
する不活性ガスとなる。
d. The exhaust gas after the water recovery device becomes an inert gas whose main component is N2 gas.

2)水分回収装置より下流側の水分釦よび水溶成分を除
去した不活性ガスを再循環し燃料ガスと混合、燃料させ
るため a、排ガス中のNOx制御ができる〔水分や水溶成分を
除去した不活性ガスを循環させると、排ガス中の中間燃
焼生成物(ラジカル、例えばHCN等)や02戒分が少
なくなる。
2) Since the moisture button on the downstream side of the moisture recovery device recirculates the inert gas from which water and water-soluble components have been removed and mixes it with fuel gas, it is possible to control NOx in the exhaust gas. When active gas is circulated, intermediate combustion products (radicals, such as HCN, etc.) and 02 compounds in the exhaust gas are reduced.

該中間燃焼生成物は、0□が多いと02と作用してNO
xを生じ、02が少量の場合は直接N2を生じる。
If there is a large amount of 0□, the intermediate combustion products will interact with 02 and become NO.
x, and if 02 is small, it directly produces N2.

従って、中間燃焼生成物や02が少なければNOx生成
も少ないのである〕。
Therefore, if there are fewer intermediate combustion products and 02, less NOx will be produced.]

特に水素燃焼の場合、N2 との混合燃焼の効果は大
きく、第2図に示すように僅かに28多のN2の添加量
でNOを1/10以下に減らすことができる。
Particularly in the case of hydrogen combustion, the mixed combustion with N2 has a great effect, and as shown in FIG. 2, NO can be reduced to less than 1/10 by adding just 28 times more N2.

第2図において点線は水素を、実線は水素に28優の窒
素を混合させて燃焼させた時のNOの発生率を示す。
In FIG. 2, the dotted line shows hydrogen, and the solid line shows the NO generation rate when hydrogen is mixed with 28% nitrogen and combusted.

なお、LNG、LPG燃料等に$−いても、ホホ同様の
効果が得られることを確認している。
It has been confirmed that the same effect can be obtained even if LNG, LPG, etc. are used as fuel.

b、純度の高い水素の場合、材料の低流水素脆化が問題
となるが、排ガスと燃料との混合により温度が高くなる
と同時に水素脆化が防止される。
b. In the case of high-purity hydrogen, low-flow hydrogen embrittlement of the material becomes a problem, but hydrogen embrittlement is prevented at the same time as the temperature increases by mixing the exhaust gas and fuel.

C0水素のような燃え易い燃料の場合、爆発限界、燃焼
速度、着火エネルギー等の安全燃焼を支配する要素を、
不活性ガスとの混合の割合を調節することにより自由に
コントロールすることができる。
In the case of easily flammable fuels such as CO hydrogen, the factors that govern safe combustion, such as explosion limits, combustion speed, and ignition energy, are
It can be freely controlled by adjusting the mixing ratio with inert gas.

3)回収水の一部を燃料と混合燃焼させることにより、
更に水の回収割合を上げることができる。
3) By mixing and burning a portion of the recovered water with fuel,
Furthermore, the water recovery rate can be increased.

水との混合燃焼作用によシ、水の蒸発潜熱(540ca
e/f! ) 分だけ多量の熱を燃焼中に消費される
ので、燃焼温度が大幅に低下し、更にNOzおよびスモ
ークを低減できる。
Due to the mixed combustion effect with water, the latent heat of vaporization of water (540ca
e/f! ) Since a large amount of heat is consumed during combustion, the combustion temperature is significantly lowered, and NOz and smoke can be further reduced.

また、スモークの低減は燃焼用の02供給量を少なくし
、その結果、燃焼温度も低下してNOx低減効果に寄与
する。
Furthermore, reduction of smoke reduces the amount of 02 supplied for combustion, and as a result, the combustion temperature also decreases, contributing to the NOx reduction effect.

4)不活性ガスと水を燃焼室に再循環させることによシ
、上記2)と3)の相乗作用が得られ、NOx生成量が
著しく低減する。
4) By recirculating inert gas and water into the combustion chamber, a synergistic effect of 2) and 3) above is obtained, and the amount of NOx produced is significantly reduced.

すなわち、水の再循環により燃焼温度が低下し、また不
活性ガスの再循環により定圧比熱CpO差で化学反応を
促進させることなく燃焼温度を低下させる。
That is, the recirculation of water lowers the combustion temperature, and the recirculation of inert gas lowers the combustion temperature without promoting the chemical reaction due to the constant pressure specific heat CpO difference.

しかも、低源の水勢よび不活性ガスが燃焼域に供給させ
ることにより、NOx生成速度係数が小さくなり、NO
x生成量が低下するのである。
Moreover, by supplying a low source of water force and inert gas to the combustion zone, the NOx production rate coefficient becomes small, and NOx
This results in a decrease in the amount of x produced.

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

第1図は、本発明の一実施態様を示すフローシートであ
る。 第2図は、本発明方法と従来法とで水素を燃焼させた際
の発生NO量を比較した図である。
FIG. 1 is a flow sheet showing one embodiment of the present invention. FIG. 2 is a diagram comparing the amount of NO generated when hydrogen is combusted by the method of the present invention and the conventional method.

Claims (1)

【特許請求の範囲】 1 燃焼して比較的多量の水を生成する燃料を燃焼させ
る系において、該燃料の燃焼排ガス通過部に水分回収装
置を設置して水分を回収すると同時に、その水分のうち
一部および前記水分回収装置の下流側の燃焼排ガスの一
部を前記燃料を燃焼させる。 燃焼室に再循環することを特徴とする燃焼方法。
[Scope of Claims] 1. In a system that burns fuel that produces a relatively large amount of water, a moisture recovery device is installed in the combustion exhaust gas passage section of the fuel to recover moisture, and at the same time collect water from the moisture. A portion of the combustion exhaust gas downstream of the moisture recovery device is burned with the fuel. A combustion method characterized by recirculation into the combustion chamber.
JP50122901A 1975-10-14 1975-10-14 Nenshiyouhouhou Expired JPS5844281B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50122901A JPS5844281B2 (en) 1975-10-14 1975-10-14 Nenshiyouhouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50122901A JPS5844281B2 (en) 1975-10-14 1975-10-14 Nenshiyouhouhou

Publications (2)

Publication Number Publication Date
JPS5248133A JPS5248133A (en) 1977-04-16
JPS5844281B2 true JPS5844281B2 (en) 1983-10-03

Family

ID=14847412

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50122901A Expired JPS5844281B2 (en) 1975-10-14 1975-10-14 Nenshiyouhouhou

Country Status (1)

Country Link
JP (1) JPS5844281B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56112790U (en) * 1980-01-31 1981-08-31
JPS56108023A (en) * 1980-01-31 1981-08-27 Tsukishima Kikai Co Ltd Method and apparatus for recovering energy from exhaust gas of sludge incinerator

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4891631A (en) * 1972-03-07 1973-11-28
JPS4963033A (en) * 1972-10-18 1974-06-19
JPS5218929B2 (en) * 1973-01-18 1977-05-25
JPS5222131B2 (en) * 1973-04-23 1977-06-15

Also Published As

Publication number Publication date
JPS5248133A (en) 1977-04-16

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