JPS6113528B2 - - Google Patents
Info
- Publication number
- JPS6113528B2 JPS6113528B2 JP7653877A JP7653877A JPS6113528B2 JP S6113528 B2 JPS6113528 B2 JP S6113528B2 JP 7653877 A JP7653877 A JP 7653877A JP 7653877 A JP7653877 A JP 7653877A JP S6113528 B2 JPS6113528 B2 JP S6113528B2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- combustion
- inlet
- containing gas
- oxygen
- 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
Links
- 238000002485 combustion reaction Methods 0.000 claims description 56
- 239000007789 gas Substances 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000006185 dispersion Substances 0.000 claims description 9
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000000446 fuel Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
この発明は、窒素酸化物(以下、NOxと記載す
る)の発生量を低減するに好適な流動層燃焼装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a fluidized bed combustion apparatus suitable for reducing the amount of nitrogen oxides (hereinafter referred to as NOx ) generated.
従来の流動層燃焼においては、燃焼用空気を流
動層底部の分散板からのみ流動層に送入してい
る。すなわち、従来の流動層燃焼装置を示す第1
図において、燃料は燃料供給管4によつて流動層
燃焼容器1内の流動層6内に供給され、燃焼用空
気は燃焼用空気導入管2によつて流動層6の底部
にある分散板5から流動層6に送入され、燃焼排
ガスは空筒部7を経由して排ガス流出管3から流
出するようになつている。
In conventional fluidized bed combustion, combustion air is introduced into the fluidized bed only through the distribution plate at the bottom of the fluidized bed. In other words, the first example shows a conventional fluidized bed combustion apparatus.
In the figure, fuel is supplied to a fluidized bed 6 in a fluidized bed combustion vessel 1 through a fuel supply pipe 4, and combustion air is supplied to a dispersion plate 5 at the bottom of the fluidized bed 6 through a combustion air introduction pipe 2. The combustion exhaust gas is introduced into the fluidized bed 6 through the hollow cylinder 7 and flows out from the exhaust gas outlet pipe 3.
この場合、流動層6内における酸素含有量は、
流動層6の下部では多く、流動層6の上部になる
にしたがつて少なくなつている。それ故、流動層
6の下部では強酸化性雰囲気中において燃焼が行
なわれるので、NOxの発生量が多いという欠点が
あり、従来から問題になつていた。 In this case, the oxygen content in the fluidized bed 6 is
It is large in the lower part of the fluidized bed 6 and decreases toward the upper part of the fluidized bed 6. Therefore, since combustion is carried out in a strongly oxidizing atmosphere in the lower part of the fluidized bed 6, there is a drawback that a large amount of NO x is generated, which has been a problem in the past.
この発明は、上記の欠点を除いて、燃焼性能そ
の他の利点を損うことなく、流動層燃焼における
NOxの発生量を低減することができるNOx低減燃
焼装置を提供することを目的とするものである。
Except for the above-mentioned drawbacks, the present invention can be used in fluidized bed combustion without compromising combustion performance or other advantages.
The object of the present invention is to provide a NO x reduction combustion device that can reduce the amount of NO x generated.
この発明は、流動層燃焼容器に少なくとも3個
の燃焼用空気送入口を設け、その内第1送入口は
流動層底部に配置される分散手段としての分散板
とし、第2の送入口は流動層内に開口させ、第3
の送入口は空筒部に開口させる。
This invention provides a fluidized bed combustion vessel with at least three combustion air inlets, the first of which is a dispersion plate disposed at the bottom of the fluidized bed as a dispersion means, and the second inlet is a dispersion plate disposed at the bottom of the fluidized bed. an opening in the layer, and a third
The inlet is opened in the hollow cylinder.
そして、少なくとも3個の燃焼用空気送入口
は、夫々1つの燃焼用空気導入管から分岐れた少
なくとも3個の枝管に連通しており、少なくとも
3個の枝管には、夫々燃焼用空気量調節弁が備え
られていることを特徴とするものである。 The at least three combustion air inlets each communicate with at least three branch pipes branched from one combustion air introduction pipe, and each of the at least three branch pipes has a combustion air inlet. It is characterized by being equipped with a quantity control valve.
この発明に係る実施例を図に基づいた説明す
る。第2図はこの発明の流動層におけるNOx低減
燃焼装置を示す図であり、既に説明した第1図に
おける部分と同一の部分には同一番号を用いてい
る。
Embodiments of the present invention will be explained based on the drawings. FIG. 2 is a diagram showing the NO x reduction combustion apparatus in a fluidized bed according to the present invention, and the same numbers are used for the same parts as those in FIG. 1 already explained.
第2図において、燃焼用空気導入管から枝管1
4,15,16が分岐している。そして、枝管1
4は流動層6の底部に配置される第1の送入口で
ある分散手段としての分散板5に、また、枝管1
5および16は流動層6内に開口する第2の送入
口である送入口11および12に、さらに、枝管
17は空筒部7に開口する第3の送入である送入
口13に、夫々連通している。また、枝管14,
15,16,17には夫々空気流量調節弁24,
25,26,27が設けてある。 In Figure 2, from the combustion air introduction pipe to the branch pipe 1
4, 15, and 16 are branched. And branch pipe 1
4 is a first inlet port located at the bottom of the fluidized bed 6, and a branch pipe 1 is connected to a dispersion plate 5 as a dispersion means.
5 and 16 are second inlet ports 11 and 12 that open into the fluidized bed 6, and a branch pipe 17 is a third inlet port 13 that opens into the hollow cylinder 7. They communicate with each other. In addition, the branch pipe 14,
15, 16, and 17 have air flow control valves 24,
25, 26, and 27 are provided.
このように構成してあるので、燃料は燃料供給
管4から流動層6内に供給され、燃焼用空気導入
管2から導入される燃焼用空気は、空気流量調節
弁24〜27によつて流量を調節されて枝管14
〜17に分割される。流量を調節されて枝管14
〜17に分割された燃焼用空気は、夫々、分散板
5から流動層6の底部に、また、分散板5をバイ
パスして送入口11および12から流動層6の内
部に、さらに、分散板5をバイパスして送入口1
3から空筒部7に、多段的に送入される。そし
て、燃焼用空気導入管2から導入される空気量
は、流動層6内の流動媒体を流動させるととも
に、燃料供給管4によつて流動層6内に供給され
る燃料を燃焼するに必要な空気量である。 With this structure, fuel is supplied from the fuel supply pipe 4 into the fluidized bed 6, and the combustion air introduced from the combustion air introduction pipe 2 is controlled in flow rate by the air flow control valves 24 to 27. The branch pipe 14 is adjusted
It is divided into ~17. Branch pipe 14 whose flow rate is adjusted
The combustion air divided into 1 to 17 flows from the distribution plate 5 to the bottom of the fluidized bed 6, bypasses the distribution plate 5 and enters the inside of the fluidized bed 6 from the inlet ports 11 and 12, and then passes through the distribution plate 5 to the bottom of the fluidized bed 6. Bypass 5 and inlet 1
3 into the hollow cylinder part 7 in multiple stages. The amount of air introduced from the combustion air introduction pipe 2 is the amount necessary to flow the fluidized medium in the fluidized bed 6 and to burn the fuel supplied into the fluidized bed 6 by the fuel supply pipe 4. It is the amount of air.
したがつて、従来の流動層燃焼におけるよう
な、酸素含有気体である燃焼用空気が流動層6の
下部に集中して存在することによる強酸化性雰囲
気中における燃焼が防止されて、酸素含有気体で
ある燃焼用空気が流動層6内および空筒部7内に
分散して存在し、流動層6内の燃料が、比較的酸
素含有量が少ないすなわち還元性に寄せた雰囲気
中において燃焼するので、NOxの発生量が低減さ
れている。 Therefore, combustion in a strongly oxidizing atmosphere due to the presence of combustion air, which is an oxygen-containing gas, concentrated in the lower part of the fluidized bed 6, as in conventional fluidized bed combustion, is prevented, and the oxygen-containing gas is Combustion air exists dispersedly within the fluidized bed 6 and the cavity 7, and the fuel within the fluidized bed 6 burns in an atmosphere with a relatively low oxygen content, that is, a reducing atmosphere. , the amount of NO x generated is reduced.
この場合、分散板5をバイパスして送入口11
および12から流動層6の内部に送入される2段
目の燃焼用空気によつて、流動層6の表面付近の
燃料が燃焼する温度は、流動層6の熱容量が大き
いため殆ど上昇せず、理想的な2段燃焼をしてお
り、NOxの発生量が低減されている。すなわち、
流動層6全体で低酸素濃度燃焼および低温度燃焼
による低NOx燃焼を行なつている。 In this case, the distribution plate 5 is bypassed and the inlet port 11 is
The temperature at which the fuel burns near the surface of the fluidized bed 6 hardly rises due to the second stage combustion air sent into the fluidized bed 6 from the fluidized bed 6 due to the large heat capacity of the fluidized bed 6. It uses ideal two-stage combustion, reducing the amount of NO x generated. That is,
The entire fluidized bed 6 performs low NO x combustion due to low oxygen concentration combustion and low temperature combustion.
そして、流動層6の低NOx燃焼によつて発生す
るCOを含む未燃焼分を、空筒部7内において、
送入口13から送入される燃焼用空気によつて燃
焼して、燃焼効率の指標の1つである燃焼排ガス
中のCOの量を無理なく低減している。 Then, the unburned portion containing CO generated by the low NOx combustion in the fluidized bed 6 is stored in the hollow cylinder 7.
Combustion is carried out by the combustion air introduced from the inlet 13, and the amount of CO in the combustion exhaust gas, which is one of the indicators of combustion efficiency, is reasonably reduced.
この発明は、以上説明したように、燃焼用空気
を分割して、流動層の底部と流動層の内部と空筒
部とに、多段的に送入している。したがつて、流
動層の熱容量が大きいために2段目の燃焼によつ
て温度が殆ど上昇せず、理想的な2段燃焼をする
ことができる。すなわち、流動層全体が低酸素濃
度燃焼および低温度燃焼による低NOx燃焼をする
ので、NOxの発生量を低減することができる効果
がある。
As explained above, in this invention, combustion air is divided and fed into the bottom of the fluidized bed, the inside of the fluidized bed, and the hollow cylinder in multiple stages. Therefore, since the heat capacity of the fluidized bed is large, the temperature hardly rises during the second stage combustion, making it possible to perform ideal two stage combustion. That is, since the entire fluidized bed performs low NO x combustion due to low oxygen concentration combustion and low temperature combustion, there is an effect that the amount of NO x generated can be reduced.
また、流動層の低NOx燃焼によつて発生する
COを含む未燃焼分を、空筒部において最終燃焼
させるので、燃焼排ガス中のCOの量を無理なく
低減することができる効果がある。 In addition, low NOx combustion in the fluidized bed generates
Since the unburned portion containing CO is finally combusted in the cavity, it is possible to reasonably reduce the amount of CO in the combustion exhaust gas.
第1図は従来の流動層燃焼装置を示す図、第2
図は、この発明の流動層におけるNOx低減燃焼装
置を示す図である。
1…流動層燃焼容器、2…燃焼用空気導入管、
3…排ガス流出管、4…燃料供給管、5…分散
板、6…流動層、7…空筒部、11,12,13
…送入口、14,15,16,17…枝管、2
4,25,26,27…空気流量調節弁。
Figure 1 shows a conventional fluidized bed combustion apparatus, Figure 2
The figure is a diagram showing a NOx reduction combustion device in a fluidized bed according to the present invention. 1...Fluidized bed combustion vessel, 2...Combustion air introduction pipe,
3...Exhaust gas outflow pipe, 4...Fuel supply pipe, 5...Dispersion plate, 6...Fluidized bed, 7...Cavity part, 11, 12, 13
...Inlet port, 14, 15, 16, 17... Branch pipe, 2
4, 25, 26, 27...Air flow control valve.
Claims (1)
素含有気体送入口を設け、その内第1の送入口は
流動層底部に配置される分散手段とし、第2の送
入口は流動層内に開口させ、第3の送入口は空筒
部に開口させることを特徴とする流動層における
窒素酸化物低減燃焼装置。 2 前記少なくとも3個の燃焼用酸素含有気体送
入口は、夫々1つの燃焼用酸素含有気体導入管よ
り分岐された少なくとも3個の枝管と連通し、前
記枝管には酸素含有気体流量調節弁が備えられて
いることを特徴とする特許請求の範囲第1項記載
の流動層における窒素酸化物低減燃焼装置。[Claims] 1. A fluidized bed combustion vessel is provided with at least three combustion oxygen-containing gas inlets, the first of which is a dispersion means disposed at the bottom of the fluidized bed, and the second inlet is a dispersion means disposed at the bottom of the fluidized bed. A combustion device for reducing nitrogen oxides in a fluidized bed, characterized in that the third inlet is opened into the fluidized bed, and the third inlet is opened into the hollow cylinder. 2. The at least three combustion oxygen-containing gas inlet ports each communicate with at least three branch pipes branched from one combustion oxygen-containing gas introduction pipe, and each of the branch pipes is provided with an oxygen-containing gas flow rate regulating valve. A nitrogen oxide reduction combustion apparatus in a fluidized bed according to claim 1, characterized in that the combustion apparatus is equipped with:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7653877A JPS5411530A (en) | 1977-06-29 | 1977-06-29 | Fluidzed bed type combustion device with reduced nox |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7653877A JPS5411530A (en) | 1977-06-29 | 1977-06-29 | Fluidzed bed type combustion device with reduced nox |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5411530A JPS5411530A (en) | 1979-01-27 |
| JPS6113528B2 true JPS6113528B2 (en) | 1986-04-14 |
Family
ID=13608038
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7653877A Granted JPS5411530A (en) | 1977-06-29 | 1977-06-29 | Fluidzed bed type combustion device with reduced nox |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5411530A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60181539U (en) * | 1984-05-14 | 1985-12-02 | バブコツク日立株式会社 | Sewage sludge incinerator |
-
1977
- 1977-06-29 JP JP7653877A patent/JPS5411530A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5411530A (en) | 1979-01-27 |
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