JPH02282610A - Prevention of dust attaching to outlet of sludge melting furnace - Google Patents
Prevention of dust attaching to outlet of sludge melting furnaceInfo
- Publication number
- JPH02282610A JPH02282610A JP10025989A JP10025989A JPH02282610A JP H02282610 A JPH02282610 A JP H02282610A JP 10025989 A JP10025989 A JP 10025989A JP 10025989 A JP10025989 A JP 10025989A JP H02282610 A JPH02282610 A JP H02282610A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- melting furnace
- combustion gas
- outlet
- slag
- 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
Links
- 238000002844 melting Methods 0.000 title claims abstract description 39
- 230000008018 melting Effects 0.000 title claims abstract description 39
- 239000010802 sludge Substances 0.000 title claims abstract description 20
- 239000000428 dust Substances 0.000 title claims description 9
- 230000002265 prevention Effects 0.000 title 1
- 238000002485 combustion reaction Methods 0.000 claims abstract description 15
- 238000007664 blowing Methods 0.000 claims abstract 3
- 238000000034 method Methods 0.000 claims description 10
- 239000002893 slag Substances 0.000 abstract description 22
- 239000000567 combustion gas Substances 0.000 abstract description 17
- 239000007789 gas Substances 0.000 abstract description 10
- 239000011449 brick Substances 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000010801 sewage sludge Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、旋回溶融式炉特に都市下水汚泥を溶融処理す
る竪形上向流型旋回式汚泥溶融炉出口のダスト付着防止
方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for preventing dust adhesion at the outlet of a vertical upward flow type swirling sludge melting furnace for melting municipal sewage sludge. be.
[従来の技術]
近年、都市下水汚泥の処理は海洋汚染並びに廃棄場所の
観点から重要な問題となっている。[Prior Art] In recent years, the treatment of urban sewage sludge has become an important issue from the viewpoints of marine pollution and disposal sites.
通常下水汚泥やし原汚泥は下水処理場やし尿処理場に集
約し、汚泥と処理水とに別け、汚泥(ヘドロ)は、脱水
後焼却炉で焼却処理されるが、このような処理後の焼却
灰は扱いに<<、また埋立用にしか利用出来ない。Normally, raw sewage sludge and palm sludge are collected at a sewage treatment plant or night soil treatment plant, separated into sludge and treated water, and the sludge (sludge) is dehydrated and then incinerated in an incinerator. Incineration ash can only be used for handling and landfilling.
この様な背景から、近年汚泥を溶融炉で溶融処理してス
ラグ化し減容化することにより、取扱の容易化とスラグ
の有効利用を図ろうとする研究が行われ、一部は既に実
用化されている。Against this background, research has been conducted in recent years to reduce the volume of sludge by melting it in a melting furnace to make it easier to handle and to make effective use of slag, and some of this has already been put into practical use. ing.
上記の廃棄物溶融炉としては、特開昭61−70314
号公報、特開昭59−205508号公報及び出願人が
先に特願昭63−300724号(出願日S[13,1
1,30)にて出願した廃棄物の溶融炉がある。As the waste melting furnace mentioned above, Japanese Patent Application Laid-Open No. 61-70314
Publication No. 59-205508 and the applicant's earlier patent application No. 63-300724 (filing date S[13,1
There is a waste melting furnace filed in 1, 30).
第2図〜第4図に上記の旋回流方式の構造の炉を示す。FIGS. 2 to 4 show a furnace having the above-mentioned swirl flow type structure.
即ち、第2図の構造炉は、竪型の大口径の煙道23の下
部側壁側に水平若しくは下流側が下向きに傾斜した旋回
流燃焼室24を有している。旋回流燃焼室24内では旋
回流が形成され、廃棄物と助燃料を熱源として溶融した
スラグは壁面に沿って流下し、煙道23の底部より系外
に排出される。燃焼ガスは旋回流燃焼室24内を溶鍛ス
ラグと同方向に流れ、旋回流燃焼室出口のど部25を主
に対流伝熱で加熱しつつ排気され、しかるのち煙道23
内で未燃燐分が完全に燃焼して排出される。That is, the structural furnace shown in FIG. 2 has a swirling combustion chamber 24 on the lower side wall side of a vertical large-diameter flue 23, the horizontal or downstream side of which is inclined downward. A swirling flow is formed within the combustion chamber 24, and the slag, which is melted using waste and auxiliary fuel as heat sources, flows down along the wall surface and is discharged from the bottom of the flue 23 to the outside of the system. The combustion gas flows in the swirling combustion chamber 24 in the same direction as the molten forged slag, heats the swirling combustion chamber outlet throat 25 mainly by convection heat transfer, and is then exhausted.
The unburned phosphorus is completely burned and discharged.
また第3図の構造炉は、竪型旋回流燃焼炉であり、炉頂
部に設けられた廃棄物バーナ26及び燃焼空気流入口2
7によって旋回流を与えて廃棄物を燃焼させ、溶融スラ
グは壁面を流下し絞り部30を通過して下方に流下する
。燃焼ガスは絞り部30を対流伝熱で加熱し、旋回流燃
焼炉を出た後、流れ方向を変えられ下流の排ガス系へ導
かれる。The structural furnace shown in FIG. 3 is a vertical swirling flow combustion furnace, with a waste burner 26 and a combustion air inlet 2 provided at the top of the furnace.
7 gives a swirling flow to burn the waste, and the molten slag flows down the wall surface, passes through the constriction part 30, and flows downward. The combustion gas heats the throttle section 30 by convection heat transfer, and after exiting the swirling combustion furnace, the flow direction is changed and guided to the downstream exhaust gas system.
また、前記特願昭63−300724号の廃棄物の溶融
炉は第4図に示す様な構造の炉である。Furthermore, the waste melting furnace disclosed in Japanese Patent Application No. 63-300724 has a structure as shown in FIG.
この炉は、上部に燃焼ガス排出口33を有し、下端にス
ラグ出湯口32を有する竪型の溶融炉本体31と、溶融
炉本体31の下部に設けられる廃棄物バーナ装置34及
び助燃バーナ装置35とからなっている。This furnace includes a vertical melting furnace main body 31 having a combustion gas outlet 33 at the upper end and a slag outlet 32 at the lower end, a waste burner device 34 and an auxiliary combustion burner device provided at the lower part of the melting furnace main body 31. It consists of 35.
またこの炉には燃焼ガス排出口33に2次燃焼室3Bが
接続されている。Further, a secondary combustion chamber 3B is connected to a combustion gas outlet 33 in this furnace.
一方これら溶融炉の排ガスは廃熱回収装置→排煙処理装
置−子熱器を経て、無害化された後煙突より大気中に放
出される。On the other hand, the exhaust gas from these melting furnaces passes through a waste heat recovery device, a flue gas treatment device, and a subheater, and after being made harmless, it is released into the atmosphere from a chimney.
上記溶融炉の工程において、溶融炉の排ガス出口部の排
ガス温度は1400℃程度でスラグは溶融状態にある。In the melting furnace process, the exhaust gas temperature at the exhaust gas outlet of the melting furnace is about 1400° C., and the slag is in a molten state.
[発明が解決しようとする課題]
上述の如く、竪形上向流型旋回式汚泥溶融炉においては
、その溶融炉の燃焼排ガス出口部は高温状態にあり、そ
のため排ガスに同伴されたスラグはその温度で炉出口を
通過すると、スラグが炉壁に付着し、やがては炉出口を
閉塞せしめるという問題が生ずる。[Problems to be Solved by the Invention] As mentioned above, in the vertical upward flow type swirling sludge melting furnace, the combustion exhaust gas outlet of the melting furnace is in a high temperature state, and therefore the slag entrained in the exhaust gas is When passed through the furnace outlet at high temperatures, a problem arises in that the slag adheres to the furnace walls and eventually blocks the furnace outlet.
本発明は、竪形上向流型旋回式汚泥溶融炉において、溶
融炉の炉出口を閉塞せしめない汚泥溶融炉出口のダスト
付着防止方法を提供することを目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for preventing dust from adhering to an outlet of a sludge melting furnace in a vertical upward flow type swirling sludge melting furnace without clogging the furnace outlet of the melting furnace.
[課題を解決するための手段]
本発明は、竪形上向流型旋回式汚泥溶融炉において、
前記溶融炉の排ガス出口部に低圧の蒸気を炉頂部から吹
込むことを特徴とする汚泥溶融炉のダスト付着防止方法
である。[Means for Solving the Problems] The present invention provides a sludge melting furnace in which low-pressure steam is blown into the exhaust gas outlet of the melting furnace from the top of the furnace in a vertical upward flow type swirling sludge melting furnace. This is a method for preventing dust from adhering to a furnace.
[作用]
本発明の汚泥溶融炉出口のダスト付着防止方法において
は、低圧の蒸気を溶融炉の燃焼排ガス出口部の炉頂部か
ら吹込むことにより、炉壁煉瓦付近の温度を下げ、溶融
スラグを固化スラグとし炉壁への付着を防止するもので
ある。[Function] In the method for preventing dust adhesion at the sludge melting furnace outlet of the present invention, low-pressure steam is blown into the furnace top at the flue gas outlet of the melting furnace to lower the temperature near the furnace wall bricks and prevent molten slag. This solidifies slag and prevents it from adhering to the furnace walls.
蒸気を用いる理由は次の通りである。The reason for using steam is as follows.
■蒸気の場合は酸素を含まないので空気比の増加とはな
らないのでNo の上昇を防ぐ。■In the case of steam, since it does not contain oxygen, it does not increase the air ratio, thus preventing a rise in No.
■蒸気は空気より比熱が大きく温度降下作用が大きい。■Steam has a higher specific heat than air and has a greater temperature-lowering effect.
■上記■により容積が増えず炉内のガス流れに対する影
響が少ない。■Because of the above (■), the volume does not increase and there is little effect on the gas flow in the furnace.
次に本発明の実施例について述べる。Next, embodiments of the present invention will be described.
[実施例]
第1図は本発明の実態様例である汚泥溶融炉出口のダス
ト付着防止方法の説明図である。[Example] FIG. 1 is an explanatory diagram of a method for preventing dust adhesion at the outlet of a sludge melting furnace, which is an embodiment of the present invention.
第1図において、1は溶融炉本体、2はスラグ出湯口、
3は燃焼ガス排出口、4は廃棄物バーナ装置、5は助燃
バーナ装置、6は蒸気バイブ、7はスラグ付着物である
。In Fig. 1, 1 is the melting furnace main body, 2 is the slag outlet,
3 is a combustion gas outlet, 4 is a waste burner device, 5 is an auxiliary combustion burner device, 6 is a steam vibrator, and 7 is a slag deposit.
第1図に示す如く、溶融炉本体1の炉内温度は廃棄物バ
ーナ装置4及び助燃バーナ装置5により1500〜16
00℃であり、燃焼ガス排出口3周辺は、1400℃程
度でスラグは溶融状態にあり、この侭では図示する如く
、スラグ付着物7が燃焼ガス排出口3に付着し、ついに
は溶融炉の燃焼ガス排出口3を閉塞せしめてしまう。As shown in FIG. 1, the temperature inside the melting furnace main body 1 is set to 1500 to 1600°C by the waste burner device 4 and the auxiliary combustion burner device 5.
00°C, and the slag is in a molten state at around 1400°C around the combustion gas outlet 3. In this situation, as shown in the figure, slag deposits 7 adhere to the combustion gas outlet 3, and eventually the melting furnace melts. The combustion gas exhaust port 3 will be blocked.
そこで本発明では、廃熱ボイラの低圧蒸気(圧力3 k
g / cj )を燃焼ガス排出口3の煉瓦を貫通して
設けた蒸気バイブロより吹込み煉瓦面を冷却した。Therefore, in the present invention, low pressure steam (pressure 3 k
g/cj) was blown into the combustion gas outlet 3 by a steam vibro provided through the brick, and the brick surface was cooled.
この結果燃焼ガス排出口3の炉壁近傍の温度は200℃
程度低下し、スラグの付着は防止出来、連続操業が可能
となった。As a result, the temperature near the furnace wall of the combustion gas outlet 3 is 200°C.
The degree of slag was reduced, slag adhesion was prevented, and continuous operation became possible.
なお本発明の実施例においては、溶融炉1は第3図に示
す構造の炉に適用したが他の竪形上向流型旋回式汚泥溶
融炉においても同様な効果を奏するものである。In the embodiment of the present invention, the melting furnace 1 is applied to a furnace having the structure shown in FIG. 3, but similar effects can be obtained in other vertical upward flow type swirling sludge melting furnaces.
[発明の効果]
本発明の汚泥溶融炉出口のダスト付着防止方法によれば
、溶融炉の燃焼ガス排出口に、スラグが付着せず、炉出
口を閉塞せしめないため、連続操業を可能とする効果を
奏するものである。[Effects of the Invention] According to the method for preventing dust adhesion at the sludge melting furnace outlet of the present invention, slag does not adhere to the combustion gas outlet of the melting furnace and does not block the furnace outlet, making continuous operation possible. It is effective.
第1図は本発明の実態様例である汚泥溶融炉出口のダス
ト付着防止方法の説明図、第2図〜第4図は従来の旋回
型溶融炉の説明図である。
図において、1:溶融炉本体、2ニスラグ出湯口、3:
燃焼ガス排出口、4:廃棄物バーナ装置、5:助燃バー
ナ装置、6:蒸気バイブ、7:スラグ付着物。
第FIG. 1 is an explanatory diagram of a method for preventing dust adhesion at the outlet of a sludge melting furnace, which is an embodiment of the present invention, and FIGS. 2 to 4 are explanatory diagrams of a conventional swirl-type melting furnace. In the figure, 1: Melting furnace main body, 2: Nislag outlet, 3:
Combustion gas outlet, 4: waste burner device, 5: auxiliary combustion burner device, 6: steam vibrator, 7: slag deposits. No.
Claims (1)
徴とする汚泥溶融炉出口のダスト付着防止方法。[Scope of Claim] A method for preventing dust adhesion at an outlet of a sludge melting furnace in a vertical upward flow type swirling sludge melting furnace, the method comprising: blowing steam into the combustion exhaust gas outlet of the melting furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10025989A JPH02282610A (en) | 1989-04-21 | 1989-04-21 | Prevention of dust attaching to outlet of sludge melting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10025989A JPH02282610A (en) | 1989-04-21 | 1989-04-21 | Prevention of dust attaching to outlet of sludge melting furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02282610A true JPH02282610A (en) | 1990-11-20 |
Family
ID=14269221
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10025989A Pending JPH02282610A (en) | 1989-04-21 | 1989-04-21 | Prevention of dust attaching to outlet of sludge melting furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02282610A (en) |
-
1989
- 1989-04-21 JP JP10025989A patent/JPH02282610A/en active Pending
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