JPS62175510A - Incinerator of waste water containing oil - Google Patents
Incinerator of waste water containing oilInfo
- Publication number
- JPS62175510A JPS62175510A JP1616886A JP1616886A JPS62175510A JP S62175510 A JPS62175510 A JP S62175510A JP 1616886 A JP1616886 A JP 1616886A JP 1616886 A JP1616886 A JP 1616886A JP S62175510 A JPS62175510 A JP S62175510A
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- primary
- burner
- waste water
- 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.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 39
- 238000002485 combustion reaction Methods 0.000 claims abstract description 69
- 238000000034 method Methods 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 238000004891 communication Methods 0.000 abstract description 4
- 238000007599 discharging Methods 0.000 abstract 2
- 239000000567 combustion gas Substances 0.000 abstract 1
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 230000008020 evaporation Effects 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 8
- 239000000446 fuel Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 239000000295 fuel oil Substances 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 101100180402 Caenorhabditis elegans jun-1 gene Proteins 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- -1 etc. Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は廃水焼却炉に関し、特に油水分離が困難な含油
廃水焼却炉に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a wastewater incinerator, and particularly to an oil-containing wastewater incinerator in which separation of oil and water is difficult.
一般に廃水焼却炉は主として油水分離が困難な廃水、排
水基準(BOD、CODなど)が厳しい環境での廃水処
理に使用される。油水分離が困難な廃水の例として水性
の樹脂、塗料、接着剤等を使用するシステムの洗浄工程
において生ずる排水、廃液や有機含浸システムの洗浄工
程において生ずる廃液等があり、これらは有機高分子物
質を多量に含んでいる。In general, wastewater incinerators are mainly used to treat wastewater where oil-water separation is difficult and in environments where wastewater standards (BOD, COD, etc.) are strict. Examples of wastewater that is difficult to separate from oil and water include wastewater and wastewater generated in the cleaning process of systems that use water-based resins, paints, adhesives, etc., and wastewater generated in the cleaning process of organic impregnation systems, which contain organic polymer substances. Contains large amounts of.
(従来の技術とその問題点)
廃水焼却炉では不完全燃焼が発生すれば煤煙や悪臭の原
因となる。このため炉内全体で完全燃焼するように炉内
温度を高温に保つ必要がある。(Conventional technology and its problems) If incomplete combustion occurs in a wastewater incinerator, it causes soot and bad odor. For this reason, it is necessary to maintain the temperature inside the furnace at a high temperature to ensure complete combustion throughout the furnace.
完全燃焼を効率よく行う方法として、壁面に廃水を噴霧
させる方法、板を設けてこれに沿って廃水を流す方法等
がある。また高温を利用する方法として排気ガスの高熱
を利用して廃水を予め濃縮処理して焼却し易(する方法
、高熱ガス中に直接廃水を噴霧する方法等がある。As methods for efficiently achieving complete combustion, there are methods such as spraying wastewater on a wall surface, and installing a board and flowing wastewater along it. Further, as methods of utilizing high temperature, there are a method of concentrating wastewater in advance using the high heat of exhaust gas to make it easier to incinerate, and a method of directly spraying wastewater into high-temperature gas.
何れの場合でも炉内全体を高温に保つ必要から大型のバ
ーナーと大量の燃料が必要になる。また一つの燃焼室で
は焼却炉自体が大型となり、これに伴って更に大量の燃
料が必要となる。In either case, it is necessary to maintain the entire inside of the furnace at a high temperature, which requires a large burner and a large amount of fuel. Moreover, in one combustion chamber, the incinerator itself becomes large-sized, and accordingly, a larger amount of fuel is required.
(問題を解決するための手段)
本発明は上述の問題を解決して、小型で完全燃焼する含
油廃水焼却炉を提供することを目的とする。(Means for Solving the Problems) An object of the present invention is to solve the above-mentioned problems and provide a small-sized oil-containing wastewater incinerator that burns completely.
即ら隣接して一次燃焼室と二次燃焼室を設け、一次燃焼
室には廃水吐出ノズルを一次バーナーの下側に設け、二
次燃焼室は前記一次燃焼室の上側に設けて二次バーナー
により前記一次燃焼室の排気の二次燃焼をおこなわせて
その排気は煙突に排出するものである。That is, a primary combustion chamber and a secondary combustion chamber are provided adjacent to each other, a waste water discharge nozzle is provided in the primary combustion chamber below the primary burner, and a secondary combustion chamber is provided above the primary combustion chamber, and a waste water discharge nozzle is provided in the primary combustion chamber and the secondary combustion chamber is provided above the primary combustion chamber. This causes secondary combustion of the exhaust gas in the primary combustion chamber, and the exhaust gas is discharged into the chimney.
更に前記二次燃焼室の容積が前記一次燃焼室の容積の5
0%以下としたものもある。Furthermore, the volume of the secondary combustion chamber is 5 times the volume of the primary combustion chamber.
In some cases, it is less than 0%.
(作用)
上述のように一次燃焼室では一次バーナーの炎に直接廃
水噴霧をしないので炎を冷却せず高温が維持できると共
に、仮に不完全燃焼が起こっても二次燃焼室で完全に燃
焼させることが出来る。(Function) As mentioned above, in the primary combustion chamber, waste water is not sprayed directly onto the flame of the primary burner, so the flame can be maintained at a high temperature without being cooled, and even if incomplete combustion occurs, it will be completely combusted in the secondary combustion chamber. I can do it.
(実施例)
第1図は本発明の含油廃水焼却炉の縦断面図、第2図は
第1図のA−Avfr面図、第3図は同じくB−B断面
図である。炉体は断熱材で囲まれて大別して一次燃焼室
1と、この上側に位置する二次燃焼室2から構成されて
いる。一次燃焼室1の側面には一次バーナー3と、この
バーナー3の下側に廃水吐出ノズル4が設けてあり、上
面の一次隔壁5には二次燃焼室2への連絡排気孔6が設
けである。二次燃焼室は一次燃焼室に比べ高さが低く(
本実施例では約30%)、かつ直径方向に片側の側面か
ら直径の273程度の長さの二次隔壁7で二次燃焼室2
を大きく部分している。この部分された片側の部分2−
1の底面(一次隔壁5)には前記連絡排気孔6が明けら
れており、側面には部分された他の部分2−2に向けて
二次バーナー8が設けである。部分された他の部分2−
2の上面には排気孔9が設けてあり、煙突10が接続し
である。(Example) FIG. 1 is a longitudinal sectional view of an oil-containing wastewater incinerator of the present invention, FIG. 2 is a sectional view taken along line A-Avfr in FIG. 1, and FIG. 3 is a sectional view taken along line BB. The furnace body is surrounded by a heat insulating material and roughly divided into a primary combustion chamber 1 and a secondary combustion chamber 2 located above the primary combustion chamber 1. A primary burner 3 is provided on the side surface of the primary combustion chamber 1, and a waste water discharge nozzle 4 is provided below the burner 3, and a communication exhaust hole 6 to the secondary combustion chamber 2 is provided in the primary partition wall 5 on the top surface. be. The height of the secondary combustion chamber is lower than that of the primary combustion chamber (
(in this embodiment, approximately 30%), and the secondary combustion chamber 2 is connected to the secondary partition wall 7 having a length of approximately 273 diameters from one side in the diametrical direction.
Large portions. This part 2-
The communication exhaust hole 6 is provided on the bottom surface (primary partition wall 5) of the fuel cell 1, and a secondary burner 8 is provided on the side surface facing the other portion 2-2. Other part 2-
An exhaust hole 9 is provided on the top surface of 2, and a chimney 10 is connected thereto.
尚一次バーナーでは25 N /hの重油を消費し、二
次バーナーでは151 /hの重油を消費する。The primary burner consumes 25 N/h of heavy oil, and the secondary burner consumes 151 N/h of heavy oil.
廃水は一次燃焼室1の廃水吐出ノズル4から一次バーナ
ー3の炎の下側に噴霧される。霧状の廃水は熱のために
直ちに水分は蒸発し、油分は燃焼してガス化し、連絡排
気孔6を通って二次燃焼室2に導かれる。この場合、低
濃度の含油廃水では水の1発潜熱で熱が奪われ、炉の温
度が700℃以下になって不完全燃焼が発生する場合が
ある。しかし本実施例のように一次バーナー3の炎の下
に廃水を噴霧すると、炎は直接噴霧で冷却されず、炉の
温度降下は起き難い。The waste water is sprayed from the waste water discharge nozzle 4 of the primary combustion chamber 1 onto the underside of the flame of the primary burner 3. The water in the mist-like wastewater is immediately evaporated due to the heat, and the oil content is combusted and gasified, and is led to the secondary combustion chamber 2 through the communication exhaust hole 6. In this case, in the case of low-concentration oil-containing wastewater, heat is taken away by one latent heat of water, and the temperature of the furnace may drop to 700° C. or lower, resulting in incomplete combustion. However, when waste water is sprayed under the flame of the primary burner 3 as in this embodiment, the flame is not directly cooled by the spray, and the temperature of the furnace is unlikely to drop.
二次燃焼室2では一次燃焼室1の排気中子完全燃焼の排
気があると二次バーナーの炎で完全燃焼する。この二次
燃焼室2では水の蒸発は行われないので、二次バーナー
8の発熱量は小さくても炉の温度降下は起きない。また
、このために燃焼室を小さく出来るので、一次燃焼室の
約20〜40%に小型化することが出来る。更に小型燃
焼室であるので小型のバーナーでも容易に所要温度(例
えば700℃)に達するqとが出来る。実施データで一
次燃焼室1を一次バーナー3で700℃に到達させるの
に2時間を要したが、二次燃焼室2を二次バーナー8で
700℃に到達させるのには1時間30分で充分であっ
た。In the secondary combustion chamber 2, if there is exhaust gas from the primary combustion chamber 1 that has completely burned the exhaust core, it will be completely combusted by the flame of the secondary burner. Since water is not evaporated in this secondary combustion chamber 2, the temperature of the furnace does not drop even if the calorific value of the secondary burner 8 is small. Moreover, since the combustion chamber can be made smaller for this reason, it can be made smaller to about 20 to 40% of the primary combustion chamber. Furthermore, since the combustion chamber is small, even a small burner can easily reach the required temperature (for example, 700° C.). According to the actual data, it took 2 hours to reach 700°C in the primary combustion chamber 1 with the primary burner 3, but it took 1 hour and 30 minutes to reach 700°C in the secondary combustion chamber 2 with the secondary burner 8. It was enough.
この結果容積の小さい二次燃焼室2を採用することによ
り、一次燃焼室2個の場合に比べ10〜30%の燃料節
約となった。As a result, by employing the secondary combustion chamber 2 with a small volume, fuel savings of 10 to 30% was achieved compared to the case of two primary combustion chambers.
廃水として有機含浸システムの洗浄工程から出る約3%
アクリルモノマーを含有する廃水を焼却処理する場合、
一次燃焼室の温度が390”Cでも二次燃焼室の温度が
700℃ならば完全燃焼して煤煙及び臭気が発生しない
。Approximately 3% of waste water from the cleaning process of organic impregnation systems
When incinerating wastewater containing acrylic monomers,
Even if the temperature of the primary combustion chamber is 390"C, if the temperature of the secondary combustion chamber is 700"C, complete combustion will occur and no soot or odor will be generated.
各種の温度の実施例のデータを第1表(次頁)に示す。Data for examples at various temperatures are shown in Table 1 (next page).
比較例として二次燃焼室を使用しない炉の場合及び二次
燃焼室のバーナー停止後の状態も示しである。As a comparative example, the case of a furnace that does not use a secondary combustion chamber and the state after the burner of the secondary combustion chamber is stopped are also shown.
(発明の効果)
一次燃焼室の廃水吐出ノズルを一次バーナーの炎の下側
に設けたことにより、一次燃焼室の温度降下を防止する
と共に、小型の二次燃焼室を設けることにより焼却炉全
体を小型化することが出来、燃料節約も可能である。(Effect of the invention) By providing the waste water discharge nozzle of the primary combustion chamber below the flame of the primary burner, the temperature drop in the primary combustion chamber is prevented, and by providing a small secondary combustion chamber, the entire incinerator It is possible to downsize and save fuel.
更に低濃度の含油廃水でも完全燃焼させることが出来る
。Furthermore, even low-concentration oil-containing wastewater can be completely combusted.
第1表Table 1
第1図は縦断面図、第2図は第1図のA−A断面図、第
3図は同じ<B−B断面図である。
に一次燃焼室、 2:二次燃焼室、 3ニ一次バー
ナー、 4:廃水吐出ノズル、 8:二次バーナー
。
淳1圏
乍2目
洛3目FIG. 1 is a longitudinal sectional view, FIG. 2 is a sectional view taken along line AA in FIG. 1, and FIG. 3 is a sectional view taken along line BB. 2: Secondary combustion chamber, 3: Primary burner, 4: Waste water discharge nozzle, 8: Secondary burner. Jun 1 area 2nd Raku 3rd
Claims (1)
次燃焼室を設け、一次燃焼室には廃水吐出ノズルを一次
バーナーの下側に設け、二次燃焼室は前記一次燃焼室の
上側に設けて二次バーナーにより前記一次燃焼室の排気
の二次燃焼をおこなわせてその排気は煙突に排出するこ
とを特徴とする含油廃水焼却炉。 2)前記二次燃焼室の容積が前記一次燃焼室の容積の5
0%以下とした特許請求の範囲第1項記載の含油廃水焼
却炉。[Claims] 1) In an oil-containing wastewater incinerator, a primary combustion chamber and a secondary combustion chamber are provided adjacent to each other, a wastewater discharge nozzle is provided in the primary combustion chamber below the primary burner, and the secondary combustion chamber is provided with a wastewater discharge nozzle below the primary burner. An oil-containing wastewater incinerator characterized in that a secondary burner is provided above the primary combustion chamber to perform secondary combustion of the exhaust gas from the primary combustion chamber, and the exhaust gas is discharged into a chimney. 2) The volume of the secondary combustion chamber is 5 times the volume of the primary combustion chamber.
An oil-containing wastewater incinerator according to claim 1, wherein the oil-containing wastewater incinerator has a concentration of 0% or less.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1616886A JPS62175510A (en) | 1986-01-27 | 1986-01-27 | Incinerator of waste water containing oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1616886A JPS62175510A (en) | 1986-01-27 | 1986-01-27 | Incinerator of waste water containing oil |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62175510A true JPS62175510A (en) | 1987-08-01 |
Family
ID=11908978
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1616886A Pending JPS62175510A (en) | 1986-01-27 | 1986-01-27 | Incinerator of waste water containing oil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62175510A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0571721A (en) * | 1991-09-09 | 1993-03-23 | Jietsuto Ro:Kk | Incinerator |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5143025U (en) * | 1974-09-26 | 1976-03-30 | ||
JPS5718090A (en) * | 1980-07-08 | 1982-01-29 | Fujitsu Ltd | Charge sensing and amplifying circuit |
JPS57155017A (en) * | 1981-03-20 | 1982-09-25 | Hitachi Metals Ltd | Energy saving type incinerator |
-
1986
- 1986-01-27 JP JP1616886A patent/JPS62175510A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5143025U (en) * | 1974-09-26 | 1976-03-30 | ||
JPS5718090A (en) * | 1980-07-08 | 1982-01-29 | Fujitsu Ltd | Charge sensing and amplifying circuit |
JPS57155017A (en) * | 1981-03-20 | 1982-09-25 | Hitachi Metals Ltd | Energy saving type incinerator |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0571721A (en) * | 1991-09-09 | 1993-03-23 | Jietsuto Ro:Kk | Incinerator |
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