JPS58213113A - Deodorizing furnace in continuous incinerator for fluid waste - Google Patents

Deodorizing furnace in continuous incinerator for fluid waste

Info

Publication number
JPS58213113A
JPS58213113A JP57161888A JP16188882A JPS58213113A JP S58213113 A JPS58213113 A JP S58213113A JP 57161888 A JP57161888 A JP 57161888A JP 16188882 A JP16188882 A JP 16188882A JP S58213113 A JPS58213113 A JP S58213113A
Authority
JP
Japan
Prior art keywords
furnace
inlet
exhaust gas
deodorizing
gas
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
JP57161888A
Other languages
Japanese (ja)
Inventor
Hirotoshi Saitou
斉藤 太都司
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.)
SHINTOU KIKO KK
Original Assignee
SHINTOU KIKO KK
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 SHINTOU KIKO KK filed Critical SHINTOU KIKO KK
Priority to JP57161888A priority Critical patent/JPS58213113A/en
Publication of JPS58213113A publication Critical patent/JPS58213113A/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
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Incineration Of Waste (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

PURPOSE:To efficiently deodorize and make harmless the gas containing an offensive and harmful component, by a method wherein the gas entering a deodorizing furnace is guided ahead by a straight guiding part, and it collides with a slanted cooliding wall at the forward end thereof to creat a turbulent flow, and a combustion flame is blown into the range of such turbulence. CONSTITUTION:A combustion chamber 3 is formed within a heat resisting wall 2 formed of heat resisting brick, and an inlet 5, through which the tip of an exhaust gas feed pipe 4 is inserted, is formed on the one side of the upper part of the combustion chamber 3. A straight guide part 6 is formed in parallel at the inlet 5, and a colliding wall 7 slanting downward is installed ahead of the guide part 6. This enables colliding of exhaust gas, fed through the inlet 5 and advancing straight in a direction A along the guide part 6, with the colliding wall 7 to creat a turbulence to form a turbulence range 8. A burner nozzle 9 faces the combustion chamber 3 in a manner to point to the turbulence range 8, exhaust gas within the tubulence range 8 is burned by a combustion flame from the nozzle 9 to incinerate an offensive and harmful component, and thereafter the exhaust gas is exhausted through an exhaust port 11.

Description

【発明の詳細な説明】 本発明は、家庭などからの一般廃棄物及び各種工場など
からの産業廃棄物の連続焼却装置における脱臭炉に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a deodorizing furnace in a continuous incinerator for general waste from households and industrial waste from various factories.

従来からこの種の連続q却装置に関して種々の提案′が
なされているが、廃棄物の燃焼効率が悪かったり、排気
ガス中に各種の汚染成分や悪臭成分を多量に含んでいた
り、燃料費が高くつくなどの欠点を有しており、未だ満
足出来る流動性廃棄物の連続焼却装置は得られていない
Various proposals have been made regarding this type of continuous q-cooling device, but they have poor waste combustion efficiency, contain large amounts of various pollutants and malodorous components in the exhaust gas, and suffer from high fuel costs. It has drawbacks such as being expensive, and a satisfactory continuous incineration system for fluid waste has not yet been obtained.

本発明は、廃棄物の燃焼効率が良く、排気カス中に汚染
成分や悪臭成分がほとんど含まれておらず、しかも燃料
費の安い流動性廃棄物の連続焼却装置を提供することを
目的とするものである。−次に本発明の一実施しリとし
て床扉の連続焼却装置を図面とともに説明するC 第1図は連続焼却装置の全体を示す略側面図であル。バ
キュームカーなどで集められた尿尿をフィルター1に通
し、混入している粗大なゴミなどを除去したのち、厘尿
中の固まりなどを破砕機2で砕キ、シかるのちポンプ3
で床扉を貯溜夕/り4に送り込む。貯溜タンク4の内部
には攪拌機構5が備えられており、この攪拌機構5は常
時または随時作動し、貯溜タンク4に収容された床扉6
の固形物が沈澱して固まるのを防止して、服尿6の流動
性、を誰持している。っ 貯溜タンク4の下部には途中に連動ポツプ7を備えた輸
送バイブ8aの一端が設置され、また貯溜夕/り4の上
部には途中にブロアー9aを備えた排気バイブ10aの
一端が設置されている。輸送バイブ8aの他端は液面感
知による計量仮構11を備えた計量夕/り12に設置さ
れ、前記計量機構11は連動ボ/ブ7の駆動部に連結し
ている。
An object of the present invention is to provide a continuous incineration device for fluid waste that has good waste combustion efficiency, contains almost no polluting components or malodorous components in exhaust gas, and has low fuel costs. It is something. - Next, as an embodiment of the present invention, a continuous incinerator with a floor door will be explained with reference to drawings. Fig. 1 is a schematic side view showing the entire continuous incinerator. Urine collected by a vacuum car, etc. is passed through a filter 1 to remove any coarse dirt that may be mixed in. After that, a crusher 2 crushes any lumps in the urine, and then the pump 3
Send the floor door to the storage tank 4. A stirring mechanism 5 is provided inside the storage tank 4, and this stirring mechanism 5 operates constantly or at any time.
This prevents the solid matter from settling and hardening, and improves the fluidity of urine. At the bottom of the storage tank 4, one end of a transport vibrator 8a is installed, which is equipped with an interlocking pop 7, and at the top of the storage tank 4, one end of an exhaust vibrator 10a, which is equipped with a blower 9a, is installed. ing. The other end of the transport vibrator 8a is installed in a weighing station 12 equipped with a temporary measuring mechanism 11 based on liquid level sensing, and the weighing mechanism 11 is connected to the drive section of the interlocking bob 7.

したがって連動ポンプ7によって貯溜タンク4中の深床
6が輸送バイブ8aを通って計量タンク12に送り込ま
れ、計量タンク12中の凍原l夜面が所定位置にくると
計量機構11が感知し、それによって連動ポンプ7の作
動が停止して、計量夕/り12に一定量の凍原6か供紛
される。
Therefore, the deep bed 6 in the storage tank 4 is fed into the measuring tank 12 by the interlocking pump 7 through the transport vibrator 8a, and when the frozen ground surface in the measuring tank 12 reaches a predetermined position, the measuring mechanism 11 senses it. As a result, the operation of the interlocking pump 7 is stopped, and a certain amount of frozen ground 6 is delivered at the measurement date 12.

計量タンク12の下部には途中に自動パルプ13を備え
た輸送バイブ8bの一端が設置され、一方計量タンク1
2の上部には途中にブロアー9bを備えた排気バイブ1
0.bの一端が設置されてい転可能に装着された回転燃
焼炉15の入口16に連設されており、更に回転燃焼炉
15の入口16には一次バーナー17が設けられている
At the bottom of the weighing tank 12, one end of a transporting vibrator 8b with an automatic pulp 13 is installed in the middle, while the weighing tank 1
At the top of 2, there is an exhaust vibe 1 with a blower 9b in the middle.
0. One end of the rotary combustion furnace 15 is connected to an inlet 16 of a rotary combustion furnace 15 which is rotatably mounted, and a primary burner 17 is further provided at the inlet 16 of the rotary combustion furnace 15.

第2図ならびに第3図は、回転燃焼炉15の断面を示す
ものである。回転燃焼炉15は左方にそれぞれ入口16
と出口18を備えた円筒状の中空体からなり、側面は内
筒19と外筒2oの二重壁となっており、内@19と外
筒20の間にはガラスウールボードやセラミックスウー
ルボードなどから断熱材21が装填されている。回転燃
焼炉15の側面のやや入口16宥りには灰の取出口22
と、この取出口22を開閉する蓋23が設けられており
、蓋23の内部にも断熱材21が装填さnている。
2 and 3 show cross sections of the rotary combustion furnace 15. FIG. The rotary combustion furnace 15 has an inlet 16 on the left side.
It consists of a cylindrical hollow body with an outlet 18 and a double wall of an inner tube 19 and an outer tube 2o. A heat insulating material 21 is loaded from, for example. There is an ash outlet 22 on the side of the rotary combustion furnace 15, slightly behind the inlet 16.
A lid 23 is provided to open and close this outlet 22, and a heat insulating material 21 is also loaded inside the lid 23.

24は内筒19と外筒20を連結する連結部で、この連
結部24は回転燃焼炉15の左右端部の近くに円周方向
へ所定の間隔をおいて設けられている。連結部24は第
4図に示すように、内筒19の外面に間隔をおいて2枚
の連結片25.25が突設され、また外筒20の内面に
前記連結片25゜25の間に挿入する連結片26が突設
されて、これら連結片25と26は挿通したボルト27
によって連結されている。外筒20の連結片26に形成
されたボルト27の挿通孔28は、第5図に示すように
斜め外周に向けて長孔状に形成されている。これは回転
燃焼炉15の使用時に内筒19と外筒20がそれぞれ軸
方向ならびに半径方向へ熱膨張しても、それを許容する
ために長孔状になっている。なお図示のものに代え、外
筒20の連結片26には円形の挿通孔28を穿設し、内
筒19の連結片25.25に斜め外周に向っだ長孔状の
挿通孔28を形成してもよい。
Reference numeral 24 denotes a connecting portion that connects the inner cylinder 19 and the outer cylinder 20, and this connecting portion 24 is provided near the left and right ends of the rotary combustion furnace 15 at a predetermined interval in the circumferential direction. As shown in FIG. 4, the connecting portion 24 has two connecting pieces 25 and 25 protruding from the outer surface of the inner cylinder 19 at intervals, and a space between the connecting pieces 25 and 25 on the inner surface of the outer cylinder 20. A connecting piece 26 is protruded to be inserted into the
connected by. The insertion hole 28 for the bolt 27 formed in the connecting piece 26 of the outer cylinder 20 is formed in the shape of a long hole diagonally toward the outer periphery, as shown in FIG. This has a long hole shape to allow thermal expansion of the inner cylinder 19 and outer cylinder 20 in the axial direction and radial direction, respectively, when the rotary combustion furnace 15 is used. Note that instead of what is shown in the drawings, a circular insertion hole 28 is formed in the connection piece 26 of the outer cylinder 20, and an elongated insertion hole 28 is formed in the connection piece 25, 25 of the inner cylinder 19 diagonally toward the outer periphery. You may.

回転燃焼炉15の内面には、凍原6を抄い上けるための
゛羽根29が第6図に示すように相互にずれた位置に所
定の間隔をおいて多数列を成して突設されている。この
羽根29の水平切断面の形状はくの字状になっており、
羽根29の開き角度0は約30〜90度が適当で、通常
はこの羽根29が開いたA方向に回転燃焼炉15が回転
する。更にこの羽根29は第2図に示すように、灰の取
出口22の方向に向いて5度程度若干傾斜して固定され
ている。このようにすれば、深尿6を燃焼して生成した
灰が羽根290回転によって取出口22の近傍に自動的
に集められる。外筒20の外側面には、回転燃焼炉15
0回転を案内するための突条30が所定の間隔をおいて
設けられている。
On the inner surface of the rotary combustion furnace 15, blades 29 for scooping up the frozen ground 6 are protruded in multiple rows at predetermined intervals at mutually shifted positions, as shown in FIG. ing. The horizontal cut surface of this blade 29 has a dogleg shape,
The opening angle 0 of the blades 29 is suitably about 30 to 90 degrees, and the rotary combustion furnace 15 usually rotates in the direction A in which the blades 29 are opened. Furthermore, as shown in FIG. 2, this blade 29 is fixed with a slight inclination of about 5 degrees toward the direction of the ash outlet 22. In this way, the ash generated by burning the deep urine 6 is automatically collected near the outlet 22 by the rotation of the blade 290. A rotary combustion furnace 15 is provided on the outer surface of the outer cylinder 20.
Projections 30 for guiding the zero rotation are provided at predetermined intervals.

回転燃焼炉15の出口18(ては、脱臭炉31が連設さ
れている。第7図に示すように脱臭炉31における排気
ガス導入口32の近傍には、二次)く−ナー33の燃焼
炎の入口34が水平に傾斜して設けられており、排気カ
スの流れに対する燃焼炎の入り角度αは約20〜23の
範囲に設定されている0脱臭炉31の内側には耐熱性レ
ンガなど力・らなる耐熱壁35が設けられており、排気
ガス導入口32から入った排気ガスは前方へ直進し、傾
斜して設けられた傾斜壁36に当って排気ガスの流れが
撹乱する。この乱気領域に二次バーナー33の・燃焼炎
が二次空気と共に吹き込1れて、排気ガス中の有−臭成
分が効率よく燃焼され、無臭性になった排気ガスがガス
放出口37がら集塵機45を通り熱風ファン38によっ
て煙突39に送られる。なお第1図に示すよう(テ、貯
溜タンク4及び計量タンク12に一端が設置された排気
バイブ10a、10bの他端は脱臭炉31に導入されて
おり、貯溜タンク4及び計量夕/り12の上部空間に溜
った有臭成分は、貯溜タンク4及び計量タンク12に深
床6が送り込まれたときに駆動するブロアー9a、9b
によって脱臭炉31に送り込まれて、−緒に燃焼される
。これらから本発明の連続焼却装置が構成ばれている。
A deodorizing furnace 31 is connected to the outlet 18 of the rotary combustion furnace 15. As shown in FIG. The inlet 34 of the combustion flame is installed horizontally and inclined, and the angle α of the combustion flame with respect to the flow of exhaust gas is set in the range of approximately 20 to 23.0 Heat-resistant bricks are installed inside the deodorizing furnace 31. A heat-resistant wall 35 is provided, and the exhaust gas entering from the exhaust gas inlet 32 travels straight forward and hits the inclined wall 36, which is provided at an angle, and the flow of the exhaust gas is disturbed. The combustion flame of the secondary burner 33 is blown into this turbulent region together with the secondary air, and the odor components in the exhaust gas are efficiently combusted, and the odorless exhaust gas is released into the gas discharge port 37. It passes through a dust collector 45 and is sent to a chimney 39 by a hot air fan 38. As shown in FIG. The odor components accumulated in the upper space of
is fed into the deodorizing furnace 31 and burned together. These constitute the continuous incineration device of the present invention.

次にこの装置の作動原理について説明する。Next, the operating principle of this device will be explained.

貯溜タンク−4に収容されている凍原6は、連動ポンプ
7により計量タンク12に送り込まれる。
The frozen ground 6 contained in the storage tank 4 is fed into the metering tank 12 by the interlocking pump 7.

計量タンク12では、深床6を回転燃焼f15に流し込
んだ際に第2図及び第3図に示すように、深床6の液面
が回転燃焼炉150回転軸部4oより下方になるように
収容量が設定されているにの収容量の調整により、深床
6が回転軸部40が −ら漏洩するのが防止出来る。
In the measuring tank 12, when the deep bed 6 is poured into the rotary combustion f15, as shown in FIGS. By adjusting the storage capacity once the storage capacity has been set, it is possible to prevent the deep bed 6 from leaking from the rotating shaft portion 40.

計量タンク12に所定量の深床6が送り込まれると計量
機構11が感知し、その作動に−より連動ポンプ7が停
止して、次に自動ノゼルブ13が開き凍原6が回転燃焼
炉15に流し込まれる。回転燃焼炉15には一次バーナ
ー17からの燃焼炎41が常時軸線方向に沿って中央空
間部42に吹き込まれているから、回転燃焼炉15の炉
内温度は高くなっているが、凍原6の流し込みによって
炉内温度は適当な速度で下がる。深床6の流し込みが終
る頃に炉内が所定温度・・・例えば200 ’C・・・
になるように、自動バルブ13の開き度合が調整されて
おり、炉内が所定温度になったところで炉内に感知部を
臨ませた熱電対43が作動する。この熱電対43は自動
バルブ13と連結しており、熱電対43の作動により自
動バルブ13が閉じる。この自動バルブ13が閉じると
同時に、自動バルブ13と連動する連動ポンプ7が駆動
して、床張6を計量タンク12に送り込み次の進備をし
ている。
When a predetermined amount of deep bed 6 is fed into the metering tank 12, the metering mechanism 11 senses, and its operation causes the interlocking pump 7 to stop, and then the automatic nozzle valve 13 opens and the frozen ground 6 is poured into the rotary combustion furnace 15. It will be done. Since the combustion flame 41 from the primary burner 17 is constantly blown into the central space 42 of the rotary combustion furnace 15 along the axial direction, the temperature inside the rotary combustion furnace 15 is high, but the temperature inside the rotary combustion furnace 15 is high. By pouring, the temperature inside the furnace decreases at an appropriate rate. By the time the deep bed 6 is poured, the temperature inside the furnace reaches a predetermined temperature...for example, 200'C...
The opening degree of the automatic valve 13 is adjusted so that the temperature inside the furnace reaches a predetermined temperature, and the thermocouple 43 whose sensing portion faces the inside of the furnace is activated. This thermocouple 43 is connected to the automatic valve 13, and the automatic valve 13 closes when the thermocouple 43 operates. At the same time as this automatic valve 13 closes, the interlocking pump 7 that is interlocked with the automatic valve 13 is driven to feed the floor covering 6 into the measuring tank 12 for the next preparation.

一方床扉6を入れた回転燃焼炉15は、羽根29の開い
たA方向に回転する。この回転に伴ない羽根29は深床
6を抄い上げて愚焼炎41に向けて掛ける。深床6は散
布されながら燃焼炎41と接触し、最初凍原6中の水分
ならびに硫化水素、メチルメルカプタン、硫化メチル、
2硫化メチル。
On the other hand, the rotary combustion furnace 15 containing the floor door 6 rotates in the direction A in which the blades 29 are opened. With this rotation, the blade 29 lifts up the deep bed 6 and hangs it toward the burning flame 41. The deep bed 6 comes into contact with the combustion flame 41 while being sprayed, and initially the moisture in the frozen ground 6 as well as hydrogen sulfide, methyl mercaptan, methyl sulfide,
Methyl disulfide.

トリエチルアミン、アンモニアなどの有臭成分。Odorous components such as triethylamine and ammonia.

イオウ酸化物、煤塵などが脱臭炉31に送り込1れて、
凍原6中の水分が無くなると粉末化し、この可・燃性の
粉末が回転燃焼炉15内で焼却される0この粉末の燃焼
により炉内温度が徐々に高まり、燃焼末期近くで約60
0〜800 C程度の高温になり、この炉内温度を熱電
対43が感知して、自動バルブ13を開き、計量タンク
12中の深床6を回転燃焼炉15に流し込み、前述と同
じ様に凍原6の焼却が行なわれる。
Sulfur oxides, soot dust, etc. are sent to the deodorizing furnace 31,
When the moisture in the frozen ground 6 disappears, it becomes powder, and this combustible and combustible powder is incinerated in the rotary combustion furnace 15.The combustion of this powder gradually increases the temperature inside the furnace, and near the end of combustion, the temperature inside the furnace reaches about 60℃.
The temperature inside the furnace reaches a high temperature of about 0 to 800 C, and the thermocouple 43 senses this temperature inside the furnace, opens the automatic valve 13, pours the deep bed 6 in the metering tank 12 into the rotary combustion furnace 15, and continues the process in the same manner as described above. Frozen Plains 6 will be incinerated.

凍原6をフィルター1及び破砕機2を通さないで、ある
いは固まりのある他の廃棄物を灰の取出口23から投入
した場合、回転燃焼炉15をB方向に回転すれば、羽根
29の尖端部44によって廃棄物中の固まりが粉砕出来
る。
If the frozen ground 6 is not passed through the filter 1 and the crusher 2, or if other solid waste is input from the ash outlet 23, if the rotary combustion furnace 15 is rotated in the direction B, the tips of the blades 29 will be removed. 44 can crush lumps in the waste.

回転燃焼炉15の内筒19ならびに羽根29の表面に、
アルミナやセラミックスなどの耐熱性。
On the surfaces of the inner cylinder 19 and blades 29 of the rotary combustion furnace 15,
Heat resistant materials such as alumina and ceramics.

耐腐蝕性の被膜を形成すれば、内筒19ならびに羽根2
9の侵蝕や熱変形が抑制される。
If a corrosion-resistant coating is formed, the inner cylinder 19 and the blades 2
9. Erosion and thermal deformation are suppressed.

本発明に係る流動性廃棄物の連続焼却装置は前述したよ
うに、流動性廃棄物を収容する貯溜タンク4こ、該貯溜
夕/り4から送られた流動性廃棄物を計量する計量夕/
り12と、燃焼炎41が軸線方向に沿って中央空間部4
2に吹込まれると共に、内面に流動性廃棄物を抄い上げ
る羽根29を多数突設した回転燃焼炉15と、該回転燃
焼炉15から排出された有臭排気ガスを燃焼する脱臭炉
とを備え、低温と高温の2点で作動する熱電対43の感
知部を前記回転燃焼炉15の炉内に臨まぜ、計量タンク
12と回転燃焼炉15を導通する輸送パイプ8bの途中
には前記執電対43の作動iCよって開閉する自動バル
ブ13が、また貯溜タンク4と計量タンク12を導通す
る輸送バイブ8aの途中には前記自動バルブ13ならび
に計量タンク12の計量機構11と連動する連動ポツプ
7とが設けられており、連動ポンプ7により貯溜夕/り
4から送り送まれだ流動性廃棄物を計量タンク12で一
定量計量したのち、自動バルブ13が開いて流動性廃棄
物を回転燃焼炉15に流し込み、燃焼開始時における回
転燃焼炉の炉内温度を熱電対43で感知して自動バルブ
13を閉じると同時に、連動ポンプ7を作動させて流動
性廃棄物を計量タンク12に送り込み、一方回転燃焼炉
】5の回転に伴ない羽根で流動性廃棄物を抄い上げて燃
焼炎41に向けて散布し、流動性廃棄物中の水分及び有
臭成分を揮散させ、該有臭成分を脱臭炉31に導いて燃
焼させると共に、流動性廃棄物中の他の可燃焼性成分を
回転燃焼炉15内で焼却させ、焼却後期における回転燃
焼炉15の炉内温度を熱電対43で感知して自動バルブ
13を開いて、計量タンク12中の流動性廃棄物を回転
燃焼炉15へ送り込む機構になっている。
As described above, the continuous incineration apparatus for fluid waste according to the present invention includes a storage tank 4 for storing fluid waste, and a measuring tank for weighing the fluid waste sent from the storage tank 4.
12, and the combustion flame 41 extends along the axial direction into the central space 4.
A rotary combustion furnace 15 has a large number of blades 29 protruding from its inner surface to scoop up fluid waste, and a deodorizing furnace burns odor-filled exhaust gas discharged from the rotary combustion furnace 15. A sensing part of a thermocouple 43 that operates at two points, low temperature and high temperature, is placed in the furnace of the rotary combustion furnace 15. There is an automatic valve 13 that opens and closes according to the operation iC of the couple 43, and an interlocking pop 7 that is interlocked with the automatic valve 13 and the metering mechanism 11 of the metering tank 12 in the middle of the transportation vibrator 8a that connects the storage tank 4 and the metering tank 12. After a certain amount of fluid waste sent from the storage tank 4 by the interlocking pump 7 is measured in the measuring tank 12, an automatic valve 13 is opened and the fluid waste is sent to the rotary combustion furnace. 15, the temperature inside the rotary combustion furnace at the start of combustion is sensed by the thermocouple 43, and the automatic valve 13 is closed, and at the same time, the interlocking pump 7 is activated to send the fluid waste into the measuring tank 12, while [Rotary Combustion Furnace] As the rotary combustion furnace rotates, the fluid waste is scooped up by the blades and dispersed toward the combustion flame 41, and the moisture and odorous components in the fluid waste are volatilized, and the odorous components are removed. At the same time, other combustible components in the fluid waste are incinerated in the rotary combustion furnace 15, and the temperature inside the rotary combustion furnace 15 in the latter stage of incineration is detected by the thermocouple 43. The mechanism is such that the automatic valve 13 is opened in order to send the fluid waste in the metering tank 12 to the rotary combustion furnace 15.

したがって流動性廃棄物が多数の羽根29:てよって抄
い上げられ、燃焼炎41に向って散布されるから、廃棄
物が効率よく燃焼炎41と接触し、水分及び有臭成分の
揮散と可燃性成分の焼却力・確実に行なわれる。
Therefore, the fluid waste is scooped up by a large number of blades 29 and dispersed toward the combustion flame 41, so that the waste efficiently contacts the combustion flame 41, vaporizes moisture and odor components, and evaporates combustible components. The ability to incinerate the sexual components is ensured.

回転燃焼炉15内で廃棄物を焼却する間自動バルブ13
は閉じているから、炉内温度を高く維持して燃焼効率を
高めることが出来ると共に、燃料費の節減が可能である
Automatic valve 13 during incineration of waste in rotary combustion furnace 15
Since the furnace is closed, it is possible to maintain a high temperature inside the furnace and increase combustion efficiency, and it is also possible to reduce fuel costs.

更に回転燃焼炉1..5から排出された有臭排気ガスは
回転燃焼炉15によってかなり高温まで加熱されている
から、脱臭炉31内での脱臭効果は極めて高く、脱臭炉
31から放出された排気カスは無臭性であるなど諸種の
利点を有し、実用的価値が極めて高い。
Furthermore, rotary combustion furnace 1. .. Since the odoriferous exhaust gas discharged from the deodorizing furnace 31 is heated to a considerably high temperature by the rotary combustion furnace 15, the deodorizing effect in the deodorizing furnace 31 is extremely high, and the exhaust gas discharged from the deodorizing furnace 31 is odorless. It has various advantages such as, and has extremely high practical value.

次の表は、前記実施例について煙突39から放出された
排気ガスの分析結果である。
The following table shows the analysis results of the exhaust gas emitted from the chimney 39 for the above example.

表 この表からも本発明の優秀性が理解出来る0table The superiority of the present invention can also be understood from this table.

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

図面は本発明の実施例を示すもので、第1図id装置の
全体を示す略側面図、第2図は回転燃焼炉の要部を切断
した側面図、第3図は第2図■−■切断面図、第4図は
回転燃焼炉に2ける内筒と外筒の連結部の拡大断面図、
第5図は該連結部に連結片の正面図、第6図は羽根の突
設状態を示す斜視図、第7図は脱臭炉の水平断面図であ
る。 1  フィルター 2  破砕機 4  貯溜タック 5  攪拌機構 6  凍原 7  連動ボノグ 8a 輸送パイプ 8b 輸送パイプ 10a  排気パイプ 10b  排気パイプ 11  計量機構 12 計量タンク 13  自動ノぐルフ゛ 15 回転燃焼炉 19 内筒 20 外筒 21 断熱材 22 灰の取出口 29 羽根 31 脱臭炉 40 回転軸部 41 燃焼炎 42 中央空間部 43 熱電対 特  許  出  願  人     斎  藤  大
部司 (IN S−1λン代  理  人  弁理士 
    古  1) 剛  啓手続補正書 昭和58年7月7日 特許庁長官 若 杉和 夫殿 1、事件の表示 昭和57年  特   願第161888号2、 発明
の名称   流動性廃棄物の連続焼却装置における脱臭
炉3、 補正をする者 事件との関係      特許 出 願人4、代理人 5゜ 補正命令の日付       自発補正6 補正
により増加する発明の数      なし7・補正0対
象            −明細書全文9図面全部 
   、−/]明       細       書 1、発明の名称 2、特許請求の範囲 1 有臭有害成分を含んだガスを導入する入口と、該入
口から炉内?こ入ったガスを前方へ案内する直進案内部
と、該直進案内部の前方に煩斜して設けられた衝突壁と
、ガスが該衝突壁に突き当って形成される乱気領域3こ
同けて燃焼炎を吹ぎ込む−4入管とを備えたことを特徴
とする脱臭炉。 2 直進案内部に対するP悦炎の導入管の傾斜角度を約
20〜23度の範囲(こ規制した特許請求の範囲第1項
記載の脱臭・戸。 3、発明の詳細な説明 本発明は硫化水素、メチルメルカプクン、硫rヒj f
 /l/ 、 2 硫化メチル、ト;1エチルアミン、
アセトアルデヒド、ホルムアルデヒドなどの有i有=成
分を含んだガスを、燃焼によって変性する脱臭炉に関す
るものである。 従来よりこの種の脱臭炉ンこついて種々提案されている
が、脱臭効果が十分てなかったり、構のか複雑となり製
作コストが高くつくなとの欠つ、を有し、未だ満足出来
る脱臭炉は得られていない。 本発明は脱臭効率が高く、しかも構造か簡単て製作コス
トの安価な脱臭炉を提供することを目的とするもので、
以下一実施例を図面と共に説明する。 脱臭炉1は、耐熱性レンガな′とからなる耐熱壁2で区
画され、内側に?−焼室3か形成されて(・る。 脱臭炉1の左側シこは排気バイブ4の先端を挿入する入
口5が設けられており、硫化水素やメチルメレカブタン
なとの有臭有害成分を含んだガスかこの人口5から炉内
ンこ導入される。入口5から炉内に入ったガスは直進案
内部6によって矢印A方向に直進し、直進案内部6の前
方に傾斜して設けられた衝突壁7の壁面に突き当る。ガ
スは衝突壁7に突き当ると流れが撹乱して、乱気領域8
が形成される。なお直進案内部6に対する衝突壁7両頭
斜角度αは、ガスの燃焼効率を考慮して約110〜16
0度が導当である。 9は入口5の横に設置したバーナーのノズルて、該ノズ
/I/9の柩焼炎を二次字数と共に脱臭炉1に導く導入
管10が入口5と水平(こ傾斜して設けられている。前
記ノズル9からの欺暁炎がガスの乱気領域8に向けて吹
き込まれるよう導入管1oの方向が設定されており、種
々の実験結果から直進案内部5に対する導入管lOの傾
斜角度βが約20−23度の′場合に極めて良好な脱臭
効果が得られる。11は脱臭炉1の排気口、12排気口
11の近傍に設けた凹部で、ガスの流れを乱して炉内滞
留時間を長くする役割を有している。 更にガスの炉内滞留時間を長くして更に脱臭効果を高め
るため、衝突壁7の延長方向に破線で示す如く耐熱性の
邪魔板13を設置することも可能である。 本発明の脱臭炉は前述したように、有具有害成9分を含
んだガスを導入する入口5と、該入口5から炉内に入っ
たガスを前方へ案内する直進案内部6と、該直進案内部
5の前方tこ傾斜して設けられた衝突壁7と、ガスが該
衝突壁7に突き当って形成される乱気領域8に向けて燃
焼炎を吹き込む導入管10とを備えている。 有臭有害成分を含んだガスが衝突壁7に突き当って撹乱
したときVこ有臭有害成分の燃焼が行なわれるから、脱
臭効果が弾めて高い。しかも構造が非常に簡単で、製作
コストが安価であるなとの利点を有し、経済的価値が高
い。 本発明の脱臭炉は、深床や家畜糞尿を焼却した際シこ発
生する有臭有害ガスの処理なとtこ使用される。 4、図面の簡単な説明 図面は本発明の実施例における脱臭炉の水平切断面図で
ある。 1   脱臭炉 5    人口 6   直進案内部 7   衝突壁 8   乱気領域 10   導入管 β   傾斜角度 特許出願人 斉藤、大部司(ほか1名)代 理 人 弁
理士  古 1)剛 啓手続補正書 昭和58年7 月11日 特許庁長官 若杉和夫殿 1、事件の表示 昭和57年  特   願第1.61888号2、発明
の名称    脱臭炉 3、 補正をする者 事件との関係   特許 出 願人 性  所 氏 名(名称)   斎  藤  太都司 (ほか1名
)4、代理人 住  所     広島市゛°−区r、−7さ】9プ 
15どし3階 「7下下=。 氏  名     (6232)升理士 古 1)剛 
啓 イ゛二5、補正命令の日付     自発補正6、
補正により増加する発明の数    なし7、補正の対
象 明細書の特許請求の範囲1発明の詳細な説明の欄   
  □明細書(昭和58年7月7日提出ンを次の通り補
正する。 (イ)特許請求の範囲を別紙の通り補正する。 (口J 第3頁第12行目 「〜23度」の「3」を「5」と補正する。 特  許  藷  求  の  範  囲1 有臭有害
成分を含んだガスを導入する入口と、該入口から炉内に
入ったガスを前方情案内する直向けて燃焼炎を吹き込む
導入管とf:備えたことを特徴とする脱臭炉。 2 直進案内部に対する燃滉炎の導入管の傾斜角度を約
20〜25度の範囲に親電・」シた特許請求の範囲第1
項記載の脱臭炉。
The drawings show an embodiment of the present invention, and Fig. 1 is a schematic side view showing the entire ID device, Fig. 2 is a side view with main parts of the rotary combustion furnace cut away, and Fig. 3 is Fig. 2 - ■Cross-sectional view, Figure 4 is an enlarged cross-sectional view of the joint between the inner cylinder and the outer cylinder in the rotary combustion furnace.
FIG. 5 is a front view of a connecting piece on the connecting portion, FIG. 6 is a perspective view showing a protruding state of the blades, and FIG. 7 is a horizontal sectional view of the deodorizing furnace. 1 Filter 2 Crusher 4 Storage tack 5 Stirring mechanism 6 Freeze ground 7 Interlocking bonog 8a Transport pipe 8b Transport pipe 10a Exhaust pipe 10b Exhaust pipe 11 Measuring mechanism 12 Measuring tank 13 Automatic noggle 15 Rotary combustion furnace 19 Inner cylinder 20 Outer cylinder 21 Insulating material 22 Ash outlet 29 Vane 31 Deodorizing furnace 40 Rotating shaft 41 Combustion flame 42 Central space 43 Thermocouple patent Applicant: Tsukasa Saito Obe (IN S-1λN agent, patent attorney)
Old 1) Written amendment to Gou Kei's procedure dated July 7, 1980, Kazuo Wakasugi, Commissioner of the Patent Office1, Indication of the case, 1982, Patent Application No. 1618882, Title of the invention: Continuous incineration device for fluid waste Deodorizing furnace 3. Relationship with the case of the person making the amendment Patent Applicant 4, Agent 5゜ Date of amendment order Voluntary amendment 6 Number of inventions increased by amendment None 7 / 0 amendments - Full text of the specification 9 All drawings
, -/] Description 1, Title of the invention 2, Claim 1 An inlet for introducing gas containing odorous harmful components, and a flow from the inlet into the furnace? A straight guide section that guides the trapped gas forward, a collision wall that is obliquely provided in front of the straight guide section, and three turbulent regions that are formed when the gas hits the collision wall. A deodorizing furnace characterized by being equipped with four inlet tubes into which combustion flame is blown. 2. The deodorizing door according to claim 1, which restricts the inclination angle of the P-yellow flame introduction pipe with respect to the straight guide part to be within a range of about 20 to 23 degrees. 3. Detailed Description of the Invention The present invention Hydrogen, methylmercapkun, sulfur
/l/, 2 methyl sulfide, 1 ethylamine,
The present invention relates to a deodorizing furnace that denatures gas containing organic components such as acetaldehyde and formaldehyde by combustion. Various proposals have been made regarding this type of deodorizing oven, but there are still some satisfactory deodorizing ovens that lack sufficient deodorizing effect, are complicated in structure, and are expensive to manufacture. Not obtained. The object of the present invention is to provide a deodorizing furnace that has high deodorizing efficiency, has a simple structure, and is inexpensive to manufacture.
An embodiment will be described below with reference to the drawings. The deodorizing furnace 1 is partitioned by a heat-resistant wall 2 made of heat-resistant bricks. - A baking chamber 3 is formed (・ru. The left side of the deodorizing furnace 1 is provided with an inlet 5 into which the tip of an exhaust vibrator 4 is inserted. The gas contained therein is introduced into the furnace through the inlet 5. The gas that enters the furnace through the inlet 5 travels straight in the direction of arrow A by a straight guide part 6, which is provided at an angle in front of the straight guide part 6. When the gas hits the collision wall 7, the flow is disturbed and a turbulent region 8
is formed. Note that the double-headed oblique angle α of the collision wall 7 with respect to the straight guide portion 6 is approximately 110 to 16 in consideration of gas combustion efficiency.
0 degrees is the standard. Reference numeral 9 denotes a nozzle of a burner installed beside the inlet 5, and an inlet pipe 10 for guiding the coffin burning flame of the nozzle/I/9 to the deodorizing furnace 1 along with the secondary character number is installed horizontally (at an angle) with the inlet 5. The direction of the introduction pipe 1o is set so that the dawning flame from the nozzle 9 is blown toward the gas turbulence region 8, and the inclination angle of the introduction pipe 1O with respect to the straight guide part 5 is determined from various experimental results. An extremely good deodorizing effect can be obtained when β is about 20-23 degrees.11 is an exhaust port of the deodorizing furnace 1, and 12 is a recess provided near the exhaust port 11, which disturbs the gas flow inside the furnace. It has the role of increasing the residence time of the gas.In order to further increase the residence time of the gas in the furnace and further enhance the deodorizing effect, a heat-resistant baffle plate 13 is installed in the extending direction of the collision wall 7 as shown by the broken line. As described above, the deodorizing furnace of the present invention has an inlet 5 for introducing gas containing harmful components, and a straight line for guiding the gas that enters the furnace from the inlet 5 forward. An introduction method in which combustion flame is blown toward the guide section 6, the collision wall 7 provided at an angle in front of the straight guide section 5, and the turbulent region 8 formed when the gas collides with the collision wall 7. The tube 10 is provided with a pipe 10. When the gas containing odorous harmful components collides with the collision wall 7 and is disturbed, the odorous harmful components are combusted, so the deodorizing effect is highly effective.Moreover, the structure The deodorizing furnace of the present invention has the advantage of being very simple and inexpensive to manufacture, and has high economic value. 4. Brief description of the drawing The drawing is a horizontal cross-sectional view of a deodorizing furnace in an embodiment of the present invention. 1. Deodorizing furnace 5 Population 6 Straight guide section 7 Collision wall 8 Turbulent region 10 Introductory pipe β Slant angle Patent applicant Saito, Tsukasa Obe (and one other person) Attorney Patent attorney Furu 1) Tsuyoshi Kei procedural amendment July 11, 1980 Commissioner of the Japan Patent Office Kazuo Wakasugi 1, Indication of the case 1981 Patent Application No. 1.618882, Title of invention: Deodorizing furnace3, Relationship with the case of the person making the amendment Patent Applicant Name: Taitoji Saito (and 1 other person)4, Agent Address: Hiroshima City゛°-ku r,-7sa]9p
15 Doshi 3rd floor "7 down =. Name (6232) Masu Rishi Ko 1) Tsuyoshi
E-25. Date of amendment order Voluntary amendment 6.
Number of inventions increased by amendment None 7, Detailed description of claim 1 invention of the specification subject to amendment
□The specification (submitted on July 7, 1988) is amended as follows. (a) The scope of claims is amended as shown in the attached sheet. "3" is corrected to "5". Scope of the patent request 1: An inlet for introducing gas containing odorous harmful components, and a direct direction for guiding the gas that enters the furnace from the inlet. A deodorizing furnace characterized by having an inlet pipe for blowing combustion flame into it; range 1
Deodorizing furnace described in section.

Claims (1)

【特許請求の範囲】[Claims] 有臭有害成分を含んだガス全導入する入口と、該入口か
ら炉内に入ったガスを前方へ案円する直進案内部と、該
直進案内部の前方Vこ傾斜して設けられた衝突壁と、ガ
スが該衝突壁に突き当って形成される乱気領域に向けて
燃焼炎を吹き込む導入管とを備えたことを特徴とする流
動性廃棄物の連続焼却#C置における脱臭炉。
An inlet for introducing all of the gas containing odorous harmful components, a straight guide part that guides the gas that enters the furnace from the inlet forward, and a collision wall that is inclined at a V angle in front of the straight guide part. A deodorizing furnace in continuous incineration #C of fluid waste, characterized in that it is equipped with: and an introduction pipe for blowing a combustion flame into a turbulent region formed when the gas hits the collision wall.
JP57161888A 1982-09-16 1982-09-16 Deodorizing furnace in continuous incinerator for fluid waste Pending JPS58213113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57161888A JPS58213113A (en) 1982-09-16 1982-09-16 Deodorizing furnace in continuous incinerator for fluid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57161888A JPS58213113A (en) 1982-09-16 1982-09-16 Deodorizing furnace in continuous incinerator for fluid waste

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP13201177A Division JPS5466570A (en) 1977-11-02 1977-11-02 Device for continuously incinerating fluid waste

Publications (1)

Publication Number Publication Date
JPS58213113A true JPS58213113A (en) 1983-12-12

Family

ID=15743897

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57161888A Pending JPS58213113A (en) 1982-09-16 1982-09-16 Deodorizing furnace in continuous incinerator for fluid waste

Country Status (1)

Country Link
JP (1) JPS58213113A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020106191A (en) * 2018-12-27 2020-07-09 株式会社神鋼環境ソリューション Structure for supporting rotary furnace

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5790924A (en) * 1980-11-27 1982-06-05 Toshiba Corp Manufacture of c cut core

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5790924A (en) * 1980-11-27 1982-06-05 Toshiba Corp Manufacture of c cut core

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020106191A (en) * 2018-12-27 2020-07-09 株式会社神鋼環境ソリューション Structure for supporting rotary furnace

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