JPS6212475Y2 - - Google Patents

Info

Publication number
JPS6212475Y2
JPS6212475Y2 JP1982084308U JP8430882U JPS6212475Y2 JP S6212475 Y2 JPS6212475 Y2 JP S6212475Y2 JP 1982084308 U JP1982084308 U JP 1982084308U JP 8430882 U JP8430882 U JP 8430882U JP S6212475 Y2 JPS6212475 Y2 JP S6212475Y2
Authority
JP
Japan
Prior art keywords
molded product
ash
cooling chamber
incinerator
trough
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
JP1982084308U
Other languages
Japanese (ja)
Other versions
JPS58185738U (en
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 filed Critical
Priority to JP8430882U priority Critical patent/JPS58185738U/en
Publication of JPS58185738U publication Critical patent/JPS58185738U/en
Application granted granted Critical
Publication of JPS6212475Y2 publication Critical patent/JPS6212475Y2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【考案の詳細な説明】 この考案は、都市ごみ焼却炉における灰固形化
装置に関し、特に、含有有害物が溶出しない成形
物を成形可能な灰固形化装置に関するものであ
る。
[Detailed Description of the Invention] This invention relates to an ash solidification device in a municipal waste incinerator, and particularly relates to an ash solidification device capable of molding a molded product from which harmful substances contained therein are not eluted.

第1図は、従来の都市ごみ焼却処理システムの
流れ図であるが、これに示すように、都市ごみ用
の焼却炉からは、二種の灰が排出している。すな
わち、焼却炉本体におけるロストルの間隙から落
下する質量の比較的大な焼却灰と、燃焼排ガス中
に飛散し集塵機にて捕集される微細な集塵灰とで
ある。そして前者はカドミウム、鉛、亜鉛等の重
金属を含有し、後者は塩化物を含有しており、共
に有害であるので、これをそのまま埋立て地へ投
棄したのでは、周辺住民の健康、農作物等に著し
い影響が出る。
FIG. 1 is a flowchart of a conventional municipal waste incineration system, and as shown, two types of ash are discharged from an incinerator for municipal waste. That is, the incinerated ash has a relatively large mass and falls from the gap between the rotors in the incinerator body, and the fine collected ash is scattered in the combustion exhaust gas and collected by the dust collector. The former contains heavy metals such as cadmium, lead, and zinc, and the latter contains chloride, both of which are harmful, so dumping them directly into a landfill will harm the health of surrounding residents and damage crops. will have a significant impact on

そこで、従来は第1図に示すとおり、炉本体か
らガス冷却室、熱交換器を経由して集塵機に到る
煙道において、スラリー状の水酸化カルシウムを
排ガスに噴霧することにより、排ガス中の塩化水
素と水酸化カルシウムとを反応させて塩化水素を
塩化カルシウムの形で固定し、これを集塵機で捕
集して、この集塵灰と、炉本体からの焼却灰と
を、水とセメントと共に混練して、この混練物を
成形機にて豆炭様の粒状に成形し、成形品ピツト
に一時貯留したのち、埋立て地に埋立てている。
Conventionally, as shown in Figure 1, calcium hydroxide in the form of a slurry is sprayed into the exhaust gas in the flue leading from the furnace main body to the gas cooling chamber, the heat exchanger, and the dust collector. Hydrogen chloride and calcium hydroxide are reacted to fix hydrogen chloride in the form of calcium chloride, which is collected by a dust collector, and this collected dust ash and incinerated ash from the furnace body are collected together with water and cement. After kneading, the kneaded product is formed into granules similar to charcoal using a molding machine, temporarily stored in a molded product pit, and then disposed of in a landfill.

このように、排出灰をセメントで固形化するこ
とにより、排出灰中の金属は固定できるが、塩化
物の溶出は防止することができず、公害原因物質
の処理方法としては完全なものではなかつた。
In this way, by solidifying the discharged ash with cement, metals in the discharged ash can be fixed, but the elution of chlorides cannot be prevented, and this method is not perfect as a treatment method for pollution-causing substances. Ta.

そこで、この考案者は、焼却炉の排出灰を成形
した成形物の表面に樹脂、防水剤モルタル等の被
膜を形成し、この被膜を焼却炉の排ガスの余熱を
利用して乾燥することにより簡便に塩化物の容出
を防止し得ることを見い出し、これに好適な装置
を考案したものである。
Therefore, the inventor of this invention formed a coating of resin, waterproof mortar, etc. on the surface of the molded product made from the ash discharged from the incinerator, and then dried this coating using the residual heat of the incinerator's exhaust gas. The authors discovered that it is possible to prevent the release of chloride, and devised a device suitable for this purpose.

特に、この考案においては、表面に被膜を形成
して成形品をガス冷却室に臨む位置まで搬送して
その余熱により被膜を乾燥するもので、ガス冷却
室は水を噴霧するため温度が200℃〜300℃であ
り、高温ガスにより被膜が融解気化する恐れがな
く適度の温度により円滑に乾燥工程を行うことを
目論んでいる。
In particular, this idea forms a film on the surface and transports the molded product to a position facing the gas cooling chamber, where the remaining heat dries the film.The temperature of the gas cooling chamber is 200°C because water is sprayed. ~300°C, and the aim is to carry out the drying process smoothly at an appropriate temperature without the risk of the film melting and vaporizing due to high-temperature gas.

以下、添付図面に示す実施例により、この考案
を詳細に説明する。
This invention will be explained in detail below with reference to embodiments shown in the accompanying drawings.

第2図は、この考案に係る灰固形化装置を含む
都市ごみの焼却処理システムの流れ図であり、第
3図は前記灰固形化装置の概要を示す縦断面図で
ある。
FIG. 2 is a flowchart of a municipal waste incineration system including the ash solidification device according to the invention, and FIG. 3 is a vertical sectional view showing an outline of the ash solidification device.

第1図と第2図とを対比すると明らかなよう
に、本考案の特徴は成形機から成形品ピツトに到
る過程に在り、その他の点においては公知技術と
同一である。
As is clear from comparing FIG. 1 and FIG. 2, the feature of the present invention lies in the process from the molding machine to the molded product pit, and in other respects it is the same as the known technology.

第3図において、20は、コンベヤで集積した
焼却灰と集塵灰とをセメントと水と共に適当な比
率で混練機に投入し混合して得られた混練物であ
つて、混練機(図示せず)からコンベヤ22によ
り搬送されて、ホツパー26から成形機24内に
投入される。成形機24は公知の構造であつて、
周面の対応位置に椀状凹部(図示せず)を有する
二つのロール28,28を並設してなり、混練物
が両ロールの周面間を通過する際に椀状凹部によ
り粒状に成形される。
In Fig. 3, 20 is a kneaded material obtained by charging incineration ash and collected dust ash accumulated on a conveyor into a kneader together with cement and water in an appropriate ratio and mixing them. 2) is conveyed by the conveyor 22, and is fed into the molding machine 24 from the hopper 26. The molding machine 24 has a known structure,
Two rolls 28, 28 having bowl-shaped recesses (not shown) at corresponding positions on the peripheral surfaces are arranged side by side, and when the kneaded material passes between the peripheral surfaces of both rolls, it is formed into granules by the bowl-shaped recesses. be done.

このようにして成形された成形物29はコンベ
ヤ30上に落下し、このコンベヤ30により搬送
されて、シユート32を経て、樹脂槽34内の樹
脂液35中に落下沈降する。
The molded article 29 formed in this manner falls onto a conveyor 30, is conveyed by the conveyor 30, passes through a chute 32, and falls and settles into the resin liquid 35 in the resin tank 34.

樹脂槽34はコンベヤトラフ34として構成さ
れており、樹脂液35はトラフ34の後端部に収
納されており、トラフ34は斜上方に延びて、ガ
ス冷却室12の下方に到り、この個所において上
方に開口38してガス冷却室12内部と連通して
いる。トラフ34の前後部にはシユート37が設
けられている。コンベヤ30に連なるシユート3
2は、トラフ34天蓋に設けた開口からトラフ3
4内に入り、その下端が樹脂液35の液中に投し
た水封式に形成されている。コンベヤ36は詳細
な図示を省略するが、両側のチエーン31,31
の間に多数のスクレーパー33を配したもので、
シユート32を経て樹脂液35中に落下し表面に
樹脂が被覆された成形物29を掻き上げて搬送
し、ガス冷却室12の下方を通過させて200℃〜
300℃の温度により樹脂被膜を乾燥し固化させ
る。しかる後、成形物29はシユート37よりト
ラフ外へ排出され、成形物ピツト(図示せず)へ
送られて貯留された後、埋立て地へ投棄される。
The resin tank 34 is configured as a conveyor trough 34, and the resin liquid 35 is stored at the rear end of the trough 34, and the trough 34 extends obliquely upward to reach the lower part of the gas cooling chamber 12. An opening 38 is opened upwardly in the gas cooling chamber 12 to communicate with the inside of the gas cooling chamber 12 . A chute 37 is provided at the front and rear of the trough 34. Chute 3 connected to conveyor 30
2 is the trough 3 from the opening provided in the trough 34 canopy.
4, and its lower end is formed in a water-seal type with its lower end immersed in the resin liquid 35. The conveyor 36 is not shown in detail, but the chains 31, 31 on both sides
A large number of scrapers 33 are arranged between the
The molded product 29, which falls into the resin liquid 35 through the chute 32 and whose surface is coated with resin, is scooped up and conveyed, and passed through the lower part of the gas cooling chamber 12 to a temperature of 200° C.
The resin film is dried and solidified at a temperature of 300°C. Thereafter, the molded product 29 is discharged from the trough through the chute 37, sent to a molded product pit (not shown), stored therein, and then disposed of in a landfill.

39は樹脂供給機であつて、図示を省略する
が、内面ライニングを施し、撹拌機を取り付けた
液剤タンクを有し、適宜の手段により樹脂液35
をトラフ34内へ送入する。
Reference numeral 39 denotes a resin feeder, which is not shown in the drawings, but has a liquid tank with inner lining and an agitator attached, and supplies the resin liquid 35 by appropriate means.
into the trough 34.

なお、10は炉本体、14はガス冷却室12の
上部に配した冷水噴射用のノズル、16は排ガス
および上記ノズル20より噴霧された水の水蒸気
等を熱交換機の方向へ流すダクトである。
In addition, 10 is a furnace main body, 14 is a nozzle for cold water injection arranged in the upper part of the gas cooling chamber 12, and 16 is a duct through which the exhaust gas and the water vapor of the water sprayed from the nozzle 20 flow in the direction of the heat exchanger.

上記実施例においては、成形物の表面被覆剤と
して樹脂液を用いたが、この場合は、ガス冷却室
12内の200℃〜300℃の温度により蒸発せずに固
化する種類の樹脂の選択が必要である。また、樹
脂に代えて、防水剤モルタルその他の被膜形成剤
を用いてもよい。
In the above example, a resin liquid was used as the surface coating agent for the molded product, but in this case, it is necessary to select a type of resin that solidifies without evaporating at the temperature of 200°C to 300°C in the gas cooling chamber 12. is necessary. Further, instead of the resin, a waterproof mortar or other film forming agent may be used.

以上のとおり、この考案においては、焼却炉の
排出灰をセメントと水とで混練し、成形機よつて
成形した成形物を、被膜形成剤が貯えられた槽に
送入してその表面に樹脂、防水剤モルタル等で被
膜を形成し、これをコンベヤによつて焼却炉のガ
ス冷却室に臨む個所を通過させることによりその
適度の余熱により被膜の乾燥と固形物の硬化とを
行うようになつている。この結果、排出灰に含ま
れる金属は、セメントによる固形化によつて固定
されると共に、排出灰に含まれる塩化物等の有害
物の溶出も、表面に形成された被膜によつて長期
にわたつて確実に防止でき、さらに、被膜の乾燥
および固形物の硬化も経済的に行えるようにな
る。
As described above, in this invention, the ash discharged from the incinerator is mixed with cement and water, the molded product is molded using a molding machine, and the molded product is sent into a tank containing a film-forming agent, and the surface is coated with resin. By forming a film with waterproofing agent mortar, etc., and passing this through the part facing the gas cooling chamber of the incinerator using a conveyor, the appropriate residual heat dries the film and hardens the solids. ing. As a result, the metals contained in the discharged ash are fixed by solidification with cement, and the elution of harmful substances such as chlorides contained in the discharged ash is prevented over a long period of time by the coating formed on the surface. This can be reliably prevented, and furthermore, the drying of the coating and the curing of the solid material can be performed economically.

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

第1図は、従来の都市ごみの焼却処理システム
を示す流れ図、第2図は、本考案に係る灰固形化
装置を含む焼却処理システムの流れ図、第3図
は、本考案に係る灰固形化装置の略示縦断面図で
ある。 符号の説明、10……焼却炉本体、12……ガ
ス冷却室、20……混練物、24……成形機、2
9……成形物、32……水封式シユート、34…
…被膜形成剤槽(トラフ)、35……被膜形成剤
液、36……コンベヤ(フライトコンベヤ)、3
8……開口。
Fig. 1 is a flowchart showing a conventional municipal waste incineration system, Fig. 2 is a flowchart of an incineration system including an ash solidification device according to the present invention, and Fig. 3 is a flowchart showing an ash solidification system according to the present invention. FIG. 2 is a schematic longitudinal cross-sectional view of the device. Explanation of symbols, 10... Incinerator main body, 12... Gas cooling chamber, 20... Kneaded material, 24... Molding machine, 2
9...Molded product, 32...Water-sealed chute, 34...
...Film forming agent tank (trough), 35... Film forming agent liquid, 36... Conveyor (flight conveyor), 3
8...Opening.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 焼却炉からの排出灰をセメントと水とで混練し
た混練物20を成形する成形機24と、成形物2
9を受容する被膜形成剤の槽34と、この槽34
内の成形物29を焼却炉本体10に連結するガス
冷却室12の内部へ臨む箇所まで搬送するコンベ
ヤ36とから成り、前記被膜形成剤槽34は内部
にコンベヤ36を有する閉塞されたトラフ34よ
りなり、前記成形物29を前記トラフ34内へ送
入する水封式のシユート32が設けられ、また、
前記トラフ34は前記冷却室12に臨む箇所にお
いて開口38していることを特徴とする都市ごみ
焼却炉における灰固形化装置。
A molding machine 24 that molds a kneaded material 20 obtained by kneading discharged ash from an incinerator with cement and water, and a molded product 2
a tank 34 of film-forming agent receiving 9;
A conveyor 36 transports the molded product 29 inside to a point facing the inside of the gas cooling chamber 12 connected to the incinerator main body 10. A water-sealed chute 32 is provided for feeding the molded product 29 into the trough 34, and
The ash solidification device in a municipal waste incinerator is characterized in that the trough 34 has an opening 38 at a location facing the cooling chamber 12.
JP8430882U 1982-06-07 1982-06-07 Ash solidification equipment in municipal waste incinerators Granted JPS58185738U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8430882U JPS58185738U (en) 1982-06-07 1982-06-07 Ash solidification equipment in municipal waste incinerators

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8430882U JPS58185738U (en) 1982-06-07 1982-06-07 Ash solidification equipment in municipal waste incinerators

Publications (2)

Publication Number Publication Date
JPS58185738U JPS58185738U (en) 1983-12-09
JPS6212475Y2 true JPS6212475Y2 (en) 1987-03-31

Family

ID=30093261

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8430882U Granted JPS58185738U (en) 1982-06-07 1982-06-07 Ash solidification equipment in municipal waste incinerators

Country Status (1)

Country Link
JP (1) JPS58185738U (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014235024A (en) * 2013-05-31 2014-12-15 株式会社E&Eテクノサービス Manufacturing method of solidified body, and solidified body manufactured by the same
JP6218119B2 (en) * 2014-03-31 2017-10-25 Jfeエンジニアリング株式会社 Incineration ash detoxification processing equipment, waste incineration equipment, incineration ash detoxification processing method and waste incineration method

Also Published As

Publication number Publication date
JPS58185738U (en) 1983-12-09

Similar Documents

Publication Publication Date Title
JPS5860113A (en) Melting method for refuse
US4467732A (en) Melting apparatus
JPS6212475Y2 (en)
US5173232A (en) Process for agglomerating stack gas desulfurization residue
US4207290A (en) Flue gas scrubber
JPS59223259A (en) Method and device for manufacturing hydraulic cement
US3929955A (en) Process for producing agglomerates from fine-grained lignite or fine grained carbonized lignite or from mixtures of the two
JP4040035B2 (en) Sewage sludge treatment method and apparatus
JPS6048234B2 (en) Solidification treatment method for municipal waste dust
JPS593235B2 (en) Dust treatment method in waste incineration treatment
JP3993802B2 (en) Method of processing dewatered sludge and ash
JPH01172246A (en) Production of artificial lightweight aggregate
JPS5520345A (en) Exhaust gas disposing device for incinerating furnace and the like
JPS5837269B2 (en) Molding method for inorganic materials
RU2022036C1 (en) Method of production of sinter cake
CA1221674A (en) Desulfurizing method for combustion exhaust gases
JPS55150415A (en) Method of effectivley utilizing sludge melting slag
JPS57205492A (en) Preparation of solid fuel by utilizing industrial waste
JPS54115569A (en) Melting system post-combustion equipment for stoker type incinerator
JPS6338256Y2 (en)
JPH07242889A (en) Method for producing solid fuel
JPS5775183A (en) Treatment of dust and fine powder
SU796623A1 (en) Slag and ash removing system
JPS5520651A (en) Incineration ash treating system
JPS6134079Y2 (en)