JPH03131398A - Sludge treatment apparatus - Google Patents
Sludge treatment apparatusInfo
- Publication number
- JPH03131398A JPH03131398A JP1268043A JP26804389A JPH03131398A JP H03131398 A JPH03131398 A JP H03131398A JP 1268043 A JP1268043 A JP 1268043A JP 26804389 A JP26804389 A JP 26804389A JP H03131398 A JPH03131398 A JP H03131398A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- vapor
- dryer
- treatment
- treatment device
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 230000009931 harmful effect Effects 0.000 claims abstract description 10
- 239000000126 substance Substances 0.000 claims abstract description 9
- 230000001590 oxidative effect Effects 0.000 claims abstract 2
- 239000012141 concentrate Substances 0.000 claims description 3
- 239000010409 thin film Substances 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 6
- 239000003054 catalyst Substances 0.000 abstract description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 3
- 239000001569 carbon dioxide Substances 0.000 abstract description 3
- 238000009833 condensation Methods 0.000 abstract description 2
- 230000005494 condensation Effects 0.000 abstract description 2
- 238000007084 catalytic combustion reaction Methods 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 239000008394 flocculating agent Substances 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は、下水処理、し尿処理、産業廃棄物処理等で排
出される汚泥を処理する汚泥処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to a sludge treatment device for treating sludge discharged in sewage treatment, human waste treatment, industrial waste treatment, etc.
(従来の技術)
第2図は従来の汚泥処理方法を示すフローシートであり
、この汚泥処理方法は、前段処理系統からの供給汚泥1
を凝集剤(無機および高分子高分子凝集剤)を添加する
こと無く濃縮・乾燥する乾燥機2と、この乾燥機によっ
て供給汚泥から加熱分離された水分(蒸発蒸気)3を冷
却水によって冷却し、凝縮させる復水器7と、復水器で
凝縮しない不凝縮ガスを排出するブロア8からなる。(Prior art) Figure 2 is a flow sheet showing a conventional sludge treatment method.
A dryer 2 that concentrates and dries the sludge without adding flocculants (inorganic and polymeric flocculants), and a dryer 2 that cools the water (evaporated steam) 3 heated and separated from the supplied sludge by this dryer with cooling water. , a condenser 7 for condensation, and a blower 8 for discharging non-condensable gas that is not condensed in the condenser.
前段処理系統から供給された汚泥は、乾燥機で加熱され
、その水分を蒸発し、乾燥汚泥となって乾無機より、排
出される。The sludge supplied from the front-stage treatment system is heated in a dryer to evaporate its water content and become dried sludge, which is then discharged from the dry inorganic system.
一方、汚泥から加熱分離された水分は、復水器で再び凝
縮しその中に含まれる有機成分を処理するために生物処
理に送られる。On the other hand, the water heated and separated from the sludge is condensed again in the condenser and sent to biological treatment to treat the organic components contained therein.
(発明が解決しようとする課題)
従来の処理方法では、凝縮水をそのまま放流するには、
放流基準を満足出来ないために、凝縮水は、生物処理へ
と送られる。この事は、全体の処理系統に生物処理が含
まれる下水処理場のような場合でも、全体の負荷が上昇
する等の問題となる。とくに、全体として、アンモニア
成分の多い汚泥を処理する場合等は、大きな問題となる
。また、産業廃棄物の処理の場合のように生物処理を特
に持ってない時は、この凝縮水の処理は、大きな問題と
なってくる。(Problem to be solved by the invention) In conventional treatment methods, in order to discharge condensed water as it is,
Since the discharge standards cannot be met, the condensed water is sent to biological treatment. This poses a problem, such as an increase in the overall load, even in the case of a sewage treatment plant where the entire treatment system includes biological treatment. In particular, this becomes a big problem when treating sludge containing a large amount of ammonia as a whole. Furthermore, when biological treatment is not available, such as in the case of industrial waste treatment, treatment of this condensed water becomes a big problem.
また、不凝縮ガスには、臭気成分が含まれており、これ
をそのまま大気中に放出することは、汚泥処理設備を設
置する場所にもよるが、住民がらの苦情等がおきる可能
性がある。In addition, non-condensable gas contains odor components, and releasing it directly into the atmosphere may cause complaints from residents, depending on the location where the sludge treatment equipment is installed. .
本発明は、このような問題点を解決するためになされた
ものであり、蒸発蒸気処理装置を設けたことにより、乾
燥機からの蒸発蒸気を再び凝縮すること無く、大気に放
出可能な状態に処理することに、全体の処理効率を上げ
ると共に、地域環境に対する影響を最小限にすることを
目的とする。The present invention was made to solve these problems, and by providing an evaporative steam treatment device, the evaporative steam from the dryer can be released into the atmosphere without being condensed again. The purpose of the treatment is to increase the overall treatment efficiency and to minimize the impact on the local environment.
(課題を解決するための手段)
本発明に関わる汚泥処理方法は、乾燥機からの蒸発蒸気
を再び凝縮すること無く酸化させることによって大気に
放出可能な状態に処理したものである。(Means for Solving the Problems) The sludge treatment method according to the present invention oxidizes evaporated steam from a dryer without condensing it again, so that it can be released into the atmosphere.
(作 用)
この発明における汚泥処理方法では、乾燥機からの蒸発
蒸気を再び凝縮すること無く、フロアにて蒸発蒸気処理
装置に送り、蒸発蒸気中の有機物に関わる有害物質や臭
気成分を酸化し、二酸化炭素や水などとし、大気中に放
出可能な状態に処理する。(Function) In the sludge treatment method of the present invention, the evaporated steam from the dryer is sent to the evaporative steam treatment device on the floor without being condensed again, and harmful substances and odor components related to organic matter in the evaporated steam are oxidized. , carbon dioxide, water, etc., and process it into a state that can be released into the atmosphere.
(実施例)
以−ド、本発明を第1図に示す実施例を用いて説明する
。(Example) The present invention will now be described using an example shown in FIG.
第1図は本発明の汚泥処理方法を示すフローシートであ
り、この汚泥処理方法は、前段処理系統からの供給汚泥
1を凝集剤(無機および高分子凝集剤)を添加すること
無く濃縮・乾燥する乾燥機2と、この乾燥機2によって
供給汚泥1より、加熱分離された水分(蒸発蒸気)3を
そのまま蒸発蒸気処理装置10に送るブロア4と、蒸発
蒸気を所定の温度まで加熱する加熱器5と触媒の作用に
より、蒸発蒸気中の有害物質や臭気成分を燃焼し。FIG. 1 is a flow sheet showing the sludge treatment method of the present invention. This sludge treatment method concentrates and dries the sludge 1 supplied from the front-stage treatment system without adding any flocculants (inorganic or polymeric flocculants). a dryer 2, a blower 4 that directly sends the water (evaporated steam) 3 heated and separated from the sludge 1 supplied by the dryer 2 to the evaporative steam treatment device 10, and a heater that heats the evaporated steam to a predetermined temperature. 5 and the action of the catalyst, the harmful substances and odor components in the evaporated steam are burned.
大気中に放出可能な状態とする触媒燃焼器6とを有する
蒸発蒸気処理装置からなる。It consists of an evaporative steam processing device having a catalytic combustor 6 that can be released into the atmosphere.
前段処理系統から供給された汚泥は、乾燥機で加熱され
、その水分を蒸発し、乾燥汚泥となって乾燥機より、排
出される。一方、汚泥より、加熱分離された水分は、蒸
発蒸気の状態のままで、ブロアにより蒸発蒸気処理装置
に送られる。蒸発蒸気処理装置では、まず加熱器により
、触媒の作用によって蒸発蒸気中の有害物質や臭気成分
などが燃焼可能な所定の温度まで加熱される。そして、
触媒燃焼器では、触媒の作用によって比較的低温で、蒸
発蒸気中の有害物質や臭気成分などが燃焼酸化し、二酸
化炭素や水などなって、大気中に放出可能な状態に処理
される。The sludge supplied from the pre-treatment system is heated in the dryer to evaporate its water content and become dried sludge, which is discharged from the dryer. On the other hand, the water that has been heated and separated from the sludge is sent to the evaporative steam treatment device by a blower while remaining in the form of evaporated steam. In the evaporative steam treatment device, first, a heater heats the evaporated steam to a predetermined temperature at which harmful substances, odor components, etc., can be combusted by the action of a catalyst. and,
In a catalytic combustor, the action of a catalyst combusts and oxidizes harmful substances and odor components in evaporated steam at relatively low temperatures, converting them into carbon dioxide and water, which can be released into the atmosphere.
これによって、乾燥機の作用によって供給汚泥から分離
された水分を処理するために再び凝縮水として、水の状
態に戻す必要はなく、また凝縮水として、生物処理に送
る必要もなくなり、全体として、汚泥処理物効率を上げ
ることができる。さらに、不凝縮ガスの中に臭気成分が
あり、地域環境に悪影響及ぼすなどの心配も無くなる。As a result, there is no need to return the water separated from the supplied sludge by the action of the dryer to water as condensed water for treatment, and there is no need to send the water to biological treatment as condensed water. Sludge treatment efficiency can be increased. Furthermore, there is no need to worry about the presence of odor components in the non-condensable gas, which may adversely affect the local environment.
以上説明したように本発明は、乾燥機の作用によって供
給汚泥から分離された水分を処理するために摂び凝縮水
として、水の状態に戻し生物処理に送る必要がなくなり
、全体として、汚泥処理効率を上げることができる。さ
らに5不凝縮ガスの中の臭気成分による地域環境に及ぼ
す悪影響などの心配も無くなる等の効果がある。As explained above, the present invention eliminates the need to treat the water separated from the supplied sludge by the action of the dryer, convert it into water as condensed water, and send it to biological treatment. It can increase efficiency. Furthermore, there is an effect that there is no need to worry about the harmful effects of odor components in the non-condensable gas on the local environment.
第1図は本発明の実施例を示すl’i泥処卵処理装置ロ
ーシート、第2図は従来のlll泥処理装置のフローシ
ー1〜である。FIG. 1 is a flow sheet of an l'i mud treatment and egg treatment apparatus showing an embodiment of the present invention, and FIG. 2 is a flow sheet 1 of a conventional lll mud treatment apparatus.
Claims (1)
、この乾燥機で加熱分離された供給汚泥中の水分(蒸発
蒸気)に含まれる有害物質や臭気成分を蒸発蒸気を凝縮
させる事なく酸化する事により除去する蒸発蒸気処理装
置と、蒸発蒸気処理装置によって処理された蒸発蒸気を
大気中に放出するための装置とからなる事を特徴とする
汚泥処理装置。 2、上記の乾燥機が、遠心薄膜乾燥機である事を特徴と
する請求項1記載の汚泥処理装置。 3、上記の蒸発蒸気処理装置が、蒸発蒸気中の有害物質
や臭気成分を燃焼させる事により除去する蒸発蒸気処理
装置である事を特徴とする請求項1記載の汚泥処理装置
。 4、上記の蒸発蒸気処理装置が、蒸発蒸気をさらに加熱
する加熱器と、この加熱器で加熱された蒸発蒸気中の臭
気成分を触媒燃焼させる燃焼器からなる事を特徴とする
請求項1記載の汚泥処理装置。[Claims] 1. A dryer that concentrates and dries supplied sludge without adding a flocculant, and a dryer that removes harmful substances and odor components contained in the water (evaporated vapor) in the supplied sludge that is heated and separated by this dryer. A sludge treatment device comprising: an evaporative vapor treatment device that removes evaporative vapor by oxidizing it without condensing it; and a device for releasing the evaporative vapor treated by the evaporative vapor treatment device into the atmosphere. 2. The sludge treatment apparatus according to claim 1, wherein the dryer is a centrifugal thin film dryer. 3. The sludge treatment device according to claim 1, wherein the evaporative steam treatment device is an evaporative steam treatment device that removes harmful substances and odor components in the evaporated steam by burning them. 4. Claim 1, wherein the evaporated steam treatment device comprises a heater that further heats the evaporated steam, and a combustor that catalytically burns odor components in the evaporated steam heated by the heater. sludge treatment equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1268043A JPH03131398A (en) | 1989-10-17 | 1989-10-17 | Sludge treatment apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1268043A JPH03131398A (en) | 1989-10-17 | 1989-10-17 | Sludge treatment apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03131398A true JPH03131398A (en) | 1991-06-04 |
Family
ID=17453088
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1268043A Pending JPH03131398A (en) | 1989-10-17 | 1989-10-17 | Sludge treatment apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03131398A (en) |
-
1989
- 1989-10-17 JP JP1268043A patent/JPH03131398A/en active Pending
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