JP4003045B2 - Dehydrating cake direct charging device - Google Patents

Dehydrating cake direct charging device Download PDF

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JP4003045B2
JP4003045B2 JP2002041937A JP2002041937A JP4003045B2 JP 4003045 B2 JP4003045 B2 JP 4003045B2 JP 2002041937 A JP2002041937 A JP 2002041937A JP 2002041937 A JP2002041937 A JP 2002041937A JP 4003045 B2 JP4003045 B2 JP 4003045B2
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cake
supply
pipe
storage tank
incinerator
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JP2003236587A (en
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廣瀬  均
卓 本松
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Sanki Engineering Co Ltd
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Sanki Engineering Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、汚泥貯留槽から焼却炉に脱水ケーキを供給する脱水ケーキ投入装置にかかるもので、脱水ケーキの嫌気発酵により供給管内圧力が上昇したとき、戻り管を介して汚泥貯留槽に循環させるようにした脱水ケーキ投入装置に関する。
【0002】
【従来の技術】
活性汚泥法によって下水処理する場合に一次、二次処理によって生じる余剰汚泥を濃縮、消化、ろ過し汚泥焼却炉に焼却される。焼却炉では、約800℃の温度で定常運転して、大気に開放される気体中に含まれるNOx等の含有量を少なくするように脱水ケーキ(脱水汚泥)を焼却炉に定量供給している。すなわち、焼却炉においては、脱水ケーキの燃焼は一定空気供給下で行われるので、脱水ケーキの供給量が所定値より少なければ、焼却排気体中の酸素濃度が高くなり、NOxの発生量が増える。一方、脱水ケーキの供給量が所定値より多ければ、焼却排気体中の酸素濃度が低くなり、脱水ケーキの燃焼過程に発生するNH及びCHの混在でHCNの発生量が増えるため、排気中に含まれる公害物質を最小限に抑えることが要求される。
このため、通常、汚泥貯留槽にある水分約75〜80%の脱水ケーキを脱水ケーキポンプによって焼却炉に供給する際、脱水ケーキポンプを駆動、調節して脱水ケーキの供給量の制御を行っている。
【0003】
【発明が解決しようとする課題】
汚泥などのガス発生を伴う物質は、配管等密閉された状態にて滞留する場合、発生ガスにより配管内で圧力が上昇する。配管内の発生ガスを脱気することなく焼却炉に投入した場合には、炉内にケーキの過剰供給・燃焼が起こり、急激な炉内圧の上昇を生じる。炉内ガスは大気放出となり安全上・環境上問題となる。そのため、ケーキ投入部に押込み機又は切出しコンベヤを備えたバッファ付供給装置を設けて配管内で圧力の上昇を防ぐことが行われているが、ケーキ投入のばらつきにより安定した燃焼を保持しにくいことがある。
【0004】
そこで、本発明は、バッファ付供給装置を付設しないで、定量性が高く、安定した燃焼制御を可能とするケーキ直接投入による汚泥焼却炉において、投入開始時の問題を解決する方法として、ケーキの嫌気発酵により発生した供給配管内のガスを脱気するようにした直接投入装置を提供するものである。
本発明のケーキ直接投入方式では、バッファタンクにて脱気が行えないことから、供給管内の脱気を以下の方法にて行う。すなわち、脱水ケーキ搬送配管内で嫌気発酵したガスを、ケーキと分離し、ガスのみを脱気することは困難であるから、その脱気方法として、投入ノズルからの投入を閉じたのち、発酵した脱水ケーキを供給元である貯留槽内のケーキを配管内に供給して発酵が進行していない脱水ケーキと置換する。嫌気発酵したケーキは、供給元である貯留槽に戻され開放及び攪拌により脱気されて再度供給が可能となり、焼却炉へ投入し焼却処理される。
【0005】
【課題を解決するための手段】
上記目的を達成するため、本発明の請求項1は、汚泥貯留槽の下方に脱水ケーキポンプを配設し、この脱水ケーキポンプと焼却炉とを供給管で接続して汚泥貯留槽からの脱水ケーキを焼却炉内に投入する脱水ケーキ投入装置において、各々脱水ケーキポンプを備える2本の各供給管に、装置弁である三方弁と圧力計とを介装して脱水ケーキ投入用ノズルをそれぞれ取付けて2系統の供給ラインとし、前記各供給ラインにおける三方弁の上流側から汚泥貯留槽に向かってそれぞれ戻り管を接続し、かつ前記各供給ラインにおける三方弁の下流側のうち、脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側同士を連通する連通配管を設け、第1又は第2の供給ラインにより脱水ケーキを投入する際、脱水ケーキの嫌気発酵により当該ラインの供給管内圧力が所定値を超えていたとき、前記三方弁を切替えて前記連通配管に脱水ケーキを流すことにより、供給ラインを1系統にし、管内の脱水ケーキを第2又は第1の供給ラインに接続した戻り管より汚泥貯留槽に戻して開放脱気するように制御する制御部を備えた、ことを特徴とする。
【0006】
このように構成することで、供給管中で脱水ケーキの嫌気発酵により管内圧力が上昇して所定の値を超えると、制御部により三方弁が駆動されて、脱水ケーキが戻り管を介して汚泥貯留槽に戻される。
【0007】
また、本発明の請求項2は、汚泥貯留槽の下方に脱水ケーキポンプを配設し、この脱水ケーキポンプと焼却炉とを供給管で接続して汚泥貯留槽からの脱水ケーキを焼却炉内に投入する脱水ケーキ投入装置において、前記汚泥貯留槽の下方に第1、第2脱水ケーキポンプを設け、これら第1、第2脱水ケーキポンプと前記焼却炉とを2本の供給ラインを構成する第1、第2の供給管でそれぞれ接続し、前記第1、第2供給管に、装置弁である第1、第2三方弁と第1、第2圧力計と前記第1、第2三方弁の下流に第1、2のケーキ投入ノズルとをそれぞれ設けると共に、前記第1、第2の三方弁の下流側より汚泥貯留槽に向けてそれぞれ戻り管を導出し、かつ、前記各供給ラインにおける三方弁の下流側のうち、脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側同士を連通する連通配管を設け、更に、前記第1又は第2の供給管を用いて脱水ケーキを焼却炉に供給する際、脱水ケーキの嫌気発酵により供給管内圧力が上昇して所定値を超えていたとき、当該供給管における三方弁及び他方の供給管における三方弁のデリバリ路を脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側に切替えて供給ラインを1系統にし、管内の脱水ケーキを戻り管より汚泥貯留槽に循環させて供給管内を脱気させたのち、当該供給管における三方弁のデリバリ路を第1又は第2の供給ラインの投入ノズル側に切替えて発酵していない脱水ケーキを焼却炉に供給するように制御する制御部を設けた、ことを特徴とする。
【0008】
このように構成することで、供給管内の圧力が上昇して所定の値を超えていたとき、制御部により三方弁及び戻り弁が駆動されて、脱水ケーキがその供給管の三方弁から配管を介して他方の三方弁に至りそこから他方の供給管及び戻り管を介して汚泥貯留槽に戻される。また、脱水ケーキの供給系統を2系統設けたので、脱水ケーキを戻す際に他方の供給管を利用するので、戻り管を軽減することができる。
【0009】
また、本発明では、前記第1、第2の供給管に第1、第2の分岐供給管を接続し、各供給管及び分岐供給管に装置弁である三方弁と圧力計と脱水ケーキ投入用ノズルとをそれぞれ取付け、しかも前記各分岐供給管は、汚泥貯留槽への戻り管開放部より高い位置で、焼却炉廻りに配設されていることを特徴とする(請求項3)。このように構成することで、脱水ケーキポンプの停止時に、投入ノズルへの分岐部周辺の上昇した圧力を、重力による自然開放して、置換する運転時間(回数)を低減できる。
【0010】
【発明の実施の形態】
以下、本発明の実施の形態を添付図面に基づいて詳述する。
図1は本発明の脱水ケーキ直接投入装置の配管図で、後述するように、第1の供給ラインを用いて投入する状態を示している。
図1において、1は汚泥貯留槽を示し、この貯留槽には、下水や屎尿中に元々含まれている懸濁固形物や下水処理(屎尿処理)の余剰汚泥固形物を脱水処理した脱水ケーキが貯留される。この汚泥貯留槽1の脱水ケーキは供給管に圧送され先端のノズルから焼却炉2に直接投入されて焼却処理される。
【0011】
焼却炉2は、例えば流動床を用いて脱水ケーキを焼却処理するものであり、焼却灰は、燃焼排ガスと共に焼却炉2から排出され熱交換器等により所定の温度に冷された後、サイクロン、電気集塵機等により脱塵処理され、排ガスが煙突から大気に放出される。
【0012】
汚泥貯留槽1の下部には、例えばモータの回転数を制御することにより搬送量(供給量)を調節することができる第1、第2脱水ケーキポンプ3、4が配置され、その吐出側に第1、第2の供給ラインを構成する供給管5、6がそれぞれ接続されている。第1、第2供給管5、6には第1、第2の吐出弁7、8、供給弁19、20、流量計17、18、含水率計27、28及び装置弁である三方弁11、21をそれぞれ介装する。供給弁19、20の下流側から分岐供給管5a、6aを分岐させて装置弁である三方弁12、22を設ける。
第1の供給ライン(第1供給管5、分岐供給管5 a に配置した三方弁11、12の切換路には、流量調整弁13a、13b、圧力計14a,14b及び装置副弁(投入遮断弁)15a,15bを介して投入ノズル16a,16bがそれぞれ接続されており、第2の供給ライン(第2供給管6、分岐供給管6 a に配置した三方弁21、22の切換路には、流量調整弁23a、23b、圧力計24a、24b及び装置副弁(投入遮断弁)25a、25bを介して投入ノズル26a、26bがそれぞれ接続されている。また、流量計17、18より下流位置の第1、第2供給管5、6から脱水ケーキを貯留槽1に循環させるため、戻り弁37、38付の戻り管35、36を設ける。
前記分岐供給管5a、6aは、汚泥貯留槽1への戻り管開放部より高い位置で焼却炉周りに配置される。このようにすることで、脱水ケーキポンプ3、4の停止時に、投入ノズルへの分岐部周辺の上昇した圧力を、重力により自然開放して、置換する運転時間(回数)を低減できる。
なお、供給弁19、20は管路のメイテナンス時に開閉操作するものである。また、三方弁は、弁の切替えができるものならばどのようなものでもよく、例えば電動式三方弁、空気式三方弁等が用いられ、弁の駆動もモータ駆動、エア駆動等が用いられる。
【0013】
さらに、供給管5、6の下流位置にある三方弁11、21のデリバリ側相互および三方弁12、22のデリバリ側相互を配管30a、30bでそれぞれ接続し、後記するように、脱水ケーキの嫌気発酵により供給管内圧力が所定値を超えていたとき、前記三方弁を切替えて供給ラインを1系統にし、管内の脱水ケーキを戻り管より汚泥貯留槽1に戻して開放脱気する。投入時には第1、第2流量計7、8の測定値に応じて制御部40により第1、第2脱水ケーキポンプ3又は4のモータが制御されて焼却炉2に供給される脱水ケーキの供給量が調節される。脱水ケーキは、脱水ケーキポンプ3、4の出力を小さくするため、例えば2から4cm/s以下の流速で供給管5、6内を搬送することが好ましい。
【0014】
また、制御部40は、2系統の供給ラインにそれぞれ設けられている流量計、濃度計、圧力計からの計測信号と所定のプログラムに基づいて演算処理して第1、第2の脱水ケーキポンプ、吐出弁、三方弁、装置弁副弁等への操作信号が出力され、バランスよく投入・循環運転するようになっている。運転開始時、供給管5、6内の脱水ケーキを汚泥貯留槽1に戻してから脱水ケーキの焼却炉2への供給を行う機能を有することが好ましい。なお、2系統のうち焼却炉2への脱水ケーキの供給を停止している供給管内に脱水ケーキを滞留しておくと、発酵して気体を発生させるため、気体が供給管5または6内に滞留しないように定期的又は不定期的に供給管内の脱水ケーキを汚泥貯留槽1に戻すように脱水ケーキポンプ3または4を駆動させることが好ましい。
【0015】
通常、脱水ケーキの投入は複数の投入ノズルを用いて行う。図示例では、焼却炉のフリーボード内の同一レベルに2本2組、計4本の投入ノズル16a、16b、26a、26bを用いている。投入ノズルは、脱水ケーキを焼却炉に投入(供給)できるならばどのように構成してもよく、例えば、高圧空気を用いて投入するようにしてもよい。なお、第1、第2供給管5、6の分岐位置は、特に限定されないが、供給管をできるだけ少なくするために焼却炉の近傍であることが好ましい。
【0016】
制御部40は、どちらか一方の脱水ケーキポンプ、例えば第1脱水ケーキポンプ3を駆動させて、汚泥貯留槽1の脱水ケーキの一部を第1供給管5を介して投入ノズル16a、26aから焼却炉2内に投入(供給)し、運転前に、第1供給管5と第1分岐供給管5aの圧力計14a、14bの測定値が所定の値を超えていたとき、第1戻り管36を介して脱水ケーキが汚泥貯留槽1に戻されるように第1三方弁11、12を切替える。
【0017】
次に作用について述べる。図1は第1の供給ラインを用いて投入する状態を示している。図中、供給ラインの実線部分は管内が開となっており、点線部分は閉じていることを示している。
【0018】
さて、投入運転開始時には、第1の供給管5における三方弁(装置弁)11、12を図1のように切替えて投入ノズル16a、16bまでをそれぞれ連通させたのち、一方の脱水ケーキポンプ3を駆動する。脱水ケーキポンプ3により汚泥貯留槽1の脱水ケーキが供給管5内に順次供給され装置弁副弁15a、15bを経てノズル16a、16bから焼却炉2内に投入され約800℃の温度で焼却される。
【0019】
図2は配管内から脱水ケーキを汚泥貯留槽に循環させる場合を示す図である。図1による運転前に、焼却炉2に搬送される供給管5中で脱水ケーキが発酵して気体が発生して管内の圧力が上昇して所定の値を超えていると、制御部40により各三方弁11、12、21、22が駆動され、配管30a、30bを接続して図2の実線ラインのように切替わり、脱水ケーキが戻り管36を介して汚泥貯留槽1に戻される。なお、図2では上記制御部40の図示を省略している。
脱水ケーキ搬送配管内で嫌気発酵したガスを、ケーキと分離し、ガスのみを脱気することは困難である。その脱気方法として、投入ノズルからの投入を閉じたのち、発酵した脱水ケーキを供給元である貯留槽内のケーキを配管内に供給して発酵が進行していない脱水ケーキと置換する。嫌気発酵したケーキは、供給元である貯留槽に戻され開放脱気されて再度供給が可能となり、焼却炉へ投入し焼却処理される。
【0020】
供給管内が陽圧になると押し出されるケーキの過剰供給を招くが、上記のように、発生した気体は脱水ケーキと共に汚泥貯留槽1に戻され、そこで開放されるため、発生した気体の焼却炉2への供給が抑制されることにより、炉内圧の急激な上昇による燃焼不具合を防ぐことができる。
【0021】
第2供給ライン6からケーキ投入運転する際には、各吐出弁、装置弁等を切替え第2の脱水ケーキポンプを駆動して第2の供給管6に脱水ケーキを送り第2の投入ノズル26a、26bから投入し、また管内圧が上昇したときには、三方弁を切替えて脱ガスの循環回路にするものであるが、第2供給ラインの運転循環時の配管については図示を省略している。
【0022】
図3は、第1、第2のラインを用いた脱水ケーキの投入・循環時における各吐出弁、装置弁、装置弁副弁及び戻り弁の開閉状態を示す図である。
脱水ケーキの供給を行う際に、供給管5、6内で気体が発生して圧力が所定の値を超えていたとき、制御部40がその供給管5、6の三方弁11、12を切替え脱気したのち、もう一方の系統の脱水ケーキポンプ及び三方弁21、22等を制御して脱水ケーキが別の供給管から投入ノズルを介して焼却炉2に所定量供給することで、焼却炉に気体が流入による脱水ケーキの過剰供給を防ぐことが可能である。
【0023】
【発明の効果】
上記のように、請求項1に記載の発明によれば、焼却炉に脱水汚泥ケーキを投入する際、第1又は第2の供給管中で汚泥ケーキが嫌気発酵して供給管内の圧力が上昇し所定の値を超えていたとき、制御部により三方弁、戻り弁を駆動して2系統の供給ラインを1系統に切替えることにより、脱水ケーキが戻り管を介して汚泥貯留槽に戻されるので供給管内で発生した気体が焼却炉に供給されることが抑制される。
【0024】
請求項2に記載の発明によれば、また、三方弁を供給管の焼却炉の近傍に設けていることで、供給管内のほぼ全部の脱水ケーキを焼却炉に戻せるので、供給管内に脱水ケーキが滞留することがなく、焼却炉への昇圧ガスの流入を確実に抑制することができる。また、請求項3に記載の発明によれば、各分岐供給管が、汚泥貯留槽への戻り管開放部より高い位置で、焼却炉廻りに配設されているので、脱水ケーキポンプの停止時に、投入ノズルへの分岐部周辺の上昇した圧力を、重力による自然開放して、置換する運転時間(回数)を低減できる。また、焼却炉への気体の流入を抑制することができると共に、脱水ケーキを戻すときに他方の供給管を利用するので戻り管を軽減することができる。
【図面の簡単な説明】
【図1】本発明脱水ケーキ投入装置の第1の供給ラインから脱水ケーキを焼却炉に投入する状態を示す説明図である。
【図2】図1の配管内で圧力上昇した脱水ケーキを汚泥貯留槽に循環させて圧力上昇のない脱水ケーキと置換を供給する場合を示す図である。
【図3】脱水ケーキの投入・循環時における各吐出弁、装置弁、装置弁副弁及び戻り弁の開閉状態を示す図である。
【符号の説明】
1 汚泥貯留槽 2 焼却炉
3 第1脱水ケーキポンプ 4 第2脱水ケーキポンプ
5 第1供給管 6 第2供給管
5a、6a 分岐供給管 7、8 吐出弁
9、10 吐出圧力計
11、12 第1装置弁(三方弁) 21、22 第2装置弁(三方弁)
13a、13b、23a、23b 流量調整弁
14a、14b、24a、24b 投入圧力計
15a、15b、25a、25b 装置弁副弁(投入遮断弁)
16a、16b 第1投入ノズル 26a、26b 第2投入ノズル
17、18 流量計 19、20 供給弁
27、28 含水率計 35、36 戻り管
37、38 戻り弁 40 制御装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a dewatered cake charging device for supplying dehydrated cake from a sludge storage tank to an incinerator, and when the pressure in the supply pipe rises due to anaerobic fermentation of the dehydrated cake, it is circulated to the sludge storage tank via a return pipe. The present invention relates to a dehydrated cake charging device.
[0002]
[Prior art]
When sewage is treated by the activated sludge method, excess sludge generated by the primary and secondary treatments is concentrated, digested, filtered, and incinerated in a sludge incinerator. In the incinerator, a steady operation is performed at a temperature of about 800 ° C., and dehydrated cake (dehydrated sludge) is quantitatively supplied to the incinerator so as to reduce the content of NOx and the like contained in the gas released to the atmosphere. . That is, in the incinerator, the dehydrated cake is burned under a constant air supply. Therefore, if the supply amount of the dehydrated cake is less than a predetermined value, the oxygen concentration in the incineration exhaust body increases and the amount of NOx generated increases. . On the other hand, if the supply amount of the dehydrated cake is larger than the predetermined value, the oxygen concentration in the incineration exhaust body becomes low, and the amount of HCN generated increases due to the mixture of NH 4 and CH 4 generated in the combustion process of the dehydrated cake. It is required to minimize the pollutants contained in it.
For this reason, when supplying a dewatered cake with a water content of about 75-80% in a sludge storage tank to an incinerator with a dewatered cake pump, the dehydrated cake pump is driven and adjusted to control the amount of dehydrated cake supplied. Yes.
[0003]
[Problems to be solved by the invention]
When a substance with gas generation such as sludge stays in a sealed state such as a pipe, the pressure increases in the pipe due to the generated gas. When the generated gas in the pipe is put into the incinerator without degassing, the cake is excessively supplied and burned in the furnace, causing a rapid rise in the furnace pressure. The gas in the furnace is released into the atmosphere, which is a safety and environmental problem. For this reason, a feeding device with a buffer equipped with an indenter or a cutting conveyor is provided in the cake charging part to prevent an increase in pressure in the piping, but it is difficult to maintain stable combustion due to variations in cake charging. There is.
[0004]
Therefore, the present invention provides a method for solving a problem at the start of charging in a sludge incinerator by direct charging of cake that has high quantitativeness and enables stable combustion control without providing a buffered supply device. The present invention provides a direct input device that degasses gas in a supply pipe generated by anaerobic fermentation.
In the cake direct charging method of the present invention, since degassing cannot be performed in the buffer tank, degassing in the supply pipe is performed by the following method. That is, it is difficult to separate the gas that has been anaerobically fermented in the dewatered cake transport pipe from the cake and degas only the gas. As a degassing method, the gas was fermented after closing the charging from the charging nozzle. The cake in the storage tank that is the supply source of the dehydrated cake is supplied into the pipe to replace the dehydrated cake that has not undergone fermentation. The cake that has been anaerobically fermented is returned to the storage tank that is the supply source, degassed by opening and stirring, and can be supplied again, and then put into an incinerator and incinerated.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, claim 1 of the present invention provides a dewatering cake pump disposed below the sludge storage tank, and the dewatering cake pump and the incinerator are connected by a supply pipe to dehydrate the sludge storage tank. In the dewatering cake charging device for charging cake into the incinerator, each of the two supply pipes each equipped with a dewatering cake pump is equipped with a three-way valve as a device valve and a pressure gauge, and a nozzle for dewatering cake charging Installed into two supply lines, connected to the return pipe from the upstream side of the three-way valve in each supply line toward the sludge storage tank, and put the dewatered cake out of the downstream side of the three-way valve in each supply line It not on the side connected to the use nozzle, the communicating pipe for communicating the other side with each other is provided, during the population dehydrated cake by the first or second supply line, the La by anaerobic fermentation of dewatered cake When the supply pipe pressure emissions exceeds the predetermined value, the by flowing dehydrated cake into the communicating pipe by switching three-way valve, a supply line to one system, supplying the dehydrated cake of the tube of the second or first having a control unit for controlling to open degassed returned to the sludge storage tank from the return tube connected to the line, characterized in that.
[0006]
With this configuration, when the pressure in the pipe rises due to anaerobic fermentation of the dehydrated cake in the supply pipe and exceeds a predetermined value, the three-way valve is driven by the control unit, and the dehydrated cake is sludge through the return pipe. Returned to storage tank.
[0007]
According to a second aspect of the present invention, a dewatering cake pump is disposed below the sludge storage tank, and the dewatering cake pump and the incinerator are connected by a supply pipe so that the dewatered cake from the sludge storage tank is placed in the incinerator. In the dewatered cake charging device to be charged into the tank, first and second dewatered cake pumps are provided below the sludge storage tank, and the first and second dewatered cake pumps and the incinerator constitute two supply lines. first, respectively connected with the second supply pipe, the first, the second supply pipe, first, second three-way valve and the first, the second pressure gauge first, second three-way a device valve first and second and cake injection nozzle provided with respective downstream of the valve, the first, towards the sludge storage tank downstream side of the second three-way valve to derive the return pipe respectively, and the respective supply line Connected to the dewatering cake charging nozzle on the downstream side of the three-way valve That is not a side, a communication pipe for communicating the other side with each other is provided, further, when the dehydrated cake is supplied to the incinerator using the first or the second supply pipe, the supply pipe by anaerobic fermentation of dewatered cake When the pressure rises and exceeds a predetermined value , switch the delivery path of the three-way valve in the supply pipe and the three-way valve in the other supply pipe to the other side, not the side connected to the nozzle for charging the dehydrated cake. After the supply line is made into one system and the dewatered cake in the pipe is circulated from the return pipe to the sludge storage tank to deaerate the supply pipe, the delivery path of the three-way valve in the supply pipe is connected to the first or second supply line. the dehydrated cake which is not fermented by switching to injection nozzle side provided with a control unit for controlling to supply the incinerator, characterized in that.
[0008]
By configuring in this way, when the pressure in the supply pipe rises and exceeds a predetermined value, the three-way valve and the return valve are driven by the control unit, and the dewatering cake connects the pipe from the three-way valve of the supply pipe. To the other three-way valve and then returned to the sludge storage tank through the other supply pipe and return pipe. In addition, since two dewatering cake supply systems are provided, the other supply pipe is used when returning the dehydrated cake, so that the return pipe can be reduced.
[0009]
In the present invention, the first and second branch supply pipes are connected to the first and second supply pipes, and a three-way valve, a pressure gauge, and a dewatered cake are added to each of the supply pipes and the branch supply pipes. In addition, each branch supply pipe is disposed around the incinerator at a position higher than the return pipe opening to the sludge storage tank. With this configuration, when the dewatering cake pump is stopped, the increased pressure around the branching portion to the charging nozzle is naturally released by gravity, and the replacement operation time (number of times) can be reduced.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 is a piping diagram of a dewatered cake direct charging apparatus according to the present invention, and shows a state of charging using a first supply line as will be described later.
In FIG. 1, reference numeral 1 denotes a sludge storage tank. In this storage tank, a dewatered cake obtained by dewatering suspended solids originally contained in sewage and manure and surplus sludge solids from sewage treatment (manure treatment). Is stored. The dewatered cake in the sludge storage tank 1 is pumped to the supply pipe, and directly fed into the incinerator 2 through the nozzle at the tip, and incinerated.
[0011]
The incinerator 2 incinerates the dehydrated cake using, for example, a fluidized bed, and the incineration ash is discharged from the incinerator 2 together with the combustion exhaust gas and cooled to a predetermined temperature by a heat exchanger or the like, and then a cyclone, The dust is removed by an electric dust collector or the like, and the exhaust gas is released from the chimney to the atmosphere.
[0012]
In the lower part of the sludge storage tank 1, for example, first and second dewatering cake pumps 3 and 4 that can adjust the transport amount (supply amount) by controlling the number of rotations of the motor are arranged, and on the discharge side thereof Supply pipes 5 and 6 constituting the first and second supply lines are connected to each other. The first and second supply pipes 5 and 6 include first and second discharge valves 7 and 8, supply valves 19 and 20, flow meters 17 and 18, moisture content meters 27 and 28, and a three-way valve 11 that is a device valve. , 21 are interposed. The branch supply pipes 5a and 6a are branched from the downstream side of the supply valves 19 and 20, and the three-way valves 12 and 22 as device valves are provided.
In the switching path of the three-way valves 11 and 12 arranged in the first supply line (the first supply pipe 5 and the branch supply pipe 5 a ) , flow rate adjusting valves 13a and 13b, pressure gauges 14a and 14b, and a device auxiliary valve (input) shut-off valve) 15a, injection nozzle 16a through 15b, 16b are connected respectively, the second supply line (second supply pipe 6, switching of the branch supply pipe 6 a) in the arranged three-way valves 21, 22換路Are connected to injection nozzles 26a and 26b through flow rate adjusting valves 23a and 23b, pressure gauges 24a and 24b, and device auxiliary valves (input cutoff valves) 25a and 25b, respectively. In addition, return pipes 35 and 36 with return valves 37 and 38 are provided in order to circulate the dehydrated cake from the first and second supply pipes 5 and 6 downstream of the flow meters 17 and 18 to the storage tank 1.
The said branch supply pipes 5a and 6a are arrange | positioned around an incinerator in the position higher than the return pipe open part to the sludge storage tank 1. FIG. In this way, when the dewatering cake pumps 3 and 4 are stopped, the increased pressure around the branching portion to the charging nozzle is naturally released by gravity, and the operation time (number of times) for replacement can be reduced.
The supply valves 19 and 20 are opened and closed during the maintenance of the pipeline. The three-way valve may be any valve that can switch the valve. For example, an electric three-way valve, a pneumatic three-way valve, or the like is used, and a motor drive, an air drive, or the like is used for driving the valve.
[0013]
Furthermore, the delivery sides of the three-way valves 11 and 21 and the delivery sides of the three-way valves 12 and 22 at the downstream positions of the supply pipes 5 and 6 are connected to each other by pipes 30a and 30b, respectively. When the pressure in the supply pipe exceeds a predetermined value due to the fermentation, the three-way valve is switched to make the supply line one system, and the dewatered cake in the pipe is returned to the sludge storage tank 1 from the return pipe and opened and deaerated. Supplying the dehydrated cake supplied to the incinerator 2 by controlling the motor of the first or second dehydrated cake pump 3 or 4 by the control unit 40 according to the measured values of the first and second flow meters 7 and 8 at the time of charging. The amount is adjusted. In order to reduce the output of the dewatering cake pumps 3, 4, the dewatered cake is preferably transported through the supply pipes 5, 6 at a flow rate of 2 to 4 cm / s or less, for example.
[0014]
In addition, the control unit 40 performs arithmetic processing based on measurement signals from a flow meter, a concentration meter, and a pressure gauge provided in each of the two supply lines and a predetermined program, and performs first and second dewatering cake pumps. Operation signals are output to the discharge valve, the three-way valve, the device valve subvalve, etc., and the charging / circulation operation is performed in a balanced manner. It is preferable to have a function of supplying the dehydrated cake to the incinerator 2 after returning the dehydrated cake in the supply pipes 5 and 6 to the sludge storage tank 1 at the start of operation. Note that if the dehydrated cake stays in the supply pipe that stops the supply of the dehydrated cake to the incinerator 2 among the two systems, the gas is fermented to generate gas, so that the gas is in the supply pipe 5 or 6. It is preferable to drive the dewatering cake pump 3 or 4 so that the dewatering cake in the supply pipe is returned to the sludge storage tank 1 periodically or irregularly so as not to stay.
[0015]
Usually, the dewatered cake is charged using a plurality of charging nozzles. In the illustrated example, two injection nozzles 16a, 16b, 26a, and 26b are used at the same level in the freeboard of the incinerator, for a total of four injection nozzles 16a, 16b, 26a, and 26b. The charging nozzle may be configured in any way as long as the dewatered cake can be charged (supplied) into the incinerator. For example, the charging nozzle may be charged using high-pressure air. The branch positions of the first and second supply pipes 5 and 6 are not particularly limited, but are preferably in the vicinity of the incinerator in order to reduce the supply pipes as much as possible.
[0016]
The control unit 40 drives either one of the dewatering cake pumps, for example, the first dewatering cake pump 3, and feeds a part of the dewatering cake of the sludge storage tank 1 from the charging nozzles 16 a and 26 a via the first supply pipe 5. When the measured values of the pressure gauges 14a and 14b of the first supply pipe 5 and the first branch supply pipe 5a exceed a predetermined value before being operated (supplied) into the incinerator 2, the first return pipe The first three-way valves 11 and 12 are switched so that the dewatered cake is returned to the sludge storage tank 1 via 36.
[0017]
Next, the operation will be described. FIG. 1 shows the state of charging using the first supply line. In the figure, the solid line portion of the supply line indicates that the inside of the pipe is open and the dotted line portion is closed.
[0018]
At the start of the charging operation, the three-way valves (device valves) 11 and 12 in the first supply pipe 5 are switched as shown in FIG. 1 to communicate with the charging nozzles 16a and 16b. Drive. The dewatered cake in the sludge storage tank 1 is sequentially supplied into the supply pipe 5 by the dewatered cake pump 3, and is introduced into the incinerator 2 from the nozzles 16a and 16b through the device valve sub valves 15a and 15b, and incinerated at a temperature of about 800 ° C. The
[0019]
FIG. 2 is a diagram showing a case where the dewatered cake is circulated from the piping to the sludge storage tank. Before the operation according to FIG. 1, when the dehydrated cake is fermented in the supply pipe 5 conveyed to the incinerator 2 to generate gas and the pressure in the pipe rises and exceeds a predetermined value, the control unit 40 Each of the three-way valves 11, 12, 21, 22 is driven to connect the pipes 30 a, 30 b and switch as shown by the solid line in FIG. 2, and the dewatered cake is returned to the sludge storage tank 1 through the return pipe 36. In addition, illustration of the said control part 40 is abbreviate | omitted in FIG.
It is difficult to separate the gas that has been anaerobically fermented in the dehydrated cake transport pipe from the cake and degas only the gas. As the deaeration method, after closing the charging from the charging nozzle, the cake in the storage tank, which is the supply source of the fermented dehydrated cake, is supplied into the pipe to replace the dehydrated cake in which fermentation has not progressed. The cake that has been anaerobically fermented is returned to the storage tank that is the supply source, opened and degassed, and can be supplied again. The cake is put into an incinerator and incinerated.
[0020]
When the inside of the supply pipe reaches a positive pressure, an excessive supply of the extruded cake is caused. As described above, the generated gas is returned to the sludge storage tank 1 together with the dehydrated cake and is released there, so that the generated gas incinerator 2 By suppressing the supply to the furnace, it is possible to prevent a combustion failure due to a rapid rise in the furnace pressure.
[0021]
When the cake charging operation is performed from the second supply line 6, the discharge valve, the device valve, and the like are switched to drive the second dewatering cake pump to send the dewatering cake to the second supply pipe 6 and the second charging nozzle 26a. 26b, and when the internal pressure of the pipe rises, the three-way valve is switched to form a degassing circulation circuit, but the illustration of the piping during the operation circulation of the second supply line is omitted.
[0022]
FIG. 3 is a diagram showing the open / closed state of each discharge valve, device valve, device valve subvalve, and return valve when dewatered cake is charged and circulated using the first and second lines.
When supplying dehydrated cake, when the gas is generated in the supply pipes 5 and 6 and the pressure exceeds a predetermined value, the control unit 40 switches the three-way valves 11 and 12 of the supply pipes 5 and 6. After deaeration, the dewatering cake pump of the other system and the three-way valves 21 and 22 are controlled so that the dewatering cake is supplied from a separate supply pipe to the incinerator 2 through the charging nozzle, thereby incinerator It is possible to prevent an excessive supply of the dehydrated cake due to the inflow of gas.
[0023]
【The invention's effect】
As described above, according to the first aspect of the present invention, when the dewatered sludge cake is introduced into the incinerator, the sludge cake is anaerobically fermented in the first or second supply pipe, and the pressure in the supply pipe increases. However, when the predetermined value is exceeded, the dewatering cake is returned to the sludge storage tank via the return pipe by driving the three-way valve and the return valve by the control unit and switching the two supply lines to one system. Supply of gas generated in the supply pipe to the incinerator is suppressed.
[0024]
According to the second aspect of the present invention, since the three-way valve is provided in the vicinity of the incinerator of the supply pipe, almost all of the dehydrated cake in the supply pipe can be returned to the incinerator. Does not stay, and the inflow of the pressurized gas to the incinerator can be reliably suppressed. Further, according to the invention described in claim 3, since each branch supply pipe is arranged around the incinerator at a position higher than the return pipe opening portion to the sludge storage tank, when the dewatering cake pump is stopped. The operating time (number of times) of replacing the increased pressure around the branching portion to the charging nozzle by naturally releasing by gravity can be reduced. Further, inflow of gas to the incinerator can be suppressed, and the other supply pipe is used when returning the dehydrated cake, so that the return pipe can be reduced.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a state in which dehydrated cake is charged into an incinerator from a first supply line of the dehydrated cake charging device of the present invention.
FIG. 2 is a diagram showing a case where a dehydrated cake whose pressure has been increased in the pipe of FIG. 1 is circulated in a sludge storage tank and a dehydrated cake and a replacement without pressure increase are supplied.
FIG. 3 is a view showing an open / closed state of each discharge valve, device valve, device valve subvalve, and return valve when charging and circulating dehydrated cake.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Sludge storage tank 2 Incinerator 3 1st dehydration cake pump 4 2nd dehydration cake pump 5 1st supply pipe 6 2nd supply pipe 5a, 6a Branch supply pipe 7, 8 Discharge valve 9, 10 Discharge pressure gauge 11, 12 1st 1 device valve (3-way valve) 21, 22 2nd device valve (3-way valve)
13a, 13b, 23a, 23b Flow rate adjusting valves 14a, 14b, 24a, 24b Input pressure gauges 15a, 15b, 25a, 25b Device valve sub-valve (input cutoff valve)
16a, 16b 1st injection nozzle 26a, 26b 2nd injection nozzle 17, 18 Flow meter 19, 20 Supply valve 27, 28 Moisture content meter 35, 36 Return pipe 37, 38 Return valve 40 Control device

Claims (3)

汚泥貯留槽の下方に脱水ケーキポンプを配設し、この脱水ケーキポンプと焼却炉とを供給管で接続して汚泥貯留槽からの脱水ケーキを焼却炉内に投入する脱水ケーキ投入装置において、
各々脱水ケーキポンプを備える2本の各供給管に、装置弁である三方弁と圧力計とを介装して脱水ケーキ投入用ノズルをそれぞれ取付けて2系統の供給ラインとし、
前記各供給ラインにおける三方弁の上流側から汚泥貯留槽に向かってそれぞれ戻り管を接続し、かつ前記各供給ラインにおける三方弁の下流側のうち、脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側同士を連通する連通配管を設け、
第1又は第2の供給ラインにより脱水ケーキを投入する際、脱水ケーキの嫌気発酵により当該ラインの供給管内圧力が所定値を超えていたとき、前記三方弁を切替えて前記連通配管に脱水ケーキを流すことにより、供給ラインを1系統にし、管内の脱水ケーキを第2又は第1の供給ラインに接続した戻り管より汚泥貯留槽に戻して開放脱気するように制御する制御部を備えた、
ことを特徴とする脱水ケーキ直接投入装置。
In the dewatering cake charging device that places the dewatering cake pump below the sludge storage tank, connects the dewatering cake pump and the incinerator with a supply pipe, and inputs the dehydrated cake from the sludge storage tank into the incinerator.
Each of two supply pipes each equipped with a dewatering cake pump is equipped with a three-way valve, which is a device valve, and a pressure gauge, and a dehydrating cake charging nozzle is attached to each of the two supply lines,
The return pipe is connected to the sludge storage tank from the upstream side of the three-way valve in each supply line, and the downstream side of the three-way valve in each supply line is not the side connected to the dewatered cake charging nozzle, Provide a communication pipe that communicates the other side,
When turning on the dewatered cake by the first or second supply line, when the supply pipe pressure of the line exceeds the predetermined value by anaerobic fermentation of dehydrated cake, the dehydrated cake in the communicating pipe by switching the three-way valve By supplying the flow line , the supply line is made into one system, and the dewatering cake in the pipe is returned to the sludge storage tank from the return pipe connected to the second or first supply line, and is equipped with a control unit that controls to open and deaerate.
A dehydrating cake direct charging device.
汚泥貯留槽の下方に脱水ケーキポンプを配設し、この脱水ケーキポンプと焼却炉とを供給管で接続して汚泥貯留槽からの脱水ケーキを焼却炉内に投入する脱水ケーキ投入装置において、
前記汚泥貯留槽の下方に第1、第2脱水ケーキポンプを設け、これら第1、第2脱水ケーキポンプと前記焼却炉とを2本の供給ラインを構成する第1、第2の供給管でそれぞれ接続し、
前記第1、第2供給管に、装置弁である第1、第2三方弁と第1、第2圧力計と前記第1、第2三方弁の下流に第1、2のケーキ投入ノズルとをそれぞれ設けると共に、前記第1、第2の三方弁の下流側より汚泥貯留槽に向けてそれぞれ戻り管を導出し、かつ、前記各供給ラインにおける三方弁の下流側のうち、脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側同士を連通する連通配管を設け、
更に、前記第1又は第2の供給管を用いて脱水ケーキを焼却炉に供給する際、脱水ケーキの嫌気発酵により供給管内圧力が上昇して所定値を超えていたとき、当該供給管における三方弁及び他方の供給管における三方弁のデリバリ路を脱水ケーキ投入用ノズルに接続する側ではない、もう一方の側に切替えて供給ラインを1系統にし、管内の脱水ケーキを戻り管より汚泥貯留槽に循環させて供給管内を脱気させたのち、
当該供給管における三方弁のデリバリ路を第1又は第2の供給ラインの投入ノズル側に切替えて発酵していない脱水ケーキを焼却炉に供給するように制御する制御部を設けた、ことを特徴とする脱水ケーキ投入装置。
In the dewatering cake charging device that places the dewatering cake pump below the sludge storage tank, connects the dewatering cake pump and the incinerator with a supply pipe, and inputs the dehydrated cake from the sludge storage tank into the incinerator.
First and second dewatering cake pumps are provided below the sludge storage tank, and these first and second dewatering cake pumps and the incinerator are first and second supply pipes constituting two supply lines. Connect each one
The first and second supply pipes are provided with first and second three-way valves and first and second pressure gauges, which are device valves, and first and second cake injection nozzles downstream of the first and second three-way valves. And a return pipe is led out toward the sludge storage tank from the downstream side of the first and second three-way valves, and the dewatering cake is charged in the downstream side of the three-way valve in each supply line. Provide a communication pipe that connects the other side, not the side connected to the nozzle,
Further, when the dehydrated cake is supplied to the incinerator using the first or second supply pipe, when the pressure in the supply pipe rises and exceeds a predetermined value due to anaerobic fermentation of the dehydrated cake, three directions in the supply pipe Switch the delivery path of the three-way valve in the valve and the other supply pipe to the other side, not the side that connects to the nozzle for charging the dehydrated cake, to make the supply line one system, and the dewatered cake in the pipe to the sludge storage tank from the return pipe After degassing the supply pipe,
A control unit is provided for controlling the delivery path of the three-way valve in the supply pipe to the input nozzle side of the first or second supply line to control the supply of the unfermented dehydrated cake to the incinerator. Dehydrating cake charging device.
前記第1、第2の供給管に第1、第2の分岐供給管を接続し、各供給管及び分岐供給管に装置弁である三方弁と圧力計と脱水ケーキ投入用ノズルとをそれぞれ取付け、しかも前記各分岐供給管は、汚泥貯留槽への戻り管開放部より高い位置で、焼却炉廻りに配設されていることを特徴とする請求項2に記載の脱水ケーキ投入装置。First and second branch supply pipes are connected to the first and second supply pipes, and a three-way valve, a pressure gauge, and a dewatering cake charging nozzle are attached to the supply pipes and the branch supply pipes, respectively. And the said each branch supply pipe | tube is arrange | positioned around an incinerator in the position higher than the return pipe open part to a sludge storage tank, The dewatering cake injection | throwing-in apparatus of Claim 2 characterized by the above-mentioned.
JP2002041937A 2002-02-19 2002-02-19 Dehydrating cake direct charging device Expired - Lifetime JP4003045B2 (en)

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JP4565554B2 (en) * 2004-12-28 2010-10-20 月島機械株式会社 Degassing device and sludge conveying equipment provided with the same

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