JP2012217969A - Cleaning device for surplus sludge transfer pipe - Google Patents

Cleaning device for surplus sludge transfer pipe Download PDF

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JP2012217969A
JP2012217969A JP2011089178A JP2011089178A JP2012217969A JP 2012217969 A JP2012217969 A JP 2012217969A JP 2011089178 A JP2011089178 A JP 2011089178A JP 2011089178 A JP2011089178 A JP 2011089178A JP 2012217969 A JP2012217969 A JP 2012217969A
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transfer pipe
excess sludge
sludge
sludge transfer
temperature steam
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JP5733683B2 (en
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Hidetoshi Mochizuki
秀俊 望月
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NEKKEN SANGYO KK
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Abstract

PROBLEM TO BE SOLVED: To provide a cleaning device for a surplus sludge transfer pipe which cleaning device certainly cleans the interior of a transfer pipe that transfers surplus sludge during operation of a sludge disposal system.SOLUTION: The cleaning device cleans a surplus sludge transfer pipe that transfers surplus sludge for methane fermentation, and includes a high-temperature steam jetting unit which jets high-temperature steam to the interior of the surplus sludge transfer pipe. It is preferable that the cleaning device further includes a heat exchanging unit which exchanges heat between post-heating surplus sludge heated by the high-temperature steam and pre-heating surplus sludge. It is also preferable that the heat exchanging unit is of a double-pipe structure composed of a surplus sludge transfer pipe that transfers the post-heating surplus sludge and a surplus sludge transfer pipe that transfers the pre-heating surplus sludge.

Description

本発明は、余剰汚泥移送管の洗浄装置に関する。   The present invention relates to a cleaning device for excess sludge transfer pipe.

一般的な下水汚泥処理システムにおいて、余剰汚泥は移送管を通じて移送され、メタン発酵される。しかしながら、この余剰汚泥は、砂や微生物等の夾雑物を含有することから粘性が高い。そのため、余剰汚泥を移送する移送管は詰まりやすいという不都合がある。   In a general sewage sludge treatment system, surplus sludge is transferred through a transfer pipe and subjected to methane fermentation. However, this excess sludge is highly viscous because it contains impurities such as sand and microorganisms. Therefore, there is an inconvenience that the transfer pipe for transferring the excess sludge is easily clogged.

このように、余剰汚泥を移送する移送管が余剰汚泥により詰まりやすいという不都合に対し、かかる移送管の詰まりを解消するための様々な技術が提供されている。例えば、運転停止後に縦配管内に残留する混合汚泥を除去し、運転再開時に配管の閉塞の発生がない油混合汚泥処理システムにおける配管の洗浄方法等が挙げられる(特開2006−130370号公報等)。   As described above, various techniques for eliminating the clogging of the transfer pipe are provided for the inconvenience that the transfer pipe for transferring the excess sludge is easily clogged by the excess sludge. For example, there is a method of cleaning a pipe in an oil mixed sludge treatment system that removes mixed sludge remaining in the vertical pipe after the operation is stopped and does not cause the pipe to be blocked when the operation is resumed (Japanese Patent Laid-Open No. 2006-130370). ).

しかしながら、上述の油混合汚泥処理システムにおける配管の洗浄方法を実施するためには、汚泥処理システムの運転を停止する必要があることから、汚泥処理システムの稼働効率を低下させる可能性がある。   However, since it is necessary to stop the operation of the sludge treatment system in order to carry out the pipe cleaning method in the oil mixed sludge treatment system described above, there is a possibility that the operating efficiency of the sludge treatment system is lowered.

つまり、余剰汚泥をメタン発酵するという一連のプロセスを含む汚泥処理システムを停止させることなく、汚泥処理システムの稼働中において、余剰汚泥を移送する移送管の内部を確実に洗浄できる余剰汚泥移送管の洗浄装置は、未だ提供されていない。   In other words, the surplus sludge transfer pipe that can reliably clean the inside of the transfer pipe that transports the excess sludge during operation of the sludge treatment system without stopping the sludge treatment system including a series of processes of methane fermentation of the surplus sludge. No cleaning device has yet been provided.

特開2006−130370号公報JP 2006-130370 A

本発明は、これらの不都合に鑑みてなされたものであり、汚泥処理システムの稼働中に余剰汚泥移送管の内部を確実に洗浄できる余剰汚泥移送管の洗浄装置の提供を目的とするものである。   The present invention has been made in view of these disadvantages, and an object of the present invention is to provide a cleaning device for an excess sludge transfer pipe that can reliably clean the interior of the excess sludge transfer pipe during operation of the sludge treatment system. .

上記課題を解決するためになされた発明は、
メタン発酵用の余剰汚泥を移送する余剰汚泥移送管を洗浄する洗浄装置であって、
上記余剰汚泥移送管の内部に高温蒸気を噴出させる高温蒸気噴出部を備えることを特徴とする余剰汚泥移送管の洗浄装置である。
The invention made to solve the above problems is
A cleaning device for cleaning an excess sludge transfer pipe for transferring excess sludge for methane fermentation,
A surplus sludge transfer pipe cleaning device comprising a high temperature steam jetting section for jetting high temperature steam inside the surplus sludge transfer pipe.

当該余剰汚泥移送管の洗浄装置は、上記余剰汚泥移送管の内部に高温蒸気を噴出させる高温蒸気噴出部を備えることで、かかる高温蒸気噴出部から噴出される高温蒸気の熱や吐出圧力により、余剰汚泥移送管における粘性の高い余剰汚泥の移送をスムーズにすることができると共に、余剰汚泥移送管の内部に付着する余剰汚泥を十分に除去し、余剰汚泥移送管内部の詰まりを確実に洗浄することができる。さらに、この高温蒸気噴出部から噴出される高温蒸気は、上記余剰汚泥移送管を通じて余剰汚泥がメタン発酵されるまでの操業プロセスを停止させることなく噴出されることから、当該余剰汚泥移送管の洗浄装置は、余剰汚泥をメタン発酵するという一連のプロセスを含む汚泥処理システムの稼働中において、余剰汚泥移送管の洗浄を確実に達成することができる。   The surplus sludge transfer pipe cleaning device is provided with a high temperature steam jet section for jetting high temperature steam inside the surplus sludge transfer pipe, so that the heat and discharge pressure of the high temperature steam jetted from the high temperature steam jet section The excess sludge transfer pipe with high viscosity can be smoothly transferred in the excess sludge transfer pipe, and the excess sludge adhering to the inside of the excess sludge transfer pipe can be removed sufficiently to reliably clean the clogs inside the excess sludge transfer pipe. be able to. Furthermore, since the high-temperature steam ejected from the high-temperature steam ejection section is ejected through the surplus sludge transfer pipe without stopping the operation process until the surplus sludge is methane-fermented, the surplus sludge transfer pipe is washed. The apparatus can reliably achieve cleaning of the excess sludge transfer pipe during operation of the sludge treatment system including a series of processes for methane fermentation of excess sludge.

当該余剰汚泥移送管の洗浄装置は、上記高温蒸気により加熱される加熱余剰汚泥と、加熱前の余剰汚泥との熱交換を行う熱交換部をさらに備えるとよい。このように、当該余剰汚泥移送管の洗浄装置が、上記高温蒸気により加熱される加熱余剰汚泥と、加熱前の余剰汚泥との熱交換を行う熱交換部を備えることで、加熱余剰汚泥から加熱前の余剰汚泥に熱が効率的に移動する。その結果、当該余剰汚泥移送管の洗浄装置は、余剰汚泥に対して噴出される高温蒸気のエネルギー量を低減でき、省エネルギー化を図ることができる。   The surplus sludge transfer pipe cleaning device may further include a heat exchanging unit that performs heat exchange between the heated surplus sludge heated by the high-temperature steam and the surplus sludge before heating. In this way, the cleaning device for the excess sludge transfer pipe includes a heat exchange unit that performs heat exchange between the heated excess sludge heated by the high-temperature steam and the excess sludge before heating. Heat efficiently moves to the previous excess sludge. As a result, the cleaning device for the excess sludge transfer pipe can reduce the energy amount of the high-temperature steam ejected with respect to the excess sludge and can save energy.

上記熱交換部は、上記加熱余剰汚泥を移送する余剰汚泥移送管と、加熱前の余剰汚泥を移送する余剰汚泥移送管との二重管式であるとよい。このように、上記熱交換部が上記加熱余剰汚泥を移送する余剰汚泥移送管と、加熱前の余剰汚泥を移送する余剰汚泥移送管との二重管式であることで、当該余剰汚泥移送管の洗浄装置は、上述した加熱余剰汚泥から加熱前の余剰汚泥への熱の移動をコンパクトな構成により効率的に行うことができ、余剰汚泥に対して噴出される高温蒸気のエネルギー量をより一層低減することができる。   The heat exchanging unit may be a double pipe type of an excess sludge transfer pipe for transferring the heated excess sludge and an excess sludge transfer pipe for transferring the excess sludge before heating. Thus, the said excess heat sludge transfer pipe is because the said heat exchange part is a double pipe type of the excess sludge transfer pipe which transfers the above-mentioned heating sludge, and the excess sludge transfer pipe which transfers the excess sludge before heating. This cleaning device can efficiently transfer heat from the above-described heated excess sludge to the excess sludge before heating with a compact configuration, and further increases the amount of energy of the high-temperature steam ejected to the excess sludge. Can be reduced.

当該余剰汚泥移送管の洗浄装置は、上記余剰汚泥移送管の内圧を計測する移送管内圧計測部をさらに備えるとよい。このように、上記余剰汚泥移送管の内圧を計測する移送管内圧計測部をさらに備えることで、当該余剰汚泥移送管の洗浄装置は、上記汚泥処理システムの稼働中において余剰汚泥移送管の内圧を計測でき、このようにして計測される内圧データを元に余剰汚泥移送管の詰まりの状態を容易に把握することができる。   The cleaning apparatus for the excess sludge transfer pipe may further include a transfer pipe internal pressure measuring unit that measures the internal pressure of the excess sludge transfer pipe. Thus, by further including a transfer pipe internal pressure measuring unit that measures the internal pressure of the excess sludge transfer pipe, the cleaning device for the excess sludge transfer pipe can reduce the internal pressure of the excess sludge transfer pipe during operation of the sludge treatment system. It is possible to measure, and it is possible to easily grasp the clogged state of the excess sludge transfer pipe based on the internal pressure data thus measured.

当該余剰汚泥移送管の洗浄装置は、上記余剰汚泥移送管における余剰汚泥の流量を調整する流量調整部をさらに備えるとよい。このように、上記余剰汚泥移送管における余剰汚泥の流量を調整する流量調整部をさらに備えることにより、当該余剰汚泥移送管の洗浄装置は、例えば、上記余剰汚泥移送管により移送される余剰汚泥の流量を少なく調整し、余剰汚泥移送管内の抵抗を減少させることができる。即ち、このように余剰汚泥移送管内の抵抗が減少することから、高温蒸気噴出部から噴出される高温蒸気が、その熱や吐出圧力の低下を最小限に留めつつ、余剰汚泥移送管の内部に付着する余剰汚泥の詰まりをより効果的に圧送でき、その結果、当該余剰汚泥移送管の洗浄装置は、余剰汚泥移送管の洗浄効果をより一層向上させることができる。   The cleaning apparatus for the excess sludge transfer pipe may further include a flow rate adjusting unit that adjusts the flow rate of the excess sludge in the excess sludge transfer pipe. Thus, by further including a flow rate adjusting unit that adjusts the flow rate of the excess sludge in the excess sludge transfer pipe, the cleaning device for the excess sludge transfer pipe is, for example, the excess sludge transferred by the excess sludge transfer pipe. The flow rate can be adjusted to be small, and the resistance in the excess sludge transfer pipe can be reduced. That is, since the resistance in the surplus sludge transfer pipe is reduced in this way, the high-temperature steam ejected from the high-temperature steam ejection section is kept inside the surplus sludge transport pipe while minimizing the decrease in heat and discharge pressure. The clogging of the attached excess sludge can be pumped more effectively, and as a result, the cleaning device for the excess sludge transfer pipe can further improve the cleaning effect of the excess sludge transfer pipe.

以上説明したように、本発明の余剰汚泥移送管の洗浄装置は、余剰汚泥をメタン発酵するという一連のプロセスにおいて、メタン発酵用の余剰汚泥を移送する余剰汚泥移送管の内部に高温蒸気を噴出させるものであることから、従来の課題である汚泥処理システムの稼働中における余剰汚泥移送管の確実な洗浄を解決することができる。   As described above, the cleaning device for surplus sludge transfer pipe of the present invention injects high-temperature steam into the surplus sludge transfer pipe for transferring surplus sludge for methane fermentation in a series of processes for methane fermentation of surplus sludge. Therefore, it is possible to solve the problem of conventional cleaning of the excess sludge transfer pipe during operation of the sludge treatment system.

本発明の第1の実施形態に係る余剰汚泥移送管の洗浄装置を含む汚泥処理システムを示すフロー図である。It is a flowchart which shows the sludge processing system containing the washing | cleaning apparatus of the excess sludge transfer pipe which concerns on the 1st Embodiment of this invention. 本発明の第1の実施形態に係る余剰汚泥移送管の洗浄装置を示す概略構成図である。It is a schematic block diagram which shows the washing | cleaning apparatus of the excess sludge transfer pipe concerning the 1st Embodiment of this invention. 本発明の第2の実施形態に係る余剰汚泥移送管の洗浄装置を含む汚泥処理システムを示すフロー図である。It is a flowchart which shows the sludge processing system containing the washing | cleaning apparatus of the excess sludge transfer pipe which concerns on the 2nd Embodiment of this invention. 本発明の第2の実施形態に係る余剰汚泥移送管の洗浄装置を示す概略構成図である。It is a schematic block diagram which shows the washing | cleaning apparatus of the excess sludge transfer pipe | tube which concerns on the 2nd Embodiment of this invention. 本発明の第3の実施形態に係る余剰汚泥移送管の洗浄装置を含む汚泥処理システムを示すフロー図である。It is a flowchart which shows the sludge processing system containing the washing | cleaning apparatus of the excess sludge transfer pipe which concerns on the 3rd Embodiment of this invention. 本発明の第3の実施形態に係る余剰汚泥移送管の洗浄装置を示す概略構成図である。It is a schematic block diagram which shows the washing | cleaning apparatus of the excess sludge transfer pipe which concerns on the 3rd Embodiment of this invention. 本発明の第4の実施形態に係る余剰汚泥移送管の洗浄装置を示す概略構成図である。It is a schematic block diagram which shows the washing | cleaning apparatus of the excess sludge transfer pipe which concerns on the 4th Embodiment of this invention.

以下、適宜図面を参照しつつ本発明の実施の形態を詳説する。なお、本発明は、これらの実施形態に限定されるものではない。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings as appropriate. Note that the present invention is not limited to these embodiments.

(第1の実施形態に係る余剰汚泥移送管の洗浄装置)
図1の汚泥処理システムにおいて、余剰汚泥Rは、メタン発酵用の汚泥であり、余剰汚泥移送管Sにより移送され、メタン発酵装置Tによりメタン発酵される。かかる図1の汚泥処理システムにおいて、第1の実施形態に係る余剰汚泥移送管の洗浄装置は、余剰汚泥移送管Sの内部に高温蒸気Uを噴出させる。なお、余剰汚泥Rの濃度については特に限定されるものではない。また、メタン発酵装置Tの種類としては、特に限定されず、公知の装置を用いることができる。
(Cleaning apparatus for excess sludge transfer pipe according to the first embodiment)
In the sludge treatment system of FIG. 1, surplus sludge R is sludge for methane fermentation, and is transported by surplus sludge transfer pipe S and methane fermented by methane fermentation apparatus T. In the sludge treatment system of FIG. 1, the surplus sludge transfer pipe cleaning device according to the first embodiment ejects high-temperature steam U into the surplus sludge transfer pipe S. The concentration of excess sludge R is not particularly limited. Moreover, it does not specifically limit as a kind of methane fermentation apparatus T, A well-known apparatus can be used.

余剰汚泥移送管Sは、余剰汚泥Rを移送するための部材である。かかる余剰汚泥移送管Sの形状としては、内部に余剰汚泥Rを十分に通過させることができるものであれば特に限定されない。また、余剰汚泥移送管Sの内径についても、内部に余剰汚泥Rを十分に通過させることができるものであれば特に限定されない。   The excess sludge transfer pipe S is a member for transferring excess sludge R. The shape of the excess sludge transfer pipe S is not particularly limited as long as the excess sludge R can be sufficiently passed through the inside. Further, the inner diameter of the excess sludge transfer pipe S is not particularly limited as long as the excess sludge R can be sufficiently passed through the inside.

図2の余剰汚泥移送管の洗浄装置1は、余剰汚泥Rを移送する余剰汚泥移送管Sを洗浄するための装置である。この余剰汚泥移送管の洗浄装置1は、高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5を主として備える。   The excess sludge transfer pipe cleaning apparatus 1 in FIG. 2 is an apparatus for cleaning the excess sludge transfer pipe S that transfers the excess sludge R. The surplus sludge transfer pipe cleaning device 1 mainly includes a high temperature steam ejection part 2, a high temperature steam generation part 3, a transfer pipe internal pressure measurement part 4, and a flow rate adjustment part 5.

高温蒸気噴出部2は、余剰汚泥移送管Sに連通し、高温蒸気Uを余剰汚泥移送管Sの内部に噴出させるための部材である。かかる高温蒸気噴出部2の構造としては、余剰汚泥移送管Sの内部に高温蒸気Uを十分に噴出できるものであれば特に限定されない。また、かかる高温蒸気噴出部2における高温蒸気Uの噴出間隔や噴出のタイミングについても、特に限定されず、例えば、毎分ごと、毎時間ごと、連続的、断続的又はこれらの組合せのパターン等が挙げられる。   The high-temperature steam ejection part 2 communicates with the excess sludge transfer pipe S and is a member for ejecting the high-temperature steam U into the excess sludge transfer pipe S. The structure of the high-temperature steam ejection part 2 is not particularly limited as long as it can sufficiently eject the high-temperature steam U into the excess sludge transfer pipe S. Further, the ejection interval and ejection timing of the high-temperature steam U in the high-temperature steam ejection section 2 are not particularly limited, and for example, every minute, every hour, continuously, intermittently, or a combination pattern thereof. Can be mentioned.

高温蒸気発生部3は、高温蒸気噴出部2から噴出される高温蒸気Uを発生させるための部材である。かかる高温蒸気発生部3の構造としては、高温蒸気Uを満足に発生させることができるものであれば特に限定されない。   The high temperature steam generation unit 3 is a member for generating the high temperature steam U ejected from the high temperature steam ejection unit 2. The structure of the high temperature steam generator 3 is not particularly limited as long as the high temperature steam U can be generated satisfactorily.

移送管内圧計測部4は、余剰汚泥移送管Sの内部の圧力を計測するための部材である。この移送管内圧計測部4は、移送管内圧計6、内圧データ処理機構7を主として備える。   The transfer pipe internal pressure measurement unit 4 is a member for measuring the pressure inside the excess sludge transfer pipe S. The transfer pipe internal pressure measuring unit 4 mainly includes a transfer pipe internal pressure gauge 6 and an internal pressure data processing mechanism 7.

移送管内圧計6は、余剰汚泥移送管Sに配設され、余剰汚泥移送管Sの内部の圧力を計測するための部材である。かかる移送管内圧計6の構造としては、余剰汚泥移送管Sの内部に余剰汚泥Rや高温蒸気Uが存在し移送されている状態であっても余剰汚泥移送管Sの内部の圧力を十分に計測できるものであれば特に限定されない。また、余剰汚泥移送管Sにおける移送管内圧計6の配設数や配設箇所についても特に限定されない。   The transfer pipe internal pressure gauge 6 is a member that is disposed in the excess sludge transfer pipe S and measures the pressure inside the excess sludge transfer pipe S. As the structure of the transfer pipe internal pressure gauge 6, the internal pressure of the excess sludge transfer pipe S is sufficiently measured even when the excess sludge R and high-temperature steam U exist and are transferred inside the excess sludge transfer pipe S. There is no particular limitation as long as it is possible. Also, the number and location of the transfer pipe internal pressure gauges 6 in the excess sludge transfer pipe S are not particularly limited.

内圧データ処理機構7は、上記移送管内圧計6で計測される余剰汚泥移送管Sの内部の圧力データを取得及び解析するための部材である。かかる内圧データ処理機構7の構成としては、上記移送管内圧計6で計測される余剰汚泥移送管Sの内部の圧力データを十分に取得及び解析できるものであれば特に限定されない。   The internal pressure data processing mechanism 7 is a member for acquiring and analyzing pressure data inside the excess sludge transfer pipe S measured by the transfer pipe internal pressure gauge 6. The configuration of the internal pressure data processing mechanism 7 is not particularly limited as long as the internal pressure data of the excess sludge transfer pipe S measured by the transfer pipe internal pressure gauge 6 can be sufficiently acquired and analyzed.

流量調整部5は、余剰汚泥移送管Sにより移送される余剰汚泥Rの流量を調整するための部材である。かかる流量調整部5は、弁8、流量データ処理機構9を主として備える。   The flow rate adjusting unit 5 is a member for adjusting the flow rate of the excess sludge R transferred by the excess sludge transfer pipe S. The flow rate adjusting unit 5 mainly includes a valve 8 and a flow rate data processing mechanism 9.

弁8は、余剰汚泥移送管Sに配設され、余剰汚泥移送管Sにより移送される余剰汚泥Rの流量を実際に調整する部材である。この弁8の構造としては、余剰汚泥移送管Sにより移送される余剰汚泥Rの流量を十分に調整できるものであれば特に限定されない。また、余剰汚泥移送管Sにおける弁8の配設数や配設箇所についても特に限定されない。   The valve 8 is a member that is disposed in the excess sludge transfer pipe S and that actually adjusts the flow rate of the excess sludge R that is transferred by the excess sludge transfer pipe S. The structure of the valve 8 is not particularly limited as long as the flow rate of the excess sludge R transferred by the excess sludge transfer pipe S can be sufficiently adjusted. Further, the number and location of the valves 8 in the excess sludge transfer pipe S are not particularly limited.

流量データ処理機構9は、余剰汚泥移送管Sにおける余剰汚泥Rの流量をデータとして取得及び解析するための部材である。この流量データ処理機構9の構成としては、余剰汚泥移送管S内部の余剰汚泥Rの流量データを十分に取得及び解析できるものであれば特に限定されない。   The flow rate data processing mechanism 9 is a member for acquiring and analyzing the flow rate of the excess sludge R in the excess sludge transfer pipe S as data. The configuration of the flow rate data processing mechanism 9 is not particularly limited as long as it can sufficiently acquire and analyze the flow rate data of the excess sludge R inside the excess sludge transfer pipe S.

次に、図2を参照して、余剰汚泥移送管の洗浄装置1の使用手順について作用効果を中心に詳説する。余剰汚泥Rが余剰汚泥移送管S内部で移送されている状態において、高温蒸気噴出部2から高温蒸気Uを噴出させることで、余剰汚泥移送管の洗浄装置1は、かかる高温蒸気Uの熱や吐出圧力により、粘性の高い余剰汚泥Rの移送をスムーズにすることができると共に、余剰汚泥移送管Sの内部に付着する余剰汚泥Rを十分に除去でき、その結果、余剰汚泥移送管S内部の詰まりを確実に洗浄することができる。さらに、この高温蒸気Uは、上記余剰汚泥移送管Sを通じて余剰汚泥Rがメタン発酵されるまでの操業プロセスを停止させることなく噴出されることから、余剰汚泥移送管の洗浄装置1は、余剰汚泥Rをメタン発酵するという一連のプロセスを含む汚泥処理システムの稼働中において、余剰汚泥移送管Sの洗浄を確実に達成することができる。   Next, with reference to FIG. 2, the use procedure of the cleaning device 1 for the excess sludge transfer pipe will be described in detail focusing on the effects. In the state in which the excess sludge R is transferred inside the excess sludge transfer pipe S, the cleaning device 1 for the excess sludge transfer pipe causes the heat of the high temperature steam U to be generated by jetting the high temperature steam U from the high temperature steam jet part 2. Due to the discharge pressure, it is possible to smoothly transfer the excess sludge R with high viscosity, and it is possible to sufficiently remove the excess sludge R adhering to the inside of the excess sludge transfer pipe S. As a result, the excess sludge transfer pipe S The clogging can be reliably cleaned. Further, since the high-temperature steam U is ejected through the surplus sludge transfer pipe S without stopping the operation process until the surplus sludge R is subjected to methane fermentation, the surplus sludge transfer pipe cleaning device 1 During operation of the sludge treatment system including a series of processes for methane fermentation of R, cleaning of the excess sludge transfer pipe S can be reliably achieved.

当該余剰汚泥移送管の洗浄装置1において、上記高温蒸気Uの噴出方向は、特に限定されないが、例えば、上記余剰汚泥移送管Sにおける余剰汚泥Rの移送方向と略同一である場合、余剰汚泥Rの移送方向と略同一方向に高温蒸気Uの熱及び吐出圧力が重点的に作用し、特にメタン発酵側(下流側)に配設される余剰汚泥移送管Sの内部を十分に洗浄することができる。   In the surplus sludge transfer pipe cleaning device 1, the jet direction of the high-temperature steam U is not particularly limited. For example, when the surplus sludge R is substantially the same as the transfer direction of the surplus sludge transfer pipe S, the excess sludge R The heat and discharge pressure of the high-temperature steam U are preferentially applied in substantially the same direction as the transfer direction, and particularly the inside of the excess sludge transfer pipe S disposed on the methane fermentation side (downstream side) can be sufficiently washed. it can.

また、当該余剰汚泥移送管の洗浄装置1は、移送管内圧計測部4を備えることで、上述の汚泥処理システム稼働中における余剰汚泥移送管S内部の圧力を計測でき、このようにして計測される余剰汚泥移送管Sの内圧データを取得及び解析し、余剰汚泥移送管Sの詰まりの状態を容易に把握することができる。具体的には、上述の汚泥処理システムの稼働中において、余剰汚泥移送管Sの内圧が高いと判断される場合、余剰汚泥移送管Sの内部に余剰汚泥Rが付着し詰まりが発生しており、余剰汚泥Rの移送がスムーズに行われていないことが容易に推定できる。   Moreover, the said excess sludge transfer pipe washing | cleaning apparatus 1 can measure the pressure inside the excess sludge transfer pipe S during operation of the above-mentioned sludge treatment system by providing the transfer pipe internal pressure measurement part 4, and is measured in this way. The internal pressure data of the excess sludge transfer pipe S can be acquired and analyzed, and the clogged state of the excess sludge transfer pipe S can be easily grasped. Specifically, when it is determined that the internal pressure of the excess sludge transfer pipe S is high during the operation of the above sludge treatment system, the excess sludge R adheres to the inside of the excess sludge transfer pipe S and clogging occurs. It can be easily estimated that the excess sludge R is not smoothly transferred.

また、当該余剰汚泥移送管の洗浄装置1は、流量調整部5を備えることで、上述の汚泥処理システム稼働中の余剰汚泥移送管Sにおいて移送される余剰汚泥Rの流量を容易に調整することができる。具体的には、上述の汚泥処理システムの稼働中において、例えば、余剰汚泥移送管Sの上流側に配設される流量調整部5(図2において図示せず)において余剰汚泥Rの流量を少なく調整すると、余剰汚泥移送管Sの内部を流れる余剰汚泥Rの流量が制限され、その結果、余剰汚泥移送管Sの内部の抵抗を減少させることができる。このように余剰汚泥移送管Sの内部の抵抗が減少することから、高温蒸気噴出部2から噴出される高温蒸気Uが、その熱や吐出圧力の低下を最小限に留めつつ、余剰汚泥移送管Sの内部に付着する余剰汚泥Rの詰まりをより効果的に圧送でき、その結果、当該余剰汚泥移送管の洗浄装置1は、余剰汚泥移送管Sの洗浄効果をより一層向上させることができる。   Moreover, the said excess sludge transfer pipe washing | cleaning apparatus 1 is easily equipped with the flow volume adjustment part 5, and adjusts the flow volume of the excess sludge R transferred in the above-mentioned excess sludge transfer pipe S in operation of the sludge treatment system. Can do. Specifically, during the operation of the above-described sludge treatment system, for example, the flow rate of the excess sludge R is reduced in the flow rate adjusting unit 5 (not shown in FIG. 2) disposed on the upstream side of the excess sludge transfer pipe S. When adjusted, the flow rate of the excess sludge R flowing inside the excess sludge transfer pipe S is limited, and as a result, the resistance inside the excess sludge transfer pipe S can be reduced. Since the internal resistance of the excess sludge transfer pipe S is reduced in this way, the high temperature steam U ejected from the high temperature steam ejection section 2 keeps the decrease in heat and discharge pressure while keeping the excess sludge transfer pipe to a minimum. The clogging of the excess sludge R adhering to the inside of S can be pumped more effectively, and as a result, the cleaning device 1 for the excess sludge transfer pipe can further improve the cleaning effect of the excess sludge transfer pipe S.

なお、上記高温蒸気Uの吐出圧力としては、特に限定されず、例えば、0.2MPa以上であれば、当該余剰汚泥移送管の洗浄装置1は、上述した余剰汚泥移送管Sの洗浄を確実に達成することができる。また、上記高温蒸気Uの温度についても、特に限定されるものではない。   The discharge pressure of the high-temperature steam U is not particularly limited. For example, if it is 0.2 MPa or more, the cleaning device 1 for the excess sludge transfer pipe surely cleans the excess sludge transfer pipe S described above. Can be achieved. Further, the temperature of the high-temperature steam U is not particularly limited.

なお、上記高温蒸気Uにより加熱された余剰汚泥Rは、粘性が低いため、余剰汚泥移送管Sの内部へ付着しにくくなる。このように余剰汚泥Rが加熱されることで、余剰汚泥移送管Sにおける余剰汚泥Rの移送が容易になる。   In addition, since the excess sludge R heated by the said high temperature steam U has low viscosity, it becomes difficult to adhere to the inside of the excess sludge transfer pipe S. Thus, the surplus sludge R is heated in the surplus sludge transfer pipe S by heating the surplus sludge R.

(第2の実施形態に係る余剰汚泥移送管の洗浄装置)
図3の汚泥処理システムにおいて、余剰汚泥R、余剰汚泥移送管S、メタン発酵装置Tについては、図1の汚泥処理システムの場合と同様であるため、同一番号を付して説明を省略する。かかる図3の汚泥処理システムにおいて、第2の実施形態に係る余剰汚泥移送管の洗浄装置は、余剰汚泥移送管Sの内部に高温蒸気Uを噴出させるものであるが、高温蒸気Uの噴出方向が上記第1の実施形態に係る余剰汚泥移送管の洗浄装置の場合とは異なる。
(Cleaning device for surplus sludge transfer pipe according to the second embodiment)
In the sludge treatment system of FIG. 3, the excess sludge R, the excess sludge transfer pipe S, and the methane fermentation apparatus T are the same as those in the sludge treatment system of FIG. In the sludge treatment system of FIG. 3, the surplus sludge transfer pipe cleaning device according to the second embodiment ejects the high temperature steam U into the surplus sludge transfer pipe S. However, this is different from the case of the cleaning apparatus for excess sludge transfer pipe according to the first embodiment.

図4の余剰汚泥移送管の洗浄装置10は、余剰汚泥Rを移送する余剰汚泥移送管Sを洗浄するための装置である。かかる余剰汚泥移送管の洗浄装置10は、高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5を主として備える。また、移送管内圧計測部4は、移送管内圧計6、内圧データ処理機構7を主として備え、流量調整部5は、弁8、流量データ処理機構9を主として備える。なお、かかる高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5、移送管内圧計6、内圧データ処理機構7、弁8、流量データ処理機構9については、上述の余剰汚泥移送管の洗浄装置1の場合と同様であるため、同一番号を付して説明を省略する。   The excess sludge transfer pipe cleaning device 10 of FIG. 4 is an apparatus for cleaning the excess sludge transfer pipe S that transfers the excess sludge R. The surplus sludge transfer pipe cleaning device 10 mainly includes a high temperature steam ejection part 2, a high temperature steam generation part 3, a transfer pipe internal pressure measurement part 4, and a flow rate adjustment part 5. The transfer pipe internal pressure measurement unit 4 mainly includes a transfer pipe internal pressure gauge 6 and an internal pressure data processing mechanism 7, and the flow rate adjustment unit 5 mainly includes a valve 8 and a flow rate data processing mechanism 9. Note that the high-temperature steam ejection unit 2, the high-temperature steam generation unit 3, the transfer pipe internal pressure measurement unit 4, the flow rate adjustment unit 5, the transfer pipe internal pressure gauge 6, the internal pressure data processing mechanism 7, the valve 8, and the flow rate data processing mechanism 9 are described above. Since it is the same as that of the case of the cleaning apparatus 1 of the excess sludge transfer pipe, the same number is assigned and the description is omitted.

次に、図4を参照して、余剰汚泥移送管の洗浄装置10の使用手順について、上記余剰汚泥移送管の洗浄装置1とは異なる作用効果を中心に詳説する。   Next, with reference to FIG. 4, the use procedure of the surplus sludge transfer pipe cleaning device 10 will be described in detail with a focus on the different effects from the surplus sludge transfer pipe cleaning device 1.

当該余剰汚泥移送管の洗浄装置10において、上記高温蒸気Uの噴出方向は、上記余剰汚泥移送管Sにおける余剰汚泥Rの移送方向と対向である。このように、上記高温蒸気Uの噴出方向が、上記余剰汚泥移送管Sにおける余剰汚泥Rの移送方向と対向である場合、余剰汚泥Rの移送方向に逆らい、上述の汚泥処理システムにおける上流側に対して高温蒸気Uの熱及び吐出圧力が重点的に作用し、上述の汚泥処理システムの稼働中であっても、特に余剰汚泥Rの供給側(上流側)に配設される余剰汚泥移送管Sの内部を十分に洗浄することができる。   In the surplus sludge transfer pipe cleaning device 10, the jet direction of the high temperature steam U is opposite to the surplus sludge R transfer direction in the surplus sludge transfer pipe S. Thus, when the ejection direction of the high temperature steam U is opposite to the transfer direction of the excess sludge R in the excess sludge transfer pipe S, the transfer direction of the excess sludge R is opposed to the upstream side in the above sludge treatment system. On the other hand, the surplus sludge transfer pipe disposed on the supply side (upstream side) of the surplus sludge R, even when the heat and discharge pressure of the high-temperature steam U acts preferentially and the sludge treatment system described above is in operation. The inside of S can be washed sufficiently.

なお、当該余剰汚泥移送管の洗浄装置10において、上述の汚泥処理システムの稼働中における余剰汚泥移送管Sの洗浄の確実な達成、移送管内圧計測部4を備えることによる余剰汚泥移送管Sの詰まりの状態の容易な把握、流量調整部5を備えることによる余剰汚泥Rの流量の容易な調整、高温蒸気Uの温度及び吐出圧力の範囲等については、上記余剰汚泥移送管の洗浄装置1の場合と同様である。   In addition, in the said excess sludge transfer pipe washing | cleaning apparatus 10, the reliable achievement of the washing | cleaning of the excess sludge transfer pipe S in the operation | movement of the above-mentioned sludge treatment system, and the surplus sludge transfer pipe S of having the transfer pipe internal pressure measurement part 4 are provided. For easy grasping of the clogging state, easy adjustment of the flow rate of the excess sludge R by providing the flow rate adjusting unit 5, the temperature and discharge pressure range of the high temperature steam U, etc. Same as the case.

(第3の実施形態に係る余剰汚泥移送管の洗浄装置)
図5の汚泥処理システムにおいて、余剰汚泥R、余剰汚泥移送管S、メタン発酵装置T、高温蒸気Uについては、図1の汚泥処理システムの場合と同様であるため、同一番号を付して説明を省略する。この図5の汚泥処理システムにおいて、第3の実施形態に係る余剰汚泥移送管の洗浄装置は、余剰汚泥移送管Sの内部に高温蒸気Uを噴出させるものであるが、高温蒸気Uにより加熱される加熱余剰汚泥Vと加熱前の余剰汚泥Rとの熱交換を行う後述の熱交換部12を備えることが、上記第1の実施形態に係る余剰汚泥移送管の洗浄装置の場合とは異なる。また、図5に示す通り、加熱前の余剰汚泥Rをメタン発酵装置Tに直接移送するバイパスを設置することもできる。このバイパスは、余剰汚泥Rを移送できる移送管であり、上記余剰汚泥移送管Sと同様のものを用いることができる。かかるバイパスにおいて、加熱前の余剰汚泥Rと熱交換部12から移送される余剰汚泥Rとを混合してメタン発酵装置Tに移送することもできる。なお、高温蒸気Uは、かかるバイパス内に対しても噴出することができる。
(Cleaning device for excess sludge transfer pipe according to the third embodiment)
In the sludge treatment system of FIG. 5, the excess sludge R, the excess sludge transfer pipe S, the methane fermentation apparatus T, and the high-temperature steam U are the same as those in the sludge treatment system of FIG. Is omitted. In the sludge treatment system of FIG. 5, the surplus sludge transfer pipe cleaning device according to the third embodiment ejects the high temperature steam U into the surplus sludge transfer pipe S, but is heated by the high temperature steam U. It differs from the case of the cleaning apparatus of the surplus sludge transfer pipe which concerns on the said 1st Embodiment to provide the below-mentioned heat exchange part 12 which heat-exchanges the surplus sludge V heated and the surplus sludge R before a heating. Moreover, as shown in FIG. 5, the bypass which transfers the surplus sludge R before a heating directly to the methane fermentation apparatus T can also be installed. This bypass is a transfer pipe capable of transferring excess sludge R, and the same as the above-described excess sludge transfer pipe S can be used. In such a bypass, the excess sludge R before heating and the excess sludge R transferred from the heat exchange unit 12 can be mixed and transferred to the methane fermentation apparatus T. The high-temperature steam U can be ejected into the bypass.

図6の余剰汚泥移送管の洗浄装置11は、余剰汚泥Rを移送する余剰汚泥移送管Sを洗浄するための装置である。この余剰汚泥移送管の洗浄装置11は、高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5、熱交換部12を主として備える。また、移送管内圧計測部4は、移送管内圧計6、内圧データ処理機構7を主として備え、流量調整部5は、弁8、流量データ処理機構9を主として備える。なお、かかる高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5、移送管内圧計6、内圧データ処理機構7、弁8、流量データ処理機構9については、上述の余剰汚泥移送管の洗浄装置1の場合と同様であるため、同一番号を付して説明を省略する。   The excess sludge transfer pipe cleaning device 11 of FIG. 6 is an apparatus for cleaning the excess sludge transfer pipe S that transfers the excess sludge R. The surplus sludge transfer pipe cleaning device 11 mainly includes a high temperature steam ejection part 2, a high temperature steam generation part 3, a transfer pipe internal pressure measurement part 4, a flow rate adjustment part 5, and a heat exchange part 12. The transfer pipe internal pressure measurement unit 4 mainly includes a transfer pipe internal pressure gauge 6 and an internal pressure data processing mechanism 7, and the flow rate adjustment unit 5 mainly includes a valve 8 and a flow rate data processing mechanism 9. Note that the high-temperature steam ejection unit 2, the high-temperature steam generation unit 3, the transfer pipe internal pressure measurement unit 4, the flow rate adjustment unit 5, the transfer pipe internal pressure gauge 6, the internal pressure data processing mechanism 7, the valve 8, and the flow rate data processing mechanism 9 are described above. Since it is the same as that of the case of the cleaning apparatus 1 of the excess sludge transfer pipe, the same number is assigned and the description is omitted.

熱交換部12は、上記余剰汚泥移送管Sにおいて、高温蒸気Uにより加熱される加熱余剰汚泥Vと、加熱前の余剰汚泥Rとの熱交換を行うための部材である。かかる熱交換部12の構造としては、上述の加熱余剰汚泥Vと加熱前の余剰汚泥Rとの熱交換を十分に達成できるものであれば特に限定されず、例えば、二重管式、多管円筒形式、プレート式等が挙げられるが、中でも後述する二重管式であることが好ましい。   The heat exchange part 12 is a member for performing heat exchange between the heated excess sludge V heated by the high-temperature steam U and the excess sludge R before heating in the excess sludge transfer pipe S. The structure of the heat exchange unit 12 is not particularly limited as long as it can sufficiently achieve heat exchange between the above-described heated excess sludge V and the excess sludge R before heating. Although a cylindrical form, a plate type, etc. are mentioned, it is preferable that it is a double pipe type mentioned later especially.

次に、図6を参照して、余剰汚泥移送管の洗浄装置11の使用手順について、上記余剰汚泥移送管の洗浄装置1及び余剰汚泥移送管の洗浄装置10とは異なる作用効果を中心に詳説する。   Next, with reference to FIG. 6, the use procedure of the surplus sludge transfer pipe cleaning device 11 will be described in detail with a focus on different effects from the surplus sludge transfer pipe cleaning device 1 and the excess sludge transfer pipe cleaning device 10. To do.

当該余剰汚泥移送管の洗浄装置11は、上記熱交換部12を備えることで、高温蒸気Uにより加熱される加熱余剰汚泥Vから、加熱前の余剰汚泥Rに熱が効率的に移動することとなる。その結果、当該余剰汚泥移送管の洗浄装置11は、加熱余剰汚泥Vにより既に加熱された余剰汚泥Rに対して高温蒸気Uを噴出することから、かかる余剰汚泥Rに対して噴出される高温蒸気のエネルギー量を低減でき、省エネルギー化を図ることができる。   The surplus sludge transfer pipe cleaning device 11 includes the heat exchanging portion 12 so that heat is efficiently transferred from the heated surplus sludge V heated by the high-temperature steam U to the surplus sludge R before heating. Become. As a result, since the cleaning device 11 for the surplus sludge transfer pipe ejects the high temperature steam U to the surplus sludge R already heated by the heated surplus sludge V, the high temperature steam ejected to the surplus sludge R. Energy amount can be reduced, and energy saving can be achieved.

なお、当該余剰汚泥移送管の洗浄装置11において、上述の汚泥処理システムの稼働中における余剰汚泥移送管Sの洗浄の確実な達成、移送管内圧計測部4を備えることによる余剰汚泥移送管Sの詰まりの状態の容易な把握、流量調整部5を備えることによる余剰汚泥Rの流量の容易な調整、高温蒸気Uの温度及び吐出圧力の範囲等については、上記余剰汚泥移送管の洗浄装置1の場合と同様である。   In addition, in the cleaning apparatus 11 for the surplus sludge transfer pipe, the surplus sludge transfer pipe S of the surplus sludge transfer pipe S provided with the reliable achievement of the cleaning of the surplus sludge transfer pipe S during the operation of the above-described sludge treatment system and the transfer pipe internal pressure measuring unit 4 is provided. For easy grasping of the clogging state, easy adjustment of the flow rate of the excess sludge R by providing the flow rate adjusting unit 5, the temperature and discharge pressure range of the high temperature steam U, etc. Same as the case.

(第4の実施形態に係る余剰汚泥移送管の洗浄装置)
図7の余剰汚泥移送管の洗浄装置13は、余剰汚泥Rを移送する余剰汚泥移送管Sを洗浄するための装置である。この余剰汚泥移送管の洗浄装置13は、高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5、二重管熱交換部14を主として備える。また、移送管内圧計測部4は、移送管内圧計6、内圧データ処理機構7を主として備える。また、流量調整部5は、弁8、流量データ処理機構9を主として備える。なお、かかる高温蒸気噴出部2、高温蒸気発生部3、移送管内圧計測部4、流量調整部5、移送管内圧計6、内圧データ処理機構7、弁8、流量データ処理機構9については、上述の余剰汚泥移送管の洗浄装置1の場合と同様であるため、同一番号を付して説明を省略する。
(Cleaning device for surplus sludge transfer pipe according to the fourth embodiment)
The excess sludge transfer pipe cleaning device 13 in FIG. 7 is an apparatus for cleaning the excess sludge transfer pipe S that transfers the excess sludge R. The excess sludge transfer pipe cleaning device 13 mainly includes a high-temperature steam ejection part 2, a high-temperature steam generation part 3, a transfer pipe internal pressure measurement part 4, a flow rate adjustment part 5, and a double pipe heat exchange part 14. The transfer pipe internal pressure measuring unit 4 mainly includes a transfer pipe internal pressure gauge 6 and an internal pressure data processing mechanism 7. The flow rate adjusting unit 5 mainly includes a valve 8 and a flow rate data processing mechanism 9. Note that the high-temperature steam ejection unit 2, the high-temperature steam generation unit 3, the transfer pipe internal pressure measurement unit 4, the flow rate adjustment unit 5, the transfer pipe internal pressure gauge 6, the internal pressure data processing mechanism 7, the valve 8, and the flow rate data processing mechanism 9 are described above. Since it is the same as that of the case of the cleaning apparatus 1 of the excess sludge transfer pipe, the same number is assigned and the description is omitted.

二重管熱交換部14は、高温蒸気Uにより加熱される加熱余剰汚泥Vと、加熱前の余剰汚泥Rとの熱交換を行うための部材である。かかる二重管熱交換部14の構造は、余剰汚泥移送管Sが二重構造となったものであり、外管部15及び内管部16から構成される。かかる二重管式熱交換部14において、外管部15では高温蒸気Uにより加熱された加熱余剰汚泥Vが移送され、内管部16では上述の汚泥処理システムの上流から余剰汚泥Rが移送される。   The double pipe heat exchanging unit 14 is a member for performing heat exchange between the heated excess sludge V heated by the high-temperature steam U and the excess sludge R before heating. The structure of the double pipe heat exchange section 14 is such that the surplus sludge transfer pipe S has a double structure, and includes an outer pipe section 15 and an inner pipe section 16. In the double-pipe heat exchanging section 14, the heated surplus sludge V heated by the high-temperature steam U is transferred in the outer pipe section 15, and the surplus sludge R is transferred from the upstream of the sludge treatment system described above in the inner pipe section 16. The

なお、上記外管部15や内管部16の内径については、余剰汚泥Rや加熱余剰汚泥Vを満足に移送することができるものであれば特に限定されない。また、上記外管部15や内管部16のそれぞれにおいて、上述の移送管内圧計6や弁8を、任意の配設箇所や配設個数を選択して配設することができる。   In addition, about the internal diameter of the said outer pipe part 15 and the inner pipe part 16, if the surplus sludge R and the heating surplus sludge V can be transferred satisfactorily, it will not specifically limit. Further, in each of the outer pipe portion 15 and the inner pipe portion 16, the transfer pipe internal pressure gauge 6 and the valve 8 described above can be arranged by selecting an arbitrary arrangement location and arrangement number.

次に、図7を参照して、余剰汚泥移送管の洗浄装置13の使用手順について、上記余剰汚泥移送管の洗浄装置1及び余剰汚泥移送管の洗浄装置10とは異なる作用効果を中心に詳説する。   Next, referring to FIG. 7, the use procedure of the excess sludge transfer pipe cleaning device 13 will be described in detail with a focus on different effects from the above-described excess sludge transfer pipe cleaning device 1 and the excess sludge transfer pipe cleaning device 10. To do.

図7に示す通り、上述の汚泥処理システムの上流側から移送される余剰汚泥Rは、まず内管部16を通じて移送され、高温蒸気噴出部2から噴出される高温蒸気Uにより加熱され加熱余剰汚泥Vとなる。次いで、かかる加熱余剰汚泥Vは、外管部15に移送され、内管部16内部の余剰汚泥Rと熱交換を行い、上述の汚泥処理システムの下流側へと移送される。この場合において、外管部15で移送される加熱余剰汚泥Vにより内管部16内の余剰汚泥Rが加熱されることから、かかる余剰汚泥Rが高温蒸気噴出部2に達する時点で既に加熱されていることとなる。つまり、当該余剰汚泥移送管の洗浄装置13は、二重管熱交換部14を備えることで、上述した加熱余剰汚泥Vから余剰汚泥Rへの熱の移動をコンパクトな構成により効率的に行うことができ、その結果、余剰汚泥Rに対して噴出される高温蒸気のエネルギー量をより一層低減することができる。   As shown in FIG. 7, surplus sludge R transferred from the upstream side of the above-described sludge treatment system is first transferred through the inner pipe portion 16 and heated by the high-temperature steam U ejected from the high-temperature steam ejection section 2 to be heated surplus sludge. V. Next, the heated surplus sludge V is transferred to the outer pipe portion 15, exchanges heat with the surplus sludge R inside the inner pipe portion 16, and is transferred to the downstream side of the above-described sludge treatment system. In this case, since the surplus sludge R in the inner pipe portion 16 is heated by the heated surplus sludge V transferred by the outer pipe portion 15, the surplus sludge R is already heated when it reaches the high temperature steam ejection portion 2. Will be. That is, the surplus sludge transfer pipe cleaning device 13 includes the double pipe heat exchanging section 14 so that the heat transfer from the heated surplus sludge V to the surplus sludge R can be efficiently performed with a compact configuration. As a result, it is possible to further reduce the energy amount of the high-temperature steam ejected to the excess sludge R.

なお、当該余剰汚泥移送管の洗浄装置13において、上述の汚泥処理システムの稼働中における余剰汚泥移送管Sの洗浄の確実な達成、移送管内圧計測部4を備えることによる余剰汚泥移送管Sの詰まりの状態の容易な把握、流量調整部5を備えることによる余剰汚泥Rの流量の容易な調整、高温蒸気Uの温度及び吐出圧力の範囲等については、上記余剰汚泥移送管の洗浄装置1の場合と同様である。なお、かかる加熱余剰汚泥Vは、上述の高温蒸気Uにより加熱された余剰汚泥Rと同様に粘性が低いため、余剰汚泥移送管Sの内部へ付着しにくくなる。このように余剰汚泥Rが加熱されることで、余剰汚泥移送管Sにおける余剰汚泥Rの移送が容易になる。   In addition, in the cleaning apparatus 13 for the surplus sludge transfer pipe, the surplus sludge transfer pipe S of the surplus sludge transfer pipe S provided with the reliable achievement of the cleaning of the surplus sludge transfer pipe S during the operation of the above-described sludge treatment system and the transfer pipe internal pressure measuring unit 4 is provided. For easy grasping of the clogging state, easy adjustment of the flow rate of the excess sludge R by providing the flow rate adjusting unit 5, the temperature and discharge pressure range of the high temperature steam U, etc. Same as the case. In addition, since this heating surplus sludge V has low viscosity similarly to the surplus sludge R heated with the above-mentioned high temperature steam U, it becomes difficult to adhere to the inside of the surplus sludge transfer pipe S. Thus, the surplus sludge R is heated in the surplus sludge transfer pipe S by heating the surplus sludge R.

なお、本発明の余剰汚泥移送管の洗浄装置は、上記実施形態に限定されない。例えば、本発明の余剰汚泥移送管の洗浄装置において、余剰汚泥移送管の洗浄状態を確認する手段として、余剰汚泥移送管の表面温度を測定する手段を採用することもできる。かかる手段は、具体的には、余剰汚泥移送管の内部に高温蒸気を噴出させた後、余剰汚泥移送管の任意の箇所において、表面温度が例えば100℃以上に急激に上昇する場合、かかる任意の箇所において高温蒸気が余剰汚泥移送管内部に付着した余剰汚泥を圧出し、洗浄が達成されたと判断するものである。   The surplus sludge transfer pipe cleaning device of the present invention is not limited to the above embodiment. For example, in the apparatus for cleaning an excess sludge transfer pipe of the present invention, a means for measuring the surface temperature of the excess sludge transfer pipe can be employed as a means for confirming the cleaning state of the excess sludge transfer pipe. Specifically, such a means is used in the case where the surface temperature rapidly rises to, for example, 100 ° C. or more at an arbitrary position of the excess sludge transfer pipe after jetting high temperature steam into the excess sludge transfer pipe. At this point, the high temperature steam presses out the excess sludge adhering to the inside of the excess sludge transfer pipe, and it is judged that the cleaning has been achieved.

また、例えば、発明の余剰汚泥移送管の洗浄装置において、余剰汚泥等を移送するためのポンプにより、余剰汚泥移送管により移送される余剰汚泥の流量を調整することもできる。なお、かかるポンプの種類については、特に限定されず、公知のものを用いることができる。   For example, in the cleaning apparatus for excess sludge transfer pipe of the invention, the flow rate of excess sludge transferred by the excess sludge transfer pipe can be adjusted by a pump for transferring excess sludge and the like. In addition, it does not specifically limit about the kind of this pump, A well-known thing can be used.

また、例えば、本発明の余剰汚泥移送管の洗浄装置において、高温蒸気の噴出方向を自由に変更できる機構を採用することもできる。かかる機構の種類としては、特に限定されず、公知のものを採用することができ、例えば、自動式、手動式又はこれらの組合せのパターン等が挙げられる。   In addition, for example, in the cleaning device for excess sludge transfer pipe of the present invention, a mechanism that can freely change the jet direction of the high-temperature steam can be employed. The type of the mechanism is not particularly limited, and a known mechanism can be adopted, and examples thereof include an automatic type, a manual type, or a combination pattern thereof.

また、例えば、本発明の余剰汚泥移送管の洗浄装置において、上述した汚泥処理システム上流の余剰汚泥移送管に配設される弁を微開状態に設定し、下流の余剰汚泥移送管に配設される弁を十分解放することで、下流の余剰汚泥移送管をより短時間で強力に洗浄することができる。また、上述した汚泥処理システム下流の余剰汚泥移送管に配設される弁を微開状態に設定し、上流の余剰汚泥移送管に配設される弁を十分解放することで、上流の余剰汚泥移送管をより短時間で強力に洗浄することもできる。   Also, for example, in the cleaning apparatus for excess sludge transfer pipe of the present invention, the valve disposed in the above-described excess sludge transfer pipe upstream of the sludge treatment system is set in a slightly open state and disposed in the downstream excess sludge transfer pipe. By sufficiently releasing the valve, the downstream excess sludge transfer pipe can be washed strongly in a shorter time. Further, by setting the valve disposed in the surplus sludge transfer pipe downstream of the above-described sludge treatment system to a slightly open state and sufficiently releasing the valve disposed in the upstream sludge transfer pipe, the upstream surplus sludge The transfer tube can also be cleaned strongly in a shorter time.

以上のように、本発明の余剰汚泥移送管の洗浄装置は、一般的な汚泥処理システムにおいて、余剰汚泥を移送する余剰汚泥移送管の洗浄に好適に使用され得る。   As described above, the cleaning device for excess sludge transfer pipe of the present invention can be suitably used for cleaning the excess sludge transfer pipe for transferring excess sludge in a general sludge treatment system.

1 余剰汚泥移送管の洗浄装置
2 高温蒸気噴出部
3 高温蒸気発生部
4 移送管内圧計測部
5 流量調整部
6 移送管内圧計
7 内圧データ処理機構
8 弁
9 流量データ処理機構
10 余剰汚泥移送管の洗浄装置
11 余剰汚泥移送管の洗浄装置
12 熱交換部
13 余剰汚泥移送管の洗浄装置
14 二重管熱交換部
15 外管部
16 内管部
R 余剰汚泥
S 余剰汚泥移送管
T メタン発酵装置
U 高温蒸気
V 加熱余剰汚泥

DESCRIPTION OF SYMBOLS 1 Cleaning apparatus of excess sludge transfer pipe 2 High temperature steam injection part 3 High temperature steam generation part 4 Transfer pipe internal pressure measurement part 5 Flow rate adjustment part 6 Transfer pipe internal pressure gauge 7 Internal pressure data processing mechanism 8 Valve 9 Flow rate data processing mechanism 10 Excess sludge transfer pipe Cleaning device 11 Cleaning device for surplus sludge transfer pipe 12 Heat exchange section 13 Cleaning device for surplus sludge transfer pipe 14 Double pipe heat exchange section 15 Outer pipe section 16 Inner pipe section R Surplus sludge S Surplus sludge transfer pipe T Methane fermentation unit U High temperature steam V Heated excess sludge

Claims (5)

メタン発酵用の余剰汚泥を移送する余剰汚泥移送管を洗浄する洗浄装置であって、
上記余剰汚泥移送管の内部に高温蒸気を噴出させる高温蒸気噴出部を備えることを特徴とする余剰汚泥移送管の洗浄装置。
A cleaning device for cleaning an excess sludge transfer pipe for transferring excess sludge for methane fermentation,
An apparatus for cleaning an excess sludge transfer pipe, comprising a high temperature steam jetting part for jetting high temperature steam inside the excess sludge transfer pipe.
上記高温蒸気により加熱される加熱余剰汚泥と、加熱前の余剰汚泥との熱交換を行う熱交換部をさらに備える請求項1記載の余剰汚泥移送管の洗浄装置。   The apparatus for cleaning an excess sludge transfer pipe according to claim 1, further comprising a heat exchanging unit that performs heat exchange between the heated excess sludge heated by the high-temperature steam and the excess sludge before heating. 上記熱交換部が、上記加熱余剰汚泥を移送する余剰汚泥移送管と、加熱前の余剰汚泥を移送する余剰汚泥移送管との二重管式である請求項1又は請求項2記載の余剰汚泥移送管の洗浄装置。   The surplus sludge according to claim 1 or 2, wherein the heat exchanging part is a double pipe type of a surplus sludge transfer pipe for transferring the heated surplus sludge and a surplus sludge transfer pipe for transferring the surplus sludge before heating. Transfer pipe cleaning device. 上記余剰汚泥移送管の内圧を計測する移送管内圧計測部をさらに備える請求項1〜3のいずれか1項に記載の余剰汚泥移送管の洗浄装置。   The cleaning apparatus for an excess sludge transfer pipe according to any one of claims 1 to 3, further comprising a transfer pipe internal pressure measurement unit that measures an internal pressure of the excess sludge transfer pipe. 上記余剰汚泥移送管における余剰汚泥の流量を調整する流量調整部をさらに備える請求項1〜4のいずれか1項に記載の余剰汚泥移送管の洗浄装置。

The cleaning device for an excess sludge transfer pipe according to any one of claims 1 to 4, further comprising a flow rate adjusting unit for adjusting a flow rate of the excess sludge in the excess sludge transfer pipe.

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018143903A (en) * 2017-03-01 2018-09-20 鹿島建設株式会社 Methane fermentation bioreactor and method for washing the same
CN112404051A (en) * 2020-09-21 2021-02-26 中石化宁波工程有限公司 Steam pipe network integrated purging system and method

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5037279A (en) * 1973-08-06 1975-04-07
JPS5990700A (en) * 1982-11-12 1984-05-25 Hitachi Chem Co Ltd Methane fermentation treatment
JPH0639400A (en) * 1992-04-01 1994-02-15 Texaco Dev Corp Method for treating sewage sludge
JP2002355700A (en) * 2001-05-31 2002-12-10 Japan Sewage Works Agency Supercritical water oxidative decomposition apparatus
JP2003500208A (en) * 1999-05-31 2003-01-07 キャンビ アーエス Method and apparatus for continuously hydrolyzing organic materials
JP2003117526A (en) * 2001-10-09 2003-04-22 Ishikawajima Harima Heavy Ind Co Ltd Biogasification treating method for organic waste
JP2003305498A (en) * 2002-04-11 2003-10-28 Kurita Water Ind Ltd Sludge treatment apparatus
JP2004290779A (en) * 2003-03-26 2004-10-21 Hitachi Kiden Kogyo Ltd Sludge treatment method
JP2006130370A (en) * 2004-11-02 2006-05-25 Mitsui Eng & Shipbuild Co Ltd Method for cleaning piping in oil-mixed sludge treatment system
JP2008221075A (en) * 2007-03-09 2008-09-25 Nippon Petroleum Refining Co Ltd Cleaning method in piping system
JP2009213990A (en) * 2008-03-10 2009-09-24 Fuji Electric Holdings Co Ltd Methane fermentation method and apparatus
WO2009121873A1 (en) * 2008-03-31 2009-10-08 Krüger Off-Shore A/S An apparatus and a method for continuous thermal hydrolysis of biological material
JP2011098249A (en) * 2009-11-03 2011-05-19 Techno Plan:Kk Sludge solubilizing apparatus and method therefor

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5037279A (en) * 1973-08-06 1975-04-07
JPS5990700A (en) * 1982-11-12 1984-05-25 Hitachi Chem Co Ltd Methane fermentation treatment
JPH0639400A (en) * 1992-04-01 1994-02-15 Texaco Dev Corp Method for treating sewage sludge
JP2003500208A (en) * 1999-05-31 2003-01-07 キャンビ アーエス Method and apparatus for continuously hydrolyzing organic materials
JP2002355700A (en) * 2001-05-31 2002-12-10 Japan Sewage Works Agency Supercritical water oxidative decomposition apparatus
JP2003117526A (en) * 2001-10-09 2003-04-22 Ishikawajima Harima Heavy Ind Co Ltd Biogasification treating method for organic waste
JP2003305498A (en) * 2002-04-11 2003-10-28 Kurita Water Ind Ltd Sludge treatment apparatus
JP2004290779A (en) * 2003-03-26 2004-10-21 Hitachi Kiden Kogyo Ltd Sludge treatment method
JP2006130370A (en) * 2004-11-02 2006-05-25 Mitsui Eng & Shipbuild Co Ltd Method for cleaning piping in oil-mixed sludge treatment system
JP2008221075A (en) * 2007-03-09 2008-09-25 Nippon Petroleum Refining Co Ltd Cleaning method in piping system
JP2009213990A (en) * 2008-03-10 2009-09-24 Fuji Electric Holdings Co Ltd Methane fermentation method and apparatus
WO2009121873A1 (en) * 2008-03-31 2009-10-08 Krüger Off-Shore A/S An apparatus and a method for continuous thermal hydrolysis of biological material
JP2011098249A (en) * 2009-11-03 2011-05-19 Techno Plan:Kk Sludge solubilizing apparatus and method therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018143903A (en) * 2017-03-01 2018-09-20 鹿島建設株式会社 Methane fermentation bioreactor and method for washing the same
CN112404051A (en) * 2020-09-21 2021-02-26 中石化宁波工程有限公司 Steam pipe network integrated purging system and method

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