JP2008055281A - Apparatus for supplying sludge to carbonizing furnace - Google Patents

Apparatus for supplying sludge to carbonizing furnace Download PDF

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JP2008055281A
JP2008055281A JP2006233451A JP2006233451A JP2008055281A JP 2008055281 A JP2008055281 A JP 2008055281A JP 2006233451 A JP2006233451 A JP 2006233451A JP 2006233451 A JP2006233451 A JP 2006233451A JP 2008055281 A JP2008055281 A JP 2008055281A
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sludge
furnace
supplied
dried
weight
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JP4848894B2 (en
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Tadatoshi Kabuto
忠敏 甲
Masashi Kato
正士 加藤
Makoto Kitabayashi
誠 北林
Akihiro Ueda
晃弘 植田
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Daido Steel Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To realize a stable operation of a carbonizing furnace by properly supplying dried sludge to the carbonizing furnace even if the moisture content of the dried sludge changes. <P>SOLUTION: A quantitative feeder 21 for quantitatively supplying dehydrated sludge WS1 to a sludge drying furnace 3 is installed, and an intermediate hopper 5 airtightly connected to the carbonizing furnace 7 is installed between the sludge drying furnace 3 and the carbonizing furnace 7. A load cell 51 for detecting the weight of dried sludge WS2 supplied from the sludge drying furnace 3 to be stored in the intermediate hopper 5 is installed in the intermediate hopper 5, and a screw conveyor 52 for supplying the dried sludge in the intermediate hopper 5 to the carbonizing furnace 7 is installed on the outlet side of the intermediate hopper 5. A controller 6 for controlling the feeding amount of the screw conveyor 52 so that the weight of the detected sludge is always constant is installed. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は炭化炉への汚泥供給装置に関し、炭化炉の安定操業を可能とする汚泥供給装置に関する。   The present invention relates to a sludge supply apparatus for a carbonization furnace, and relates to a sludge supply apparatus that enables stable operation of the carbonization furnace.

下水処理に伴い生じる汚泥を汚泥乾燥炉で含水率40%程度の乾燥汚泥とした後、炭化炉にて低酸素状態で熱分解して有機可燃成分の残存した炭化物として再利用することが行われている。通常、上記汚泥乾燥炉と炭化炉の間には、負圧となった炭化炉に気密的に連結されて、切り出し装置を付設した中継ホッパが設けられている。この中継ホッパには所定量以上の乾燥汚泥が貯留されて、負圧となった炭化炉に空気が侵入して当該炭化炉内の温度が変動することを防止している。また、中継ホッパの容量は、汚泥乾燥炉から供給される乾燥汚泥1時間分以上を貯留できるものとなっており、炭化炉がトラブル等で停止した場合に、汚泥乾燥炉から供給される乾燥汚泥を一時的に貯留できるようになっている。そして、切出し装置によって、常時所定重量の乾燥汚泥を炭化炉へ供給するようにしている。ところが、汚泥乾燥炉からの乾燥汚泥の含水率は一定ではなく、ある範囲で変動するため、スクリューコンベアを定回転で運転しても実際に炭化炉へ供給される単位時間当たりの乾燥汚泥の重量(切出し量)は、乾燥汚泥の含水率で変動してしまう。   Sludge produced by sewage treatment is converted into dried sludge with a moisture content of about 40% in a sludge drying furnace, and then pyrolyzed in a low-oxygen state in a carbonization furnace to be reused as carbides with residual organic combustible components. ing. Usually, between the said sludge drying furnace and the carbonization furnace, the relay hopper which connected airtightly to the carbonization furnace used as the negative pressure and attached the cutting device is provided. In this relay hopper, a predetermined amount or more of dry sludge is stored to prevent air from entering the carbonization furnace having a negative pressure and changing the temperature in the carbonization furnace. Moreover, the capacity of the relay hopper is such that the dried sludge supplied from the sludge drying furnace can be stored for one hour or more, and the dried sludge supplied from the sludge drying furnace when the carbonization furnace is stopped due to trouble or the like. Can be temporarily stored. Then, a dry sludge having a predetermined weight is always supplied to the carbonization furnace by the cutting device. However, since the moisture content of the dried sludge from the sludge drying furnace is not constant and varies within a certain range, the weight of the dried sludge per unit time actually supplied to the carbonization furnace even when the screw conveyor is operated at a constant rotation (Cut amount) varies depending on the moisture content of the dried sludge.

すなわち、乾燥汚泥の含水率が上昇すると嵩比重が小さくなるため定容積式のスクリューコンベアによる切出し量は小さくなり、一方、含水率が低下すると嵩比重が大きくなって切出し量も大きくなる。そこで、例えば特許文献1では、切出し量に相当する、スクリューコンベア前段の中継ホッパでの重量変化をロードセルで検出して、切出し量が小さくなった場合には汚泥乾燥炉における乾燥条件を強くして乾燥汚泥の含水率を低下させ、切出し量が大きくなった場合には汚泥乾燥条件を弱くして乾燥汚泥の含水率を上昇させるようにして、常に切出し量が一定となるように制御する汚泥供給方法が提案されている。
特開2006−55743
That is, when the moisture content of the dried sludge increases, the bulk specific gravity decreases, so that the cut-out amount by the constant volume screw conveyor decreases. On the other hand, when the water content decreases, the bulk specific gravity increases and the cut-out amount increases. Therefore, for example, in Patent Document 1, the load change in the relay hopper upstream of the screw conveyor corresponding to the cutting amount is detected by the load cell, and when the cutting amount becomes small, the drying condition in the sludge drying furnace is increased. Sludge supply that reduces the moisture content of the dried sludge and increases the moisture content of the dried sludge by decreasing the sludge drying conditions when the amount of the cut is increased, so that the amount of the dried sludge is constantly controlled. A method has been proposed.
JP 2006-55743 A

しかし、上記従来の汚泥供給方法では、汚泥乾燥炉の乾燥条件を変化させても乾燥汚泥の含水率は速やかには所望の値に戻らないために、切出し量の変動が比較的長く続くという不具合がある。    However, in the above conventional sludge supply method, even if the drying conditions of the sludge drying furnace are changed, the moisture content of the dried sludge does not quickly return to the desired value. There is.

そこで、本発明はこのような課題を解決するもので、乾燥汚泥の含水率が変動しても炭化炉への乾燥汚泥の供給を適正に行うことができ、もって炭化炉の安定操業を実現できる炭化炉への汚泥供給装置を提供することを目的とする。   Therefore, the present invention solves such a problem, and even if the moisture content of the dried sludge varies, the dried sludge can be properly supplied to the carbonizing furnace, thereby realizing stable operation of the carbonizing furnace. It aims at providing the sludge supply apparatus to a carbonization furnace.

発明者等は、炭化炉の安定操業が、これに供給される乾燥汚泥中の固形分を常に一定にすることによって達成されることを見いだした。本発明はこのような知見に基づいてなされたもので、汚泥乾燥炉(3)に対して脱水汚泥(WS1)を定量供給する定量供給装置(21)を設けるとともに、汚泥乾燥炉(3)と炭化炉(7)の間には当該炭化炉(7)に気密的に連結された中継ホッパ(5)を設け、中継ホッパ(5)には汚泥乾燥炉(3)から供給されて当該中継ホッパ(5)内に貯留された乾燥汚泥(WS2)の重量を検出する重量検出器(51)を設けるとともに、中継ホッパ(5)の出口側には当該中継ホッパ(5)内の乾燥汚泥(WS2)を炭化炉(7)へ供給するための切出し装置(52)を設け、かつ上記検出される汚泥重量が常に一定になるように切出し装置(52)の切出し量を制御する制御装置(6)を設ける。   The inventors have found that the stable operation of the carbonization furnace can be achieved by always keeping the solid content in the dried sludge supplied thereto constant. The present invention has been made on the basis of such knowledge, and provided with a quantitative supply device (21) for quantitatively supplying dewatered sludge (WS1) to the sludge drying furnace (3), and the sludge drying furnace (3), A relay hopper (5) airtightly connected to the carbonization furnace (7) is provided between the carbonization furnaces (7), and the relay hopper (5) is supplied from the sludge drying furnace (3) and is connected to the relay hopper (5). (5) A weight detector (51) for detecting the weight of the dried sludge (WS2) stored therein is provided, and the dried sludge (WS2) in the relay hopper (5) is provided at the outlet side of the relay hopper (5). ) Is supplied to the carbonization furnace (7), and a control device (6) for controlling the cutting amount of the cutting device (52) so that the detected sludge weight is always constant. Is provided.

本発明において、汚泥乾燥炉へは定量供給装置によって単位時間当たり定容量の脱水汚泥が供給されている。汚泥は固形分と水分よりなるものであり、脱水汚泥は一定含水率であるから汚泥乾燥炉へは単位時間当たり定重量の固形分が供給される。汚泥乾燥炉内では水分のみが蒸発させられるから、含水率が変動しても、汚泥乾燥炉から排出される単位時間当たりの乾燥汚泥に含まれる固形分は常に一定である。したがって中継ホッパに供給される乾燥汚泥量(重量)と同じ量だけ切出し装置で切り出して炭化炉へ供給すれば、炭化炉内へ供給される乾燥汚泥中の固形分は単位時間当たり常に一定量となり、炭化炉の安定的な操業が実現される。   In the present invention, a fixed volume of dewatered sludge is supplied to the sludge drying furnace per unit time by a fixed supply device. Sludge consists of solids and moisture, and dehydrated sludge has a constant moisture content, so that a constant weight of solids per unit time is supplied to the sludge drying furnace. Since only moisture is evaporated in the sludge drying furnace, the solid content contained in the dried sludge per unit time discharged from the sludge drying furnace is always constant even if the moisture content fluctuates. Therefore, if the amount of dry sludge (weight) supplied to the relay hopper is cut out by the cutting device and supplied to the carbonization furnace, the solid content in the dry sludge supplied to the carbonization furnace is always a constant amount per unit time. Stable operation of the carbonization furnace is realized.

なお、上記カッコ内の符号は、後述する実施形態に記載の具体的手段との対応関係を示すものである。   In addition, the code | symbol in the said parenthesis shows the correspondence with the specific means as described in embodiment mentioned later.

以上のように、本発明の炭化炉への汚泥供給装置によれば、乾燥汚泥の含水率が変動しても炭化炉への乾燥汚泥の供給を適正に行うことができ、炭化炉の安定操業が実現できる。   As described above, according to the sludge supply device to the carbonization furnace of the present invention, even if the moisture content of the dry sludge varies, the dry sludge can be properly supplied to the carbonization furnace, and the stable operation of the carbonization furnace can be achieved. Can be realized.

図1には本発明の方法を適用する汚泥炭化設備の系統図を示す。図1において、受入ホッパ1には含水率80%程度に脱水された脱水汚泥WS1が投入される。脱水汚泥WS1は受入ホッパ1からコンベア11,12によって定量供給装置21へ供給され、これを経て汚泥乾燥炉3へ供給される。汚泥乾燥炉3では熱風炉4から供給される熱風によって加熱されて脱水汚泥WS1は含水率35%〜45%の乾燥汚泥WS2となる。乾燥汚泥WS2はコンベア31,32で中継ホッパ5へ搬送されてこれに供給される。中継ホッパ5にはロードセル等の重量検出器51が付設されており、その検出信号51aがコントローラ6へ入力している。中継ホッパ5内の乾燥汚泥WS2はその出口側に設けた定容積式のスクリューコンベア52で切り出されて、炭化炉7内へ供給される。炭化炉7のレトルト内を通過する間に乾留され炭化された汚泥CSは、冷却機71を経てコンベア71,72により出口側の貯留ホッパ73へ供給される。なお、負圧となった炭化炉7内への外気の侵入を防止するために、炭化炉7の入口側とスクリューコンベア52を設けた中継ホッパ5の出口側とは実際には気密的に連結されている。   FIG. 1 shows a system diagram of a sludge carbonization facility to which the method of the present invention is applied. In FIG. 1, a dewatered sludge WS1 dehydrated to a moisture content of about 80% is charged into a receiving hopper 1. The dewatered sludge WS1 is supplied from the receiving hopper 1 to the fixed supply device 21 by the conveyors 11 and 12, and is supplied to the sludge drying furnace 3 through this. In the sludge drying furnace 3, it is heated by the hot air supplied from the hot air furnace 4, and the dewatered sludge WS1 becomes a dry sludge WS2 having a moisture content of 35% to 45%. The dried sludge WS2 is conveyed to the relay hopper 5 by the conveyors 31 and 32 and supplied thereto. The relay hopper 5 is provided with a weight detector 51 such as a load cell, and the detection signal 51 a is input to the controller 6. The dried sludge WS2 in the relay hopper 5 is cut out by a constant displacement screw conveyor 52 provided on the outlet side and supplied into the carbonization furnace 7. The sludge CS carbonized and carbonized while passing through the retort of the carbonization furnace 7 is supplied to the storage hopper 73 on the outlet side by the conveyors 71 and 72 through the cooler 71. In order to prevent the outside air from entering the carbonization furnace 7 having a negative pressure, the inlet side of the carbonization furnace 7 and the outlet side of the relay hopper 5 provided with the screw conveyor 52 are actually connected in an airtight manner. Has been.

ここで、本実施形態ではスクリューコンベア52の回転数がコントローラ6の出力信号6aによって制御されている。すなわち、コントローラ6は重量検出器51からの検出信号51aによって中継ホッパ5内の乾燥汚泥WS2の貯留量(重量)を知り、当該貯留量が一定値となるようにスクリューコンベア52の回転数、すなわち切り出し量を制御する。これにより、中継ホッパ5内の乾燥汚泥WS2は、これへの供給分(重量)だけ切り出し排出されることになる。   Here, in this embodiment, the rotation speed of the screw conveyor 52 is controlled by the output signal 6 a of the controller 6. That is, the controller 6 knows the storage amount (weight) of the dried sludge WS2 in the relay hopper 5 from the detection signal 51a from the weight detector 51, and the rotation speed of the screw conveyor 52 so that the storage amount becomes a constant value, that is, Control the amount of clipping. As a result, the dried sludge WS2 in the relay hopper 5 is cut out and discharged by the amount supplied (weight).

ところで、汚泥乾燥炉3へはほぼ一定含水率の脱水汚泥WS1が、モーノポンプ等の定量供給装置21によって単位時間当たり定容量で供給されている。汚泥は固形分と水分よりなるものであり、脱水汚泥WS1は一定含水率であるから汚泥乾燥炉3へは単位時間当たり定重量の固形分が供給される。   By the way, the dewatered sludge WS1 having a substantially constant water content is supplied to the sludge drying furnace 3 at a constant capacity per unit time by a constant supply device 21 such as a Mono pump. The sludge is composed of solids and moisture, and the dehydrated sludge WS1 has a constant water content, so that a constant weight of solids per unit time is supplied to the sludge drying furnace 3.

汚泥乾燥炉3内では水分のみが蒸発させられるから、含水率が35%〜45%と変動しても、汚泥乾燥炉3から排出される単位時間当たりの乾燥汚泥WS2に含まれる固形分は常に一定である。したがって、中継ホッパ5に供給される乾燥汚泥量(重量)と同じ量だけスクリューコンベア52で切り出して炭化炉7へ供給すれば、炭化炉7内へ供給される乾燥汚泥WS2中の固形分は単位時間当たり常に一定量となり、炭化行程が良好に遂行される。   Since only moisture is evaporated in the sludge drying furnace 3, even if the moisture content fluctuates from 35% to 45%, the solid content contained in the dried sludge WS2 per unit time discharged from the sludge drying furnace 3 is always constant. It is constant. Therefore, if the amount of dry sludge supplied to the relay hopper 5 (weight) is cut out by the screw conveyor 52 and supplied to the carbonization furnace 7, the solid content in the dry sludge WS2 supplied into the carbonization furnace 7 is a unit. The amount is always constant per hour, and the carbonization process is performed well.

本発明の一実施形態を示す汚泥供給装置の系統図である。It is a systematic diagram of the sludge supply apparatus which shows one Embodiment of this invention.

符号の説明Explanation of symbols

21…定量供給装置、3…汚泥乾燥炉、5…中継ホッパ、51…ロードセル(重量検出器)、52…スクリューコンベア(切出し装置)、6…コントローラ(制御装置)、7…炭化炉、WS2…乾燥汚泥、WS1…脱水汚泥。 DESCRIPTION OF SYMBOLS 21 ... Fixed quantity supply apparatus, 3 ... Sludge drying furnace, 5 ... Relay hopper, 51 ... Load cell (weight detector), 52 ... Screw conveyor (cutting device), 6 ... Controller (control apparatus), 7 ... Carbonization furnace, WS2 ... Dry sludge, WS1 ... dehydrated sludge.

Claims (1)

汚泥乾燥炉に対して脱水汚泥を定量供給する定量供給装置を設けるとともに、前記汚泥乾燥炉と炭化炉の間には当該炭化炉に気密的に連結された中継ホッパを設け、前記中継ホッパには前記汚泥乾燥炉から供給されて当該中継ホッパ内に貯留された乾燥汚泥の重量を検出する重量検出器を設けるとともに、前記中継ホッパの出口側には当該中継ホッパ内の乾燥汚泥を前記炭化炉へ供給するための切出し装置を設け、かつ前記検出される汚泥重量が常に一定になるように前記切出し装置の切出し量を制御する制御装置を設けたことを特徴とする炭化炉への汚泥供給装置。 A fixed amount supply device for supplying dehydrated sludge to the sludge drying furnace is provided, and a relay hopper that is airtightly connected to the carbonization furnace is provided between the sludge drying furnace and the carbonization furnace. A weight detector for detecting the weight of the dried sludge supplied from the sludge drying furnace and stored in the relay hopper is provided, and the dried sludge in the relay hopper is supplied to the carbonization furnace on the outlet side of the relay hopper. A sludge supply apparatus for a carbonization furnace, characterized in that a cut-out apparatus for supply is provided, and a control device for controlling a cut-out amount of the cut-out apparatus so that the detected sludge weight is always constant.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101864322A (en) * 2010-05-26 2010-10-20 东北电力大学 Dry-type decoking method of oil shale gas retort with screw conveying structure
KR101029482B1 (en) 2008-10-10 2011-04-18 엘에스니꼬동제련 주식회사 Silver Crystal Treatment Automation Apparatus
JP2017087126A (en) * 2015-11-09 2017-05-25 大同特殊鋼株式会社 Carbonization facility of sludge
CN114593853A (en) * 2022-03-14 2022-06-07 苏州西热节能环保技术有限公司 Online monitoring device for output of sludge drying system, checking method of online monitoring device and storage medium

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5756098A (en) * 1980-09-22 1982-04-03 Tsukishima Kikai Co Ltd Method for making fuel from organic sludge
JPH046309A (en) * 1990-04-23 1992-01-10 Jgc Corp Incineration and melting processing device
JPH078936A (en) * 1993-04-13 1995-01-13 Nakayasu:Kk Method and apparatus for carbonizing organic waste
JPH11309490A (en) * 1998-04-28 1999-11-09 Nkk Corp Sludge treatment and equipment therefor
JP2001279264A (en) * 2000-03-29 2001-10-10 Toshiba Corp Thermal cracking furnace unit
JP2002066598A (en) * 2000-08-30 2002-03-05 Meidensha Corp Method and facility for heating object to be treated, which contains water
JP2004008917A (en) * 2002-06-06 2004-01-15 Meidensha Corp Heating treatment method for sludge and facilities therefor
JP2004114004A (en) * 2002-09-30 2004-04-15 Meidensha Corp Sludge transfer system and sludge heat treatment facility
JP2004283784A (en) * 2003-03-25 2004-10-14 Meidensha Corp Heat treatment method for sludge and its facility
JP2006055743A (en) * 2004-08-19 2006-03-02 Daido Steel Co Ltd Control method for water content in dried sludge from sludge drying furnace

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5756098A (en) * 1980-09-22 1982-04-03 Tsukishima Kikai Co Ltd Method for making fuel from organic sludge
JPH046309A (en) * 1990-04-23 1992-01-10 Jgc Corp Incineration and melting processing device
JPH078936A (en) * 1993-04-13 1995-01-13 Nakayasu:Kk Method and apparatus for carbonizing organic waste
JPH11309490A (en) * 1998-04-28 1999-11-09 Nkk Corp Sludge treatment and equipment therefor
JP2001279264A (en) * 2000-03-29 2001-10-10 Toshiba Corp Thermal cracking furnace unit
JP2002066598A (en) * 2000-08-30 2002-03-05 Meidensha Corp Method and facility for heating object to be treated, which contains water
JP2004008917A (en) * 2002-06-06 2004-01-15 Meidensha Corp Heating treatment method for sludge and facilities therefor
JP2004114004A (en) * 2002-09-30 2004-04-15 Meidensha Corp Sludge transfer system and sludge heat treatment facility
JP2004283784A (en) * 2003-03-25 2004-10-14 Meidensha Corp Heat treatment method for sludge and its facility
JP2006055743A (en) * 2004-08-19 2006-03-02 Daido Steel Co Ltd Control method for water content in dried sludge from sludge drying furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101029482B1 (en) 2008-10-10 2011-04-18 엘에스니꼬동제련 주식회사 Silver Crystal Treatment Automation Apparatus
CN101864322A (en) * 2010-05-26 2010-10-20 东北电力大学 Dry-type decoking method of oil shale gas retort with screw conveying structure
JP2017087126A (en) * 2015-11-09 2017-05-25 大同特殊鋼株式会社 Carbonization facility of sludge
CN114593853A (en) * 2022-03-14 2022-06-07 苏州西热节能环保技术有限公司 Online monitoring device for output of sludge drying system, checking method of online monitoring device and storage medium
CN114593853B (en) * 2022-03-14 2024-04-09 苏州西热节能环保技术有限公司 Online monitoring device for sludge drying system output, checking method thereof and storage medium

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