JPH0771676B2 - Pumping method of dehydrated sludge in sludge treatment equipment - Google Patents
Pumping method of dehydrated sludge in sludge treatment equipmentInfo
- Publication number
- JPH0771676B2 JPH0771676B2 JP1067946A JP6794689A JPH0771676B2 JP H0771676 B2 JPH0771676 B2 JP H0771676B2 JP 1067946 A JP1067946 A JP 1067946A JP 6794689 A JP6794689 A JP 6794689A JP H0771676 B2 JPH0771676 B2 JP H0771676B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- dehydrated
- pumping
- dehydrated sludge
- protein
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000010802 sludge Substances 0.000 title claims description 68
- 238000005086 pumping Methods 0.000 title claims description 16
- 238000000034 method Methods 0.000 title claims description 10
- 102000004169 proteins and genes Human genes 0.000 claims description 16
- 108090000623 proteins and genes Proteins 0.000 claims description 16
- 239000010801 sewage sludge Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 description 19
- 239000002918 waste heat Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 208000005156 Dehydration Diseases 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000000017 hydrogel Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は、下水処理場のような汚泥処理設備から発生す
る下水汚泥を脱水した主成分が蛋白質である脱水汚泥
(脱水ケーキ)を、焼却設備等の次工程へ移送するため
に用いられる汚泥処理設備における脱水汚泥の圧送方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention incinerates dehydrated sludge (dehydrated cake) whose main component is protein, which is obtained by dehydrating sewage sludge generated from a sludge treatment facility such as a sewage treatment plant. The present invention relates to a method for pumping dewatered sludge in a sludge treatment facility used to transfer it to the next process such as equipment.
(従来の技術) 下水処理場等においては、流入する汚泥を活性汚泥処理
したのち、発生した余剰汚泥、初沈汚泥、混合生汚泥等
を脱水し、脱水により得られた脱水汚泥(脱水ケーキ)
をコンベヤ等で焼却炉等の焼却設備まで移送して焼却
し、焼却灰として処分することが行われている。ところ
が脱水ケーキをコンベヤで移送すると途中で脱水ケーキ
の一部が飛散、落下して環境を悪化させるおそれがある
うえ、コンベヤは密閉構造ではないために臭気対策が必
要である等の欠点があった。(Prior art) In a sewage treatment plant, etc., after inflowing sludge is treated with activated sludge, dehydrated sludge (dehydrated cake) obtained by dewatering excess sludge, initial sludge, mixed raw sludge, etc.
It is carried out by transferring it to an incinerator such as an incinerator by a conveyor or the like, incinerating it, and disposing as incinerated ash. However, when the dehydrated cake was transferred by a conveyor, some of the dehydrated cake might be scattered and dropped on the way to worsen the environment, and the conveyor had not a closed structure, so odor countermeasures were necessary. .
このため、脱水汚泥をポンプによって焼却設備まで圧送
するポンプ圧送方法が検討されているが、脱水汚泥は粘
性は高いうえに汚泥脱水処理設備と焼却設備との間は数
十〜数百mも離れているのが普通であるため、汚泥圧送
用の配管内の圧力損失が極めて大きくなり、ポンプ部品
のロータやステータの負荷が過大となり摩耗や破損によ
る故障を生じ易いという問題があった。For this reason, a pumping method for pumping the dehydrated sludge to the incinerator by a pump has been studied. However, the dehydrated sludge has a high viscosity, and the sludge dewatering treatment facility and the incinerator are separated by several tens to several hundred meters. However, there is a problem in that the pressure loss in the sludge pumping pipe becomes extremely large, and the load on the rotor and the stator of the pump component becomes excessively large, which easily causes a failure due to wear or damage.
(発明が解決しようとする課題) 本発明はこのような従来の問題点を解決して、下水汚泥
を脱水することにより得られた高粘性の脱水汚泥を円滑
に焼却設備等の次工程までポンプにより圧送することが
できる汚泥処理設備における脱水汚泥の圧送方法を目的
として完成されたものである。(Problems to be Solved by the Invention) The present invention solves such conventional problems and smoothly pumps highly viscous dewatered sludge obtained by dewatering sewage sludge to the next step such as incineration equipment. It was completed for the purpose of the method of pumping dewatered sludge in a sludge treatment facility that can be pumped by.
(課題を解決するための手段) 上記の課題は、汚泥処理設備から発生する下水汚泥等を
脱水した主成分が蛋白質である高粘性の脱水汚泥をポン
プにより次工程へ圧送する際に、圧送される前記脱水汚
泥を90℃以下の温度に加温することにより蛋白質を変質
させ、配管内の圧力損失を低下させつつ圧送することを
特徴とする汚泥処理設備における脱水汚泥の圧送方法に
よって解決することができる。(Means for Solving the Problem) The above-mentioned problem is pressure-fed when pumping a highly viscous dewatered sludge whose main component is protein, which is obtained by dehydrating sewage sludge generated from sludge treatment equipment, to the next process. A method of pumping dehydrated sludge in a sludge treatment facility, characterized in that the dehydrated sludge is heated to a temperature of 90 ° C. or lower to modify the protein and pressure-fed while reducing the pressure loss in the pipe. You can
(実施例) 次に本発明を図面を参照しつつ更に詳細に説明すると、
第1図において(1)は汚泥処理設備から発生した下水
汚泥を脱水することにより得られた主成分が蛋白質であ
る脱水汚泥を貯留する汚泥貯留槽、(2)は数十m〜数
百m離れた場所に設けられている焼却炉のような焼却設
備である。(3)は汚泥貯留槽(1)から脱水汚泥を焼
却設備(2)まで圧送するためのポンプ、(4)は汚泥
圧送用の配管である。ポンプ(3)としては回転容積型
の一軸偏心ねじポンプを使用することが好ましい。この
型式のポンプは断面が真円のねじ状のロータを断面が長
円形のステータの内部で回転させることにより連続的に
汚泥の圧送を行わせることができるものである。(Example) Next, the present invention will be described in more detail with reference to the drawings.
In FIG. 1, (1) is a sludge storage tank for storing dehydrated sludge whose main component is protein obtained by dehydrating sewage sludge generated from sludge treatment equipment, and (2) is several tens to several hundreds of meters. It is an incinerator such as an incinerator installed at a remote place. (3) is a pump for pumping the dehydrated sludge from the sludge storage tank (1) to the incinerator (2), and (4) is a pipe for pumping sludge. As the pump (3), it is preferable to use a rotary displacement type uniaxial eccentric screw pump. This type of pump is capable of continuously pumping sludge by rotating a screw-shaped rotor having a perfect circular cross section inside a stator having an oval cross section.
本実施例では、汚泥貯留槽(1)とポンプ(3)との間
に脱水汚泥の加温手段(5)が設けられている。この加
温手段(5)としては例えばパドルドライヤ等が用いら
れる。脱水汚泥は大量の有機物特に蛋白質を含有してお
り、この内部を通過する間に90℃以下の温度に加温され
るので、蛋白質の変質が生ずる。すなわち蛋白質を含有
するヒドロゲルのゲル構造が熱分解され、内蔵されてい
る水分が分離するいわゆる離漿現象が発生し、粘性を低
下させるとともに冷却設備への汚泥供給を容易に行わせ
ることができる。In this embodiment, a heating means (5) for the dehydrated sludge is provided between the sludge storage tank (1) and the pump (3). For example, a paddle dryer or the like is used as the heating means (5). Dehydrated sludge contains a large amount of organic substances, especially proteins, and is heated to a temperature of 90 ° C. or less while passing through the inside thereof, so that the quality of proteins is altered. That is, the gel structure of the hydrogel containing protein is thermally decomposed, a so-called syneresis phenomenon occurs in which the water contained therein is separated, the viscosity is reduced, and the sludge can be easily supplied to the cooling equipment.
(6)は焼却設備(2)の高温の拝ガスから熱回収を行
う廃熱回収装置であり、実施例では回収された熱はスチ
ーム又は温水として廃熱循環ライン(7)を通じて加温
手段(5)へ供給される。しかし加温手段(5)の熱源
はこれに限定されるものではなく、任意の熱源を使用で
きる。(6) is a waste heat recovery device that recovers heat from the high temperature gas of the incineration facility (2). In the embodiment, the recovered heat is heated as steam or hot water through the waste heat circulation line (7) for heating means ( 5) is supplied. However, the heat source of the heating means (5) is not limited to this, and any heat source can be used.
本発明においては、ポンプ(3)から吐出された主成分
が蛋白質である脱水汚泥を焼却設備等の次工程まで導く
ための配管(4)の一部または全部に、脱水汚泥の加温
手段(9)が設けられる。前記したように主成分が蛋白
質である脱水汚泥は90℃以下の温度に加温されると離漿
現象により粘性を低下させ、焼却設備への汚泥供給を容
易に行わせることができる。なお、脱水汚泥の加温温度
が90℃を越えると有機物中の蛋白質が凝固し、配管の途
中で冷却固化されたような場合には起動時に再加温して
も流動性が回復しないこととなり、再起動が困難とな
る。このために本発明では脱水汚泥の加温温度を90℃以
下としている。In the present invention, the heating means for the dehydrated sludge (a part or the whole of the pipe (4) for guiding the dehydrated sludge whose main component is protein discharged from the pump (3) to the next step such as incineration equipment ( 9) is provided. As described above, when the dehydrated sludge whose main component is protein is heated to a temperature of 90 ° C. or lower, the viscosity decreases due to syneresis and the sludge can be easily supplied to the incinerator. If the heating temperature of the dehydrated sludge exceeds 90 ° C, the protein in the organic matter will solidify, and if it is cooled and solidified in the middle of the piping, the fluidity will not recover even if it is reheated at startup. , It becomes difficult to restart. Therefore, in the present invention, the heating temperature of the dehydrated sludge is set to 90 ° C or lower.
実施例では加温手段(9)に廃熱循環ライン(8)によ
って熱が供給され、圧送される脱水汚泥を90℃以下の温
度に維持している。この場合にも加温手段(9)の熱源
は廃熱に限定されるものではなく、電気ヒータのような
独立した熱源を使用することができるほか、脱水汚泥の
内部に直接蒸気を吹き込むようにすることもできる。な
お、加温手段(5)と加温手段(9)とはそれぞれ単独
でも、あるいは実施例のように両方を併用してもよいこ
とはいうまでもない。In the embodiment, heat is supplied to the heating means (9) through the waste heat circulation line (8), and the dehydrated sludge that is pressure-fed is maintained at a temperature of 90 ° C. or lower. Also in this case, the heat source of the heating means (9) is not limited to waste heat, an independent heat source such as an electric heater can be used, and steam can be blown directly into the dehydrated sludge. You can also do it. Needless to say, the heating means (5) and the heating means (9) may be used alone or in combination as in the embodiment.
第2図は、本発明の方法によって脱水汚泥の圧送を行っ
た場合の配管圧損の低下を示したグラフである。このデ
ータは、汚泥濃度3%の混合生汚泥に高分子凝集剤を0.
5%添加し脱水処理して得られたケーキ水分75〜80%の
脱水汚泥を90℃以下の温度に加温し、一軸偏心ねじポン
プにより口径100Aの配管を通じて1トン/Hrの流速で水
平に11m圧送した場合のデータである。FIG. 2 is a graph showing a decrease in pipe pressure loss when the dehydrated sludge is pumped by the method of the present invention. This data shows that polymer coagulant was added to mixed raw sludge with sludge concentration of 3%.
Dehydrated sludge containing 5-80% of cake water obtained by adding 5% and dehydration treatment is heated to a temperature of 90 ° C or less, and is horizontally leveled at a flow rate of 1 ton / hr through a pipe of 100A with a uniaxial eccentric screw pump. This is the data when pumping 11m.
第2図のグラフに示されるとおり、配管(4)内の圧力
損失は加温により急激に低下する。これは前記したよう
に加温により脱水汚泥の主成分である蛋白質が変質する
ためであると考えられ、脱水汚泥の圧送が極めて円滑に
行えるようになる。なお脱水汚泥の温度が90℃を越えて
も圧力損失の低下はわずかになるうえ、前記したように
配管の途中で冷却固化されたような場合の再起動が困難
となるから、加温は90℃以下の温度とする。なお、配管
圧損を数Kg/cm2以下に押さえるため、脱水汚泥の水分や
性状により異なるが、脱水汚泥の加温は40〜80℃の温度
とすることがより好ましい。また前述のように、脱水汚
泥の内部に直接蒸気を吹き込む方法によっても同様の効
果を得ることができる。As shown in the graph of FIG. 2, the pressure loss in the pipe (4) sharply drops due to heating. It is considered that this is because the protein, which is the main component of the dehydrated sludge, is deteriorated by heating as described above, and the dehydrated sludge can be pumped very smoothly. Note that even if the temperature of the dehydrated sludge exceeds 90 ° C, the decrease in pressure loss will be slight, and it will be difficult to restart when it has been cooled and solidified in the middle of the pipe as described above, so heating at 90 The temperature shall be below ℃. In order to suppress the pressure loss of the pipe to several Kg / cm 2 or less, it is more preferable to heat the dehydrated sludge at a temperature of 40 to 80 ° C., though it depends on the water content and properties of the dehydrated sludge. Further, as described above, the same effect can be obtained by directly blowing steam into the dehydrated sludge.
(作用) 本発明によれば、汚泥貯留槽(1)内の主成分が蛋白質
である脱水汚泥を加温手段(5)によって90℃以下の温
度に加温し、あるいは配管(4)の一部または全部を加
温手段(9)によって90℃以下の温度に加温しつつ、脱
水汚泥をポンプ(3)によって圧送し、数十m〜数百m
離れた焼却設備(2)において焼却処理する。脱水汚泥
は例えば焼却設備(2)の廃熱によって90℃以下の温
度、より好ましくは40〜80℃の温度に加温されているた
めに、前記したように蛋白質の変質により粘度が小さく
なり、配管(4)内の圧力損失を従来よりも大幅に低下
させることができる。この結果、ポンプ(3)の動力が
従来の70〜80%にまで低下したのみならず、ポンプ
(3)のステータとロータの寿命が従来は2000〜3000時
間と6000〜9000時間であったのを、本発明によればそれ
ぞれ4000〜6000時間と12000〜18000時間と2倍に延長す
ることができた。(Operation) According to the present invention, the dehydrated sludge whose main component is protein in the sludge storage tank (1) is heated to a temperature of 90 ° C. or lower by the heating means (5), or one of the pipes (4) While heating a part or the whole to a temperature of 90 ° C. or lower by a heating means (9), the dehydrated sludge is pressure-fed by a pump (3) to tens to hundreds of meters.
Incinerate in a separate incinerator (2). Since the dehydrated sludge is heated to a temperature of 90 ° C. or lower, more preferably 40 to 80 ° C. by the waste heat of the incineration facility (2), the viscosity becomes small due to the alteration of the protein as described above, The pressure loss in the pipe (4) can be significantly reduced as compared with the conventional case. As a result, not only was the power of the pump (3) reduced to 70-80% of the conventional one, but the life of the stator and rotor of the pump (3) was conventionally 2000-3000 hours and 6000-9000 hours. According to the present invention, it was possible to double the time by 4000 to 6000 hours and 12000 to 18000 hours, respectively.
さらに実施例のように、脱水汚泥の加温を焼却設備の廃
熱によって行うようにすれば、泥泥処理設備及び焼却設
備全体の熱効率を向上させることができる。Further, if the dehydrated sludge is heated by the waste heat of the incineration facility as in the embodiment, the thermal efficiency of the entire sludge treatment facility and the incineration facility can be improved.
(発明の効果) 本発明は以上の説明から明らかなように、主成分が蛋白
質である高粘性の脱水汚泥を低圧力で焼却設備等の次工
程へポンプ圧送することができるもので、圧力損失を低
下させ、圧送に要するポンプ動力を減少させるとともに
従来よりも長距離の圧送が可能となる。また本発明によ
ればポンプ圧送に用いられる機器類の故障を減少させる
ことができ、メンテナンスのコストも節減することがで
きるうえ、設備全体の熱効率及び稼働率の向上を図るこ
ともできる。更にまた脱水汚泥の移送経路を密封構造に
できるので、加温汚泥の防臭対策も容易となる。よって
本発明は従来の問題点を一掃したものとして、産業の発
展に寄与するところは極めて大である。(Effect of the invention) As is apparent from the above description, the present invention is capable of pumping highly viscous dewatered sludge whose main component is protein to the next process such as incineration equipment at low pressure, resulting in pressure loss. The pump power required for the pressure feeding can be reduced, and the pressure feeding can be performed over a longer distance than in the past. Further, according to the present invention, it is possible to reduce the breakdown of the devices used for pumping, reduce the maintenance cost, and improve the thermal efficiency and operating rate of the entire facility. Furthermore, since the transfer route of the dehydrated sludge can be made into a sealed structure, it becomes easy to prevent the warmed sludge from deodorizing. Therefore, the present invention is extremely large in that it contributes to the development of industry by eliminating the conventional problems.
第1図は本発明の実施例を示す配管系統図、第2図は圧
送される脱水汚泥の温度と配管内の圧力損失との関係を
示すグラフである。 (1):汚泥貯留槽、(2):焼却設備、(3):ポン
プ、(4):配管、(5):加温手段、(6):廃熱回
収装置、(7)、(8):廃熱循環ライン、(9):加
温手段FIG. 1 is a piping system diagram showing an embodiment of the present invention, and FIG. 2 is a graph showing the relationship between the temperature of the dehydrated sludge pumped and the pressure loss in the pipe. (1): Sludge storage tank, (2): Incinerator, (3): Pump, (4): Pipe, (5): Heating means, (6): Waste heat recovery device, (7), (8) ): Waste heat circulation line, (9): Heating means
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭55−72718(JP,A) 特開 昭50−37279(JP,A) 特開 昭63−224799(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-55-72718 (JP, A) JP-A-50-37279 (JP, A) JP-A-63-224799 (JP, A)
Claims (1)
水した主成分が蛋白質である高粘性の脱水汚泥をポンプ
により次工程へ圧送する際に、圧送される前記脱水汚泥
を90℃以下の温度に加温することにより蛋白質を変質さ
せ、配管内の圧力損失を低下させつつ圧送することを特
徴とする汚泥処理設備における脱水汚泥の圧送方法。1. When pumping a highly viscous dehydrated sludge, whose main component is protein, which is obtained by dehydrating sewage sludge generated from sludge treatment equipment, to the next step by pump, A method for pumping dewatered sludge in a sludge treatment facility, characterized in that the protein is denatured by being heated to a temperature, and the pressure loss in the pipe is reduced while pressure-feeding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1067946A JPH0771676B2 (en) | 1988-03-25 | 1989-03-20 | Pumping method of dehydrated sludge in sludge treatment equipment |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7223388 | 1988-03-25 | ||
| JP63-72233 | 1988-05-31 | ||
| JP1067946A JPH0771676B2 (en) | 1988-03-25 | 1989-03-20 | Pumping method of dehydrated sludge in sludge treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01315396A JPH01315396A (en) | 1989-12-20 |
| JPH0771676B2 true JPH0771676B2 (en) | 1995-08-02 |
Family
ID=26409171
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1067946A Expired - Fee Related JPH0771676B2 (en) | 1988-03-25 | 1989-03-20 | Pumping method of dehydrated sludge in sludge treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0771676B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5157052B2 (en) * | 2005-08-19 | 2013-03-06 | 住友大阪セメント株式会社 | Low moisture content sludge transportation method and equipment, and cement manufacturing facility |
| JP5027697B2 (en) * | 2008-03-13 | 2012-09-19 | メタウォーター株式会社 | Sewage sludge treatment method |
| JP5139847B2 (en) * | 2008-03-13 | 2013-02-06 | メタウォーター株式会社 | Sewage sludge treatment system |
| JP2013057498A (en) * | 2012-11-02 | 2013-03-28 | Metawater Co Ltd | Sewage sludge supply device for incinerator |
| JP7677583B2 (en) * | 2021-11-05 | 2025-05-15 | メタウォーター株式会社 | Incineration system and viscosity adjustment method for materials to be incinerated |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5037279A (en) * | 1973-08-06 | 1975-04-07 | ||
| JPS5349788U (en) * | 1976-10-01 | 1978-04-26 | ||
| JPS5572718A (en) * | 1978-11-22 | 1980-05-31 | Ube Ind Ltd | Method and apparatus for incineration of organic sludge |
| JPS59227622A (en) * | 1983-06-06 | 1984-12-20 | Mitsubishi Electric Corp | Method and device for transportation |
| JPS63224799A (en) * | 1987-03-13 | 1988-09-19 | Takashi Nakano | Dehydration of sludge or the like |
-
1989
- 1989-03-20 JP JP1067946A patent/JPH0771676B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01315396A (en) | 1989-12-20 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |