JP4002536B2 - Sludge drying method - Google Patents
Sludge drying method Download PDFInfo
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- JP4002536B2 JP4002536B2 JP2003127509A JP2003127509A JP4002536B2 JP 4002536 B2 JP4002536 B2 JP 4002536B2 JP 2003127509 A JP2003127509 A JP 2003127509A JP 2003127509 A JP2003127509 A JP 2003127509A JP 4002536 B2 JP4002536 B2 JP 4002536B2
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Description
【0001】
【発明の属する技術分野】
本発明は、排水汚泥、とくに浄水場から排出される汚泥の天日乾燥法に関する。具体的には、汚泥の凍結・融解処理を利用して汚泥の天日乾燥における高効率化を図るものである。本発明において、「生汚泥」は乾燥するために天日乾燥床に投入される凍結・融解処理の施されていない汚泥を、「凍結・融解汚泥」は前記の凍結・融解処理を施された汚泥をいう。
【0002】
【従来の技術】
通常、浄水場、排水処理場等では、取り込んだ原水中に含まれている懸濁物質等を排泥池や濃縮装置を設けて汚泥として濃縮、分離し、濃縮した汚泥を乾燥装置や脱水装置を用いてさらに共存する水を分離した後、適法に処理している。天日乾燥法は、前記の濃縮汚泥を乾燥する一手段であって、一般には、排泥池、濃縮装置などを利用して水分率が2〜5重量%程度になるまで濃縮した生汚泥を天日乾燥床に投入して静置し、上澄水およびろ過水を除去して汚泥中の水分率を低下させ、さらに天日等の自然蒸発によって汚泥乾燥を行う方法である。搬送、利用のし易さから水分率を30〜65重量%程度まで乾燥させることが多く、汚泥の濃縮、脱水工程における最終工程として位置づけられている。このようにして乾燥された汚泥は園芸用土等に有効利用することができる。天日乾燥法は、排泥の頻度が少なく、立地、気象条件が適し用地の確保が容易な場合、他の脱水法に比較して設備及び操業コストが小さく、維持管理が容易な優れた方法である。
【0003】
図1は天日乾燥床の一例を示す平面図、図2は図1に記載したA部の垂直方向断面図である。天日乾燥床は、上面を開放したプール状のコンクリート枠体1内部を適宜の広さの乾燥床2に区切って形成されており、それぞれの乾燥床の底部3にはろ過水を集めて導出するための集水主管4及び必要によっては集水支管5が設られている。乾燥床2にはろ材として砂利、採石等(4号程度の大きさが一般的、大きさの異なる砂利を複数の層に重ねることもある)を敷き、その上に川砂等を敷き詰める。汚泥8はろ材7の表面から150cm程度まで投入する。汚泥投入後はそのまま固形分を沈降させ、上澄水は角落とし(溢流堰の一種、上下にスライドし液高を調整できる)9により上澄水取出口10を通って抜き出される。ろ過水は集水管5、4を経て上澄水とともに排水の排出口6から乾燥床外に導出される。残る汚泥は、自然乾燥されてろ材上、数十cm程度の乾燥汚泥になる。乾燥汚泥はシャベル等機械的に乾燥床から取り出し、粉砕して例えば園芸用土や埋土として利用する。ろ過水や上澄水は原水の取水口の返送されるか、適法に処理して河川等に放流される。
【0004】
【発明が解決しようとする課題】
ところで天日乾燥法には、設備や操業のためのコストが小さいという利点がある反面、弱点は乾燥に時間がかかり大きな敷地を必要とすることである。通常、生汚泥は、ろ過性が悪く、とくに冬場にその傾向が顕著であり、1回の乾燥に6〜10か月を要する場合がある。また、乾燥汚泥は、厚さが数十cmになるので天日乾燥汚泥を園芸培養土等に有効利用するためには、これを天日乾燥床から取り出し、2〜5cm程度の粒子に粉砕する必要がある。しかし、一般に天日乾燥汚泥の塊は硬く粉砕しにくいという問題がある。前記したこれらの課題を解決して効率のよい天日乾燥法と粉砕しやすい乾燥汚泥を取得するために研究を重ねた結果、本発明を完成するに至ったものである。
【0005】
【課題を解決するための手段】
前記の課題を解決する手段として本発明は、天日乾燥する生汚泥に、凍結・融解処理を施した汚泥を混合して天日乾燥床に投入し、乾燥することを特徴とする汚泥の天日乾燥法を提供する。さらに、本発明は、凍結・融解処理を施した汚泥と生汚泥とを少なくとも1層づつ、交互に天日乾燥床に投入することを特徴とする汚泥の天日乾燥法を提供する。前記の天日乾燥法においては、天日乾燥床に投入する汚泥中の凍結・融解汚泥の比率は、30〜100重量%の範囲に調整することが好ましい。また、前記の凍結・融解処理を施した汚泥に替えて、汚泥を凍結・融解した後、凍結・融解汚泥を沈殿させ上澄水を分離して濃縮した凍結・融解・濃縮汚泥を用いれば、さらに効率的に天日乾燥を施すことができる。
【0006】
【発明の実施の形態】
本発明を詳しく具体的に説明する。本発明を利用して乾燥させようとする生汚泥は、有機質でも無機質でもよく、沈降分離されたままの汚泥、あるいは何らかの方法でさらに濃縮されている汚泥であってもよい。また、本発明において汚泥の水分率(重量%)は、重量W1の汚泥を105℃の熱風循環乾燥機内に入れて完全に乾燥した後、乾燥重量W2を測定し{(W1−W2)/W1}×100%を算出した。
【0007】
さて、本発明は、乾燥しようとする生汚泥に凍結・溶融処理を施した汚泥を混合し、乾燥床に投入して天日乾燥すれば、乾燥に要する日数が大幅に短縮され、かつ、乾燥汚泥が従来のように硬く固まらずに粉砕が容易になる、という効果を見出すことにより、天日乾燥法における前記の課題を解決する手段として、完成されたものである。生汚泥と凍結・乾燥汚泥とは、あらかじめ混合して投入してもよく、また、少なくとも1層ずつを交互に投入し積層てもよい。後者の場合、好ましくは凍結・融解汚泥層を最下層にする。天日乾燥床に投入する汚泥中の凍結・融解汚泥量は、扱う汚泥の特性や操業条件にもよるが、一般的に好ましくは30〜100重量%、とくに40〜80重量%の範囲が好ましい。30重量%以下では凍結・融解汚泥の混入効果が小さくなり、多すぎると凍結・融解汚泥の費用がかさみ経済的有利性が失われる。
【0008】
汚泥の凍結・融解には、例えば槽内部に伝熱管を配列した凍結・融解槽を用いる。濃縮槽等からの排泥を凍結・融解槽に投入し、伝熱管に冷媒を流して投入汚泥を凍結する。凍結条件は、装置の構造や処理する汚泥の特性、供給温度など及び予備試験や経験にもとづいて決めることが多い。一般的には伝熱管等に−10〜−30℃の冷ブラインを1〜3時間流通させて凍結させる。所定の凍結処理後に冷媒を熱媒に切り替えて凍結汚泥を融解させることによって、汚泥の凍結・融解処理を実施する。凍結・融解用の汚泥には、一般に乾燥させようとする生汚泥を使用するがそれに限られるものではない。また、凍結汚泥を融解した後、汚泥を沈降させて上澄水を系外に排出して汚泥を濃縮し、凍結・融解・濃縮汚泥にして乾燥工程での負荷を小さくしておくと効率的である。
【0009】
汚泥は、凍結時、固体中に取り込まれている水が、伝熱管冷却面に引き抜かれて氷になり固形分が凝集する。すなわち、汚泥中の水を凍結することによって汚泥がミクロ的に水から分離されて凝集し、ろ過性、脱水性が向上するとともに、乾燥後、凍結処理した汚泥は硬く固化することがなくなる。生汚泥に、凝集した凍結・融解汚泥を混用することにより、生汚泥のろ過性、脱水性は向上し、生汚泥の乾燥による固化が防止される。さらに、凍結・融解汚泥自体が、Al2O3を20〜30重量%程度含有しており、生汚泥に対し硫酸アルミニウムやポリ塩化アルミニウムと同様に凝集沈殿助剤としての効果を奏し、生汚泥の凝集を促進させる作用があるので、混用する生汚泥の特性改良に寄与したものと考えられている。
【0010】
このようにして処理された凍結・融解汚泥と生汚泥との混合汚泥は、沈殿性が向上して上澄水との分離が速く容易であるのみならず、汚泥のろ過特性が向上して脱水汚泥中の残量水分率を低下させる効果を有する。さらにろ材(ろ布)の目詰まりトラブルが減少し、また、脱水終了後の汚泥は従来の乾燥汚泥のように硬く固まっておらず容易に粉砕することができる。かつ、ろ材(ろ布)との分離も容易になる。
【0011】
【実施例】
本発明の効果を確認するため、実験用の汚泥天日乾燥床を使用して実験したので、図3及び図4を参照して説明する。図3は前記実験用汚泥乾燥床の断面図である。実験用には、鋼板製容器21の側壁及び底板を厚さ5cmの断熱材22で覆った外寸が50×50×90(深さ)の乾燥床を6基用い、いづれも底からから10cmの厚さに10〜20mmφの砂利23を、その上10cmの厚さに4〜6mmφの砂利24を、さらに5cmの厚さに1〜2mmφの砂利25を敷き、さらにその上10cmの厚さで川砂26を敷いた。また、底板にはろ過水を連続的に排出する排出口27を取り付けた。この乾燥床の処理汚泥容量は約0.125m3であった。
【0012】
一方、伝熱コイルを内蔵する容量0.6m3の冷凍・融解槽(不図示)に、生汚泥約0.6m3を投入して伝熱コイルに−20℃の冷媒を100分間流して汚泥を凍結させた後、冷媒を30℃の熱媒に切り替えて90分間流し凍結汚泥を融解して凍結・融解汚泥とした。
【0013】
前記の実験用汚泥乾燥床に、全体の汚泥量100重量部に対し、それぞれ凍結・融解汚泥をイ:0、ロ:20、ハ:40、ニ:60、ホ:80、ヘ:100各重量部、残部を生汚泥とする6種類の混合汚泥28を0.125m3づつ調合し、各乾燥床に投入した。投入汚泥の水分はいずれも96重量%であった。底部のろ過水排出口は常時開放し、上澄水は2日に1回、汚泥表面まで排出させた。汚泥/上澄水の界面高さの経日変化を約60日後の含有水分率とともに図4に示す。また、得られた乾燥汚泥のうちハ〜ヘは、塊を指で強く押さえると容易に崩れる程度の硬さであった。
【0014】
【発明の効果】
本発明を利用し、原汚泥に凍結・融解あるいは凍結・融解・濃縮された汚泥を添加して天日乾燥することによって、天日乾燥に要する日数を短縮することができる。天日乾燥床の処理効率が向上し、機械脱水量を低減して排水処理コスト下げる効果がある。また、前記の本発明に係る天日乾燥汚泥は、従来の天日乾燥汚泥のように硬く固まらないので粉砕しやすく、容易に2mmφ程度にまで粉砕できるので、園芸用土等として有効に利用しやすい。
【図面の簡単な説明】
【図1】 天日乾燥床の一例を示す平面図、
【図2】 図1に記載したA部の垂直方向断面図
【図3】 実験用汚泥乾燥床の断面図
【図4】 実施例の結果(凍結・融解汚泥の混合比をパラメータとする、汚泥/上澄水の界面高さの経日変化、及び汚泥水分率)を示したグラフ
【符号の説明】
1:上面を開放したプール状のコンクリート枠体
2:乾燥床 3:乾燥床底
4:ろ過水を床外に排出するための集水主管
5:同前集水支管 6:上澄水、ろ過水排出口
7:ろ材(砂利、採石等) 8:川砂等
9:汚泥 10:角落とし
11:上澄水取出口 12:仕切溝
21:鋼板製容器 22:断熱材
23:10〜20mmφの砂利 24:4〜6mmφの砂利
25:1〜2mmφの砂利 26:川砂
27:上澄水及びろ過水の排出口 28:調合汚泥[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a sun drying method for wastewater sludge, particularly sludge discharged from a water purification plant. Specifically, the sludge freezing and thawing process is used to increase the efficiency of sludge drying in the sun. In the present invention, “raw sludge” is sludge that has been subjected to freezing / thawing treatment that is put into a sun-dried bed for drying, and “freezing / thawing sludge” is subjected to the above-described freezing / thawing treatment. It refers to sludge.
[0002]
[Prior art]
Usually, in water purification plants, wastewater treatment plants, etc., suspended substances contained in the taken raw water are concentrated and separated as sludge by installing a drainage pond or concentrating device, and the concentrated sludge is dried or dehydrated. After separating the coexisting water using, it is treated legally. The sun drying method is a means for drying the concentrated sludge, and generally, the raw sludge concentrated until the moisture content becomes about 2 to 5% by weight using a drainage pond, a concentrating device, or the like. This is a method in which the slurry is put into a sun-dried bed and allowed to stand, and the supernatant water and filtered water are removed to reduce the moisture content in the sludge, and further sludge drying is performed by natural evaporation such as sun. In many cases, the moisture content is dried to about 30 to 65% by weight for ease of transportation and use, and it is positioned as the final step in the sludge concentration and dehydration step. The sludge dried in this way can be effectively used as horticultural soil. The solar drying method is an excellent method that requires less equipment and operation costs and is easy to maintain and maintain compared to other dehydration methods when the frequency of waste mud is low, the location and weather conditions are suitable, and the site is easy to secure. It is.
[0003]
FIG. 1 is a plan view showing an example of a sun-drying bed, and FIG. 2 is a vertical sectional view of a portion A shown in FIG. The sun-dried floor is formed by dividing the inside of a pool-shaped concrete frame 1 with an open upper surface into
[0004]
[Problems to be solved by the invention]
By the way, the sun drying method has the advantage that the cost for equipment and operation is small, but the weak point is that it takes time to dry and requires a large site. Normally, raw sludge has poor filterability, and its tendency is particularly remarkable in winter, and it may take 6 to 10 months for one drying. In addition, since the dried sludge has a thickness of several tens of centimeters, in order to effectively use the sun-dried sludge as horticultural culture soil, etc., it is taken out from the sun-dried bed and crushed into particles of about 2 to 5 cm. There is a need. However, the sun-dried sludge mass is generally hard and difficult to grind. The present invention has been completed as a result of repeated studies to solve the above-mentioned problems and to obtain an efficient sun drying method and a dry sludge that can be easily pulverized.
[0005]
[Means for Solving the Problems]
As a means for solving the above-mentioned problems, the present invention provides a sludge ceiling characterized by mixing raw sludge to be sun-dried with sludge that has been subjected to freezing and thawing treatment, putting it into a sun-drying bed, and drying it. Provide sun drying method. Furthermore, the present invention provides a sun drying method for sludge, characterized in that at least one layer of frozen and thawed sludge and raw sludge are alternately put into a sun drying bed. In the above-mentioned sun drying method, the ratio of the frozen / thawed sludge in the sludge to be put into the sun drying bed is preferably adjusted to a range of 30 to 100% by weight. In addition, if the frozen / thawed / concentrated sludge is used after the frozen / thawed sludge is frozen / thawed, the frozen / thawed sludge is precipitated and the supernatant water is separated and concentrated. Sun drying can be performed efficiently.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
The present invention will be described in detail and specifically. The raw sludge to be dried using the present invention may be organic or inorganic, and may be sludge that has been separated by settling, or sludge that has been further concentrated by some method. The water content of the sludge in the present invention (wt%), after completely dried for sludge weight W 1 in a hot air circulating dryer at 105 ° C., a dry weight W 2 was measured {(W 1 -W 2 ) / W 1 } × 100% was calculated.
[0007]
Now, in the present invention, if the raw sludge to be dried is mixed with the sludge that has been subjected to freezing and melting treatment, and put into a dry bed and sun-dried, the number of days required for drying is greatly reduced, and drying is performed. By finding the effect that the sludge does not harden and harden as in the prior art, it can be easily pulverized. Thus, the present invention has been completed as a means for solving the above-mentioned problems in the sun drying method. Raw sludge and frozen / dried sludge may be mixed and charged in advance, or at least one layer may be alternately charged and stacked. In the latter case, the frozen / thawed sludge layer is preferably the lowest layer. The amount of frozen / thawed sludge in the sludge to be put into the sun-dried bed is generally preferably 30 to 100% by weight, particularly preferably 40 to 80% by weight, although it depends on the characteristics and operating conditions of the sludge to be handled. . If it is 30% by weight or less, the effect of freezing / thawing sludge becomes small, and if it is too much, the cost of freezing / thawing sludge increases and the economic advantage is lost.
[0008]
For freezing / thawing of sludge, for example, a freezing / thawing tank in which heat transfer tubes are arranged inside the tank is used. The sludge from the concentrating tank is put into the freezing / thawing tank, and the introduced sludge is frozen by flowing the refrigerant through the heat transfer tube. Freezing conditions are often determined based on the structure of the apparatus, the characteristics of the sludge to be treated, the supply temperature, etc., and preliminary tests and experience. In general, cold brine at −10 to −30 ° C. is passed through a heat transfer tube or the like for 1 to 3 hours and frozen. The sludge is frozen and thawed by switching the refrigerant to a heat medium after the predetermined freezing treatment to melt the frozen sludge. The sludge for freezing and thawing generally uses raw sludge to be dried, but is not limited thereto. It is also effective to melt the frozen sludge, set the sludge, discharge the supernatant water out of the system, concentrate the sludge, freeze / thaw / concentrate sludge, and reduce the load in the drying process. is there.
[0009]
When the sludge is frozen, the water taken into the solid is drawn out to the cooling surface of the heat transfer tube and becomes ice, and the solids agglomerate. That is, by freezing the water in the sludge, the sludge is microscopically separated from the water and agglomerates to improve filterability and dewaterability, and after drying, the frozen sludge is not hardened and solidified. By mixing aggregated frozen / melted sludge with raw sludge, the filterability and dewaterability of raw sludge are improved, and solidification due to drying of raw sludge is prevented. Furthermore, the frozen / thawed sludge itself contains about 20 to 30% by weight of Al 2 O 3 , and has the same effect as a coagulation precipitation aid on the raw sludge in the same manner as aluminum sulfate and polyaluminum chloride. It is thought that it contributed to the improvement of the characteristics of the mixed raw sludge.
[0010]
The mixed sludge of frozen / thawed sludge and raw sludge treated in this way is not only improved in sedimentation and fast and easy to separate from the supernatant water, but also improved in sludge filtration characteristics and dehydrated sludge. It has the effect of reducing the residual moisture content. Further, the trouble of clogging of the filter medium (filter cloth) is reduced, and the sludge after dehydration is not hardened unlike conventional dry sludge and can be easily pulverized. In addition, separation from the filter medium (filter cloth) becomes easy.
[0011]
【Example】
In order to confirm the effect of this invention, it experimented using the experimental sludge sun drying bed, and it demonstrates with reference to FIG.3 and FIG.4. FIG. 3 is a sectional view of the experimental sludge drying bed. For the experiment, six dry floors with outer dimensions of 50 × 50 × 90 (depth), in which the side wall and bottom plate of the
[0012]
On the other hand, about 0.6 m 3 of raw sludge is put into a 0.6 m 3 freezing / melting tank (not shown) with a built-in heat transfer coil, and a -20 ° C refrigerant flows through the heat transfer coil for 100 minutes. After freezing, the refrigerant was switched to a heating medium at 30 ° C. and flowed for 90 minutes to melt the frozen sludge to obtain frozen / thawed sludge.
[0013]
In the above experimental sludge drying bed, freezing and thawing sludge is respectively 0: 1, 2), 20: 40,
[0014]
【The invention's effect】
Utilizing the present invention, the number of days required for sun-drying can be shortened by adding sun sludge frozen / thawed or frozen / thawed / concentrated to the raw sludge and sun-drying. The treatment efficiency of the sun-drying bed is improved, and the amount of mechanical dewatering is reduced, and the wastewater treatment cost is reduced. In addition, the sun-dried sludge according to the present invention is not hard and hardened like the conventional sun-dried sludge, so it can be easily pulverized and easily pulverized to about 2 mmφ, so that it can be effectively used as horticultural soil. .
[Brief description of the drawings]
FIG. 1 is a plan view showing an example of a sun-drying bed,
2 is a vertical cross-sectional view of part A shown in FIG. 1. FIG. 3 is a cross-sectional view of an experimental sludge drying bed. FIG. 4 is a result of an example (sludge with a mixing ratio of frozen and thawed sludge as a parameter). / Graph showing the interfacial height of the supernatant water and the sludge moisture content.
1: Pool-like concrete frame with open top surface 2: Dry floor 3: Dry floor bottom 4: Water collection main pipe for discharging filtrate out of the floor 5: The same water collection branch 6: Supernatant water, filtered water Discharge port 7: Filter medium (gravel, quarrying, etc.) 8: River sand, etc. 9: Sludge 10: Corner drop 11: Clear water outlet 12: Partition groove 21: Steel plate container 22: Insulating material 23: Gravel with 10-20 mmφ 24: 4-6mmφ gravel 25: 1-2mmφ gravel 26: River sand 27: Outlet of supernatant water and filtered water 28: Blended sludge
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003127509A JP4002536B2 (en) | 2003-05-02 | 2003-05-02 | Sludge drying method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003127509A JP4002536B2 (en) | 2003-05-02 | 2003-05-02 | Sludge drying method |
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| Publication Number | Publication Date |
|---|---|
| JP2004330031A JP2004330031A (en) | 2004-11-25 |
| JP4002536B2 true JP4002536B2 (en) | 2007-11-07 |
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| JP2003127509A Expired - Fee Related JP4002536B2 (en) | 2003-05-02 | 2003-05-02 | Sludge drying method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2014031536A (en) * | 2012-08-02 | 2014-02-20 | Hitachi Ltd | Separation recovery method and separation recovery system of rare earth element |
| CN105330119B (en) * | 2015-10-30 | 2017-11-28 | 中国科学院广州能源研究所 | A kind of method using solar energy and smoke residual heat to dry sludge |
| CN110143742A (en) * | 2019-05-10 | 2019-08-20 | 广东中绿园林集团有限公司 | A kind of river sludge processing method and processing device |
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