JP2000051898A - Film-like sludge dryer - Google Patents

Film-like sludge dryer

Info

Publication number
JP2000051898A
JP2000051898A JP10254505A JP25450598A JP2000051898A JP 2000051898 A JP2000051898 A JP 2000051898A JP 10254505 A JP10254505 A JP 10254505A JP 25450598 A JP25450598 A JP 25450598A JP 2000051898 A JP2000051898 A JP 2000051898A
Authority
JP
Japan
Prior art keywords
sludge
drying
net
dried
film
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.)
Pending
Application number
JP10254505A
Other languages
Japanese (ja)
Inventor
Takeshi Sasayama
猛 笹山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP10254505A priority Critical patent/JP2000051898A/en
Publication of JP2000051898A publication Critical patent/JP2000051898A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a dryer which requires a short drying time, can save space, can be small-sized, and gives dried products usable in a wide range by sufficiently dewatering objects to be dried attached to a net by a compression dewatering mechanism and drying the objects in the form of a film having a small drying depth. SOLUTION: A resin-made net 1 with sludge attached thereto is conveyed by many sending rollers 18 so that it goes around until the completion of drying. First, wastewater with floating sludge is supplied at a supply port 2 for materials to be treated, and sludge deposited on the meshes of a net 5 is compressed and dewatered together with the net 5 by compression rollers 4. Next, the conveying speed is controlled so that the drying is completed during the tour through a heat-generation evaporation chamber 15, and thus the drying of the sludge deposited on the net 1 is completed. Then, the dried hard sludge tightly adhering to the meshes of the net is scraped down by the swinging from side to side at a roller 10 and by the scraping with a roller brush 8. Thus, the dried sludge falls through a dried sludge take-out port 12 and is collected in a dried sludge receptacle 13.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業の利用分野】この発明は、食品加工、などで生ず
る廃棄物の処理に関わるもので、含有する肥料、あるい
は飼料としての成分を回収し、処理とともに資源の有効
活用を図る装置である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the treatment of waste generated in food processing and the like, and is an apparatus for recovering contained fertilizers or components as feed, and effectively utilizing resources together with the treatment.

【0002】[0002]

【従来の技術】廃棄物の中には、粘性が高く濾過、脱水
が困難なものが多く、かつ水分移動抵抗が大きいため乾
燥は極めて困難で、乾燥処理や焼却には多大のエネルギ
ーを必要としていた。また乾燥しても有効利用には多額
の費用を要していた。このため従来は一般に荒地などに
投棄されている所が多く、公共施設などで環境に配慮す
る所では経費を惜しまずプレスなどにより絞り脱水し、
焼却あるいはコーンポスト化し、緑農地に還元が行なわ
れていた。しかしこれらの資源活用には何れも乾燥が困
難なこと、また乾燥すると硬化し塊となって利用が困難
なため充分な乾燥を行なわず、重量のある資材として活
用を図っていた。このため貯蔵費、運搬費に意外に費用
を要し、有効利用範囲が制限され、次第に活用されない
傾向にあった。最近バクテリヤによる処理が試行されて
いるが、これらの処理には多くスペースと時間を要し、
このため活用場所は制限されている。
2. Description of the Related Art Many wastes are highly viscous and difficult to filter and dehydrate, and because of their high moisture transfer resistance, drying is extremely difficult. Therefore, a large amount of energy is required for drying and incineration. Was. Even if it dries, it costs a lot of money for effective use. For this reason, conventionally, there are many places that are generally dumped in wasteland, etc., and in places where the environment is considered in public facilities, etc.
They were incinerated or converted into cornpost and returned to green farmland. However, all of these resources are difficult to dry, and when they are dried, they harden and become a lump, making it difficult to use them. For this reason, storage costs and transportation costs are unexpectedly expensive, the effective use range is limited, and there is a tendency that the storage is not utilized gradually. Recently, bacterial treatments have been attempted, but these treatments take a lot of space and time,
For this reason, utilization places are restricted.

【0003】[0003]

【発明が解決しようとする課題】廃棄物処理は直接生産
が伴わず、投資の効果がない。このため資源の回収を図
るには少ない経費で処理出来ることが必要条件である。
これには処理や、処理後における保管、運搬による経
費節減のため、現地で発生後ただちに乾燥処理し軽量、
小容量にすること、また処理したものを整理するため
肥料、飼料として価値を高め、需要先を広げ即座に売却
出来ること。またこれらの工程において悪臭、粉塵発
生など環境面に影響を与えないこと、さらにこれらの
作業が自動的に行なわれるような簡易な設備であること
などが必要である。
SUMMARY OF THE INVENTION Waste treatment does not involve direct production and is ineffective. Therefore, in order to recover resources, it is a necessary condition that the processing can be performed with low cost.
For this purpose, to reduce the cost of processing, storage and transportation after processing, dry processing is carried out immediately after it occurs on site,
To reduce the volume, increase the value of fertilizers and feeds in order to sort out processed foods, expand demand, and sell them immediately. In addition, it is necessary that these processes do not affect the environment, such as generation of offensive odor and dust, and that the facilities be simple equipment for automatically performing these operations.

【0004】[0004]

【課題を解決するための手段】この発明は乾燥の消費エ
ネルギーを少なくするため、微小体積の圧縮脱水機構を
つくり充分な脱水を行い、また乾燥時間を短縮するため
に、乾燥表面を大きく、乾燥深さの浅いフイルム状を形
成させることを考えた。フイルム状の乾燥物を保持する
には基盤が必要になるが、これに濾過工程で必要になる
網の利用に着目した。これによれば乾燥前に欠かせない
濾過、脱水作業が自然に行なわれ、かつ期待する迅速な
乾燥装置が形成される。
According to the present invention, a small-volume compression dewatering mechanism is provided to reduce the energy consumption for drying, and sufficient dehydration is performed. To shorten the drying time, a large drying surface is used. The idea was to form a film with a shallow depth. A substrate is needed to hold the film-like dried product, and we focused on the use of a net required in the filtration process. According to this, filtration and dehydration operations which are indispensable before drying are naturally performed, and an expected quick drying device is formed.

【0005】[0005]

【作 用】水分の多い汚泥は先ず濾過が必要になる
が、粘性の高い汚泥はこの濾過工程で、網目に目詰まり
が生じ、網目を大きくすると排水が基準に適合せず、凝
縮剤の多量使用や、充分な脱水が進まずトラブルが多か
った。しかしこの発明では、むしろこの網目に浮遊物を
付着させることが必要でり、付着した浮遊物は乾燥後機
械的に落とされ、繰り返し使用するので、自然にこの問
題の解決が図られる。 汚泥を網目に付着させるため圧縮が必要になるが、こ
の工程で自然に充分な脱水が行なわれ、従来行なってい
た脱水工程が不要になる。
[Action] Sludge with a large amount of water requires filtration first, but sludge with high viscosity may cause clogging in the network during this filtration process. Use and sufficient dehydration did not progress, and there were many troubles. However, in the present invention, it is necessary to attach the suspended matter to the mesh, and the adhered suspended matter is mechanically dropped after drying and is used repeatedly, so that this problem can be solved naturally. Although compression is required to attach the sludge to the mesh, sufficient dewatering is naturally performed in this step, and the conventional dehydration step is not required.

【0006】[0006]

【実施例】以下、図面により本発明の実施例について詳
細に説明する。この実施例は食品工場の汚泥を乾燥処理
し、含有する資源の回収を図るものである。汚泥は多く
の澱粉質の滓汁と、余剰活性汚泥を混ぜたもので、大き
な固形残滓は既に除かれ、水中に浮遊する汚泥は凝縮剤
により凝縮されたものを取り入れる。したがって食堂な
どで本実施例を利用するには、この装置と別に、生ゴミ
の粉砕装置と、此処から本発明の装置間までの輸送が必
要になる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described below in detail with reference to the drawings. In this embodiment, sludge of a food factory is dried to recover contained resources. Sludge is a mixture of a large amount of starchy sap and excess activated sludge, large solid residues have already been removed, and sludge floating in water takes in what has been condensed by a condensing agent. Therefore, in order to use this embodiment in a cafeteria or the like, it is necessary to separately transport the garbage from the apparatus to the apparatus of the present invention separately from this apparatus.

【0007】1、は汚泥が付着したもの、5、は剥ぎ落
とされたので、いずれも同じエンドレスの樹脂制の網
で、多くの18、の送りローラーにより、乾燥完了にあ
わせて一巡するように送られる。2、はこ乾燥処理の原
料の供給口で、汚泥が浮遊する汚水が供給され、水は通
過し、汚泥は5、の上に懸かる。3、は懸かった汚泥を
散乱しないよう囲う枠である。汚水供給はこの滞積量を
検出して制御される。4、は圧縮ローラーで、網5、と
共に網目に堆積した汚泥を圧縮する。この場合汚泥は所
定の厚さに圧縮し1、になるが、余剰が生じた場合、
3、に滞積することになる。6、は5、により濾過され
た水、及び圧縮によって生じた水を受ける排水受けで排
水に通じる。7、は固定送りローラーで、5、を強く挟
んで規定の速度で送り、変形すること防ぐ。8、9、1
0、11、は後述のようにして、乾燥物を剥ぎ落とすロ
ーラーである。ここを通過した1、は、5、に変わる。
12、は剥ぎ落とした乾燥完了材取出し口で13、の乾
燥物受けタンクに受ける。14、は発熱体で15、の発
熱蒸発室の熱源である。16、は緊張ローラーで1、の
弛みを修正する。17は湿度検出器で1、の一巡で乾燥
完了するよう送り速度を制御する。
[0007] 1, the sludge adhered, 5 was peeled off, all are the same endless resin nets, many by 18 feed rollers to make a round when the drying is completed Sent. 2. At the feed port of the raw material for the drying of the sludge, the sewage in which the sludge floats is supplied, the water passes through, and the sludge hangs on 5. 3 is a frame that surrounds suspended sludge so as not to be scattered. Sewage supply is controlled by detecting the amount of accumulation. Reference numeral 4 denotes a compression roller for compressing sludge accumulated in the mesh together with the net 5. In this case, the sludge is compressed to a predetermined thickness and becomes 1, but if excess occurs,
3 will accumulate. 6. The drain catches the water filtered by 5, and the water generated by the compression, leading to drainage. Reference numeral 7 denotes a fixed feed roller which feeds at a specified speed while strongly sandwiching 5 to prevent deformation. 8, 9, 1
Reference numerals 0 and 11 denote rollers for peeling off the dried material as described later. 1 that passed here changes to 5.
Reference numeral 12 denotes a stripped-out dried-out material take-out port, which receives the dried-product receiving tank 13. Reference numeral 14 denotes a heating element, which is a heat source of the heat generation evaporation chamber of 15. 16. Correct the looseness of 1 with tension roller. Reference numeral 17 denotes a humidity detector which controls the feeding speed so that drying is completed in one cycle.

【0008】4、の圧縮ローラーは汚泥と、5、を共に
圧縮し、汚泥を5、に付着させるが、この場合4、の方
にも付着し、5、への付着が剥がれることがある。これ
を防止するため4、の表面速度より5、の送りを遅くす
る。これにより基盤の網5、への付着を確実にする。
5、の送りは7、により行なわれる。
[0008] The compression roller 4 compresses the sludge and 5, together, and attaches the sludge to 5, but in this case, it adheres also to 4 and the adhesion to 5 may come off. In order to prevent this, the feed of 5 is made slower than the surface speed of 4. This ensures adhesion to the substrate net 5.
The feed of 5 is performed by 7.

【0009】1、の網に付着した汚泥は硬化し、剥ぎ取
りは困難になるが、本発明の方法を第2図により述べ
る。1、に付着した汚泥は既に乾燥完了している。9、
11、は固定送りローラーで、規定速で送られている。
10、のローラーも同じ固定送りローラーであるが、図
の矢線で示すように左右に揺振しながら送るので、1、
の網目を変形させることになる。しかし、しっかり網目
に付着して硬化した乾燥物は変形出来ず、結局乾燥物は
弾き落ちる。しかし長い繊維など若干引っ掛かった乾物
は9、のブラシにより掻き落とされる。このようにして
落下した乾物は12、の乾燥完了材取出し口より落下し
13、乾燥完了材受けで集荷処理される。
The sludge adhering to the net is hardened and it is difficult to remove the sludge. The method of the present invention will be described with reference to FIG. The sludge adhering to 1 has already been dried. 9,
Reference numeral 11 denotes a fixed feed roller which is fed at a specified speed.
The roller 10 is also the same fixed feed roller, but is fed while swinging left and right as shown by the arrow in the figure.
Will be deformed. However, the dried product that adheres to the mesh firmly and hardens cannot be deformed, and eventually the dried product flips off. However, some dry matter, such as long fibers, is scraped off by a brush. The dried matter dropped in this way falls from the dried material take-out port 12 and is collected by the dried material receiver.

【0010】14、は発熱体で1、と1、との間に設け
てスペースの活用を図り、加熱の均一化及び加熱効果を
高める。この実施例ではセラミックス製の遠赤外線放射
板を使用している。15、は加熱蒸発室で、その両側に
平行して冷却凝縮室21、がある。両室間は断熱してい
るが上部と下部に開口部を設け、気流が通じるようにな
っている。15、室は発熱体14、によって加熱され、
中の空気は汚泥からの発生蒸気とともに上昇する。上部
にいたつた空気は開口部から両側の冷却凝縮室20、に
流出する。20、室には19、の冷却配管があり発生蒸
気はここで冷却凝縮され、放熱し低温になった空気は下
降し再び15、室に流入する。このように気温の差によ
って気流が生じ、循環し蒸発、凝縮によって乾燥が行な
われる。乾燥が進むにつれ湿気が減少するので3分割
し、それぞれ適切な条件で行う。この実施例では悪臭の
影響を避け大気と隔離したが、悪臭の発生など環境への
影響のない場合は、20、を大気に通じ下部から大気を
導入し上部から排出する。熱体7、の熱源は最もエネル
ギーを消費するので、この選択は重要である。本発明で
は高温を要さないので、コーゼネレーションや、デーゼ
ルの温排水などの利用が図られる。またヒートポンプを
利用すれば設備費は高価になるが、成績係数が高くエネ
ルギーの消費が少なく、運転保守が容易になる。近時深
夜電力が大幅に安価になったので、本実施例はこの利用
を図った。
A heating element 14 is provided between the heating elements 1 and 1 so as to utilize the space and to make the heating uniform and enhance the heating effect. In this embodiment, a far-infrared radiation plate made of ceramics is used. Reference numeral 15 denotes a heating and evaporating chamber, and a cooling and condensing chamber 21 is provided in parallel on both sides thereof. Although the two chambers are insulated, openings are provided at the top and bottom to allow air flow. 15, the chamber is heated by the heating element 14,
The air inside rises with the steam generated from the sludge. The air that has reached the upper part flows out of the opening into the cooling condensation chambers 20 on both sides. There are 20 and 19 cooling pipes in the chamber, and the generated steam is cooled and condensed here, and the radiated and cooled air descends and flows again into the chamber. As described above, an airflow is generated due to a difference in temperature, and circulates to dry by evaporation and condensation. Since the humidity decreases as the drying proceeds, it is divided into three parts, and each is performed under appropriate conditions. In this embodiment, the influence of the bad odor is avoided and the air is isolated. However, when there is no influence on the environment such as the generation of the bad odor, 20 is introduced into the air, the air is introduced from the lower part and discharged from the upper part. This choice is important because the heat source of the heating element 7 consumes the most energy. Since the present invention does not require a high temperature, utilization of cogeneration, hot drainage of diesel, and the like can be achieved. If a heat pump is used, the equipment cost will be high, but the coefficient of performance will be high, energy consumption will be low, and operation and maintenance will be easy. In the present embodiment, the use of this power was attempted because the power of late-night power has recently become significantly cheaper.

【0011】[0011]

【発明の効果】従来トラブルの多い濾過、脱水の工程
が不要になる。 乾燥物が薄いフイルムを形成してい
るので、両面から乾燥が進み、短時間に乾燥が完了す
る。このため乾燥温度を高める必要は無く熱量、損失熱
量も少ない。 短時間の乾燥が出来るのでスペースが
少なく、装置を小型化にできる。 乾燥完了後は極め
て薄い乾燥物になるので、運搬、保管が容易になり、地
域的な利用範囲は広範に亘る。 資源の活用面では、
製品が薄く、細かい粉状物質なので加工が容易で利用範
囲も広い。 気流を利用して乾燥するため、気流を作
る動力を要さず、床面積を少なく高さを高くするので床
面の有効活用が図れる。 網がエンドレスで流れ操業
が出来るので、自動化し運転経費の節減が図られる。
高温を要さないので、デーゼルなどの温排水の利用、
また時間を制約しなければ深夜電力の利用などが出来、
安価な料金が適用される。 低温なので網は樹脂類で
よく、可撓性に優れ操作性、磨耗性も優れ、軽量で装置
の構造が簡単になる。 ▲10▼乾燥材は低温乾燥のた
め変質を受けることなく、肥料、飼料としての成分を温
存し、活性処理によって資源の回収が図りうる。▲11
▼さらに発生蒸気を凝縮排水することにより悪臭、粉塵
の発生はない。
According to the present invention, the conventional troublesome filtration and dehydration steps become unnecessary. Since the dried product forms a thin film, the drying proceeds from both sides, and the drying is completed in a short time. Therefore, there is no need to raise the drying temperature, and the amount of heat and the amount of heat loss are small. Since drying can be performed in a short time, the space is small and the apparatus can be downsized. After the drying is completed, the dried product becomes extremely thin, so that it can be easily transported and stored, and has a wide range of local applications. In terms of resource utilization,
Since the product is thin and fine powder, it is easy to process and has a wide range of applications. Since drying is performed using an air current, no power is required to generate the air current, and the floor area is reduced and the height is increased, so that the floor surface can be effectively used. Since the network can be operated endlessly, it can be automated and operation costs can be reduced.
Because high temperature is not required, use of hot drainage such as diesel
If you do not restrict the time, you can use electricity at midnight,
Cheaper rates apply. Since the temperature is low, the net may be made of a resin, and has excellent flexibility, excellent operability and abrasion, light weight and a simple structure of the apparatus. {10} The dried material is not degraded due to low-temperature drying, preserves components as fertilizer and feed, and can recover resources by active treatment. ▲ 11
▼ Furthermore, the generated steam is condensed and drained, so no odor or dust is generated.

【0012】[0012]

【図面の簡単な説明】[Brief description of the drawings]

【第1図】本発明の乾燥装置側面の断面の説明図。FIG. 1 is an explanatory view of a cross section of a side of a drying device of the present invention.

【第2図】第1図のA−A断面図。FIG. 2 is a sectional view taken along line AA of FIG.

【第3図】本発明の乾燥装置の乾燥物の剥ぎ取り部分の
説明図。
FIG. 3 is an explanatory view of a portion of the drying device of the present invention for removing a dried product.

【符号の説明】[Explanation of symbols]

1、網(汚泥が付着している) 2、原料供給口 (汚水) 3、汚泥滞積枠 4、圧縮ローラー 5、網(汚泥が落とされている) 6、排水受 7、固定送りローラー 8、ローラーブラシ 9、固定送りローラー 10、左右揺振ローラー 11、固定送りローラー 12、乾燥完了材取出し口 13、乾燥完了材受 14、発熱体 15、加熱蒸発室 16、緊張ローラー 17、湿度検出器 18、送りローラー 19、冷却水管 20、冷却凝縮室 1, net (sludge is attached) 2, raw material supply port (sewage) 3, sludge accumulation frame 4, compression roller 5, net (sludge is dropped) 6, drainage 7, fixed feed roller 8 , Roller brush 9, fixed feed roller 10, left and right swing roller 11, fixed feed roller 12, dried material take-out port 13, dried material receiver 14, heating element 15, heating evaporation chamber 16, tension roller 17, humidity detector 18, feed roller 19, cooling water pipe 20, cooling condensing chamber

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01D 33/58 B01D 33/36 B30B 9/24 F26B 13/14 Fターム(参考) 3L113 AA08 AB06 AB09 AC10 AC19 AC21 AC31 AC45 AC46 AC48 AC49 AC54 AC62 AC64 AC79 BA37 CA05 CA09 CA11 DA02 DA05 DA06 DA08 DA10 DA13 DA14 DA17 DA24 DA26 4D026 BA03 BB05 BC13 BD02 BD05 BE06 BF12 BF15 BF18 4D059 AA07 BD11 BD26 BE17 CB27 CC01 CC02 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B01D 33/58 B01D 33/36 B30B 9/24 F26B 13/14 F term (Reference) 3L113 AA08 AB06 AB09 AC10 AC19 AC21 AC31 AC45 AC46 AC48 AC49 AC54 AC62 AC64 AC79 BA37 CA05 CA09 CA11 DA02 DA05 DA06 DA08 DA10 DA13 DA14 DA17 DA24 DA26 4D026 BA03 BB05 BC13 BD02 BD05 BE06 BF12 BF15 BF18 4D059 AA07 BD11 BD26 BE17 CB27 CC01 CC02 CC02

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 網(5)に付着した乾燥物を、(5)と
共に圧縮ローラー(4)に挟んで圧縮脱水し、フイルム
状として乾燥するフイルム状乾汚泥燥装置。
1. A film-type dry sludge drying apparatus for drying and drying a dried product adhering to a net (5) with a compression roller (4) together with (5), and drying the film as a film.
【請求項2】 圧縮ローラー(4)の面の移動速度を、
網(5)の移動速度より速くして、圧縮ローラー(4)
の面への乾燥物付着を防止する特許請求の範囲第1項の
フイルム状汚泥乾燥装置。
2. The moving speed of the surface of the compression roller (4) is
Compression roller (4), faster than the moving speed of the net (5)
2. A film-like sludge drying apparatus according to claim 1, which prevents adhesion of dried matter to the surface of the sludge.
【請求項3】 網(1)に付着して乾燥完了した乾燥物
を、図2のように固定送りローラー(9)(10)(1
1)で挟み(10)を左右に揺振するなどして、網目を
変形させて乾燥物を弾き落とす特許請求の範囲第1項、
または第2項のフイルム状汚泥乾燥装置。
3. The dried material adhered to the net (1) and dried is fixedly fed to the rollers (9), (10) and (1) as shown in FIG.
2. The method according to claim 1, wherein the mesh is deformed and the dried material is flipped off by, for example, shaking the pinch (10) right and left in 1).
Alternatively, the film-like sludge drying apparatus according to item 2.
【請求項4】 加熱蒸発室(15)に平行して冷却凝縮
室(21)を設け、この間を断熱し上部と下部に両室に
通ずる開口部を設け、両室の気温の差で生じる気流によ
って乾燥を行なう特許請求の範囲第1項、または第2
項、または第3項のフイルム状汚泥乾燥装置。
4. A cooling and condensing chamber (21) is provided in parallel with the heating and evaporating chamber (15), and the space between the cooling and condensing chamber (21) is insulated, and an opening communicating with both chambers is provided at an upper part and a lower part. Claims 1 or 2 wherein drying is performed by
Item or the film-like sludge drying device according to Item 3.
JP10254505A 1998-08-04 1998-08-04 Film-like sludge dryer Pending JP2000051898A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10254505A JP2000051898A (en) 1998-08-04 1998-08-04 Film-like sludge dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10254505A JP2000051898A (en) 1998-08-04 1998-08-04 Film-like sludge dryer

Publications (1)

Publication Number Publication Date
JP2000051898A true JP2000051898A (en) 2000-02-22

Family

ID=17265996

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10254505A Pending JP2000051898A (en) 1998-08-04 1998-08-04 Film-like sludge dryer

Country Status (1)

Country Link
JP (1) JP2000051898A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020043526A (en) * 2002-05-16 2002-06-10 진영섭 Organic / Inorganic Sludge Dryer
FR2960871A1 (en) * 2010-06-08 2011-12-09 Degremont Drying pasty materials e.g. sludge from treatment plant, by subjecting sludge exiting from mechanical dehydration by pressing to laying operation that is moderated to preserve structure of sludge present in outlet of mechanical dehydration
CN103712425A (en) * 2013-12-13 2014-04-09 柳城县鼎铭金属制品有限公司 Drying device in high-speed rough drawing production line
CN112197558A (en) * 2020-10-16 2021-01-08 温州宇岚科技有限公司 Energy-saving and environment-friendly garment material non-contact lifting, positioning and drying equipment
CN113639541A (en) * 2021-08-23 2021-11-12 张玉成 Drying method for carbon fiber material production

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020043526A (en) * 2002-05-16 2002-06-10 진영섭 Organic / Inorganic Sludge Dryer
FR2960871A1 (en) * 2010-06-08 2011-12-09 Degremont Drying pasty materials e.g. sludge from treatment plant, by subjecting sludge exiting from mechanical dehydration by pressing to laying operation that is moderated to preserve structure of sludge present in outlet of mechanical dehydration
CN103712425A (en) * 2013-12-13 2014-04-09 柳城县鼎铭金属制品有限公司 Drying device in high-speed rough drawing production line
CN112197558A (en) * 2020-10-16 2021-01-08 温州宇岚科技有限公司 Energy-saving and environment-friendly garment material non-contact lifting, positioning and drying equipment
CN113639541A (en) * 2021-08-23 2021-11-12 张玉成 Drying method for carbon fiber material production
CN113639541B (en) * 2021-08-23 2022-11-15 烟台锐泽化学品有限公司 Drying method for carbon fiber material production

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