JPS6017681A - Dehydrating drier for muddy material - Google Patents

Dehydrating drier for muddy material

Info

Publication number
JPS6017681A
JPS6017681A JP58125129A JP12512983A JPS6017681A JP S6017681 A JPS6017681 A JP S6017681A JP 58125129 A JP58125129 A JP 58125129A JP 12512983 A JP12512983 A JP 12512983A JP S6017681 A JPS6017681 A JP S6017681A
Authority
JP
Japan
Prior art keywords
drying
water
air
sludge
dewatering
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
JP58125129A
Other languages
Japanese (ja)
Inventor
環 石井
須賀 清四郎
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP58125129A priority Critical patent/JPS6017681A/en
Publication of JPS6017681A publication Critical patent/JPS6017681A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、下水汚泥等の泥状物を小川(莫で月安価に1
1(2水、乾燥させ得る泥−状物1112水乾燥装置に
関づる。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for removing muddy materials such as sewage sludge from streams (at a low cost per month).
1 (2) Water, slurry that can be dried 1112 Relates to water drying equipment.

近年の下水1口の発達は目覚ましく、大都市から小都市
へ、小都市から更に町村へと漸時普及している。
The development of sewage systems in recent years has been remarkable, and they are gradually spreading from large cities to small cities, and from small cities to towns and villages.

現在の下水汚泥等の脱水、乾燥装置等下水道設備は大部
重用に開発されたちのCあり、その規模が大きい。更に
泥状物のfII2水・乾燥はその性状からり「作業であ
り、高11ヒ率とする為には大型の高級(ふとならざる
を得ず、設備費、運転費、保守費が巨額なものとなると
共に熟練者、技術者を必要とした。
Most of the current sewage equipment, such as dewatering and drying equipment for sewage sludge, was developed for heavy use and is large in scale. Furthermore, fII2 watering and drying of muddy materials is a laborious process due to its nature, and in order to achieve a high 11 hit rate, it is necessary to use a large, high-grade (unfortunately) facility, which requires huge equipment costs, operation costs, and maintenance costs. As it became more popular, it required skilled workers and engineers.

然し、小都市、町刊で要求される下水設備の場合、小規
模C゛安価且つ熟練者、技術者を必要どしないものが要
求され、上記した下水道設備は小都市、町利には適して
なく、又これら要求に適した下水道R211fl+がな
いのが現状である。
However, in the case of sewage facilities required by small cities and towns, small-scale C ``low cost and no need for skilled workers and engineers are required, and the above-mentioned sewage facilities are not suitable for small cities and towns. Currently, there is no sewer R211fl+ suitable for these requirements.

本発明は斯かる現状に鑑みてなしたちのであり、ベル1
〜式脱水、乾燥テーブルを立体的に積重ね、段数を多く
とることにより作用面積と作用時間を十分与え、脱水は
m力脱水、乾燥は対向流空気による風乾を主体とするこ
とによって、構造が簡単で而も運転費が安く無人化運転
の可能な泥状物脱水乾燥装置を提供することを目的とす
る。
The present invention was made in view of the current situation, and Bell 1
- Dehydration and drying tables are stacked three-dimensionally and the number of stages is increased to provide sufficient action area and time, dehydration is performed by m-force dehydration, and drying is performed mainly by air drying using countercurrent air, resulting in a simple structure. The object of the present invention is to provide a sludge dewatering and drying device that has low operating costs and can be operated unmanned.

以下本発明の実施例を図面を参HH+7. シつつ説明
づる。
Examples of the present invention will be described below with reference to the drawings.HH+7. I will explain it in detail.

人41“(角l1fq1の頂部に汚泥供給管2を設り、
該f’7泥1バ給管2の直下にIl++水テーブル3、
更にその゛ド方に乾燥テーブル4(4a・・・III)
を所要段設(′J、人型角槽1の底部に排出コンベア5
を設4Jる。
Person 41" (Sludge supply pipe 2 is installed at the top of corner l1fq1,
Immediately below the f'7 mud 1 bar supply pipe 2 is an Il++ water table 3,
Furthermore, there is a drying table 4 (4a...III) on the other side.
('J, a discharge conveyor 5 is installed at the bottom of the human-shaped square tank 1.
Established 4J.

前記11;1水デープル3は、両端の駆動ロール6゜6
に所要のメツシュにしたエンドレスl1t2水ベルト7
を掛渡し、1j;2水ベルト7の」:側を水平となる様
ガイドローラ8で支持し、又下側の垂下りを防止づる為
ガイド[l−ラ9を支1−1l+lる構3古であり、脱
水ベル1〜7は駆動[1−ル6によって反111泪方向
にti tjさlる様にし−(ある。又1.ガイド1−
1−ラ8の1Z方には水受111110を、19(]、
該水受111110 ”C:受()た汚水は外部に段(
Jら(〕た汚水処理装置(図示せず)に送給される。
The 11;1 water lap 3 has drive rolls 6°6 at both ends.
Endless l1t2 water belt 7 with the required mesh
The side of the water belt 7 is supported by guide rollers 8 so that it is horizontal, and the guide [l-ra 9 is supported by the guide roller 8 to prevent the lower side from drooping. The dewatering bells 1 to 7 are driven by the guide 6 in a direction opposite to the 111 direction.
1-A water tray 111110 is placed on the 1Z side of La 8, 19(],
The water receptacle 111110 ”C: The received sewage is placed on an external stage (
J et al. () to a sewage treatment facility (not shown).

前記1j(2水テーブル3の」方に形枠11を上下動D
J能に設(〕、形枠下位同C脱水ベルト7の上面に密着
し、形枠11内に汚泥水を貯留し得る様にし、又、l1
t2水テーブル3の所要位バに圧縮空気を脱水ベル1〜
7の内側より外側に吹出す様エアジエツ]・スクラバ1
2を設ける。
Move the form 11 up and down in the direction of 1j (2 water table 3).
The lower part of the formwork is installed in the lower part of the C dewatering belt 7 so as to be in close contact with the upper surface of the dewatering belt 7 so that sludge water can be stored in the formwork 11.
t2 Dehydrate compressed air to the required location on water table 3.
Air jets that blow out from the inside of 7 to the outside]・Scrubber 1
2 will be provided.

前記乾燥テーブル4(4a・・・4g>は、それぞれ駆
動ロール13.13にエンドレスベル1〜14を掛回し
、エンドレスベル1−14をガイド上1−ル15,16
により案内する構成であり、夫々上段のテーブル(脱水
デープル、乾燥テーブル双方を示づ)に対し逆方向にエ
ンドレスベル1〜14を走行させる様に構成してあり、
各乾燥テーブル4(4a・・・4g>は上段のテーブル
に対し水平方向に交互にずらしである。
The drying table 4 (4a...4g> has endless bells 1 to 14 wound around drive rolls 13 and 13, respectively, and endless bells 1 to 14 on guides 1 to 15 and 16.
The endless bells 1 to 14 are configured to run in the opposite direction to the upper table (both the dewatering table and the drying table are shown).
Each drying table 4 (4a...4g>) is alternately shifted in the horizontal direction with respect to the upper table.

前記DI2I2−ブル3と最上段の乾燥テーブル4aど
の間に仕切板17を設け、n12水テーブル3の左側駆
動ロール(ベルトが下方に方向変換りる側のロール)6
に対峙させ人型角槽1.側壁にガイド板18を設(プ、
該ガイド板18ど前記f」切板17の端に設(〕たカイ
ト板19とCシュート20を構成せしめる。
A partition plate 17 is provided between the DI2I2-blue 3 and the top drying table 4a, and the left drive roll (roll on the side where the belt changes direction downward) 6 of the n12 water table 3 is installed.
A humanoid square tank 1. A guide plate 18 is installed on the side wall.
The guide plate 18 constitutes a kite plate 19 and a C chute 20, which are installed at the end of the cutting plate 17.

叉、各段の乾燥デーグル4のベルl−’a士方に方向変
換づる側の駆動ロール13に対峙ざUて力rド板18を
ぞれそ゛れ設置Jる。
Further, a power board 18 is installed on each side of the drying dagel 4 at each stage, facing the drive roll 13 on the direction changing side.

人型角槽1の側壁、最下段乾燥ブープル4g下方の位置
に空気供給1」21を設り、人型角槽1の側′壁上部に
空気IJI出口22を設【プ、荒気供給口21の、L:
”Atには空気供給ファン、空気1ノ1出口22の下;
Aコには脱臭装置(いずれも図示Uず)を接続し、ソど
気1ハ給1121からは常[14空気を供給Jる杼にり
る。
An air supply 1' 21 is installed on the side wall of the human-shaped square tank 1, below the lowest drying bubble 4g, and an air IJI outlet 22 is installed on the upper part of the side wall of the human-shaped square tank 1. 21, L:
``At the air supply fan, below the air 1 no 1 outlet 22;
A deodorizing device (both not shown in the figure) is connected to A, and air is always supplied from the air supply 1121 to the shuttle.

次に1−記装置に於ける乾燥f[動について説明りる。Next, the drying process in the apparatus described in 1-1 will be explained.

n(2水j−ゾル3、乾燥=7=ゾル4が全て1宇II
−した状態で形枠11を下し、汚泥供給?22より汚泥
水を形枠11内に供給りる。
n (2 water j - sol 3, dry = 7 = sol 4 is all 1 u II
Lower the form 11 in the - state and supply sludge? Sludge water is supplied into the form 11 from 22.

この汚泥水供給は1日1回、1[」分が供給され、又1
i2水アーブル3、乾燥ラーノル4の駆動は1日1 (
Jイクルとりる。
This sludge water is supplied once a day for 1
i2 Water Havre 3 and Dry Lanol 4 are driven once a day (
Take Jicle.

汚泥水の水分は重力よりIII;!水ベルl−7を通過
し、直下の水受皿10で集められ、外部の汚水処理装置
にf〕(給され処Jg!される。
The water content of sludge water is higher than gravity. The water passes through the water bell 1-7, is collected in the water tray 10 directly below it, and is fed to an external sewage treatment device.

翌日形枠11を引上げ、Lアジエラ1ヘスクラバ12を
l’l動さIJると共に1j))水テーブル3、全乾燥
デープル4a・・・4g及び刊出コンベア5を一斉に駆
動覆る。
The next day, the frame 11 is pulled up, the L Asialer 1 Hescrubber 12 is moved, and the water table 3, dry table 4a...4g, and publication conveyor 5 are driven and covered all at once.

脱水されたPj泥はtill水ペル1−7の走行と共に
順次シュー1〜20より落下し、下段の乾燥ラーブル4
aに移変えられる。このl18711i2水ベル1−7
ど」−ン1〜レスベルト14どの走行速度を一致させて
お【プば移し変えは平均化され月下段のデープル4aに
落下する際に自動的に汚泥の反転、切崩し効果が生ずる
The dehydrated Pj mud falls sequentially from the shoes 1 to 20 as the till water pels 1 to 7 run, and is transferred to the dry rubble 4 in the lower stage.
It can be transferred to a. This l18711i2 water bell 1-7
By matching the running speeds of the dowels 1 to 14, the transfer is averaged, and the effect of turning over and breaking down the sludge automatically occurs when it falls to the daple 4a at the bottom of the sludge.

汚泥が夫々一段下に移変えが完了ηるど乾燥テーブル4
a・・・4す、排出コンベア5は一斉に停止りる1、脱
水テーブル3は乾燥7−−ノール4a・・・4gが停止
した後す数回転走行し、この走行の間に脱水ベル1〜7
の目詰りがエアシーLツ1〜スクラバ12によってi?
化される。
The sludge has been transferred to the lower level η Drying table 4
a...4, the discharge conveyor 5 stops all at once 1, the dewatering table 3 runs several times after the drying 7--nols 4a...4g stop, and during this running the dewatering bell 1 ~7
Is the clogging caused by Air Sea Lts 1 to Scrubber 12?
be converted into

脱水テーブル3が停止すると再び形枠11が下され汚泥
供給室2より汚泥水が供給され形枠11内に貯留され、
1日11ノイクルの1稈が完了す“る。
When the dewatering table 3 stops, the form 11 is lowered again and sludge water is supplied from the sludge supply chamber 2 and stored in the form 11.
One culm of 11 noikuru is completed in a day.

1!Iiかる一f稈を繰返えVば汚泥は順次下段の乾燥
テーブル4に移変えられ、移変え毎に反転、切崩し効果
が発生し、最下段に至った汚泥は排出゛コンベア5′c
外部のホッパー等に排出される。
1! By repeating the culm, the sludge is sequentially transferred to the lower drying table 4, and at each transfer, a reversal and cutting effect occurs, and the sludge that has reached the lowest stage is discharged onto the conveyor 5'c.
It is discharged into an external hopper, etc.

又、前記空気供給口21J、り供給し・た空気は各乾燥
テーブル4a・・・4g毎に設けられたガイド板18に
突当り方向変換し、汚泥の流れに対向して流れ、最終的
には空気排出口22より排出される。
Further, the air supplied through the air supply port 21J hits the guide plate 18 provided for each drying table 4a...4g, changes direction, flows against the flow of sludge, and finally The air is discharged from the air outlet 22.

JIJiかる空気の流れを規制する流路は各乾燥テーブ
ル4a・・・4g、ガイド板18、仕切板11、脱水テ
ーブル3によって構成されている。
The flow path that regulates the flow of air is constituted by the drying tables 4a...4g, the guide plate 18, the partition plate 11, and the dewatering table 3.

而して、各テーブルによる下段への汚泥の移変え、空気
の流れにより、汚泥の屈1乾は下段に至る程進行し、排
出時には風乾が充2分行われた状態どなっている。又、
供給りる空気量は、空気IJI +Jt II 22を
出る時に水分が飽和状態に近(=Iいている程度が経済
上好ましい。
Due to the transfer of the sludge to the lower stage by each table and the flow of air, the sludge dries until it reaches the lower stage, and by the time of discharge, it has been air-dried for a full 2 minutes. or,
The amount of air to be supplied is preferably such that the water content is close to the saturated state (=I) when the air leaves the air IJI + Jt II 22 from an economic standpoint.

尚、第2図は他の実施例を示すもので、第1図に於(プ
る△−A矢視図に相当りる。
Incidentally, FIG. 2 shows another embodiment, and corresponds to the view taken along the arrow Δ-A in FIG.

第1図に示した実施例では、乾燥用空気を汚泥走行に対
し完全な対向流どしたが、第2図C示す実施例では、汚
泥走行に対し直角に横断さけて流している場合であり、
この場合も下段から上段に流れ同じく対向流である。
In the embodiment shown in Fig. 1, the drying air is flowed completely in the opposite direction to the sludge running, but in the embodiment shown in Fig. 2C, it is flowed across the sludge running at right angles. ,
In this case as well, the flow flows from the lower stage to the upper stage, and the flow is also counter-current.

尚、第1図、第2図中23は汚泥の走行方向、24は空
気の流れ方向である。
In FIGS. 1 and 2, 23 is the running direction of the sludge, and 24 is the air flow direction.

又、上記実施例ひは1E11サイクルとして説明したが
、2サイクル以上としてもよいことは勿論であり、I]
t2水テーブルの段数、乾燥゛テーブルの段数も上記実
施例に限定するものではない。
In addition, although the above embodiment was explained using 1E11 cycles, it is of course possible to use 2 or more cycles.
The number of stages of the t2 water table and the number of stages of the drying table are not limited to those in the above embodiment.

更に、乾燥テーブルを1日1段の割合で超微速連続運転
してもよく、各乾燥デーフルの速度を相対的に変化させ
てもよい。
Further, the drying table may be operated continuously at a very slow speed at one stage per day, or the speed of each drying dauffle may be relatively changed.

更に又、汚泥の性状によっては形枠を必要としない場合
も考えられる。
Furthermore, depending on the properties of the sludge, a frame may not be necessary.

以上述べlζ如く本発明にJこれは、 (1)1日1回程度の簡単なスイッヂ操作C操業が可能
であり、特殊技術が不要である、(韮) 短時間の駆動
以外は静止させているので無人操業が容易に行える、 0 短詩間駆動であるので所要エネルギが極めて少ない
と共に長寿命である、 (へ) 構造が甲純であるので安価である、(ν)、空
間を立体的に利用するので設置スペースが少なくてずむ
、 等種々の優れた効果を発揮する。
As stated above, the present invention has the following advantages: (1) It can be operated by a simple switch operation about once a day, and no special technology is required. 0. Since it is a short-term drive, it requires extremely little energy and has a long life. (f) The structure is simple, so it is inexpensive. (v). Since it is used, it has various excellent effects such as requiring less installation space.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実7II例の正面から見た縦断面概略
図、第2図は同前他の実施例の側面から見た縦断面概略
図ひある。 1は犬型角槽、2は汚泥供給菅、3はn12水テーブル
、4は乾燥”7− ’フル、18は刀イド仮、24は空
気流を示す。 第1図 第2図 414
FIG. 1 is a schematic vertical cross-sectional view of the 7II embodiment of the present invention as seen from the front, and FIG. 2 is a schematic vertical cross-sectional view of another embodiment of the same as seen from the side. 1 is a dog-shaped square tank, 2 is a sludge supply tube, 3 is an N12 water table, 4 is a drying "7-' full, 18 is a sword id temporary, and 24 is an air flow. Figure 1 Figure 2 414

Claims (1)

【特許請求の範囲】[Claims] 1) 角漕の頂部に設けられた泥状物供給(」の直′下
に走行可能なエンドレス1112水ベルトが水平方向に
張設され、該11;2水ベル1〜下方に水受部を有する
脱水テーブルを設置し、該脱水テーブル下方に上段テー
ブルに対し順次逆1)向に走行可能なエンドレスベルト
を備えた乾燥テーブルを所要段数段買し、乾燥用空気が
前記各テーブルの下段から順次士民に対向流する様空気
通路を形成したことを特徴とでる泥状物脱水乾燥装置。
1) An endless 1112 water belt that can run is stretched horizontally just below the slurry supply installed at the top of the square tank, and a water receiving part is installed below the 11;2 water belt. Install a dewatering table with a drying table, and purchase the required number of drying tables equipped with endless belts that can run in the opposite direction to the upper table below the dewatering table, and drying air is supplied sequentially from the bottom of each table. A sludge dehydrating and drying device characterized by forming an air passage so that the air flows counter-currently to the civilians.
JP58125129A 1983-07-09 1983-07-09 Dehydrating drier for muddy material Pending JPS6017681A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58125129A JPS6017681A (en) 1983-07-09 1983-07-09 Dehydrating drier for muddy material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58125129A JPS6017681A (en) 1983-07-09 1983-07-09 Dehydrating drier for muddy material

Publications (1)

Publication Number Publication Date
JPS6017681A true JPS6017681A (en) 1985-01-29

Family

ID=14902567

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58125129A Pending JPS6017681A (en) 1983-07-09 1983-07-09 Dehydrating drier for muddy material

Country Status (1)

Country Link
JP (1) JPS6017681A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61204703U (en) * 1985-06-13 1986-12-24
JPH0275400A (en) * 1988-09-09 1990-03-15 Jgc Corp Multistage dryer
US4934628A (en) * 1987-01-23 1990-06-19 Daiwa Seiko, Inc. Counter housing for fishing
JPH035000A (en) * 1989-06-02 1991-01-10 Ishigaki Kiko Kk Dehydrating and drying apparatus
JP2002052399A (en) * 2000-08-10 2002-02-19 Parker Engineering Kk Chemical forming sludge dehydrating and drying apparatus
JP2002162164A (en) * 2000-11-22 2002-06-07 Masami Takagi Drying system
KR100358842B1 (en) * 2000-06-08 2002-10-30 박대식 Converse churn dry-construction that the moisture holding life and industry waste sludge or adulterated thing

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61204703U (en) * 1985-06-13 1986-12-24
US4934628A (en) * 1987-01-23 1990-06-19 Daiwa Seiko, Inc. Counter housing for fishing
JPH0275400A (en) * 1988-09-09 1990-03-15 Jgc Corp Multistage dryer
JPH0553560B2 (en) * 1988-09-09 1993-08-10 Jgc Corp
JPH035000A (en) * 1989-06-02 1991-01-10 Ishigaki Kiko Kk Dehydrating and drying apparatus
KR100358842B1 (en) * 2000-06-08 2002-10-30 박대식 Converse churn dry-construction that the moisture holding life and industry waste sludge or adulterated thing
JP2002052399A (en) * 2000-08-10 2002-02-19 Parker Engineering Kk Chemical forming sludge dehydrating and drying apparatus
JP2002162164A (en) * 2000-11-22 2002-06-07 Masami Takagi Drying system
JP4502348B2 (en) * 2000-11-22 2010-07-14 正巳 高木 Drying equipment

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