JPS62502109A - Organic gas generation treatment equipment - Google Patents

Organic gas generation treatment equipment

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Publication number
JPS62502109A
JPS62502109A JP61501667A JP50166786A JPS62502109A JP S62502109 A JPS62502109 A JP S62502109A JP 61501667 A JP61501667 A JP 61501667A JP 50166786 A JP50166786 A JP 50166786A JP S62502109 A JPS62502109 A JP S62502109A
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JP
Japan
Prior art keywords
drum
baffles
gas
guide ribs
baffle
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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
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JP61501667A
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Japanese (ja)
Inventor
シクリスト、ゲオルグ
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Individual
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Individual
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Publication of JPS62502109A publication Critical patent/JPS62502109A/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • C02F11/04Anaerobic treatment; Production of methane by such processes
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F29/00Mixers with rotating receptacles
    • B01F29/60Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers
    • B01F29/63Mixers with rotating receptacles rotating about a horizontal or inclined axis, e.g. drum mixers with fixed bars, i.e. stationary, or fixed on the receptacle
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90Heating or cooling systems
    • B01F35/92Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/36Means for collection or storage of gas; Gas holders
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/10Rotating vessel
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/18Flow directing inserts
    • C12M27/20Baffles; Ribs; Ribbons; Auger vanes
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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】 有機物のガス発生処理装置 本発明は有機物質のガス発生処理、特に醗酵や熟成用の装置に関する。さらに詳 述すると、本発明は請求の範囲の公知部に記載したごとき装置に関する。[Detailed description of the invention] Organic gas generation treatment equipment The present invention relates to equipment for gas generation treatment of organic substances, particularly for fermentation and ripening. More details Specifically, the invention relates to a device as defined in the well-known part of the claims.

本発明による装置は、水平中心軸を中心に回転するよう゛になっている水平処理 ドラムと、該ドラムの内部に固着した処理物質移送手段とから成る。The device according to the invention comprises a horizontal processing device adapted to rotate about a horizontal central axis. It consists of a drum and means for transporting the material to be treated fixed inside the drum.

処理対象が工業または家庭廃棄物の場合、その廃棄物の大部分は腐敗不能な固形 物質である。かかる固形物質は、砂、じゃり、金属等沈澱作用によって懸濁液か ら分離しやすい高比重物質と、懸濁液上面に浮上浮遊しやすくいわゆる浮環層を 形成する低比重物質との両方から成る。When dealing with industrial or domestic waste, most of the waste is non-perishable and solid. It is a substance. Such solid substances, such as sand, gravel, and metals, can be turned into a suspension by settling. high-density substances that are easily separated from the suspension, and a so-called floating ring layer that is easy to float on the top surface of the suspension. It consists of both a low specific gravity substance and a substance that forms.

本発明の目的は処理ドラム内に比較的長い一定時間に亘って残留させる必要のあ る腐敗可能な物質に比べ腐敗不能物質の方をより迅速に内部移送させる処理ドラ ムを上述の装置内に設けることにある。The purpose of the present invention is to remove the A process driver that allows non-perishable materials to be transported internally more quickly than perishable materials. The present invention is to provide a system within the above-mentioned apparatus.

このため、本発明による装置における物質移送手段は、該ドラムの長手方向で離 間し該ドラムの横断平面と鋭角をなし、該ドラムの軸方向に延在し固定支持面に 固着した複数のガイドリブから成り、該ガイドリブはその側面でドラム内の沈澱 物質を捕捉し該ドラムの一端へと偏向させるよう構成されている。For this reason, the material transfer means in the device according to the invention are spaced apart in the longitudinal direction of the drum. a fixed support surface extending in the axial direction of the drum and forming an acute angle with the transverse plane of the drum; It consists of a plurality of fixed guide ribs, the sides of which guide the sediment in the drum. The drum is configured to capture and deflect material toward one end of the drum.

後述の詳細説明から明らかなように、本発明は懸濁液から分離しやすい物質の上 下移動を利用し、ガイドリブによって該上下移動をドラムの出口端方向へ変更さ せ、ドラムの回転に伴なって出口端へ該物質を移送すると0うものである。As will be clear from the detailed description below, the present invention is directed to Using the downward movement, the guide rib changes the vertical movement towards the exit end of the drum. The substance is transferred to the outlet end as the drum rotates.

本発明に関わる装置においては、ドラムが非常ζこ大きく、工業、家庭、農業廃 棄物の熟成処理用装置シこあってはドラム容量は1万一以上となる。従ってドラ ムを水中浸漬してドラム支持体への負荷を軽減した場合でも、ドラム回転駆動に 要する回転モーメントは大きなものとなる。それ故駆動手段は相当量の出力を有 し、ドラムに適用しうる寸法でなければならず、高価なものとなる。In the device related to the present invention, the drum is very large and is suitable for industrial, domestic, and agricultural waste. In the case of a waste aging treatment apparatus, the drum capacity is 10,000 or more. Therefore Dora Even if the drum is immersed in water to reduce the load on the drum support, the drum rotational drive The required rotational moment becomes large. The drive means therefore have a considerable amount of power. However, it must have dimensions that can be applied to the drum, making it expensive.

従って、本発明の別の目的は該ドラムの回転のため外力として用いられる駆動力 を大幅に減縮するか、ある(1は不要とすることを目的とする。Therefore, another object of the invention is to provide a driving force used as an external force for the rotation of the drum. The purpose is to significantly reduce or eliminate the need for (1).

この点において、本発明は処理物質のドラム内における分布不均衡を生じさせる ことで所定方向への回転モーメントをドラムに付与させる手段として、処理作用 中の発生ガス(熟成作用にあっては主にメタンと二酸化炭素)を利用するという 概念に基づくものである。In this regard, the present invention creates an imbalance in the distribution of the treated material within the drum. As a means of applying rotational moment to the drum in a predetermined direction, the processing action The gas generated inside (mainly methane and carbon dioxide for the aging process) is used. It is conceptually based.

この目的のため、本発明による装置のドラム内に複数のドラムの角変位位置にバ ッフルを設け、かかるノ(ツフルはドラムの内面と協働で、ドラム中心軸を包含 する垂直平面から離間している下向開口ガス捕集空間を形成している。For this purpose, in the drum of the device according to the invention there are a plurality of bars at angular displacement positions of the drum. A baffle is provided, and the baffle cooperates with the inner surface of the drum to encompass the center axis of the drum. A downwardly opening gas collection space is formed which is spaced apart from the vertical plane.

この捕集空間に発生ガスの少なくとも大半が処理作用中に捕集される。捕集した ガスによりドラム内の流体またはスラリー状物質が該中心軸包含垂直平面の両側 に均一に分布しないようになっている。この結果、処理物質の大半が該垂直平面 に対しガス捕集空間のある側とは反対の側に位置することになり、こうして回転 モーメントが該ドラムにかかりガス捕集空間とドラムにおけるその隣接部とが上 動されてドラムを回転させる。At least the majority of the generated gas is collected in this collection space during the treatment operation. collected The gas causes the fluid or slurry-like material in the drum to move on both sides of the vertical plane containing the central axis. is not evenly distributed. As a result, most of the processed material is on the vertical plane. It is located on the side opposite to the side where the gas collection space is located, and thus the rotating A moment is applied to the drum, causing the gas collection space and its adjacent portion of the drum to rise. is moved to rotate the drum.

好ましくは、ドラムを間欠的に回転させる。その場合熟成処理装置は上述の角変 位位置毎にドラムを停止させる制御手段を備えてい葛のがよい。Preferably, the drum is rotated intermittently. In that case, the ripening treatment equipment is It is best to have a control means to stop the drum at each position.

本発明の詳細を以下添付の概略図面を用いて説明する。The details of the invention will be explained below using the accompanying schematic drawings.

第1図は本発明を実施した処理装置、つまり熟成処理装置の一部破断側面図、 第3図は、第1図の装置の断面図、 第3図と第4図は処理ドラムの回転状態を示すもので、各々停止位置にある状態 と、2つの停止位置間を回転移動状態にあるドラムの断面図、 第5図は沈澱物と浮滓層とを中心軸方向へ移送する手段を示す一部破断斜視図。FIG. 1 is a partially cutaway side view of a processing apparatus in which the present invention is implemented, that is, a ripening processing apparatus; FIG. 3 is a sectional view of the device of FIG. 1; Figures 3 and 4 show the rotational state of the processing drum, each in its stopped position. and a cross-sectional view of the drum in rotational movement between two stop positions; FIG. 5 is a partially cutaway perspective view showing a means for transporting the sediment and the floating slag layer in the direction of the central axis.

図示するごとく、本発明による装置はコンクリート等で作られ、温度管理された 水(12)をほぼ満タンに充填シタハウジング(11)を有する。ハウジング( 11)内には水平円筒ドラム(13)で形成した熟成処理タンクが密閉配設され 、同円筒ドラムはほぼ全体が水中に浸漬され、水平中心軸(L)を中心に回転す るよう数個の支持ローラ(14)により支持されている。ドラム(13)の一方 の端壁(15)には処理物質をドラム内に連続または間欠供給するための供給手 段(17)へ自在カップリングを介して連結した入口管(16)が設けられてい る。この物質は主に有機物質の水性懸濁液またはスラリーであって、無機物質、 熟成不可固形物質を包含してもよい。ドラムの他方の端壁(18)の中央には熟 成処理物質用の出口管(19)が設けられている。入口管(16)も出口管(1 9)も共にハウジング(11)の端壁(IIA、 IIB)に密封状態に嵌合さ れている。As shown in the figure, the device according to the present invention is made of concrete or the like and is temperature-controlled. It has a housing (11) filled almost completely with water (12). housing( 11) Inside, a maturing tank formed by a horizontal cylindrical drum (13) is sealed. , the cylindrical drum is almost entirely immersed in water and rotates around a horizontal central axis (L). It is supported by several support rollers (14) so as to One side of the drum (13) The end wall (15) is provided with a supply hand for continuously or intermittently supplying the substance to be treated into the drum. An inlet pipe (16) is provided which is connected to the stage (17) via a swivel coupling. Ru. This substance is primarily an aqueous suspension or slurry of organic substances, including inorganic substances, Non-ripenable solid materials may also be included. In the center of the other end wall (18) of the drum is a An outlet pipe (19) is provided for the treatment material. The inlet pipe (16) and the outlet pipe (1 9) are also tightly fitted into the end walls (IIA, IIB) of the housing (11). It is.

端壁(15,18)の入口管と出口管以外は、ドラムは密閉され、プラスチック 、シート状金属、コンクリート等で作られている。Except for the inlet and outlet tubes in the end walls (15, 18), the drum is sealed and made of plastic. , made of sheet metal, concrete, etc.

横断仕切壁(20)によりドラム(13)の内部は2つの空間部に分割され、こ の2つの空間部は該仕切壁に設けた中央開口部(2OA )と円周部近傍に設け た小開口部(20B)によって相互連通している。仕切部(IIC)はこれに対 応してハウジング(11)を仕切っている。こうして仕切られたハウジングの2 つの空間部は温度の異なる水を収容し、ドラムの2つの空間部(13A、 II B)内の処理物質を別々の温度に保つようになっている。無論、ドラムとハウジ ングとは各々2つ以上の空間部に分割されてもよい。The inside of the drum (13) is divided into two spaces by the transverse partition wall (20). The two spaces are a central opening (2OA) provided in the partition wall and a space provided near the circumference. They communicate with each other through a small opening (20B). The partition (IIC) The housing (11) is partitioned accordingly. Two of the housings partitioned in this way The two cavities accommodate water of different temperatures, and the two cavities (13A, II B) The materials to be processed within the system are kept at different temperatures. Of course, the drum and housing Each space may be divided into two or more spaces.

ドラムの仕切壁(20)の中央開口部(20A)により処理物質のドラム空間部 (13A )からドラム空間部(13B)への移送が可能になる。The central opening (20A) of the partition wall (20) of the drum allows the drum space for the material to be treated. (13A) to the drum space (13B) becomes possible.

ドラム(13)内には3つの平坦なバッフル (21A。Inside the drum (13) are three flat baffles (21A).

21−B 、 21C)がドラムの全長に亘って延在し、ドラムの内面(13C )に円周方向へ120度の角度で相互に離間し固着されている。第3図と第4図 とに主に示すごとく、バッフルの幅はドラムの半径に略等しいが、バッフルの軸 方向線部すなわち半径内方自由端(22A、 22B、 22C)は中心軸(L )とドラムに固着した各バッフルの半径外方端縁とを通る半径(RA、RB、R o)から一方向へ互に連通している。隣接するバッフル (21A 、 21B  。21-B, 21C) extend the entire length of the drum, and the inner surface of the drum (13C ) are fixedly spaced from each other at an angle of 120 degrees in the circumferential direction. Figures 3 and 4 The width of the baffle is approximately equal to the radius of the drum, but the axis of the baffle is The direction line portions, that is, the radially inner free ends (22A, 22B, 22C) are aligned with the central axis (L ) and the radius outer edge of each baffle fixed to the drum (RA, RB, R They communicate with each other in one direction from o). Adjacent baffles (21A, 21B .

21C)の内方端縁同土間の開口通路すなわち間隙(24A、 24B、 24 C)の幅は決定的要素とならないが、好適幅はドラム内半径の0,2〜086倍 である。同様にバッフルの幅はドラムの内面(IIC)に固着した半径外方端縁 と半径内方自由端縁(22A〜22C)との間の距離であであるのが好ましい。The inner edge of 21C) has an open passage or gap between the same earthen floors (24A, 24B, 24 The width of C) is not a determining factor, but the preferred width is 0.2 to 0.86 times the inner radius of the drum. It is. Similarly, the width of the baffle is determined by the radial outer edge fixed to the inner surface (IIC) of the drum. and the radially inner free edge (22A-22C).

ドラムは120度の回転角度毎に間欠回転するよう支持され、一回転は3段階か ら成る。制御装置は図示していないがドラムの回転運動を120度毎に段階分け するようになっている。回転運動の動力の全て、または少なくともその大部分は ドラム内にて処理される物質によって発生される。すなわち、以下第3、第4図 と共に説明するごとく熟成処理過程で発生したガスにより処理物質の分布の「不 均衡」が生じる結果として動力が生まれる。The drum is supported to rotate intermittently at every rotation angle of 120 degrees, and one revolution consists of three stages. It consists of Although the control device is not shown, it divides the rotational movement of the drum into stages every 120 degrees. It is supposed to be done. All, or at least most of the power for rotational motion is Generated by materials being processed in the drum. That is, Figures 3 and 4 below As explained above, the gases generated during the aging process cause "imperfections" in the distribution of the treated substances. Power is generated as a result of "equilibrium."

第3図はドラム(i3)が3つの停止位置のうちの1つに位置している状態を示 す。Figure 3 shows the drum (i3) in one of three stopping positions. vinegar.

第3図の、停止位置にドラムが位置している間に、ドラム(13)の左側で熟成 により発生したガスの大部分すなわちバッフル(21A)下方に位置する熟成物 質内で発生したガスは、上方向および側方がドラム(13)の内面(13C)と バッフル(21A)とにより区切られ、下方向がドラムの内面とバッフル(21 A)との間に延在している熟成物質の水平面(SA)すなわち浮滓層(F)によ り区切られたガス捕集空間(25A )内に捕集される。While the drum is in the stop position as shown in Figure 3, ripening is carried out on the left side of the drum (13). Most of the gas generated by the aging product located below the baffle (21A) The gas generated inside the drum is connected upwardly and laterally to the inner surface (13C) of the drum (13). baffle (21A), and the lower side is the inner surface of the drum and the baffle (21A). A), the horizontal surface (SA) of the ripening material, that is, the floating layer (F), extends between The gas is collected in the gas collection space (25A) divided by

ガス捕集空間(25A )内に捕集されたガス量はドラムの停止期間中に徐々に 増大し、下方限界たる水平面、(SA)は徐々に押し下げられる。The amount of gas collected in the gas collection space (25A) gradually decreases during the period when the drum is stopped. The horizontal plane, (SA), which is the lower limit, is gradually pushed down.

同様にバッフル(21B)の下方の熟成物質から発生したガスはガス捕集空間( 26B)内に捕集される。しかし。Similarly, the gas generated from the aged material below the baffle (21B) is absorbed into the gas collection space ( 26B). but.

バッフル(21B)下方の熟成物質から発生するガスの量はバッフル(21A) 下方の熟成物質から発生するガスの量に比べて少it(すなわち物質の量が少な い)であり、しかもガス捕集空間(26A)中の捕集ガスは好適間隔でドラムの 全長に沿って設けた数個の移送管(27)を通ってガス捕集空間(25A)へ移 送される。The amount of gas generated from the ripening material below the baffle (21B) is It is small compared to the amount of gas generated from the ripening material below (i.e. the amount of material is small). ), and the collected gas in the gas collecting space (26A) is collected from the drum at suitable intervals. The gas is transferred to the gas collection space (25A) through several transfer pipes (27) provided along the entire length. sent.

ドラム内で熟成により発生したガスのうち上記以外の部分はドラム内最上位置の 空間(28)へ上昇し、この空間(28)から端壁(15)に隣接しドラムの円 周部近くに設けたガス排出口(29B)を通って排出される。Of the gas generated during aging in the drum, the portion other than the above is located at the top of the drum. rises into the space (28) and from this space (28) adjoins the end wall (15) the circle of the drum The gas is discharged through a gas discharge port (29B) provided near the periphery.

図示の停止位置において、ガス排出口(29B)はドラム端壁(15)のすぐ内 側に設けたエンドチャンバー(31の最上部のガス排出空間(30)に連通して いる。このエンドチャンバーは、他のガス外周排出口(29A、 29C)に常 に連通していて、ある程度まで熟成処理物質が充填されている。ガス排出空間( 30)内には入口管(16)内を通る導管(33)を通じてガス貯蔵室(図示せ ず)に連結したガス排出フード(32)が設けられている。In the stop position shown, the gas outlet (29B) is located just inside the drum end wall (15). The end chamber (31) provided on the side communicates with the gas exhaust space (30) at the top. There is. This end chamber is always connected to other gas peripheral exhaust ports (29A, 29C). and is filled to some extent with a maturing substance. Gas exhaust space ( 30) has a gas storage chamber (not shown) through a conduit (33) passing through the inlet pipe (16). A gas exhaust hood (32) is provided which is connected to the gas exhaust hood (32).

第3図から明らかなように、ガス捕集空間(25A )内に捕集されたガスはド ラム停止期間中にドラムの中心軸(L)を包含する垂直平面CC’)の両側の両 ドラム空間部の同土間に熟成処理物質分布の不均衡を生じさせる。As is clear from Figure 3, the gas collected in the gas collection space (25A) is Both sides of the vertical plane CC') encompassing the central axis (L) of the drum during the ram stop period. This causes an imbalance in the distribution of ripening substances on the same earth floor in the drum space.

、 その結果熟成物質はドラムに作用する回転モーメントを生じドラムを第3図 で右廻りに回転させようとする。, As a result, the ripening material creates a rotational moment acting on the drum, causing the drum to move as shown in Figure 3. Try to rotate it clockwise.

しかし、すでに言及した制御手段によってドラムの回転は、一定時間が経過し、 場合によっては回転モーメントが一定値に達するまで、あるいはその他の所定条 件が充たされるまで阻止される。However, the rotation of the drum is controlled by the control means already mentioned after a certain period of time has elapsed. In some cases, the torque may be increased until the rotational moment reaches a certain value or under other specified conditions. will be blocked until the conditions are met.

こうした条件が充たされた時、ドラムは120度回転させられ、バッフル(21 A)が先の停止期間中のバッフル(21B)の位置を占め、バッフル(21B) が先の停止期間中のバッフル(21C)の位置を占め、バッフル(21C)が先 の停止期間中のバッフル(2LA)の位置を占める。ガス捕集空間(25A)中 のガスは、ドラムの回1) 転によりドラム最上位置に移動したガス排出口(2 9A)′を通じて排出される。上述の工程はその後繰返される。When these conditions are met, the drum is rotated 120 degrees and the baffle (21 A) occupies the position of the baffle (21B) during the previous stop period, and the baffle (21B) occupies the position of the baffle (21C) during the previous stop period, and the baffle (21C) occupies the position of the baffle (2LA) during the stop period. Inside the gas collection space (25A) The gas is discharged from the gas outlet (2) which has moved to the top position of the drum due to rotation of the drum (1). 9A)'. The above steps are then repeated.

ドラムの回転運動は比較的高速であるから、ドラム中の熟成物質はそれに伴なっ て高速で撹拌され、全面的混合作用が生じる。この撹拌作用により同物質のうち の固形状軽比重部分が分離しやすくなる。この部分はそれ自体の浮力により浮滓 層(F)へ浮上し、ドラム中の懸濁、液表面上に浮遊するが、これらの部分は例 えばプラスチックフィルム片、その他家庭廃棄物中にしばしば含まれる軽量物質 がそれに該当する。Since the rotational motion of the drum is relatively fast, the aging material in the drum is The mixture is stirred at high speed to create an all-over mixing action. Due to this stirring action, the The solid light specific gravity part of the liquid becomes easier to separate. This part floats due to its own buoyancy. It floats to the layer (F), is suspended in the drum, and floats on the liquid surface, but these parts are e.g. pieces of plastic film and other lightweight materials often found in household waste. falls under this category.

ドラム(13)の上述の自転作用により、通常作用中にはドラムを外力にて回転 される必要が全く、あるいはほとんどなくなる。しかし、ドラムに外方から回転 モーメントを加える必要が生じた場合に利用できるよう別個の補助駆動ユニット を装置に設けるのが好ましい。外方回転モーメントを加える必要が生じるのは、 例えば熟成処理物質が一部しか充填されていない状態にある装置の立上り時や運 転休止時またはガス発生量が不充分等の場合である。その場合駆動ユニットはド ラム回転に、必要な全ての駆動力を駆動ユニットで常時負担させる場合に比べ、 ずっと小型で単純構造となり、しかも安価となる。上述のごとく補助駆動を目的 とする駆動ユニットが第2図に略示され符号(35)で示されている。この駆動 ユニットは上述の制御ユニットと組合わせて用いられる。Due to the above-mentioned rotation of the drum (13), the drum cannot be rotated by external force during normal operation. There is no or almost no need to do so. However, the drum rotates from the outside. Separate auxiliary drive unit available in case of need to apply moments It is preferable to provide the device with a. The need to add an external rotational moment arises because For example, during start-up or operation of a device that is only partially filled with the ripening material. This occurs when the engine is not running or when the amount of gas generated is insufficient. In that case, the drive unit Compared to the case where the drive unit always bears all the driving force required for ram rotation, It is much smaller, has a simpler structure, and is cheaper. As mentioned above, for the purpose of auxiliary drive A drive unit is shown schematically in FIG. 2 and designated by the reference numeral (35). This drive The unit is used in combination with the control unit described above.

バッフル(21A、 21B 、 21C)は、ドラム駆動機構の一部を形成し ている他に、ドラム(13)の物質移送機構の一部も形成している。この目的の ため、バッフルの両面にはドラムの内面(13C)からバッフルの半径内方長手 自由端縁(22A〜22C)へ延在している立役ガイドリブ(37,38)が設 けられている。各面のリブはほぼ直線状かつ相互に平行となっていて、平行なバ ッフル長手端縁とドラムの中心軸に垂直な平面とに対し鋭角を成している。バッ フルに設けたリブのうち、ドラム(13)の回転方向に向っている(ドラムは第 2図〜第5図で右廻りに回転する)立設リブ(37)は、ドラムの内面(13C )からバッフルの半径内方の長手自由端縁に向って見ると、ドラムの出口端へ向 って斜めに延在している。バッフルの反対面に設けた立設リブ(38)はやはり ドラム内面からバッフルの半径内方の長手自由端縁に向って見るとドラムの出口 端から離反する方向へ斜めに延在している。The baffles (21A, 21B, 21C) form part of the drum drive mechanism. In addition to forming part of the mass transfer mechanism of the drum (13). for this purpose Therefore, on both sides of the baffle, there is a long distance from the inner surface of the drum (13C) to the inside radius of the baffle. Upright guide ribs (37, 38) extending to the free edges (22A to 22C) are provided. I'm being kicked. The ribs on each side are almost straight and parallel to each other, and the ribs are parallel to each other. The longitudinal edge of the ffle forms an acute angle with a plane perpendicular to the central axis of the drum. bag Of the fully provided ribs, the one facing the direction of rotation of the drum (13) The standing rib (37) (which rotates clockwise in Figures 2 to 5) is located on the inner surface of the drum (13C). ) towards the radially inward free longitudinal edge of the baffle, towards the exit end of the drum. It extends diagonally. The standing rib (38) provided on the opposite side of the baffle is still The exit of the drum when viewed from the inner surface of the drum toward the radially inner longitudinal free edge of the baffle. It extends diagonally in a direction away from the end.

熟成物質移送機構はさらにドラムの内面(13C)に固着され立設した数個のリ ブ(39)を左ねじれ状態に延在させて構成される。これらのリブ(39)はド ラムの軸方向のほぼ全長に亘って設けられ、ドラムのほぼ全周に亘って延在して いる。The ripening material transfer mechanism further includes several ribs fixed and erected on the inner surface (13C) of the drum. It is constructed by extending the tube (39) in a left-handed twisted state. These ribs (39) It is provided over almost the entire length of the ram in the axial direction, and extends around almost the entire circumference of the drum. There is.

バッフル(21A、 21B、 21C)およびリブ(37,38゜39)によ って形成された物質移送機構は、主に腐敗不能でありドラム内滞在時間を極力短 くすべき、砂、じやり、金属片等の沈澱しやすい物質に対しドラム内を速やかに 移送させる役目をする。便宜上それらの物質は以下沈澱物質と呼ぶ。懸濁液の最 上部に浮上しゃすく浮滓層(F)の一部を成す物質についてもリブ(38)の作 用により速やかに移送される。Baffles (21A, 21B, 21C) and ribs (37, 38°39) The material transfer mechanism formed by Immediately clean the inside of the drum for substances that tend to settle, such as sand, sand, metal pieces, etc. It serves the purpose of transport. For convenience, these substances are hereinafter referred to as precipitated substances. suspension top Ribs (38) are also created for the material that floats to the top and forms part of the floating slag layer (F). Transported as soon as possible.

物質移送機構の作用について第3図〜第5図と共に以下に説明する。The operation of the substance transfer mechanism will be explained below in conjunction with FIGS. 3 to 5.

ドラムが第3図の位置に位置する停止期間中に、沈澱物質はドラムの最下部に向 ってゆっくり沈下し、この沈澱物質の一部はバッフル(21A)により捕捉され 、別の部分はバッフル(21B)により捕捉され、さらに別の部分はバッフル( 21B)と(2IC)との間に延在しているドラム(13)の内面の一部によっ て捕捉され、さらに別ノ部分カハッフル(21C)の左側に位置するドラムの内 面の一部によって捕捉される。バッフル(21A)によりの長手自由端縁(22 A )へ向って摺動するのと並行して、リブ(38)のドラム出口端に面する側 の側面(38A )により出口端へ向って移動させられる。バッフル(21A  )の長手自由端縁(22A )へ到達すると、この物質の一部がバッフル(21 B)へ落下し、長手自由端縁(22B)の隣接部でこのバッフルにより捕捉され る。同物質のうちにはそこからドラムに内面の最下部分へ垂直平面(C)に隣接 して落下するものもある。During the stop period when the drum is in the position shown in Figure 3, the precipitated material is directed towards the bottom of the drum. , and some of this precipitated material is captured by the baffle (21A). , another portion is captured by the baffle (21B), and yet another portion is captured by the baffle (21B). 21B) and (2IC) by a portion of the inner surface of the drum (13). In addition, another part of the drum located on the left side of Ka Huffle (21C) is captured. Captured by a portion of the surface. Long free edge (22) by baffle (21A) In parallel with sliding towards A), the side of the rib (38) facing the drum exit end is moved towards the outlet end by the side surface (38A) of. Baffle (21A) ), a portion of this material reaches the baffle (21A). B) and is caught by this baffle adjacent to the longitudinal free edge (22B). Ru. Inside the same material adjoin the vertical plane (C) from there to the lowest part of the inner surface of the drum Some things fall.

ドラムが全回転の3分の1だけ右廻りに回転して第4図の位置を通り次の停止位 置へ至ると、その後次に記すごとく作用する。The drum rotates clockwise by one-third of its full rotation and passes through the position shown in Figure 4 to the next stopping position. Once the position is reached, it then operates as described below.

バッフル(21A)表面上に残留していた全ての沈澱物質は上述したごとく摺動 落下して、リブ(37)の側面(37A )によりドラムの出口端に向って移動 される。この沈澱物質がバッフル(21B)に至ると、同バッフルによりすでに 捕捉されていた沈澱物質と共にドラムの内面(13c)へ向って摺動する。この 摺動移動中に沈澱物質はリブ(38)の出口端に面する側面(38A )により ドラム出口端へ向っである距離に亘り偏向される。この時沈澱物質はドラムの内 面の隣接位置に一時的に留める。All precipitated material remaining on the baffle (21A) surface is removed by sliding as described above. It falls and moves towards the exit end of the drum by the side surface (37A) of the rib (37). be done. When this precipitated material reaches the baffle (21B), the baffle has already caused It slides along with the trapped precipitated material towards the inner surface (13c) of the drum. this During the sliding movement, the precipitated material is collected by the side surface (38A) facing the outlet end of the rib (38). It is deflected over a distance towards the drum exit end. At this time, the precipitated material is inside the drum. Temporarily fasten to a position adjacent to a surface.

ドラムの回転中または回転後、ドラムの内面によりバッフル(21B)とバッフ ル(21C)との間で捕捉された沈澱物質の多くはドラム内面に沿っCその時点 で最下位置に位置するドラムの部分へ向って移動する。この時、沈澱物質は、リ ブ(39)のドラム出口端に面する側面(39A )によって出口端へ向って移 動される。During or after the rotation of the drum, the inner surface of the drum causes the baffle (21B) and Most of the precipitated material trapped between the drum (21C) and C to move toward the part of the drum located at the lowest position. At this time, the precipitated material The side surface (39A) facing the drum outlet end of the drum (39) moves the drum toward the outlet end. be moved.

この回転中、ドラムの内面でバッフル(21C)の右廻り先行側で捕捉された沈 澱物質はバッフル(21C)が第3図のバッフル(2LA)の位置に至るまで担 持される。During this rotation, sediment caught on the clockwise leading side of the baffle (21C) on the inner surface of the drum. The sludge material is carried by the baffle (21C) up to the position of the baffle (2LA) in Figure 3. held.

バッフル(21C)がその位置に至ると、この物質の少なくとも一部がバッフル (21C)の表面上をドラムの中心部へ向って移動し始める、。この時、沈澱物 質はバッフルのリブ(37)の側面(37A )によってドラムの出口端へ向っ て偏向される。When the baffle (21C) reaches its position, at least a portion of this material begins to move towards the center of the drum on the surface of (21C). At this time, the precipitate The quality is directed towards the exit end of the drum by the sides (37A) of the ribs (37) of the baffle. is deflected.

回転中、バッフル(21B)の下方で捕捉されて浮環層(F)の一部もバッフル の下面沿いに上向きに摺動移動しく第4図参照)、リブ(37)の側面(37B )は浮環層のこの部分をドラムの出口端へ向って偏向させ、同部分はバッフル( 21B)の自由端縁(22B)から離れて、ドラムの最上部へ上昇するに至る。During rotation, part of the floating ring layer (F) is also caught below the baffle (21B) and the baffle (see Figure 4) and the side surface of the rib (37) (37B). ) deflects this part of the float layer towards the exit end of the drum, and the baffle ( 21B) and rises to the top of the drum, away from the free edge (22B).

この回転作用に続く停止期間およびさらに次の回転作用(ドラムの3分の2回転 終了後に続く回転)中に、上述の分離作用と移送作用とが繰返されて、その後次 の各停止期間と回転作用の間に再び繰返される。This rotational action is followed by a period of rest and a further rotational action (two-thirds of a revolution of the drum). During the subsequent rotation), the above-mentioned separation and transfer actions are repeated, and then the next is repeated again during each stop period and rotation action.

上述の説明から沈澱物質の大部分と浮環層(F)の少ない方のまたは多い方の部 分がドラムの各回転によりドラムの出口端へ向って移動することが明らかである 。沈澱物質の粒子または本体、あるいはドラム(13)へ入口端から進入する軽 比重粒子はドラム中の懸濁液の大部分の滞留時間に比べて短い時間内にドラムを 通過移動することが可能である。From the above explanation, the majority of the precipitated material and the part with less or more floating ring layer (F) It is clear that the minutes move towards the exit end of the drum with each rotation of the drum. . Particles or bodies of precipitated material or light particles entering the drum (13) from the inlet end. Density particles leave the drum within a short time compared to the residence time of the bulk of the suspension in the drum. It is possible to move through.

一バッフルのリブ(37,38)は、他のバッフルのリブおよびドラムの内面の リブ(39)に対し、各リブの最大限の長さ部分がドラム軸方向移送に際して利 用されうるよう配設する必要がある。リブ(37,,3g)の高さは決定的要素 ではないが、例えばドラム半径の0,01〜0.05倍とする。The ribs (37, 38) of one baffle are connected to the ribs of the other baffle and the inner surface of the drum. With respect to the ribs (39), the maximum length of each rib is utilized for axial transfer of the drum. It is necessary to arrange it so that it can be used. The height of the rib (37, 3g) is the deciding factor However, it is, for example, 0.01 to 0.05 times the drum radius.

ドラムの出口端の隣接部ではバッフル(21A〜21C)およびリブ(37〜3 9)の形状が図示はしていないが沈澱物質と浮環層(F)が出口管(19)に向 いドラム(13)からハウジング(11)内部または近傍に設けた図示されない 畳込部へと移送されるような形状に変更されている。Adjacent to the exit end of the drum are baffles (21A-21C) and ribs (37-3 Although the shape of 9) is not shown, the precipitated material and floating ring layer (F) are directed toward the outlet pipe (19). (not shown) provided inside or near the housing (11) from the drum (13). The shape has been changed so that it can be transferred to the convolution section.

熟成処理された物質もドラム(13)からこの畳込部内へ排出される。ドラムの 仕切壁(20)の近傍においてもやはりバッフルとリブの形状が同様に変更され 沈澱物質と浮環層(F)とが仕切部の中央開口部へ移送され同開口部を通って移 送される。The aged material is also discharged from the drum (13) into this convolution. drum's The shapes of the baffles and ribs were similarly changed near the partition wall (20). The precipitated material and the floating ring layer (F) are transferred to and through the central opening of the partition. sent.

再循環管(40)が熟成用ドラム(13)の中心軸に沿って延在し、図示してい ない方法で全体があるいはほぼ全体が熟成された物質の一部をドラムの出口端近 傍位蓋から入口端近傍位置まで再循環させるようになっている。A recirculation pipe (40) extends along the central axis of the aging drum (13) and is not shown. A portion of the material that has been wholly or nearly wholly aged in a manner that does not Recirculation is provided from the proximal lid to a position near the inlet end.

再循環された物質は新たに供給された物質の接種材料として作用し供給された物 質の熟成作用を促進する。The recycled material acts as an inoculum for the newly supplied material and Promotes quality ripening.

上述した図示の実施例では一定角度で離間した3つのバッフル(21A〜21C )を備えている。この構成が少なくとも特定の場合には好ましいことが判明して いる。しかし、異なる数のバッフルを設け、図示し既述したものと異なる形状お よび異なる配置に構成することも本発明の範囲に包含される。例えばバッフルの 断面について別゛の状態に屈曲させたり傾斜させたりしてもよいし、バッフルの 半径外方長手端縁を通る半径(R,R,R)BC と成す角度を広範囲内で変更してもよい。既述の実施例では、バッフルがこの半 径(R,R,R)かう回ABC 転方向ヘズしているが、必要に応じ反対方向ヘズラしてもよい。好ましくは、バ ッフルと各半径との成す角度を+/−30度未満とする。In the illustrated embodiment described above, there are three baffles (21A to 21C) spaced apart at a constant angle. ). This configuration has been found to be preferable, at least in certain cases. There is. However, a different number of baffles and a different shape and shape than those shown and described above may be used. It is also within the scope of the present invention to configure it in a different arrangement. For example, the baffle The cross section may be bent or inclined in a different state, or the baffle Radius passing through the outer longitudinal edge (R, R, R) BC The angle formed by this may be varied within a wide range. In the embodiment described, the baffle is Diameter (R, R, R) Rotation ABC Although it is deflected in the direction of rotation, it may be deflected in the opposite direction if necessary. Preferably, The angle between the fuffle and each radius is less than +/-30 degrees.

上述の処理物質移送機構はドラムが連続回転または小きざみに間欠回転する場合 にも有用である。ドラムが外部駆動機構により回転させられる場合にも有用であ る。The above-mentioned processing material transfer mechanism is used when the drum rotates continuously or intermittently in small steps. It is also useful. Also useful when the drum is rotated by an external drive mechanism. Ru.

さらに上述のドラム回転発生機構は物質移送機構と独立して利用することもでき る。Furthermore, the drum rotation generation mechanism described above can also be used independently of the material transfer mechanism. Ru.

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Claims (1)

【特許請求の範囲】 〔1〕自軸を中心に回転可能であり、一端に物質供給用入口を、他端に物質排出 用出口を有し、内部に物質移送手段が固着された長手水平処理ドラムから成る、 特に懸濁液中に含有された有機物の醗酵熟成処理等のガス発生処理用の装置にお いて、前記物質移送手段はドラム(13)の長手方向に離隔し前記ドラムの横断 平面と鋭角を成す複数のガイドリブ(37,38,39)を包含し、同ガイドリ ブは前記ドラムの長手方向へ延在してドラムに固定された支持面(21A,21 B,21C,13C)に固着され、前記ドラム内に沈澱し前記ガイドリブの側面 (37A,38A,39A)により捕捉された粒子を前記側面によりドラムの前 記他端へ向って偏向させるよう配設されている装置。 〔2〕一群の前記ガイドリブ(37)を支持する前記支持面(21A〜21C) が前記ドラムの内面に固着されドラムの反対側内面へ向って延在しているバッフ ルの前面から成る、請求の範囲第1項記載の装置。 〔3〕一群の前記ガイドリブまたは別の一群の前記ガイドリブの支持面(13C )が前記ドラム(13)の円周内面である、請求の範囲第1項または第2項記載 の装置。 〔4〕別の複数のガイドリブ(38)が前記ドラム(13)の長手方向に離隔し 、ドラムの横断平面と鋭角を成して前記バッフル(21A,21B,21C)の 裏面に固着され、前記ドラム内に沈澱し前記別の複数のガイドリブ(38)の側 面(38A)により捕捉した粒子を前記側面(38A)によってドラムの前記他 端へ向うよう偏向させるようになっている、請求の範囲第2項または第2項に従 属する第3項に記載の装置。 〔5〕前記バッフル(21A,21B,21C)とドラムの前記他端に隣接する 前記ガイドリブ(37,38,39)はさらに前記粒子を前記ドラムの中央区域 (19)へ向うよう偏向させるようになっている、請求の範囲第2項または第2 項に従属する第3項、または第4項記載の装置。 〔6〕自軸を中心に回転可能な長手水平処理ドラムと、懸濁液を注入・排出する 手段と、前記ドラム内で発生したガスを捕集する手段とから成り、特に懸濁液に 含有される有機物の醗酵熟成処理等のガス発生処理用の装置であって、前記ドラ ム内に取付けたバッフル(21A,21B,21C)がドラムの複数の角変位位 置に配設されて前記ドラム(13)の内面と協働で、前記ドラムの中心軸(L) を包含する垂直平面(C)から離隔し下方向へ開口しているガス捕集空間(25 A)を形成している請求の範囲第1項から第5項のいずれか一項記載の装置。 〔7〕前記バッフル(21A,21B,21C)は、前記ドラムの中心軸から離 間した軸方向平面位置に固着されドラムの前記内面(13C)から軸方向線部( 22A,22B,22C)へ向って延在し、ドラムの内面(13C)から前記軸 方向線部までの距離がドラム半径の小さくとも0.5倍となっている、請求の範 囲第6項記載の装置。 〔8〕前記バッフル(21A,21B,21C)は前記ドラム(13)のほぼ全 長に亘って延在している、請求の範囲第6項または第7項記載の装置。 〔9〕前記バッフル(21A,21B,21C)の数は3つであり、円周方向へ 等間隔で離間している、請求の範囲第6項から第8項記載の装置。 〔10〕前記ドラムの中心軸(L)を包含する垂直平面(C)について前記ガス 捕集空間のある側と反対側で発生したガスをガス捕集空間(25A)へ移送する 導管手段(27)を有する、請求の範囲第6項から第9項のいずれか一項記載の 装置。 〔11〕前記ドラム(13)を前記角変位位置の各々で一時的に停止させる手段 (35)を有する、請求の範囲第6項から第11項のいずれか一項記載の装置。 〔12〕前記角変位位置と前記バッフル(21A,21B,21C)とは同数で あり、円周方向へ等間隔に離間している、請求の範囲第6項から第11項のいず れか一項記載の装置。 〔13〕全ての前記バッフル(21A,21B,21C)は前記角変位位置にお いて水平面とある角度を成している、請求の範囲第6項から第12項のいずれか 一項記載の装置。[Claims] [1] It can rotate around its own axis, with a material supply inlet at one end and a material discharge port at the other end. consisting of a longitudinal horizontal processing drum having an outlet for use and having a material transfer means affixed therein; Particularly suitable for gas generation processing equipment such as fermentation and maturing processing of organic matter contained in suspensions. and the material transfer means are spaced apart longitudinally of the drum (13) and transversely of the drum (13). It includes a plurality of guide ribs (37, 38, 39) forming acute angles with the plane, and the guide ribs (37, 38, 39) The support surface (21A, 21 B, 21C, 13C), deposited in the drum and formed on the side surface of the guide rib. The particles captured by (37A, 38A, 39A) are transferred to the front of the drum by the side surface. A device arranged to deflect the beam toward the other end. [2] The support surface (21A to 21C) that supports a group of the guide ribs (37) a buff fixed to the inner surface of the drum and extending toward the opposite inner surface of the drum; 2. The device of claim 1, comprising a front surface of a wall. [3] Support surface of one group of said guide ribs or another group of said guide ribs (13C ) is the circumferential inner surface of the drum (13), according to claim 1 or 2. equipment. [4] Another plurality of guide ribs (38) are spaced apart from each other in the longitudinal direction of the drum (13). , of the baffles (21A, 21B, 21C) forming an acute angle with the transverse plane of the drum. adhered to the back surface, deposited in the drum, and on the side of the other plurality of guide ribs (38). The particles captured by the surface (38A) are transferred to the drum by the side surface (38A). According to claim 2 or 2, the device is adapted to be deflected towards an end. Apparatus according to paragraph 3 below. [5] Adjacent to the baffle (21A, 21B, 21C) and the other end of the drum The guide ribs (37, 38, 39) further direct the particles to the central area of the drum. (19) Apparatus according to sub-clauses 3 or 4. [6] Longitudinal horizontal processing drum that can rotate around its own axis and injects and discharges suspension. and means for collecting the gas generated in said drum, especially for suspensions. An apparatus for gas generation treatment such as fermentation and ripening treatment of organic matter contained, the device comprising: Baffles (21A, 21B, 21C) installed inside the drum allow multiple angular displacements of the drum. The central axis (L) of the drum (13) A gas collection space (25 6. A device according to any one of claims 1 to 5, forming: A). [7] The baffles (21A, 21B, 21C) are spaced apart from the central axis of the drum. The axial line portion ( 22A, 22B, 22C), and the shaft extends from the inner surface (13C) of the drum. Claims in which the distance to the direction line portion is at least 0.5 times the drum radius 6. The device according to paragraph 6. [8] The baffles (21A, 21B, 21C) cover almost the entire drum (13). 8. A device according to claim 6 or 7, extending over a length. [9] The number of the baffles (21A, 21B, 21C) is three, and in the circumferential direction 9. Apparatus according to claims 6 to 8, which are equidistantly spaced. [10] The gas about the vertical plane (C) that includes the central axis (L) of the drum Transfer the gas generated on the side opposite to the collection space to the gas collection space (25A) 9. A device according to any one of claims 6 to 9, comprising conduit means (27). Device. [11] Means for temporarily stopping the drum (13) at each of the angular displacement positions (35) The device according to any one of claims 6 to 11. [12] The angular displacement position and the baffles (21A, 21B, 21C) are the same in number. any of claims 6 to 11, which are arranged at equal intervals in the circumferential direction. The device described in any one of the above. [13] All the baffles (21A, 21B, 21C) are in the angular displacement position. Any one of claims 6 to 12, which forms a certain angle with a horizontal plane. The device according to paragraph 1.
JP61501667A 1985-03-08 1986-03-07 Organic gas generation treatment equipment Pending JPS62502109A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8501167-4 1985-03-08
SE8501167A SE451324B (en) 1985-03-08 1985-03-08 GASAL BEACH TREATMENT, SEPARATELY ROTATING OR YEASTING, OF ORGANIC MATERIAL INCLUDED IN A FLUID SLIDE

Publications (1)

Publication Number Publication Date
JPS62502109A true JPS62502109A (en) 1987-08-20

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP61501667A Pending JPS62502109A (en) 1985-03-08 1986-03-07 Organic gas generation treatment equipment

Country Status (8)

Country Link
EP (1) EP0253815A1 (en)
JP (1) JPS62502109A (en)
KR (1) KR870700060A (en)
AU (1) AU5622386A (en)
BR (1) BR8607081A (en)
OA (1) OA08654A (en)
SE (1) SE451324B (en)
WO (1) WO1986005171A1 (en)

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Publication number Priority date Publication date Assignee Title
EP0374708A1 (en) * 1988-12-13 1990-06-27 Josef Probst Biogas reactor
DE4119798A1 (en) * 1991-06-15 1992-12-17 Adolf Prof Dipl Ing Voss METHOD FOR THE PRODUCTION OF BIOGAS AND USE OF A MIXER AS A BIOGAS PLANT
AUPM452094A0 (en) * 1994-03-17 1994-04-14 University Of Queensland, The Waste treatment plant and process
DE19733813A1 (en) * 1997-08-05 1999-02-11 Humunite Holding Ltd Method and device for extracting biogas
DK2477747T3 (en) * 2009-09-15 2019-05-13 Renescience As Enzymatic treatment of household waste
DE102012015908A1 (en) * 2012-08-10 2014-05-15 Jan Kuclo Continuous biochemical conversion of biomass for producing biogas with large optimization of the conversion method into narrow boundaries provided by the surrounding, comprises e.g. preparing and heating the biomass into a charging lock
WO2019243664A1 (en) * 2018-06-18 2019-12-26 Eneferm Oy Device and method for treating biomass

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU54404A1 (en) * 1967-08-30 1969-06-10
FI66338C (en) * 1982-12-09 1984-10-10 Ahlstroem Oy the bioreactor

Also Published As

Publication number Publication date
KR870700060A (en) 1987-02-28
OA08654A (en) 1988-11-30
SE451324B (en) 1987-09-28
AU5622386A (en) 1986-09-24
EP0253815A1 (en) 1988-01-27
BR8607081A (en) 1988-01-19
WO1986005171A1 (en) 1986-09-12
SE8501167L (en) 1986-09-09
SE8501167D0 (en) 1985-03-08

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