JPS61500062A - Equipment for anaerobic fermentation - Google Patents
Equipment for anaerobic fermentationInfo
- Publication number
- JPS61500062A JPS61500062A JP59503571A JP50357184A JPS61500062A JP S61500062 A JPS61500062 A JP S61500062A JP 59503571 A JP59503571 A JP 59503571A JP 50357184 A JP50357184 A JP 50357184A JP S61500062 A JPS61500062 A JP S61500062A
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- JP
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- fermentation
- liquid
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- spaces
- section
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
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- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Fertilizers (AREA)
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】 嫌気性発酵用装置 本発明は嫌気性発酵用装置及びその装置内で実施する嫌気性発酵方法に関する。[Detailed description of the invention] Equipment for anaerobic fermentation The present invention relates to an apparatus for anaerobic fermentation and an anaerobic fermentation method carried out within the apparatus.
水性液体廃棄物や廃液の液体基質の嫌気発酵は公知の方法である。通例かかる方 法は、液体M質を連続的または半連続的に密閉発酵容器へ供給し、その容器内で 該液体基質を多くは温間にて嫌気発酵させ、気体生成物(通常はメタン)を製造 するものである。発酵作用中に−は、固体物質や非発酵性物質および発酵残留物 がスラッジとして空間の底に沈澱し、余分な発酵済み液体基質は発酵容器から除 去される。発酵作用を行なう際、容器中の液体はほぼ静止状態かまたは撹拌状態 となっている。このような方法における問題点は、発酵に預かる微生物を担持し ている固体物質の粒子が容器内の液体本体と共に特に発酵作用中←二発生するカ スの浮上作用により上方向へ飛沫同伴してしまうことである。。Anaerobic fermentation of liquid substrates from aqueous liquid wastes and effluents is a known method. Those who usually take The method involves supplying liquid M continuously or semi-continuously to a closed fermentation container, and then Anaerobic fermentation of the liquid substrate, often at warm temperatures, to produce a gaseous product (usually methane) It is something to do. During the fermentation process - solid substances, non-fermentable substances and fermentation residues will settle to the bottom of the space as sludge and excess fermented liquid substrate will be removed from the fermentation vessel. be removed. During the fermentation process, the liquid in the container is either almost static or stirred. It becomes. The problem with this method is that it does not support the microorganisms involved in fermentation. Particles of solid substances that are present together with the liquid body in the container are particularly susceptible to the forces generated during the fermentation process. This is because the droplets are entrained upward due to the floating action of the droplets. .
本発明によれば、化学工業において、例えば蒸溜塔、除θ塔、加湿装置等におけ る流体/流体接触装置で用いる流体/流体接触エレメント片を無作為または規則 的に配列して形成した層である充填物の液体透過層を用いて液体による固体物質 粉′子の飛沫同伴を明止することができる。According to the present invention, in the chemical industry, for example, distillation towers, removal θ towers, humidification equipment, etc. Fluid/fluid contact element pieces used in fluid/fluid contact devices can be arranged randomly or regularly. A liquid-permeable layer of a packed material is formed by arranging the liquid into a solid material. Entrainment of powder droplets can be eliminated.
こうした流体/流体接触エレメントは格子状、管状、シート状等の規則的形状を 成していてもよい。しかし、好ましい流体/流体接触エレメントはラーシッピリ ング、レシンブリング、パルリング(Pall)、テレリートリング(Tell erete) 、クラ(B erlやI ntalox)やカスケードミニリン グ(直径より全長の方が短いリング)等の分離エレメントである。流体/流体接 触エレメントが分離エレメントである場合、充填材料層(バッキング層)は有孔 支持部に支持された無作為的配列したエレメント層で形成するのが好ましい。These fluid/fluid contact elements have regular shapes such as grids, tubes, sheets, etc. may be completed. However, the preferred fluid/fluid contact element is ring, resing ring, pal ring (Pall), tell ring (Tell) erete), Kula (Berl and Intalox) and cascade minirin (a ring whose overall length is shorter than its diameter). Fluid/Fluid contact If the contact element is a separating element, the layer of filling material (backing layer) is perforated. Preferably, it is formed of a randomly arranged layer of elements supported on a support.
本発明の目的は、複数の発酵区域を包含し各々の発酵区域が上述した充填材料層 を包含して成る嫌気性発酵容器を提供することにある。It is an object of the invention to include a plurality of fermentation zones, each fermentation zone having a layer of packed material as described above. An object of the present invention is to provide an anaerobic fermentation vessel comprising:
本発明による嫌気性発酵用装置は、はぼ水平方向の長手中心線を有し、1対の端 板で密閉されているほぼ円筒状の外被部と、この外被部の幅および長さ方向に延 びて外被部の内部を重なり合う2つの空間に分割している仕切部であって、各々 の空間には充填材料から成るほぼ水平方向の液体透過層が横切って延び上段部と 下段部とに分割するようになっている仕切部と、液体基質を各空間の各下段部に 導入する手段と、各下段部からスラッジを除去する手段と、各上段部からガスを 除去する手段と、各上段部から発酵処理済み液体を除去する手段とから成る。The apparatus for anaerobic fermentation according to the present invention has a longitudinal centerline in a substantially horizontal direction, and has a pair of ends. A nearly cylindrical envelope sealed by a plate and extending in the width and length direction of this envelope. A partition section that extends and divides the interior of the outer covering section into two overlapping spaces, each of which has a A generally horizontal liquid-permeable layer of filler material extends across the space between the upper and A partition section that divides the space into a lower section and a liquid substrate into each lower section of each space. means for introducing gas, means for removing sludge from each lower section, and means for introducing gas from each upper section. and means for removing the fermented liquid from each upper stage.
発酵用装置の外被部を2つの空間に分割している仕切部は平らであってもよいが 、好ましくは図示したごとく外被部の幅方向断面が円弧状となるよう形成するの が好ましい。The partition dividing the outer shell of the fermentation device into two spaces may be flat; , Preferably, the cross section of the outer covering portion in the width direction is formed in an arc shape as shown in the figure. is preferred.
このように断面円弧状に形成した場合、仕切部は断面が下方向に窪むように湾曲 しているのが好ましい。When formed with an arcuate cross section in this way, the partition section is curved so that the cross section is concave downward. It is preferable to do so.
さらに、充填材料層の下方における液体の平均深度は100〜3000mmとす るのがよいが、より好ましくは200〜1500mmどする。液体深度を約15 00mm以下とすれば、発酵用装置の単位体積当りの発酵速度は増加し、一方3 000n+m以上とした場合には発酵速度が有効程度にまで増加しない。すなわ ち、反応容器中の充填材料層下の液体総量を一定量以上に増加させた場合、単位 体積当りの総体発酵速度がそれに伴なって増加することはない。Furthermore, the average depth of the liquid below the filling material layer is 100 to 3000 mm. The length is preferably 200 to 1500 mm. Liquid depth about 15 00 mm or less, the fermentation rate per unit volume of the fermentation device increases; 000 n+m or more, the fermentation rate will not increase to an effective level. Sunawa In other words, if the total amount of liquid under the filling material layer in the reaction vessel is increased beyond a certain amount, the unit There is no corresponding increase in the overall fermentation rate per volume.
本発明が充分に理解しうるよう、以下において図面の説明をする。BRIEF DESCRIPTION OF THE DRAWINGS In order that the present invention may be fully understood, the following description of the drawings is provided.
第1図は本発明による発酵用装置の幅方向断面図、第2図は第1図に示ず装置の 発酵用装置の長手方向断面図9 図示したごとく、本発明による発酵用装置は1対の端板(2,2a)により密閉 されたほぼ円筒状の外被部(1)から成る。下方向で窪んでいる円弧状仕切部( 3)がこの外被部り1〉の全幅に亘って延在し、外被部内部を下方空間と下方空 間と′に分割している。上・下面空間の各々は有効支持体(7a、7b )で支 持されている無作為配列の分離した流体/流体接触エレメントから成る液体透過 層(6a、6b )により上方のガスゾーン(4a、4b )と、下方の液体ゾ ーン(5a、5b )とに分割されている。ガスゾーン(4a、4b ) ’r よ端板〈2)に設(プたポートを介してバルブ付ガス排出導管(8)に連結され ている。1組の液体供給パイプ(9a、9b )が液体ゾーン(5a、5b ) の全長に亘って延在し、端板(2)を貫通してマニホールド(図示せず)に連結 し、さらにバルブ付液体供給導管(図示せず)に連結している。各液体供給パイ プ(9a、9b )には該パイプから液体ゾーン(5a、5b)中・\液体を放 出する孔やノズルが設けられている。該ノズルや孔は液体が液体ゾーン中へ水平 方向または下方向へ放出されるよう配設されている。Figure 1 is a cross-sectional view in the width direction of a fermentation apparatus according to the present invention, and Figure 2 is a cross-sectional view of the apparatus not shown in Figure 1. Longitudinal sectional view 9 of the fermentation device As shown, the fermentation apparatus according to the present invention is sealed by a pair of end plates (2, 2a). It consists of a substantially cylindrical outer covering part (1). An arc-shaped partition that is concave at the bottom ( 3) extends over the entire width of this outer covering part 1〉, and connects the inside of the outer covering part to the lower space and the lower air. It is divided into between and ′. Each of the upper and lower spaces is supported by effective supports (7a, 7b). Liquid permeation consisting of a random array of separate fluid/fluid contacting elements The layers (6a, 6b) separate the upper gas zone (4a, 4b) from the lower liquid zone. It is divided into zones (5a, 5b). Gas zone (4a, 4b)’r It is connected to the gas exhaust conduit (8) with a valve through the port located on the end plate (2). ing. One set of liquid supply pipes (9a, 9b) is connected to the liquid zone (5a, 5b) extending the entire length of the plate and passing through the end plate (2) to connect to the manifold (not shown). and is further connected to a valved liquid supply conduit (not shown). Each liquid supply pipe The liquid in the liquid zone (5a, 5b) is released from the pipe (9a, 9b). There is a hole or nozzle for ejecting the water. The nozzle or hole allows the liquid to flow horizontally into the liquid zone. arranged to emit in a direction or downward direction.
液体ゾーン(5a、5b )を通ってスラッジ排出パイプ(10a、10b ) が設けられ、液体供給パイプ(9a、9b )より下方でかつ各液体ゾーン(5 a、5b )の底部に近接して配設されている。スラッジ排出パイプ(10a、 10b )は端板(2)を貫通して延び、好適なバルブ付スラッジ排出導F’< Ila、1lb)に連絡している。Sludge discharge pipe (10a, 10b) through the liquid zone (5a, 5b) is provided below the liquid supply pipes (9a, 9b) and in each liquid zone (5). a, 5b) is disposed close to the bottom. Sludge discharge pipe (10a, 10b) extends through the end plate (2) and has a suitable valved sludge discharge conduit F'< Ila, 1lb).
充填材11層(ea、6b )の上部には各々上方に開[1した溝部(12a、 12b )が外被部(1)の長手方向に延びていて、端板(2)に設けたポート ・を介してバルブ付液体排出導管□(13a、13b )に連結されている。溝 部(12a、12b )の上方縁は発酵用装置の2つの空間の各々における液体 上面を決め、発酵処理済みの液体を空間から除去する堰とし−C作用している。At the top of the 11 layers (ea, 6b) of the filler material, there are grooves (12a, 12a, 12b) that are open upward. 12b) extends in the longitudinal direction of the outer jacket part (1) and has a port provided in the end plate (2). ・It is connected to the liquid discharge conduit □ (13a, 13b) with a valve. groove The upper edges of the sections (12a, 12b) are arranged so that the liquid in each of the two spaces of the fermentation device The upper surface is defined and acts as a weir to remove the fermented liquid from the space.
本発明による装置の作用時には、スラッジが(破線(14a、14b )で示す ごとく)各液体ゾーン(5a、5b )の下部に堆積し、この堆積レベルの上方 から充填材料層の下面までの高さが該充填材料層−下方の液体の有効平均深度と なり、好ましくけずでに述べたとおり200〜1500mmである。During operation of the device according to the invention, the sludge (shown by dashed lines (14a, 14b)) ) is deposited at the bottom of each liquid zone (5a, 5b) and above this deposition level. The height from The length is preferably 200 to 1500 mm as described in the introduction.
外被部(1)の直径は2〜4mとし、好ましくは約3mであり、該外被部(1) の全長は例えは5〜30mで好ましくは10〜20mである。しかして、本発明 の発酵用装置は2つの発酵区域を包含して構成単位を成しており、この構成単位 は容易に製作でき、現場以外の場所での組立てが可能であり、組立て後所定の場 所へ移送できる。さらに、全体の発酵設備は、本発明による複数の発酵用装置か ら構成することができ、各構成単位の数は発酵すべき基質の総量に基づいて決ま る。The outer covering part (1) has a diameter of 2 to 4 m, preferably about 3 m, and the outer covering part (1) The total length is, for example, 5 to 30 m, preferably 10 to 20 m. However, the present invention The fermentation equipment includes two fermentation zones and forms a unit, and this unit is easy to manufacture, can be assembled off-site, and can be moved to the designated location after assembly. It can be transported to a location. Furthermore, the entire fermentation facility may consist of multiple fermentation devices according to the present invention. The number of each building block is determined based on the total amount of substrate to be fermented. Ru.
作用時には、液体供給が仕切部(3)によって形成されるト・′上空間の各々へ 流体供給パイプ(9a、 9b)を介して行なわれ、各液体ゾーン(5a、 5 b)を通って上方に流れくここにおいて発酵作用を成し)続いて充填材料層(6 a。In operation, the liquid supply is directed to each of the upper spaces formed by the partitions (3). This is done via the fluid supply pipes (9a, 9b), and each liquid zone (5a, 5 b) flows upwardly through the layer of filling material (6) where the fermentation action takes place) a.
6())を通り、発酵処理済み液体は溝(12a、12b )を介して排出され 、発酵1により発生したガスはガス排出導管(8a。6 ()), the fermented liquid is discharged through the grooves (12a, 12b). , the gas generated by fermentation 1 is discharged through the gas exhaust conduit (8a).
8b)を介して排出される。スラッジは下方の液体ゾーン(5a、 5b)から スラッジ排出パイプ(10a、10b )により、概ね断続的に除去される。8b). Sludge comes from the lower liquid zone (5a, 5b) The sludge is removed intermittently by the sludge discharge pipes (10a, 10b).
本発明による発酵用装置を用いて実施される発酵方法は適切な温度下、例えば1 0〜70℃で実施でき、その場合、発酵用装置の上下両空間には、内部または外 部の加熱手段が設けられ、さらに外被部(1)には外部断熱材が設けられている 。The fermentation process carried out using the fermentation device according to the invention is carried out at a suitable temperature, e.g. It can be carried out at a temperature of 0 to 70°C, and in that case, both the upper and lower spaces of the fermentation equipment are The outer covering part (1) is further provided with an external heat insulating material. .
本発明によって発酵されるのに適する基質には、クエン酸製造による廃液、製紙 パルプ製造による廃液、糖蜜発酵による廃液、食用油製造業及び乳製品、医薬品 、醸造品、食料品等の製造業による廃液等が含まれる。Substrates suitable to be fermented according to the invention include effluent from citric acid production, paper manufacturing Waste liquid from pulp manufacturing, waste liquid from molasses fermentation, edible oil manufacturing industry, dairy products, pharmaceuticals This includes waste liquid from manufacturing industries such as brewing products and foodstuffs.
本発明は内部仕切部により単に′1対の区域に分割された発酵用装置について説 明したが、例えば1対の仕切部を用いて3つの空間に分割し、各空間に流体/流 体接触エレメントから成る液体透過層と、液体を供給および除去する適切な手段 と、スラッジの排出手段およびガス除去手段とを゛設けて構成してもよい。The present invention describes a fermentation device that is divided into just a pair of zones by an internal partition. As explained above, for example, a pair of partitions can be used to divide the space into three spaces, and each space can be divided into three spaces. a liquid-permeable layer consisting of body-contacting elements and suitable means for supplying and removing liquid; , a sludge discharge means, and a gas removal means may be provided.
本発明による発酵用装置を利用すれば、2つの別々の発酵方法を異なる基質につ いて実施することが可能となる。Using the fermentation device according to the invention, two separate fermentation methods can be carried out on different substrates. This makes it possible to implement the system.
または、発酵用装置の発酵作用部を順次連結して単一の基質について順次発酵を 行なってもよい。Alternatively, the fermentation units of fermentation equipment can be sequentially connected to sequentially ferment a single substrate. You may do so.
浄書(内容に変更なし) 手続ネ市正書(方式) %式% 2、発明の名称 嫌気性発酵用装置 3、補正をする者 事件との関係 特許出願人 名 称 バイオマス・リミテッド 5、補正命令の日付 昭和60年10月22日(発送日〉6、補正の対象 特許法第184条の5第1項の規定による書面、(特許出願人の代表者の欄) 願書翻訳文 (■欄の1英国民Jを削除、 ■欄のし韓国」の≠;千中追加)、 国際調査報告Engraving (no changes to the content) Procedure Ne City Official Book (Method) %formula% 2. Name of the invention: Anaerobic fermentation device 3. Person who makes corrections Relationship to the incident: Patent applicant Name Biomass Limited 5. Date of amendment order: October 22, 1985 (shipment date) 6. Subject of amendment Document pursuant to the provisions of Article 184-5, Paragraph 1 of the Patent Law (column for representative of patent applicant) Application translation (Delete 1 British citizen J in column ■, ■Column ``Korea'' ≠; Senchu added), international search report
Claims (1)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8325286 | 1983-09-21 | ||
GB8325286A GB2149815A (en) | 1983-09-21 | 1983-09-21 | Anaerobic fermenter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61500062A true JPS61500062A (en) | 1986-01-16 |
JPH0461715B2 JPH0461715B2 (en) | 1992-10-01 |
Family
ID=10549095
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59503571A Granted JPS61500062A (en) | 1983-09-21 | 1984-09-21 | Equipment for anaerobic fermentation |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0156866A1 (en) |
JP (1) | JPS61500062A (en) |
KR (1) | KR920001260B1 (en) |
AU (1) | AU3431484A (en) |
BR (1) | BR8407073A (en) |
ES (1) | ES536168A0 (en) |
GB (1) | GB2149815A (en) |
GR (1) | GR80446B (en) |
IT (1) | IT1176753B (en) |
WO (1) | WO1985001282A1 (en) |
ZA (1) | ZA847433B (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4248972A (en) * | 1979-11-08 | 1981-02-03 | Universal Research And Development Corp. | Stacked modules for anaerobic digestion |
EP0084042A1 (en) * | 1981-07-24 | 1983-07-27 | McKEOWN, Kevin Joseph | Anaerobic fermentation |
US4579654A (en) * | 1982-06-25 | 1986-04-01 | Corite Investments Ltd. | Apparatus for the anaerobic fermentation of organic waste material such as liquid manure |
US4613433A (en) * | 1982-12-24 | 1986-09-23 | Biomass Limited | Anaerobic fermentor |
-
1983
- 1983-09-21 GB GB8325286A patent/GB2149815A/en not_active Withdrawn
-
1984
- 1984-09-21 ZA ZA847433A patent/ZA847433B/en unknown
- 1984-09-21 GR GR80446A patent/GR80446B/en unknown
- 1984-09-21 EP EP84903555A patent/EP0156866A1/en not_active Withdrawn
- 1984-09-21 JP JP59503571A patent/JPS61500062A/en active Granted
- 1984-09-21 BR BR8407073A patent/BR8407073A/en unknown
- 1984-09-21 IT IT2276184A patent/IT1176753B/en active
- 1984-09-21 WO PCT/GB1984/000323 patent/WO1985001282A1/en not_active Application Discontinuation
- 1984-09-21 ES ES536168A patent/ES536168A0/en active Granted
- 1984-09-21 KR KR1019850700048A patent/KR920001260B1/en not_active IP Right Cessation
- 1984-09-21 AU AU34314/84A patent/AU3431484A/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
GB8325286D0 (en) | 1983-10-26 |
ZA847433B (en) | 1985-05-29 |
IT8422761A1 (en) | 1986-03-21 |
KR850700029A (en) | 1985-10-21 |
IT1176753B (en) | 1987-08-18 |
AU3431484A (en) | 1985-04-11 |
GB2149815A (en) | 1985-06-19 |
KR920001260B1 (en) | 1992-02-08 |
BR8407073A (en) | 1985-08-13 |
IT8422761A0 (en) | 1984-09-21 |
GR80446B (en) | 1985-01-23 |
JPH0461715B2 (en) | 1992-10-01 |
WO1985001282A1 (en) | 1985-03-28 |
ES8602111A1 (en) | 1985-11-01 |
EP0156866A1 (en) | 1985-10-09 |
ES536168A0 (en) | 1985-11-01 |
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