JPH04310292A - Treatment of methanol-containing waste water - Google Patents
Treatment of methanol-containing waste waterInfo
- Publication number
- JPH04310292A JPH04310292A JP3103420A JP10342091A JPH04310292A JP H04310292 A JPH04310292 A JP H04310292A JP 3103420 A JP3103420 A JP 3103420A JP 10342091 A JP10342091 A JP 10342091A JP H04310292 A JPH04310292 A JP H04310292A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- methanol
- methane fermentation
- fermentation treatment
- seed
- 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.)
- Granted
Links
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000002351 wastewater Substances 0.000 title claims abstract description 20
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000010802 sludge Substances 0.000 claims abstract description 56
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000000855 fermentation Methods 0.000 claims abstract description 16
- 230000004151 fermentation Effects 0.000 claims abstract description 16
- 239000008187 granular material Substances 0.000 claims description 18
- 230000029087 digestion Effects 0.000 claims description 3
- 238000003672 processing method Methods 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 22
- 241000203353 Methanococcus Species 0.000 abstract description 5
- 230000001174 ascending effect Effects 0.000 abstract 1
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 8
- 241000205276 Methanosarcina Species 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000000123 paper Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 241000205011 Methanothrix Species 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000002655 kraft paper Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241001478240 Coccus Species 0.000 description 1
- 241000205286 Methanosarcina sp. Species 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- Y02W10/12—
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は食品、化学、紙パルプ工
業等より排出されるメタノールを含む有機性廃水を対象
とした上向流式嫌気性汚泥床法(UpflowAnae
robic Sludge BlanketProce
ss, 以後UASB法と記す。)に関するものであ
る。[Industrial Application Field] The present invention is an upflow anaerobic sludge bed method (Upflow Anaerobic Sludge Bed Process) for organic wastewater containing methanol discharged from food, chemical, pulp and paper industries, etc.
robic Sludge BlanketProce
ss, hereinafter referred to as the UASB method. ).
【0002】0002
【従来の技術】メタノールを含有する有機廃水は食品、
化学、紙パルプ工業等に見られる。特に、紙パルプ工業
において高温で排出されるクラフトパルプドレン廃水中
にはメタノールが多く含まれており、高温メタン発酵処
理の適用性が高い。メタノールを高温(50〜55℃)
で資化できるメタン菌はメタノサルシナ属、メタノコッ
カス属に限定される。これらの菌は球状の形態をしてい
るため、UASB法において嫌気性消化汚泥を種汚泥と
してスタートアップするとグラニュール化しにくく、通
常は固定床メタン発酵処理が適用されていた。(紙パル
プ技術タイムズ 昭和63年8月 P66〜P70
)[Prior art] Organic wastewater containing methanol is
Found in the chemical, paper and pulp industries, etc. In particular, kraft pulp drain wastewater discharged at high temperatures in the pulp and paper industry contains a large amount of methanol, making it highly applicable to high-temperature methane fermentation treatment. Methanol at high temperature (50-55℃)
The methane bacteria that can be assimilated are limited to the genus Methanosarcina and Methanococcus. Since these bacteria have a spherical shape, they are difficult to turn into granules when starting up with anaerobic digestion sludge as seed sludge in the UASB method, and fixed bed methane fermentation treatment is usually applied. (Paper and Pulp Technology Times, August 1988, P66-P70
)
【0003】0003
【発明が解決しようとする課題】本発明は、上記の従来
技術における問題点を解消するために、中温メタン発酵
のUASBリアクターから得られるグラニュール汚泥を
種汚泥として、これにメタノサルシナ属、あるいはメタ
ノコッカス属のメタン菌を生息させ、高負荷なメタン発
酵処理を可能とするメタノール含有廃水の処理法を提供
することを目的とする。[Problems to be Solved by the Invention] In order to solve the above-mentioned problems in the prior art, the present invention uses granular sludge obtained from a UASB reactor for medium-temperature methane fermentation as a seed sludge, and uses Methanosarcina sp. The purpose of the present invention is to provide a method for treating methanol-containing wastewater that allows methane bacteria of the genus Coccus to live and enables high-load methane fermentation treatment.
【0004】0004
【課題を解決するための手段】上記目的を達成するため
に、本発明では、メタノール含有廃水を上向流式嫌気性
汚泥床法で高温メタン発酵処理する方法において、中温
メタン発酵処理のグラニュール汚泥を種汚泥としてスタ
ートアップすることを特徴とするメタノール含有廃水の
処理法としたものであり、また、本発明では、メタノー
ル含有廃水を上向流式嫌気性汚泥床法で高温メタン発酵
処理する方法において、中温メタン発酵処理のグラニュ
ール汚泥と嫌気性消化汚泥とを種汚泥としてスタートア
ップすることを特徴とするメタノール含有廃水の処理法
としたものである。[Means for Solving the Problems] In order to achieve the above object, the present invention provides a method for treating methanol-containing wastewater with high-temperature methane fermentation using an upflow anaerobic sludge bed method. This is a method for treating methanol-containing wastewater characterized by starting up sludge as seed sludge, and the present invention also provides a method for treating methanol-containing wastewater by high-temperature methane fermentation using an upflow anaerobic sludge bed method. , a method for treating methanol-containing wastewater is characterized by starting up granule sludge from mesophilic methane fermentation treatment and anaerobic digestion sludge as seed sludge.
【0005】UASB法は、原水を発酵槽の下部より上
向流として流入させ、菌の付着担体を用いることなく、
汚泥(菌)をフロック化若しくは粒状化せしめることに
より汚泥床(スラッジベット)を形成させ、発酵槽中に
高濃度の微生物を確保するためにより高容積負荷を許容
しうる嫌気性微生物処理技術であり、中温グラニュール
汚泥を種汚泥として圧密状態にリアクター低部から1〜
1.5m充填し、原廃水を上向流にて通水する。中温グ
ラニュール汚泥内部には酢酸を資化する糸状性のメタノ
スリクス属のメタン菌が多く生息している。廃水中に酢
酸が含まれずメタノールのみになるため、メタノスリク
ス属のメタン菌は徐々に失活し、グラニュール内にはそ
れに変わってメタノサルシナ属、あるいはメタノコッカ
ス属のメタン菌が生息し始める。通常、グラニュール汚
泥は廃水の成分によって異なるが20〜40%のCa,
Fe等の無機化合物を含み、かつこれらがメタン菌のサ
ポートとなっているため、球状の形態をしたメタノサル
シナ属、あるいはメタノコッカス属のメタン菌でも生息
しやすい環境にある。このようなグラニュール汚泥特有
の構造を生かすことで形状の異なるメタン菌の固定化が
可能となった。さらに、中温グラニュール汚泥と高温消
化汚泥を混合して種汚泥としてスタートアップすること
で前者は高温メタン菌のサポートになり、後者は高温メ
タン菌の植種となる。両者の混合比率はMLVSS重量
比で1:4〜2:1、好ましくは1:2〜1:1程度で
よい。[0005] The UASB method allows raw water to flow upward from the bottom of the fermenter, without using a carrier for bacteria to adhere to.
It is an anaerobic microbial treatment technology that forms a sludge bed by flocculating or granulating sludge (bacteria) and can tolerate a higher volume load to ensure a high concentration of microorganisms in the fermenter. , medium-temperature granule sludge is used as seed sludge in a compacted state from the bottom of the reactor.
The tank is filled to a depth of 1.5 m, and raw wastewater is passed through in an upward flow. Inside the mesophilic granule sludge, there are many filamentous methane bacteria of the genus Methanothrix that assimilate acetic acid. Since the wastewater contains no acetic acid and only methanol, the methane bacteria belonging to the genus Methanothrix gradually become inactive, and in their place, methane bacteria belonging to the genus Methanosarcina or Methanococcus begin to inhabit the granules. Usually, granule sludge contains 20 to 40% Ca, depending on the wastewater composition.
Because it contains inorganic compounds such as Fe, and these serve as a support for methane bacteria, it is an environment in which even spherical methane bacteria of the genus Methanosarcina or Methanococcus can easily inhabit. By taking advantage of this unique structure of granule sludge, it has become possible to immobilize methane bacteria of different shapes. Furthermore, by mixing medium-temperature granule sludge and high-temperature digested sludge and starting up as seed sludge, the former will support high-temperature methane bacteria, and the latter will serve as a seed for high-temperature methane bacteria. The mixing ratio of both may be about 1:4 to 2:1, preferably about 1:2 to 1:1 in MLVSS weight ratio.
【0006】[0006]
【作用】メタノールを含有した廃水の高温メタン発酵処
理として、通常行われている固定床法では、充填材にメ
タノサルシナ属あるいはメタノコッカス属のメタン菌を
付着させるため、ろ材表面の性状により付着状態が変わ
ったり、リアクター内の菌体量把握がむずかしい。本発
明においては、グラニュール汚泥内部、及び表面部分に
菌を固定化できるため、通常の中温UASB法と同様な
運転が可能となるため、リアクター内の菌体量把握及び
ハンドリングが容易となる。[Effect] In the fixed bed method that is commonly used for high-temperature methane fermentation treatment of methanol-containing wastewater, methane bacteria of the genus Methanosarcina or Methanococcus are attached to the packing material, so the adhesion state may vary depending on the properties of the surface of the filter material. It is difficult to understand the amount of bacteria in the reactor. In the present invention, since bacteria can be immobilized inside and on the surface of the granule sludge, operation similar to the normal medium temperature UASB method is possible, making it easy to grasp and handle the amount of bacteria in the reactor.
【0007】[0007]
【実施例】以下本発明を実施例により具体的に説明する
が、本発明はこれらの実施例に限定されるものでない。
実施例1
槽有効容量33リットルのUASBリアクターを用いて
50〜55℃の温度条件で食品工場より排出されるメタ
ノールを多く含む廃水を対象として中温のグラニュール
汚泥を種汚泥とした場合(Run 1)と高温の下水消
化汚泥を種汚泥とした場合(Run 2)について比較
実験を行った。下記に原水性状を示す。有機物の大半は
メタノールである。
原水性状・・・ pH : 7.7メタ
ノール: 8300mg/l
TOC : 3800 〃
BOD : 8600 〃
CODcr :14000 〃SS
: 10 〃[Examples] The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to these Examples. Example 1 Using a UASB reactor with a tank effective capacity of 33 liters and using medium-temperature granule sludge as the seed sludge for wastewater containing a large amount of methanol discharged from a food factory at a temperature of 50 to 55 °C (Run 1) ) and when high temperature sewage digested sludge was used as seed sludge (Run 2), a comparative experiment was conducted. The raw water properties are shown below. Most of the organic matter is methanol. Raw water properties... pH: 7.7 Methanol: 8300mg/l TOC: 3800 BOD: 8600 CODcr: 14000 SS
: 10〃
【0008】図1に処理成績
の概要を示す。Run 1(中温グラニュール汚泥を種
汚泥としたもの)は、CODcr 負荷を段階的に上げ
ていき40日目には15Kg/m3 ・d、70日目に
は40Kg/m3 ・dになった。処理水CODcr
は100mg/l前後で安定している。スラッジベット
内のMLVSS濃度は初期には若干低下したが、COD
cr 負荷の増加とともに徐々に増加し、130日目で
8%に達した。この時の槽内のグラニュール汚泥を採取
し、走査型電子顕微鏡にて観察すると、メタノサルシナ
属のメタン菌がグラニュール表面、内部に多く生息して
いることが確認できた。FIG. 1 shows an overview of the processing results. In Run 1 (in which medium-temperature granule sludge was used as the seed sludge), the CODcr load was increased stepwise to 15 Kg/m3·d on the 40th day and 40 Kg/m3·d on the 70th day. Treated water CODcr
is stable at around 100 mg/l. Although the MLVSS concentration in the sludge bed decreased slightly at the beginning, COD
cr gradually increased with increasing load and reached 8% at day 130. When the granule sludge in the tank was collected and observed under a scanning electron microscope, it was confirmed that many methane bacteria of the genus Methanosarcina were living on the surface and inside of the granules.
【0009】一方、Run 2(高温の下水消化汚泥を
種汚泥とした場合)は、CODcr 負荷15Kg/m
3 ・dまでは順調であるが、それ以上になると(70
日目)処理水CODcrが高くなり、処理成績が悪化し
た。また、スラッジベット内のMLVSS濃度は初期に
2%であったものが、3〜4%までは上がるが、それ以
上にはならなかった。リアクター汚泥を採取し、走査電
子顕微鏡にて観察すると、粒径0.1〜0.3mm程度
で、だんご状のメタノサルシナ属のメタン菌がかたまっ
ているのがわかった。このように消化汚泥を種汚泥とし
たケースは球状をしたメタノサルシナ属のメタン菌を固
定化させるための担体になるべきものがないため、高負
荷になった時は菌の洗い落としが起こるものと考えられ
る。On the other hand, in Run 2 (when high-temperature sewage digested sludge is used as seed sludge), the CODcr load is 15 kg/m
Things are going well up to 3.d, but beyond that (70
Day 2) The treated water CODcr increased and the treatment results deteriorated. Furthermore, the MLVSS concentration in the sludge bed was initially 2%, but it increased to 3 to 4%, but did not rise above that. When the reactor sludge was collected and observed under a scanning electron microscope, it was found that the methane bacteria of the genus Methanosarcina were clustered in a lump shape with a particle size of about 0.1 to 0.3 mm. In this case, when digested sludge is used as seed sludge, there is no carrier to immobilize the spherical methane bacteria of the genus Methanosarcina, so it is thought that when the load becomes high, the bacteria will be washed away. It will be done.
【0010】実施例2
実施例1と同じUASBリアクターを用いて50〜55
℃の温度条件で紙パルプ工場より排出されるクラフトパ
ルプドレン廃水*(全有機物の70〜80%をメタノー
ルが占めている。)について中温グラニュール汚泥と高
温消化汚泥を種汚泥(混合比率1:1)として行った実
験例を示す。原水性状は以下の通りである。
pH : 9.0
メタノール: 4500mg/l
TOC : 3360 〃
BOD : 6000 〃
CODcr : 9520 〃*スチーム
ストリッピング後(イオウ分は大半除去されている。)
表1に経過日数とCODcr 容積負荷、CODcr
除去率、スラッジベット内のグラニュール汚泥のメタン
生成活性度との関係を示す。Example 2 Using the same UASB reactor as Example 1,
Regarding kraft pulp drain wastewater* (methanol accounts for 70 to 80% of the total organic matter) discharged from a pulp and paper mill at a temperature of An example of an experiment conducted as 1) is shown below. The raw water properties are as follows. pH: 9.0 Methanol: 4500mg/l TOC: 3360 BOD: 6000 CODcr: 9520 *After steam stripping (most of the sulfur content has been removed)
Table 1 shows elapsed days and CODcr, volumetric load, CODcr
The relationship between the removal rate and the methane production activity of the granule sludge in the sludge bed is shown.
【0011】表1より明らかなように実施例1の中温グ
ラニュール汚泥を全量植種した場合に比べると若干立上
がりが遅くなるが、実験開始後120日目にはCODc
r 容積負荷20Kg/m3 ・dでCODcr 除去
率80%と安定した処理結果が得られている。[0011] As is clear from Table 1, the start-up is slightly slower than when the entire amount of medium-temperature granule sludge in Example 1 is inoculated, but the CODc
A stable treatment result with a CODcr removal rate of 80% was obtained at a volumetric load of 20 Kg/m3/d.
【表1】[Table 1]
【0012】0012
【発明の効果】以上の結果からも明らかなように、本発
明では、中温のグラニュール汚泥を種汚泥とすることで
、メタノール含有有機性廃水の高温UASB処理を可能
とした。[Effects of the Invention] As is clear from the above results, in the present invention, by using medium-temperature granule sludge as seed sludge, high-temperature UASB treatment of methanol-containing organic wastewater is made possible.
【図1】実施例1の処理結果を示すグラフである。FIG. 1 is a graph showing the processing results of Example 1.
Claims (2)
汚泥床法で高温メタン発酵処理する方法において、中温
メタン発酵処理のグラニュール汚泥を種汚泥としてスタ
ートアップすることを特徴とするメタノール含有廃水の
処理法。Claim 1: A method for treating methanol-containing wastewater by high-temperature methane fermentation using an upflow anaerobic sludge bed method, characterized in that granule sludge from medium-temperature methane fermentation treatment is started up as seed sludge. Processing method.
汚泥床法で高温メタン発酵処理する方法において、中温
メタン発酵処理のグラニュール汚泥と嫌気性消化汚泥と
を種汚泥としてスタートアップすることを特徴とするメ
タノール含有廃水の処理法。2. A method for treating methanol-containing wastewater by high-temperature methane fermentation using an upflow anaerobic sludge bed method, characterized in that granule sludge from medium-temperature methane fermentation treatment and anaerobic digestion sludge are used as seed sludge for startup. A method for treating methanol-containing wastewater.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10342091A JP2511331B2 (en) | 1991-04-09 | 1991-04-09 | Method for treating wastewater containing methanol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10342091A JP2511331B2 (en) | 1991-04-09 | 1991-04-09 | Method for treating wastewater containing methanol |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04310292A true JPH04310292A (en) | 1992-11-02 |
JP2511331B2 JP2511331B2 (en) | 1996-06-26 |
Family
ID=14353549
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10342091A Expired - Fee Related JP2511331B2 (en) | 1991-04-09 | 1991-04-09 | Method for treating wastewater containing methanol |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2511331B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19702461C2 (en) * | 1996-10-07 | 1999-11-18 | Taiseikozai Co | All-round flexible cutting line for a mower or lawn trimmer and mower or lawn trimmer with all-round flexible cutting line |
JP2007509737A (en) * | 2003-10-29 | 2007-04-19 | ヘルディング ゲゼルシャフト ミット ベシュレンクテル ハフツング フィルターテヒニク | Anaerobic wastewater treatment reactor |
JP2007136363A (en) * | 2005-11-18 | 2007-06-07 | Sumitomo Heavy Ind Ltd | Granular microbial sludge generation method |
JP2011224569A (en) * | 2011-07-20 | 2011-11-10 | Sumitomo Heavy Ind Ltd | Granular microbial sludge generation method |
JP2014100680A (en) * | 2012-11-21 | 2014-06-05 | Kuraray Co Ltd | Anaerobic wastewater treatment method using carrier |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100467406C (en) * | 2007-06-25 | 2009-03-11 | 张立省 | Process of treating acetic acid producing effluent and papermaking waste water comprehensively |
-
1991
- 1991-04-09 JP JP10342091A patent/JP2511331B2/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19702461C2 (en) * | 1996-10-07 | 1999-11-18 | Taiseikozai Co | All-round flexible cutting line for a mower or lawn trimmer and mower or lawn trimmer with all-round flexible cutting line |
JP2007509737A (en) * | 2003-10-29 | 2007-04-19 | ヘルディング ゲゼルシャフト ミット ベシュレンクテル ハフツング フィルターテヒニク | Anaerobic wastewater treatment reactor |
JP2007136363A (en) * | 2005-11-18 | 2007-06-07 | Sumitomo Heavy Ind Ltd | Granular microbial sludge generation method |
JP2011224569A (en) * | 2011-07-20 | 2011-11-10 | Sumitomo Heavy Ind Ltd | Granular microbial sludge generation method |
JP2014100680A (en) * | 2012-11-21 | 2014-06-05 | Kuraray Co Ltd | Anaerobic wastewater treatment method using carrier |
Also Published As
Publication number | Publication date |
---|---|
JP2511331B2 (en) | 1996-06-26 |
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