JP2013517129A - モジュール式エネルギー回収水処理装置 - Google Patents
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- H01M2300/00—Electrolytes
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- Y—GENERAL 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
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- Y—GENERAL 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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
Description
20ガロン容量の微生物燃料電池リアクタが、直列に動作する4つの独立したMFCカラムで構築された。各カラムは、ナイロンの薄い絶縁層で外側を包まれた内部アノードで構築された。ナイロンメッシュ(孔サイズ28μm)は、アノードとカソードとの間の電気的接触を防止するための絶縁障壁の役割を果たしたが、しかしまだコンパートメント間のイオン輸送を促進していた。アノードは、円柱状であって、チタンメッシュによって所定位置に保持された炭素顆粒を収容していた。カソードは、アノードと最も近いカソード円筒との間に約1cmの距離を置いて、アノードの周りに巻き付けられた2つの円筒で構成された。アノードおよびカソードの両方が充填層構成であった。チタンメッシュは、アノードおよびカソード円筒枠に用いられ、各コンパートメントのリード線の役割を果たした。アノードおよびカソードは、活性表面積を増加させるために、各々が非対称合成黒鉛顆粒(最大径1/4インチまで)で充填された。各内部アノードコンパートメントは、2.8Lの総容積を有していた。
Claims (24)
- 複数の微生物燃料電池(MFC)を含み、複数のMFCの各々が導電性材料によってカソードに接続されたアノードを含む、モジュール式水処理システムであって、
アノードは、第一微生物個体群と物理的に結びついており、
カソードは、第二微生物個体群または非生物触媒と物理的に結びついている、水処理システム。 - アノードとカソードとの間に陽子選択的材料が存在しない、請求項1に記載の水処理システム。
- アノードとカソードとの間に多孔質絶縁材料をさらに含む、請求項2に記載の水処理システム。
- 多孔質絶縁材料が、約30μm以下の孔径を有する、請求項3に記載の水処理システム。
- 第一微生物個体群が、エネルギーのために多様な炭素源を用いて嫌気性環境中で成長することが可能な微生物のために富化されている、請求項1に記載の水処理システム。
- 第二微生物個体群が、エネルギーのためにカソードからの電子を用いて好気性環境中で成長することが可能な微生物のために富化されている、請求項5に記載の水処理システム。
- 第一微生物個体群および第二微生物個体群が同じ親微生物個体群に由来する、請求項6に記載の水処理システム。
- 親微生物個体群が、下水廃水またはスラッジ中に自然に発生する微生物個体群である、請求項7に記載の水処理システム。
- アノードがカソードの内部に位置している、請求項1に記載の水処理システム。
- アノードおよびカソードが2cm以下の距離だけ離れている、請求項1に記載の水処理システム。
- カソードの表面積がアノードの表面積の少なくとも2倍である、請求項1に記載の水処理システム。
- アノードが、保持材によって所定位置に保持されている複数の導電性粒子を含む、請求項1に記載の水処理システム。
- 複数の導電性粒子が、黒鉛顆粒、黒鉛フェルト、黒鉛布、黒鉛ブラシ、またはこれらの組み合わせを含む、請求項12に記載の水処理システム。
- 保持材が、チタンメッシュ、ステンレス鋼メッシュ、プラスチックメッシュ、またはこれらの組み合わせを含む、請求項12に記載の水処理システム。
- カソードもまた、保持材によって所定位置に保持されている複数の導電性粒子を含む、請求項12に記載の水処理システム。
- カソードまたはアノードが、円筒形または円柱形である、請求項1に記載の水処理システム。
- アノードの第一末端に位置する液体流入手段、およびアノードの第二末端に位置する液体流出手段をさらに含む、請求項9に記載の水処理システム。
- 少なくともMFCのサブセットが直列で動作する、請求項1に記載の水処理システム。
- 少なくともMFCのサブセットが並列で動作する、請求項1に記載の水処理システム。
- 廃水処理のために微生物燃料電池(MFC)のアノードの微生物個体群を最適化する方法にであって、
(a)アノードを、親微生物個体群および廃水と接触させるステップと、
(b)アノードの微生物個体群のバイオマスを増加させるために、十分な時間にわたって比較的高抵抗でMFCを動作させるステップと、
(c)アノードの微生物個体群の代謝を最適化するために、十分な時間にわたって中抵抗でMFCを動作させるステップと、
(d)廃水の微生物分解を最適化するために、十分な時間にわたって低抵抗でMFCを動作させるステップと、を含む方法。 - 親微生物個体群が、廃水中に自然に発生する微生物個体群である、請求項20に記載の方法。
- 高抵抗が約1000から5000Ωの範囲内である、請求項20に記載の方法。
- 中抵抗が約100〜500Ωの範囲内である、請求項20に記載の方法。
- 低抵抗が約10〜500Ωの範囲である、請求項20に記載の方法。
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US29484110P | 2010-01-14 | 2010-01-14 | |
US61/294,841 | 2010-01-14 | ||
PCT/US2011/021338 WO2011088348A2 (en) | 2010-01-14 | 2011-01-14 | Modular energy recovering water treatment devices |
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US (2) | US9505636B2 (ja) |
EP (1) | EP2524411A4 (ja) |
JP (2) | JP2013517129A (ja) |
CN (2) | CN103098283B (ja) |
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JP7404080B2 (ja) | 2020-01-17 | 2023-12-25 | 住友重機械工業株式会社 | 排水処理装置及び排水処理方法並びに処理システム |
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CN103098283A (zh) | 2013-05-08 |
IL220904A (en) | 2017-04-30 |
AU2016203249A1 (en) | 2016-06-09 |
IL246279A0 (en) | 2016-07-31 |
WO2011088348A2 (en) | 2011-07-21 |
IL246279A (en) | 2017-10-31 |
CN103098283B (zh) | 2016-04-06 |
AU2011205747B2 (en) | 2016-06-02 |
US20150251934A1 (en) | 2015-09-10 |
EP2524411A2 (en) | 2012-11-21 |
CN105600916A (zh) | 2016-05-25 |
AU2011205747A1 (en) | 2012-08-16 |
CA2787030A1 (en) | 2011-07-21 |
WO2011088348A3 (en) | 2011-12-01 |
US9505636B2 (en) | 2016-11-29 |
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US20130137000A1 (en) | 2013-05-30 |
EP2524411A4 (en) | 2013-10-09 |
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