JP2010119963A - Waste water treatment apparatus for space station and method therefor - Google Patents

Waste water treatment apparatus for space station and method therefor Download PDF

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JP2010119963A
JP2010119963A JP2008296586A JP2008296586A JP2010119963A JP 2010119963 A JP2010119963 A JP 2010119963A JP 2008296586 A JP2008296586 A JP 2008296586A JP 2008296586 A JP2008296586 A JP 2008296586A JP 2010119963 A JP2010119963 A JP 2010119963A
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space station
biodegradation
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JP5463022B2 (en
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Naoki Ogawa
尚樹 小川
Atsuko Honma
敦子 本馬
Hiroshi Murase
浩史 村瀬
Akira Kakimoto
朗 柿本
Yoshiaki Kiyama
嘉明 木山
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Mitsubishi Heavy Industries Ltd
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    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a waste water treatment apparatus for a space station and a method therefor, in each of which the water to be treated can be treated by a simple constitution in the space station. <P>SOLUTION: The waste water treatment apparatus 10A for the space station is provided with: a biodegradation unit 12 for subjecting the water 11, which is to be treated and is the waste water generated in the space station or the water discharged from the human body, to biodegradation using activated sludge; a membrane separation unit 14 for separating a solid 14a from pretreated water 13 pretreated in the biodegradation unit 12 by using a membrane; a produced water production unit 18 for distilling or freezing the separated water 16, which is obtained when the solid 14a is separated, to obtain produced water 17; and an oxygen supply unit 19 for supplying oxygen when the water to be treated is subjected to the biodegradation. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、宇宙ステーションまたは将来の月・火星ミッションに搭載される排水処理技術(尿処理、生活排水処理)に用いる宇宙ステーション用の排水処理装置及び方法に関する。   The present invention relates to a wastewater treatment apparatus and method for a space station used for wastewater treatment technology (urine treatment, domestic wastewater treatment) to be mounted on a space station or a future moon / Mars mission.

宇宙ステーションまたは将来の月・火星ミッションにおいて、排出される排水又は作業員から排出される尿を再利用することが提案されており、その一つとして水の膜蒸留方法がある。   It has been proposed to recycle discharged effluent or urine discharged from workers in the space station or future Moon and Mars missions, one of which is the water film distillation method.

排出水には不純物があるので、膜蒸留装置により膜蒸留した後において、蒸留水に含まれる不純物を吸着除去する必要がある。   Since there is an impurity in the discharged water, it is necessary to adsorb and remove the impurity contained in the distilled water after membrane distillation with the membrane distillation apparatus.

このため、前処理として不純物を活性炭により吸着することが提案されているが、人体から排出されるアンモニアは前記活性炭では吸着除去できない、という問題がある。   For this reason, it has been proposed to adsorb impurities by activated carbon as a pretreatment, but there is a problem that ammonia discharged from the human body cannot be adsorbed and removed by the activated carbon.

前記膜蒸留を用いた排水処理方法は、蒸発を伴うため、純粋な処理水を得ることができることから、広い用途で再生水を使用することが可能である。
一方、膜蒸留方法は有機物による膜表面のファウリングや、低沸点成分の処理水中への同伴が起こるため、被処理水側の成分調整が必要となる場合がある。
今回、宇宙ステーション等で作業する作業員から排出される尿では、たんぱく質などの有機物や尿素が分解して生成したアンモニア等が含まれるが、これらの分解で増殖するバクテリア等が、膜蒸留性能を劣化させる要因となる。
Since the wastewater treatment method using membrane distillation involves evaporation, pure treated water can be obtained, and thus it is possible to use reclaimed water in a wide range of applications.
On the other hand, in the membrane distillation method, fouling of the membrane surface with organic substances and entrainment of low boiling point components in the treated water may occur, so that component adjustment on the treated water side may be required.
This time, the urine discharged from workers working at the space station, etc. contains organic substances such as proteins and ammonia produced by the decomposition of urea. Deteriorating factor.

そこで、劣化要因除去対策として、有機物等の活性炭吸着による除去(前処理)方法や、処理水中のアンモニアのイオン交換樹脂または活性炭吸着による除去(後処理)方法等が提案されている。   Therefore, as measures for removing deterioration factors, a removal (pretreatment) method by adsorption of activated carbon such as organic substances, a removal (post treatment) method of ammonia in the treated water by ion exchange resin or activated carbon adsorption, and the like have been proposed.

ここで、膜蒸留の後処理として吸着法を採用した一例を図4に示す。
図4に示すように、従来の排水浄化装置は、送液管54により供給された被処理水を蒸留するパーベーパレーション装置2と、2つの不純物吸着装置3、3と、それぞれの不純物吸着装置3、3に設けられた再生装置とから構成される。前記パーベーパレーション装置2における透過膜201としては、カチオン基を有する緻密質膜からなる透過膜を用いている(特許文献1参照)。なお、符号202は透過側(二次側)であり、203は供給側(一次側)である。
Here, FIG. 4 shows an example in which an adsorption method is employed as a post-treatment of membrane distillation.
As shown in FIG. 4, the conventional waste water purification apparatus includes a pervaporation apparatus 2 that distills the water to be treated supplied by a liquid feeding pipe 54, two impurity adsorption apparatuses 3 and 3, and each impurity adsorption apparatus. 3 and 3 are provided. As the permeable membrane 201 in the pervaporation apparatus 2, a permeable membrane made of a dense membrane having a cation group is used (see Patent Document 1). Reference numeral 202 denotes a transmission side (secondary side), and 203 denotes a supply side (primary side).

また、不純物吸着装置3としては、無機質多孔粒体等の吸着剤であり、前記無機質多孔粒体としては、活性炭、シリカゲル、活性アルミナ、バーミキュライト、木炭、ゼオライト等がある。図示例の被処理水の連続浄化装置1においては、二つの不純物吸着装置3、3が設けられており、送気管53に介装された方向制御弁61の切替により交互に再生している。
この不純物吸着装置3にはそれぞれ再生装置が設けられている。この再生装置は加熱手段4と減圧手段(例えば真空ポンプ等、図示せず)とを備え、吸着剤を減圧した状態で加熱することにより再生する装置である。減圧条件は10Pa以下の圧力とされ、また加熱条件は、100〜200℃とされる。尚、図示例の水の連続浄化装置1においては、再生装置を構成する減圧手段は、後流側に設けられている。
The impurity adsorbing device 3 is an adsorbent such as an inorganic porous particle, and examples of the inorganic porous particle include activated carbon, silica gel, activated alumina, vermiculite, charcoal, and zeolite. In the continuous water purification apparatus 1 of the illustrated example, two impurity adsorption devices 3 and 3 are provided, and are regenerated alternately by switching the direction control valve 61 interposed in the air supply pipe 53.
Each of the impurity adsorption devices 3 is provided with a regeneration device. This regenerating apparatus is provided with a heating means 4 and a depressurizing means (for example, a vacuum pump or the like, not shown), and regenerates by heating the adsorbent in a depressurized state. The decompression condition is a pressure of 10 Pa or less, and the heating condition is 100 to 200 ° C. In the continuous water purification apparatus 1 of the illustrated example, the decompression means constituting the regenerator is provided on the downstream side.

特開2006−095526号公報JP 2006-095526 A

しかしながら、不純物吸着装置3として用いる無機質多孔粒体(活性炭等)は、再生を繰り返したとしても、最後には破過による吸着剤の交換が必須であり、高濃度の除去対象物を含む被処理水であれば、破過の速度が速くなり、この結果吸着剤の交換頻度が多くなる、という問題がある。   However, even if inorganic porous particles (activated carbon, etc.) used as the impurity adsorbing device 3 are repeatedly regenerated, the adsorbent must be replaced by breakthrough at the end, and the object to be treated containing a high concentration removal target In the case of water, there is a problem that the breakthrough speed is increased, and as a result, the frequency of replacement of the adsorbent is increased.

また、宇宙空間では、クルーの作業時間は制限されており、機器のメンテナンス時間は最小限となることが要求されており、吸着剤の交換頻度が増えることは宇宙用機器として致命的であり、レスメンテナンスな設備が求められている。   In space, crew work time is limited, and equipment maintenance time is required to be minimal. Increasing the frequency of adsorbent replacement is fatal for space equipment, Less maintenance equipment is required.

さらに、破過によって交換した吸着剤は、地上へ返還することとなり、その交換費用と手間がかかるという問題もある。   Furthermore, the adsorbent exchanged by breakthrough is returned to the ground, and there is a problem that the exchange cost and labor are required.

本発明は、前記問題に鑑み、宇宙ステーション内において、簡易な構成で被処理水を処理することができる宇宙ステーション用の排水処理装置及び方法を提供することを課題とする。   In view of the above problems, an object of the present invention is to provide a wastewater treatment apparatus and method for a space station that can treat water to be treated with a simple configuration in the space station.

上述した課題を解決するための本発明の第1の発明は、宇宙ステーション等で利用した排水又は人体排出水等の被処理水を活性汚泥の生物分解により処理する生物分解処理装置と、前記固形物を分離した分離水を蒸留又は凍結して生産水を得る生産水製造装置と、前記生物分解処理の際に、酸素を供給する酸素供給装置とを具備することを特徴とする宇宙ステーション用の排水処理装置にある。   The first invention of the present invention for solving the above-mentioned problems is a biodegradation treatment apparatus for treating treated water such as waste water or human body discharged water used in a space station by biodegradation of activated sludge, and the solid For a space station, comprising: a production water production apparatus that obtains production water by distilling or freezing separated water from which substances are separated; and an oxygen supply apparatus that supplies oxygen during the biodegradation treatment. It is in the wastewater treatment equipment.

第2の発明は、第1の発明において、該生物分解処理装置で前処理された前処理水から固形物を膜分離する膜分離装置を具備することを特徴とする宇宙ステーション用の排水処理装置にある。   According to a second aspect of the present invention, there is provided a wastewater treatment apparatus for a space station, characterized in that in the first aspect, the apparatus comprises a membrane separation device for membrane-separating solids from pretreated water pretreated by the biodegradation treatment device. It is in.

第3の発明は、第1の発明において、該生物分解処理装置が膜分離活性汚泥装置(MBR)であることを特徴とする宇宙ステーション用の排水処理装置にある。   According to a third aspect of the present invention, there is provided a wastewater treatment apparatus for a space station according to the first aspect, wherein the biodegradation treatment apparatus is a membrane separation activated sludge apparatus (MBR).

第4の発明は、第1乃至3のいずれか一つの発明において、酸素供給装置に、酸素濃縮装置から更に酸素を供給してなることを特徴とする宇宙ステーション用の排水処理装置にある。   According to a fourth aspect of the present invention, there is provided a wastewater treatment apparatus for a space station, characterized in that, in any one of the first to third aspects, oxygen is further supplied from an oxygen concentrator to the oxygen supply unit.

第5の発明は、第1乃至4のいずれか一つの発明において、前記生産水製造装置が、膜蒸留装置又は凍結濃縮装置であることを特徴とする宇宙ステーション用の排水処理装置にある。   A fifth invention is the wastewater treatment apparatus for a space station according to any one of the first to fourth inventions, wherein the production water production apparatus is a membrane distillation apparatus or a freeze concentration apparatus.

第6の発明は、被処理水中の有機物を除去すると共に、アンモニアを酸化させる生物分解処理工程と、前記生物分解処理工程で前処理された前処理水から固形物を膜分離する膜分離工程と、膜分離工程で固形物を分離した分離水を蒸留又は凍結する生産水製造工程とを含むことを特徴とする宇宙ステーション用の排水処理方法にある。   A sixth invention includes a biodegradation treatment step for removing organic substances in the water to be treated and oxidizing ammonia, and a membrane separation step for membrane separation of solids from pretreated water pretreated in the biodegradation treatment step, And a production water production step of distilling or freezing the separated water separated from the solid in the membrane separation step.

第7の発明は、第6の発明において、前記生産水製造工程が、膜蒸留工程又は凍結濃縮工程であることを特徴とする宇宙ステーション用の排水処理方法にある。   A seventh invention is the waste water treatment method for a space station according to the sixth invention, wherein the production water production step is a membrane distillation step or a freeze concentration step.

本発明によれば、活性汚泥の生物分解による生物分解処理装置により、有機物の分解とアンモニアの酸化とが同時に達成でき、膜蒸留装置における劣化要因を取り除くことができる。
生物分解処理工程は自己増殖により性能が維持されるため、吸着剤のような交換作業が不要となると共に、増加した固形物(微生物)は、必要に応じて膜分離工程によって除去されるため、系内の微生物量も一定範囲に維持することができる。
ADVANTAGE OF THE INVENTION According to this invention, the biodegradation processing apparatus by biodegradation of activated sludge can achieve simultaneously decomposition | disassembly of organic substance and oxidation of ammonia, and can eliminate the deterioration factor in a membrane distillation apparatus.
Since the performance of the biodegradation process is maintained by self-growth, replacement work such as an adsorbent is unnecessary, and the increased solid matter (microorganisms) is removed by the membrane separation process as necessary. The amount of microorganisms in the system can also be maintained within a certain range.

これにより、人間の生命維持に欠くことのできない水を再利用することができ、宇宙での人間の長期滞在が可能となることができる。   This makes it possible to reuse the water that is indispensable for the maintenance of human life, and enables long-term stay in space.

以下、この発明につき図面を参照しつつ詳細に説明する。なお、この実施例によりこの発明が限定されるものではない。また、下記実施例における構成要素には、当業者が容易に想定できるもの、あるいは実質的に同一のものが含まれる。   Hereinafter, the present invention will be described in detail with reference to the drawings. Note that the present invention is not limited to the embodiments. In addition, constituent elements in the following embodiments include those that can be easily assumed by those skilled in the art or those that are substantially the same.

本発明による実施例に係る宇宙ステーション用の排水処理装置について、図面を参照して説明する。
図1は、実施例1に係る宇宙ステーション用の排水処理装置の概略図である。
図1に示すように、本実施例に係る宇宙ステーション用の排水処理装置10Aは、宇宙ステーション等で利用した排水又は人体排出水等の被処理水11を活性汚泥の生物分解により処理する生物分解処理装置12と、該生物分解処理装置12で前処理された前処理水13から固形物14aを膜分離する膜分離装置14と、前記固形物14aを分離した分離水16を蒸留又は凍結して生産水17を得る生産水製造装置18と、生物分解処理の際に、酸素を供給する酸素供給装置19とを具備するものである。
A wastewater treatment apparatus for a space station according to an embodiment of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic diagram of a wastewater treatment apparatus for a space station according to a first embodiment.
As shown in FIG. 1, a wastewater treatment apparatus 10A for a space station according to the present embodiment is a biodegradation that treats water 11 to be treated such as wastewater used in the space station or the like or human body drainage water by biodegradation of activated sludge. Distilling or freezing the treatment device 12, the membrane separation device 14 for separating the solid matter 14a from the pretreated water 13 pretreated by the biodegradation treatment device 12, and the separated water 16 separating the solid matter 14a A production water production device 18 for obtaining the production water 17 and an oxygen supply device 19 for supplying oxygen at the time of biodegradation treatment are provided.

本実施例においては、前記生産水17を得るための生産水製造装置18としては、例えば膜蒸留装置又は凍結濃縮装置を例示することができる。
ここで、膜蒸留装置は、蒸気は通すが液は通さない疎水性多孔膜を用いて、膜の両側に高温の分離水16と冷却水を流し、高温の分離水16から水蒸気が膜を透過し、冷却水側に移動して生産水17を得る装置である。
また、前記凍結濃縮装置は、分離水16を凍結させ、生成した氷と溶液を分離することにより生産水17を得る装置である。
In the present embodiment, examples of the production water production apparatus 18 for obtaining the production water 17 include a membrane distillation apparatus and a freeze concentration apparatus.
Here, the membrane distillation apparatus uses a hydrophobic porous membrane that allows vapor to pass but not liquid to flow high-temperature separation water 16 and cooling water on both sides of the membrane, and water vapor passes through the membrane from the high-temperature separation water 16. In this case, the product water 17 is obtained by moving to the cooling water side.
The freeze concentration apparatus is an apparatus for obtaining the production water 17 by freezing the separation water 16 and separating the generated ice and the solution.

本実施例では、前記生産水製造装置18の前処理装置として、活性汚泥の生物分解により処理する生物分解処理装置12を配し、被処理水11中の有機物の除去とアンモニアの酸化とを同時に行わせ、例えば膜蒸留装置又は凍結濃縮装置等の性能を劣化させる不純物を除去するようにしている。   In the present embodiment, a biodegradation treatment device 12 that performs treatment by biodegradation of activated sludge is disposed as a pretreatment device of the production water production device 18, and the removal of organic substances in the treated water 11 and the oxidation of ammonia are simultaneously performed. For example, impurities that deteriorate the performance of, for example, a membrane distillation apparatus or a freeze concentration apparatus are removed.

ここで、前記生物分解処理装置12には、尿中に含まれる有機物、アンモニアを酸化する機能を持つバクテリア、真菌(酵母、カビ)、原生動物を含んだ活性汚泥と称される微生物集落を含むものである。
また、前記活性汚泥を生物分解処理装置内に維持するために、付着担体と称される固形物(例えばセラミックス、ガラス、砂、プラスチック等)に担持させ、これを充填するようにしてもよい。
Here, the biodegradation treatment apparatus 12 includes microbial colonies called activated sludge containing organic substances contained in urine, bacteria having a function of oxidizing ammonia, fungi (yeast, mold), and protozoa. It is a waste.
Further, in order to maintain the activated sludge in the biodegradation processing apparatus, it may be supported on a solid substance (for example, ceramic, glass, sand, plastic, etc.) called an adhesion carrier and filled therewith.

生物分解処理装置12からの前処理水13中には、微生物を担体で担持していない場合には、微生物(固体)を含んでいるため、膜分離装置14を設け、これにより固形物14aの除去を行った後、分離水16を生産水製造装置18へ供給して、生産水17を製造するようにしている。   In the pretreated water 13 from the biodegradation treatment apparatus 12, when the microorganisms are not supported by the carrier, since the microorganisms (solid) are contained, a membrane separation device 14 is provided. After the removal, the separated water 16 is supplied to the production water production apparatus 18 to produce the production water 17.

また、前記膜分離装置14で分離された粒子等の固形物14aや、生産水製造置18の濃縮により溶解度を越えた析出成分等の固形物18aは、脱水装置21での脱水処理工程を経て固形物22として回収処分される。なお、脱水された水は生物分解処理装置12の前流側に、返送水23として返送され、被処理水11と共に再度処理される。   Further, the solid matter 14 a such as particles separated by the membrane separation device 14 and the solid matter 18 a such as a precipitated component that has exceeded solubility due to concentration in the production water production unit 18 are subjected to a dehydration process in the dehydration device 21. It is recovered and disposed as a solid 22. The dehydrated water is returned to the upstream side of the biodegradation treatment device 12 as return water 23 and is treated again with the water to be treated 11.

ここで、前記膜分離装置14は、該生物分解処理装置12で前処理された前処理水13から固形物14aを膜分離するものであればいずれでも良いが、例えばMF膜(精密濾過膜)やUF膜(限外濾過膜)等を用いるようにすればよい。   Here, the membrane separation device 14 may be any device that separates the solid matter 14a from the pretreated water 13 pretreated by the biodegradation treatment device 12. For example, an MF membrane (microfiltration membrane) Or a UF membrane (ultrafiltration membrane) may be used.

また、生物分解処理装置12において、活性汚泥を処理槽内に維持するために、付着担体等に固形物に充填する場合や、MBR(Membrane Bio Reactor:膜分離活性汚泥装置)を用いることが特に好ましい。
この膜分離活性汚泥装置(MBR)は、活性汚泥法と膜分離法を組み合わせたプロセスであり、通常分離膜としては精密濾過膜(MF膜)又は限外濾過膜(UF膜)が使用され、この膜の固液分離作用で汚泥流出を阻止することができ、バイオリアクターの生物濃度を高められ、この結果装置の小型化が可能であると共に余剰汚泥の生成量が少ないものとなる。
よって、MBRを用いた場合においては、固形物流失が防止されるので、本実施例においても膜分離装置14を省略するようにしてもよい。
In addition, in order to maintain the activated sludge in the treatment tank in the biodegradation treatment apparatus 12, it is particularly preferable to use solid MBR or a MBR (Membrane Bio Reactor) to maintain the activated sludge in the treatment tank. preferable.
This membrane separation activated sludge apparatus (MBR) is a process that combines activated sludge method and membrane separation method, and usually a microfiltration membrane (MF membrane) or ultrafiltration membrane (UF membrane) is used as the separation membrane, Sludge outflow can be prevented by the solid-liquid separation action of this membrane, and the biological concentration of the bioreactor can be increased. As a result, the apparatus can be miniaturized and the amount of surplus sludge produced is small.
Therefore, when MBR is used, the loss of solid logistics is prevented, so the membrane separation device 14 may be omitted also in this embodiment.

また、前記生物分解処理装置12には、所定量の酸素の供給が必須であるが、その酸素は宇宙ステーションのキャビンからの空気を生物分解処理装置12と並列に配置した酸素供給装置19を通して供給するようにしている。   The biodegradation processing apparatus 12 is required to supply a predetermined amount of oxygen, and the oxygen is supplied from the space station cabin through an oxygen supply apparatus 19 arranged in parallel with the biodegradation processing apparatus 12. Like to do.

ここで、前記酸素供給装置19としては、キャビン内の空気から酸素を分離するものであればいずれでも良いが、例えば人工肺を例示することができる。   Here, the oxygen supply device 19 may be any device as long as it separates oxygen from the air in the cabin. For example, an oxygenator can be exemplified.

さらに、酸素供給の効率を高めるために、キャビン内の空気を酸素濃縮装置25(PSA(Pressure Swing Adsorption)、酸素富化膜等)で濃縮し、更に供給することも可能である。
ここで、酸素濃縮装置25はキャビン内での空気24を取込み、酸素(O2)を濃縮し、窒素(N2)を分離するものである。
この場合には、例えば人工肺でのガス供給量が少なくなり、人工肺のコンパクト化を図ることができる。
なお、酸素供給装置19の人工肺からは二酸化炭素(CO2)が排出される。
Furthermore, in order to increase the efficiency of oxygen supply, the air in the cabin can be concentrated by an oxygen concentrator 25 (PSA (Pressure Swing Adsorption), oxygen-enriched membrane, etc.) and further supplied.
Here, the oxygen concentrator 25 takes in the air 24 in the cabin, concentrates oxygen (O 2 ), and separates nitrogen (N 2 ).
In this case, for example, the gas supply amount in the oxygenator is reduced, and the oxygenator can be made compact.
Carbon dioxide (CO 2 ) is discharged from the oxygenator of the oxygen supply device 19.

このような、宇宙ステーション用の排水処理装置を用いて宇宙ステーション内で発生する排水や尿等は以下の工程により処理される。
(工程1)
先ず、生物分解処理装置12により、被処理水11中の有機物を除去すると共に、アンモニアを酸化させる生物分解処理工程。
(工程2)
前記生物分解処理工程で前処理された前処理水13から固形物を膜分離する膜分離工程。
(工程3)
膜分離工程で固形物14aを分離した分離水16を膜蒸留又は凍結濃縮等により生産水17を製造する生産水製造工程。
Wastewater, urine and the like generated in the space station using such a wastewater treatment apparatus for the space station are processed by the following steps.
(Process 1)
First, a biodegradation process in which the biodegradation apparatus 12 removes organic substances in the water to be treated 11 and oxidizes ammonia.
(Process 2)
A membrane separation step of membrane-separating solids from the pretreated water 13 pretreated in the biodegradation treatment step.
(Process 3)
A production water production process for producing the production water 17 by membrane distillation or freeze concentration of the separated water 16 from which the solid matter 14a has been separated in the membrane separation process.

このように、工程1における生物分解による生物分解処理工程により、有機物の分解とアンモニアの酸化とが同時に達成でき、膜蒸留装置や凍結濃縮装置における劣化要因を取り除くことができる。
生物分解処理工程は自己増殖により性能が維持されるため、吸着剤のような交換作業が不要となると共に、増加した固形物(微生物)は、必要に応じて工程2の膜分離工程によって除去されるため、系内の微生物量も一定範囲に維持することができる。
これにより、工程3における生産水製造工程により、人間の生命維持に欠くことのできない生産水17を製造することができ、宇宙での人間の長期滞在を可能にすることができる。
よって、本実施例の宇宙ステーション用の排水処理装置を備えた宇宙ステーションの生命維持装置は、長期間に亙って連続的に良質な生産水を製造することができる。
Thus, the biodegradation treatment step by biodegradation in step 1 can simultaneously achieve the decomposition of the organic matter and the oxidation of ammonia, and can eliminate the deterioration factors in the membrane distillation apparatus and the freeze concentration apparatus.
Since the performance of the biodegradation process is maintained by self-growth, replacement work such as an adsorbent is unnecessary, and the increased solid matter (microorganisms) is removed by the membrane separation process of process 2 as necessary. Therefore, the amount of microorganisms in the system can also be maintained within a certain range.
Thereby, the production water 17 indispensable for human life maintenance can be manufactured by the production water manufacturing process in the process 3, and the long-term stay of the human in space can be enabled.
Therefore, the life support apparatus of the space station provided with the wastewater treatment apparatus for the space station of the present embodiment can continuously produce high quality product water over a long period of time.

本発明による実施例に係る宇宙ステーション用の排水処理装置について、図面を参照して説明する。
図2は、実施例2に係る宇宙ステーション用の排水処理装置の概略図である。
図2に示すように、本実施例に係る宇宙ステーション用の排水処理装置10Bは、宇宙ステーション等で利用した排水又は人体排出水等の被処理水11中に酸素を供給する酸素供給装置19と、酸素が供給された被処理水を活性汚泥の生物分解により処理する生物分解処理装置(MBR)12と、活性汚泥により処理された前処理水13を蒸留又は凍結して生産水17を得る生産水製造装置18とを具備するものである。
A wastewater treatment apparatus for a space station according to an embodiment of the present invention will be described with reference to the drawings.
FIG. 2 is a schematic diagram of a wastewater treatment apparatus for a space station according to the second embodiment.
As shown in FIG. 2, the wastewater treatment apparatus 10B for the space station according to the present embodiment includes an oxygen supply device 19 for supplying oxygen into the treated water 11 such as wastewater used in the space station or the like or human body drainage water. Production to obtain product water 17 by distilling or freezing biodegradation treatment device (MBR) 12 for treating the treated water supplied with oxygen by biodegradation of activated sludge and pretreated water 13 treated with activated sludge A water production device 18.

本実施例では、人工肺等の酸素供給装置19を直列に設け、直接酸素を被処理水11内に供給するようにしている。
また、生物分解処理装置12においては、付着担体による微生物の固定化法や、膜分離活性汚泥法(MBR)としているので、実施例1のような被処理水中に微生物が混入することが解消され、膜分離装置の設置が不要となる。
In this embodiment, an oxygen supply device 19 such as an artificial lung is provided in series to supply oxygen directly into the water to be treated 11.
In addition, since the biodegradation treatment apparatus 12 employs a method of immobilizing microorganisms with an adherent carrier or a membrane separation activated sludge method (MBR), it is possible to eliminate the contamination of microorganisms into the water to be treated as in Example 1. This eliminates the need to install a membrane separator.

また、図3に示す宇宙ステーション用の排水処理装置10Cのように、生物分解処置装置12の処理後の前処理水13の一部を生物分解処理装置12の上流に戻し、循環を行うことで、高濃度の被処理物(有機物、アンモニア)を含む水に対しても処理可能となる。尚、循環する液の比率は有機物、アンモニアの初期濃度によって決定されるものである。   Further, as in the wastewater treatment apparatus 10C for the space station shown in FIG. 3, a part of the pretreated water 13 after the treatment of the biodegradation treatment apparatus 12 is returned to the upstream of the biodegradation treatment apparatus 12 and circulated. Further, it is possible to treat even water containing a high concentration object (organic matter, ammonia). The ratio of the circulating liquid is determined by the initial concentrations of organic matter and ammonia.

本実施例によれば、実施例1の効果に加え、生物分解処理装置12の下流に設けた膜分離装置が不要となり、システム全体の簡素化(コンパクト化)を図ることができる。   According to the present embodiment, in addition to the effects of the first embodiment, a membrane separation device provided downstream of the biodegradation processing device 12 is not necessary, and the entire system can be simplified (compact).

以上のように、本発明に係る宇宙ステーション用の排水処理技術によれば、簡単な構成により有害物質や尿を前処理することができ、膜蒸留装置や凍結濃縮装置における劣化要因を取り除くことができ、宇宙ステーションの生命維持装置に用いて適している。   As described above, according to the wastewater treatment technology for a space station according to the present invention, harmful substances and urine can be pretreated with a simple configuration, and the deterioration factor in the membrane distillation apparatus and the freeze concentration apparatus can be removed. It is suitable for use in life support equipment for space stations.

実施例1に係る宇宙ステーション用の排水処理装置の概略図である。1 is a schematic diagram of a wastewater treatment apparatus for a space station according to Embodiment 1. FIG. 実施例2に係る宇宙ステーション用の排水処理装置の概略図である。It is the schematic of the waste water treatment equipment for space stations concerning Example 2. FIG. 実施例2に係る宇宙ステーション用の他の排水処理装置の概略図である。It is the schematic of the other waste water treatment equipment for the space station which concerns on Example 2. FIG. 従来の排水浄化装置の概略図である。It is the schematic of the conventional waste water purification apparatus.

符号の説明Explanation of symbols

10A、10B、10C 宇宙ステーション用の排水処理装置
11 被処理水
12 生物分解処理装置
13 前処理水
14a 固形物
14 膜分離装置
16 分離水
17 生産水
18 生産水製造装置
18a 固形物
19 酸素供給装置
21 脱水装置
22 固形物
23 返送水
24 空気
25 酸素濃縮装置
10A, 10B, 10C Space station wastewater treatment equipment 11 Water to be treated 12 Biodegradation treatment equipment 13 Pretreatment water 14a Solid matter 14 Membrane separation device 16 Separation water 17 Production water 18 Production water production equipment 18a Solid matter 19 Oxygen supply equipment 21 Dehydrator 22 Solid matter 23 Return water 24 Air 25 Oxygen concentrator

Claims (7)

宇宙ステーション等で利用した排水又は人体排出水等の被処理水を活性汚泥の生物分解により処理する生物分解処理装置と、
固形物を分離した分離水を蒸留又は凍結して生産水を得る生産水製造装置と、
生物分解処理の際に、酸素を供給する酸素供給装置とを具備することを特徴とする宇宙ステーション用の排水処理装置。
A biodegradation treatment apparatus that treats treated water such as waste water or human body effluent used in a space station by biodegradation of activated sludge;
A production water production apparatus for obtaining product water by distilling or freezing the separated water from which the solids have been separated;
A wastewater treatment apparatus for a space station, comprising: an oxygen supply device that supplies oxygen during biodegradation treatment.
請求項1において、
該生物分解処理装置で前処理された前処理水から固形物を膜分離する膜分離装置を具備することを特徴とする宇宙ステーション用の排水処理装置。
In claim 1,
A wastewater treatment device for a space station, comprising a membrane separation device for membrane separation of solid matter from pretreated water pretreated by the biodegradation treatment device.
請求項1において、
該生物分解処理装置が膜分離活性汚泥装置であることを特徴とする宇宙ステーション用の排水処理装置。
In claim 1,
A wastewater treatment apparatus for a space station, wherein the biodegradation treatment apparatus is a membrane separation activated sludge apparatus.
請求項1乃至3のいずれか一つにおいて、
酸素供給装置に、酸素濃縮装置から更に酸素を供給してなることを特徴とする宇宙ステーション用の排水処理装置。
In any one of Claims 1 thru | or 3,
A wastewater treatment apparatus for a space station, wherein oxygen is further supplied from an oxygen concentrator to an oxygen supply apparatus.
請求項1乃至4のいずれか一つにおいて、
前記生産水製造装置が、膜蒸留装置又は凍結濃縮装置であることを特徴とする宇宙ステーション用の排水処理装置。
In any one of Claims 1 thru | or 4,
The waste water treatment apparatus for a space station, wherein the production water production apparatus is a membrane distillation apparatus or a freeze concentration apparatus.
被処理水中の有機物を除去すると共に、アンモニアを酸化させる生物分解処理工程と、
前記生物分解処理工程で前処理された前処理水から固形物を膜分離する膜分離工程と、
膜分離工程で固形物を分離した分離水を蒸留又は凍結する生産水製造工程とを含むことを特徴とする宇宙ステーション用の排水処理方法。
A biodegradation process that removes organic matter in the water to be treated and oxidizes ammonia;
A membrane separation step of membrane-separating solids from the pretreated water pretreated in the biodegradation treatment step;
A wastewater treatment method for a space station, comprising a production water production step of distilling or freezing the separated water obtained by separating the solids in the membrane separation step.
請求項6において、
前記生産水製造工程が、膜蒸留工程又は凍結濃縮工程であることを特徴とする宇宙ステーション用の排水処理方法。
In claim 6,
The waste water treatment method for a space station, wherein the production water production process is a membrane distillation process or a freeze concentration process.
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