JPH05301097A - Method for purification of treated sewage using microalgae and for simultaneous production of hydrocarbon - Google Patents
Method for purification of treated sewage using microalgae and for simultaneous production of hydrocarbonInfo
- Publication number
- JPH05301097A JPH05301097A JP13204392A JP13204392A JPH05301097A JP H05301097 A JPH05301097 A JP H05301097A JP 13204392 A JP13204392 A JP 13204392A JP 13204392 A JP13204392 A JP 13204392A JP H05301097 A JPH05301097 A JP H05301097A
- Authority
- JP
- Japan
- Prior art keywords
- microalgae
- sewage
- treated sewage
- hydrocarbon
- hydrocarbons
- 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.)
- Pending
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は下水処理水から微細藻類
を用いて炭化水素を製造するとともに、下水処理水を浄
化する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing hydrocarbons from sewage-treated water by using microalgae and purifying the sewage-treated water.
【0002】[0002]
【従来技術及びその問題点】従来、微細藻類によって炭
化水素を製造する場合、培地としては人工合成培地が用
いられており、水及び窒素やリンなどの栄養塩を準備す
る必要があった。しかしながら、このような方法では炭
化水素を製造するに当たって微細藻類の培養が高価にな
ることから、その実用化には大きな困難がある。また、
下水処理水を微細藻類によって浄化しようとした試みは
あるが、有用物質を生産しない微細藻類では、得られた
藻体の処理法が困難であり、また有用物質を生産しない
ため経済的にも不利である。2. Description of the Related Art Conventionally, when a hydrocarbon is produced by microalgae, an artificial synthetic medium has been used as a medium, and it has been necessary to prepare water and nutrient salts such as nitrogen and phosphorus. However, such a method is very difficult to put into practical use because the culture of microalgae becomes expensive in producing hydrocarbons. Also,
Although there have been attempts to purify sewage treated water with microalgae, microalgae that do not produce useful substances make it difficult to treat the obtained algal cells, and also economically disadvantageous because they do not produce useful substances. Is.
【0003】[0003]
【発明が解決しようとする課題】本発明は、前記のよう
な従来法とは異なり、それ自体では有効利用されず、し
かもその廃棄に際しては浄化されることが望ましい下水
処理水を有効利用するとともに、浄化する方法を提供す
ることを課題とする。The present invention differs from the above-mentioned conventional methods in that it makes effective use of sewage treated water, which is not effectively used by itself and is preferably purified when it is discarded. , To provide a method of purification.
【0004】[0004]
【発明を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意研究を重ねた結果、本発明を完成する
に至った。即ち、本発明によれば、下水処理水を培地と
し、炭化水素生産性微細藻類を培養することにより、炭
化水素を生産するとともに、下水処理水中の無機物を減
少させその水質を改良する方法が提供される。The present inventors have completed the present invention as a result of intensive studies to solve the above problems. That is, according to the present invention, a method for producing hydrocarbons by culturing a hydrocarbon-producing microalgae using sewage-treated water as a medium and reducing the inorganic substances in the sewage-treated water to improve its water quality is provided. To be done.
【0005】本発明における下水処理水には、一般の下
水処理水の他、一般家庭及び工場から排出された汚水を
好気的または嫌気的に微生物等を用いて処理し、元の水
よりも有機物及び無機物の量が減少した水溶液等が包含
される。In the sewage treatment water in the present invention, in addition to general sewage treatment water, sewage discharged from ordinary households and factories is treated aerobically or anaerobically with microorganisms, etc. An aqueous solution in which the amount of organic substances and inorganic substances are reduced is included.
【0006】本発明の方法を実施するには、下水処理水
をそのまま、または無菌処理、必要に応じてpHや栄養
塩類を調整したものを、炭化水素を生産する微細藻類の
培養液として使用すればよい。この場合、培養方法は燃
焼排気等による二酸化炭素の供給・光ファイバー法・エ
アーリフト法などを用いることが可能で、培養条件は従
来の各々の微細藻類に適した条件で培養することができ
る。炭化水素生産性微細藻類としては、従来公知のもの
を使用することができる。このようなものとしては、例
えば、ボトリコッカス、ブラウニ(Botrycoccusbrauni
i)等が挙げられる。In order to carry out the method of the present invention, treated sewage water as it is, or aseptic treatment, pH and nutrients adjusted if necessary, may be used as a culture solution of microalgae producing hydrocarbons. Good. In this case, as the culturing method, supply of carbon dioxide by combustion exhaust gas, an optical fiber method, an air lift method, or the like can be used, and the culturing condition can be a condition suitable for each conventional microalgae. As the hydrocarbon-producing microalga, conventionally known ones can be used. Examples of such a product include Botrycoccus brauni ( Botrycoccus brauni).
i ) and the like.
【0007】前記のようにして下水処理水を、炭化水素
を生産する微細藻類の培地として使用することにより、
炭化水素を効率よく生産でき、同時に培養に使用した下
水処理水は元の水質に比べて、無機物濃度を低下させる
ことができる。無機物としては、窒素やリンを含む各種
無機塩類が挙げられる。By using the treated sewage water as a medium for microalgae producing hydrocarbons as described above,
Hydrocarbons can be produced efficiently, and at the same time, the sewage treatment water used for cultivation can have a lower concentration of inorganic substances than the original water quality. Examples of the inorganic substance include various inorganic salts containing nitrogen and phosphorus.
【0008】[0008]
【発明の効果】本発明は前記のような構成であり、下水
処理水から微細藻類を用いて炭化水素を製造し、同時に
下水処理水の水質を改善できる。INDUSTRIAL APPLICABILITY The present invention is constructed as described above, and can produce hydrocarbons from sewage-treated water by using microalgae, and at the same time improve the quality of sewage-treated water.
【0009】[0009]
【実施例】次に本発明を実施例によりさらに詳細に説明
する。本実施例で用いた微細藻類は、Botryococcus bra
uniiバークレイ株である。下水処理水は茨城県下の家庭
排水の下水処理場2カ所より得た下水処理水A及びBで
ある。EXAMPLES Next, the present invention will be described in more detail by way of examples. The microalgae used in this example are Botryococcus bra
unii is a Berkeley strain. The sewage treatment water is sewage treatment water A and B obtained from two domestic wastewater sewage treatment plants in Ibaraki prefecture.
【0010】実施例1 Chu13培地で25℃、照度3000lux、1%の
二酸化炭素を供給した条件で培養したB.brauniiを、2
0μmメッシュのナイロン網で濾過し、下水処理水Aで
洗浄濾過した。その後、洗浄した藻体を、湿熱滅菌した
下水処理水3リットルの入った3リットル用フラスコ中
に移植し、先の条件で培養した。その結果得られた藻体
の凍結乾燥重量は0.35gで、ヘキサンで抽出された
炭化水素の割合は53%であった。培養の結果を図1に
示す。B. brauniiの増殖は図1の折れ線1のクロロフィ
ル量として測定し、最終的に初期量の2.8倍の濃度と
なった。折れ線2は硝酸濃度を示すが、初期濃度7.7
6Nmg/1は培養9日目には検出されなくなった。折
れ線3はリン酸濃度を示すが、初期濃度0.015Pm
g/lは培養1日目で0.01Pmg/l以下に低下し
た。[0010] 25 ° C. Example 1 Chu13 medium, the B.braunii cultured under conditions that supplied the illuminance 3000 lux, 1% carbon dioxide, 2
The mixture was filtered through a nylon mesh of 0 μm mesh, washed with sewage-treated water A, and filtered. Then, the washed algal cells were transplanted into a 3 liter flask containing 3 liters of sewage-treated water that had been subjected to wet heat sterilization, and cultured under the above conditions. The freeze-dried weight of the resulting algal cells was 0.35 g, and the proportion of hydrocarbons extracted with hexane was 53%. The result of the culture is shown in FIG. The growth of B. braunii was measured as the amount of chlorophyll in the polygonal line 1 in FIG. 1, and finally the concentration was 2.8 times the initial amount. Line 2 shows the nitric acid concentration, but the initial concentration is 7.7.
6 Nmg / 1 was not detected on the 9th day of culture. Line 3 shows the phosphoric acid concentration, but the initial concentration is 0.015 Pm
The g / l decreased to 0.01 Pmg / l or less on the first day of culture.
【0011】実施例2 Chu13培地で25℃、照度3000lux、1%の
二酸化炭素を供給した条件で培養したB. brauniiを、2
0μmメッシュのナイロン網で濾過し、下水処理水Bで
洗浄濾過した。その後、洗浄した藻体を、湿熱滅菌した
下水処理水3リットルの入った3リットル用フラスコ中
に移植し、先の条件で培養した。その結果得られた藻体
の凍結乾燥重量は0.34gで、ヘキサンで抽出された
炭化水素の割合は40%であった。培養の結果を図2に
示す。B. brauniiの増殖は図2の折れ線1のクロロフィ
ル量として測定し、最終的に初期量の2.8倍の濃度と
なった。折れ線2は硝酸濃度を示すが、初期濃度4.4
8Nmg/lは、培養7日目には検出されなくなった。
折れ線3はリン酸濃度を示すが、初期濃度0.29Pm
g/lは培養5日目で0.01Pmg/l以下に低下し
た。Example 2 B. braunii cultivated in a Chu13 medium at 25 ° C. under the condition that an illuminance of 3000 lux and 1% of carbon dioxide were supplied were 2
The mixture was filtered through a nylon mesh of 0 μm mesh, washed with sewage-treated water B, and filtered. Then, the washed algal cells were transplanted into a 3 liter flask containing 3 liters of sewage-treated water that had been sterilized by wet heat, and cultured under the above conditions. The freeze-dried weight of the resulting algal cells was 0.34 g, and the proportion of hydrocarbons extracted with hexane was 40%. The results of culture are shown in FIG. The proliferation of B. braunii was measured as the amount of chlorophyll in the polygonal line 1 in FIG. 2, and finally the concentration was 2.8 times the initial amount. Line 2 shows the nitric acid concentration, but the initial concentration is 4.4.
8 Nmg / l was no longer detected on day 7 of culture.
Line 3 shows the phosphoric acid concentration, but the initial concentration is 0.29 Pm
The g / l decreased to 0.01 Pmg / l or less on the 5th day of culture.
【0012】比較例1 Chu13培地で25℃、照度3000lux、1%の
二酸化炭素を供給した条件で培養したB. brauniiを、2
0μmメッシュのナイロン網で濾過し、Chu13培地
で洗浄濾過した。その後、洗浄した藻体を、湿熱滅菌し
たChu13培地3リットルの入った3リットル用フラ
スコ中に移植し、先の条件で培養した。その結果得られ
た藻体の凍結乾燥重量は1.34gで、ヘキサンで抽出
された炭化水素の割合は58%であった。培養の結果を
図3に示す。B. brauniiの増殖は折れ線1のクロロフィ
ル量として測定して最終的に22倍の濃度となった。折
れ線2は硝酸濃度を示すが、初期濃度32.1Nmg/
lは培養25日目には検出されなくなった。折れ線3は
リン酸濃度を示すが、初期濃度6.64Pmg/lは培
養25日目で4.21Pmg/lに低下した。Comparative Example 1 B. braunii cultivated in a Chu13 medium at 25 ° C. under the condition that an illuminance of 3000 lux and 1% of carbon dioxide were supplied were 2
The mixture was filtered through a 0 μm mesh nylon mesh, washed with Chu 13 medium, and filtered. Then, the washed algal cells were transplanted into a 3 liter flask containing 3 liters of Chu13 medium that had been sterilized by heat and humidity, and cultured under the above conditions. The freeze-dried weight of the resulting algal cells was 1.34 g, and the ratio of hydrocarbons extracted with hexane was 58%. The result of the culture is shown in FIG. The proliferation of B. braunii was measured as the amount of chlorophyll on polygonal line 1 and finally reached a concentration of 22 times. Line 2 shows the nitric acid concentration, but the initial concentration is 32.1 Nmg /
1 was not detected on the 25th day of culture. Line 3 shows the phosphoric acid concentration, but the initial concentration of 6.64 Pmg / l decreased to 4.21 Pmg / l on the 25th day of culture.
【図1】実施例1の培養結果を示すグラフである。FIG. 1 is a graph showing the culture results of Example 1.
【図2】実施例2の培養結果を示すグラフである。FIG. 2 is a graph showing the culture results of Example 2.
【図3】比較例1の培養結果を示すグラフである。FIG. 3 is a graph showing the culture results of Comparative Example 1.
1 クロロフィル濃度を示す折線 2 硝酸濃度を示す折線 3 リン酸濃度を示す折線 1 Polygonal line showing chlorophyll concentration 2 Polygonal line showing nitric acid concentration 3 Polygonal line showing phosphoric acid concentration
【手続補正書】[Procedure amendment]
【提出日】平成5年3月22日[Submission date] March 22, 1993
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0009[Correction target item name] 0009
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0009】[0009]
【実施例】次に本発明を実施例によりさらに詳細に説明
する。本実施例で用いた微細藻類は、Botryococcus bra
uniiである。下水処理水は茨城県下の家庭排水の下水処
理場2カ所より得た下水処理水A及びBである。EXAMPLES Next, the present invention will be described in more detail by way of examples. The microalgae used in this example are Botryococcus bra
unii . The sewage treatment water is sewage treatment water A and B obtained from two domestic wastewater sewage treatment plants in Ibaraki prefecture.
Claims (1)
微細藻類を培養することにより、炭化水素を生産すると
ともに、下水処理水中の無機物を減少させその水質を改
良する方法。1. A method for producing a hydrocarbon by culturing a hydrocarbon-producing microalgae using sewage-treated water as a medium to reduce the amount of inorganic substances in the sewage-treated water and improve its water quality.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13204392A JPH05301097A (en) | 1992-04-24 | 1992-04-24 | Method for purification of treated sewage using microalgae and for simultaneous production of hydrocarbon |
| US08/191,457 US5476787A (en) | 1992-04-24 | 1994-02-03 | Method of removing nitrogen impurities from water using hydrocarbon-producing microalga |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13204392A JPH05301097A (en) | 1992-04-24 | 1992-04-24 | Method for purification of treated sewage using microalgae and for simultaneous production of hydrocarbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH05301097A true JPH05301097A (en) | 1993-11-16 |
Family
ID=15072181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13204392A Pending JPH05301097A (en) | 1992-04-24 | 1992-04-24 | Method for purification of treated sewage using microalgae and for simultaneous production of hydrocarbon |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH05301097A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5476787A (en) * | 1992-04-24 | 1995-12-19 | Director-General Of Agency Of Industrial Science And Technology | Method of removing nitrogen impurities from water using hydrocarbon-producing microalga |
| KR100320786B1 (en) * | 1998-06-03 | 2002-05-13 | 박호군 | Extraction of Hydrocarbons from Microalgae |
| KR100500333B1 (en) * | 2002-03-22 | 2005-07-11 | 김미경 | Culture medium with BMW, and the processing method |
| JP2010539294A (en) * | 2007-09-11 | 2010-12-16 | サファイア エナジー,インコーポレイティド | Method for producing organic products using photosynthetic organisms, products and compositions thereof |
| JP2011212624A (en) * | 2010-04-01 | 2011-10-27 | Toyota Motor Corp | Method for flocculation separation of algae |
| WO2014025020A1 (en) | 2012-08-10 | 2014-02-13 | 株式会社神鋼環境ソリューション | Culture apparatus for microalgae and culture method for microalgae |
| JP2014108101A (en) * | 2012-12-04 | 2014-06-12 | Univ Of Tsukuba | Method for culturing algae using peritoneal dialysis wastewater as culture medium |
| JP2017039078A (en) * | 2015-08-19 | 2017-02-23 | 太平洋セメント株式会社 | Wastewater treatment method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50158145A (en) * | 1972-11-27 | 1975-12-20 | P S Delin |
-
1992
- 1992-04-24 JP JP13204392A patent/JPH05301097A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50158145A (en) * | 1972-11-27 | 1975-12-20 | P S Delin |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5476787A (en) * | 1992-04-24 | 1995-12-19 | Director-General Of Agency Of Industrial Science And Technology | Method of removing nitrogen impurities from water using hydrocarbon-producing microalga |
| KR100320786B1 (en) * | 1998-06-03 | 2002-05-13 | 박호군 | Extraction of Hydrocarbons from Microalgae |
| KR100500333B1 (en) * | 2002-03-22 | 2005-07-11 | 김미경 | Culture medium with BMW, and the processing method |
| JP2010539294A (en) * | 2007-09-11 | 2010-12-16 | サファイア エナジー,インコーポレイティド | Method for producing organic products using photosynthetic organisms, products and compositions thereof |
| JP2014159595A (en) * | 2007-09-11 | 2014-09-04 | Saphia Energy Inc | Methods of producing organic products with photosynthetic organisms and products and compositions thereof |
| JP2011212624A (en) * | 2010-04-01 | 2011-10-27 | Toyota Motor Corp | Method for flocculation separation of algae |
| WO2014025020A1 (en) | 2012-08-10 | 2014-02-13 | 株式会社神鋼環境ソリューション | Culture apparatus for microalgae and culture method for microalgae |
| JP2014108101A (en) * | 2012-12-04 | 2014-06-12 | Univ Of Tsukuba | Method for culturing algae using peritoneal dialysis wastewater as culture medium |
| JP2017039078A (en) * | 2015-08-19 | 2017-02-23 | 太平洋セメント株式会社 | Wastewater treatment method |
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