JPH1179873A - Odorless fermentation treatment of miscellaneous drainage and sludge - Google Patents
Odorless fermentation treatment of miscellaneous drainage and sludgeInfo
- Publication number
- JPH1179873A JPH1179873A JP23835397A JP23835397A JPH1179873A JP H1179873 A JPH1179873 A JP H1179873A JP 23835397 A JP23835397 A JP 23835397A JP 23835397 A JP23835397 A JP 23835397A JP H1179873 A JPH1179873 A JP H1179873A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- sludge
- water content
- treatment
- organic fertilizer
- 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
Classifications
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水分の多い終末処
理場の最終沈澱地の汚泥、澱粉粕、雑排水、人糞尿等の
無臭発酵処理法及びその処理法により製造される有機肥
料に関する。The present invention relates to an odorless fermentation treatment method for sludge, starch lees, miscellaneous wastewater, human manure, and the like in a final sediment in a terminal treatment plant having a large amount of water, and an organic fertilizer produced by the treatment method.
【0002】[0002]
【従来の技術】従来、終末処理場の汚泥、澱粉粕、雑排
水、人糞尿等は大型処理施設やなかには、海洋投棄によ
って処理されている場合もあり、都市問題や環境問題と
なるなど解決の難しい問題をかかえている。2. Description of the Related Art Conventionally, sludge, starch lees, miscellaneous wastewater, human excreta and the like in a final treatment plant are sometimes treated by large-scale treatment facilities or, in some cases, by ocean dumping, resulting in problems such as urban problems and environmental problems. I have a difficult problem.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記の
ごとき、大量に排出される終末処理場汚泥、澱粉粕、雑
排水、人糞尿等は今後、廃棄場所の新規設置困難、海洋
投棄の全面禁止により行き場を失う事は目に見えて明か
であり、不法投棄による環境汚染等様々な形での廃棄処
分が発生することは間違いない。However, in the case of the above-mentioned wastewater treatment plants, sludge, starch lees, miscellaneous wastewater, human manure, etc., which are discharged in large quantities, will be difficult to set up new disposal sites in the future and the ban on marine dumping will be banned. Losing the destination is visibly evident, and there is no doubt that illegal disposal will lead to various forms of disposal, such as environmental pollution.
【0004】本発明は上記のごとき問題点を解消したも
ので、終末処理汚泥、澱粉粕、雑排水、人糞尿等を水分
調整し、好気性発酵菌の発熱による80℃の持続高温に
より無臭になり、有機肥料化し自然に還元し、有効利用
しようとすることを目的としている。The present invention has been made to solve the above problems, and adjusts the moisture content of terminally treated sludge, starch cake, miscellaneous wastewater, human manure, etc., and makes it odorless due to the continuous high temperature of 80 ° C. due to the heat generated by aerobic fermentative bacteria. It is intended to be converted into organic fertilizer and naturally reduced for effective use.
【0005】[0005]
【課題を解決するための手段】終末汚泥、澱粉粕、雑排
水、人糞尿はいずれも水分の多い物質であり、発酵に適
した水分率を越えた水分を含む。これを水分調整材と混
合攪はんして最も発酵しやすい水分率約60%程度に調
整し、好気性発酵菌の存在下で発酵させ、65℃以下に
温度が低下しないよう注意して80℃までの範囲の温度
を維持しながら、繰り返し汚泥、澱粉粕、雑排水、人糞
尿を補充攪はんし高温発酵させ、活発な水分の蒸発によ
り、水分の不足状態を待って繰り返し、補充散布を行
い、高温発酵を持続させる。このように本発明は、高温
発酵を持続させ、充分な発酵熟成後に発酵生成物を取り
出すことを特徴とし、取り出した発酵生成物は有用な有
機肥料となる。The terminal sludge, starch lees, miscellaneous wastewater and human excreta are all substances having a high water content, and contain water exceeding a water content suitable for fermentation. This is mixed and stirred with a water conditioning material to adjust the water content to about 60%, which is the most easily fermented, and fermented in the presence of aerobic fermentation bacteria. Replenishing and stirring sludge, starch lees, miscellaneous wastewater and human excrement repeatedly at high temperature fermentation while maintaining the temperature in the range up to ℃. To maintain high temperature fermentation. As described above, the present invention is characterized in that high-temperature fermentation is sustained and a fermentation product is taken out after sufficient fermentation and maturation, and the taken out fermentation product becomes a useful organic fertilizer.
【0006】終末汚泥、澱粉粕、雑排水、人糞尿は水分
率約60〜90%程度の高い水分を含んでいる。一方、
水分調整材として水分率の低いコーヒー粕、鋸屑、木
屑、籾殻、藁、雑草等水分率約20〜30%程度の物を
使用する。[0006] Terminal sludge, starch lees, miscellaneous wastewater, and human manure contain a high water content of about 60 to 90%. on the other hand,
As a moisture adjusting material, a material having a moisture content of about 20 to 30%, such as coffee grounds, sawdust, wood chips, rice husks, straw, and weeds, having a low water percentage is used.
【0007】[0007]
【発明の実施の形態】発酵槽に、コーヒー粕、鋸屑、雑
草、藁、籾殻等の混合物を水分調整材として入れる。混
合物の水分率は約30%程度で、あらかじめ別槽で40
〜50℃に予備発酵させたものである。その上から水分
率約60〜90%程度の多量の水分を含んだ汚泥、澱粉
粕、雑排水、人糞尿等を散布、攪はんして最も発酵しや
すい水分率約60%程度になるように水分調整をする。
水分が50%以下、または70%以上では発酵温度の低
下が認められる。終末処理場の沈澱汚泥、澱粉粕、雑排
水、あるいは人糞尿とも多量の水分を含むものを使用す
る場合は水分調整材を新たに加えることもできる。好気
性発酵菌の存在下攪はんして発酵させる、発酵温度は、
発酵作業開始後、約8時間ないし18時間で65℃程度
に達する。BEST MODE FOR CARRYING OUT THE INVENTION In a fermenter, a mixture of coffee grounds, sawdust, weeds, straw, rice hulls and the like is put as a moisture adjusting material. The water content of the mixture is about 30%,
Pre-fermented at ~ 50 ° C. Spray sludge, starch lees, miscellaneous wastewater, human manure, etc., containing a large amount of water with a water content of about 60-90% from above, so that the water content is about 60%, which is most easily fermented by stirring. Adjust moisture.
When the water content is 50% or less, or 70% or more, a decrease in the fermentation temperature is observed. In the case where sediment sludge, starch lees, miscellaneous wastewater, or human manure containing a large amount of water is used in the terminal treatment plant, a water conditioner may be newly added. Fermentation by stirring in the presence of aerobic fermenters, fermentation temperature,
The temperature reaches about 65 ° C. in about 8 to 18 hours after the start of the fermentation operation.
【0008】長時間の高温発酵状態の持続により水分が
活発に蒸発して減少するので、以後発酵温度を約65℃
以下に低下しないよう注意して汚泥、澱粉粕、雑排水を
連続的、あるいは間欠的に補充散布し、攪はんを継続し
ながら発酵させる。又必要に応じてエアーレーションを
行い、高温発酵を助長促進し大量の水分の蒸発をはかる
事ができる。発酵期間は約60〜90日程度である。汚
泥、澱粉粕、雑排水、人糞尿等と水分調整材の質量によ
り異なるので特定はできないが、発酵温度は徐々に低下
する。約40℃程度まで下降するのを待って別槽に移し
2〜3回の切り返しをして、過剰水分の蒸発及び放熱を
行い発酵有機肥料を得る。得られた有機肥料は汚泥、澱
粉粕、雑排水、人糞尿中の有機質成分と水分調整材の植
物繊維組成分からなり、肥料に加えて良質の土壌改良剤
として優れている。[0008] Since the water content evaporates and decreases as the high temperature fermentation state continues for a long time, the fermentation temperature is set to about 65 ° C.
Sludge, starch lees and miscellaneous wastewater are continuously or intermittently replenished and sprayed, paying attention not to decrease below, and fermented while continuing stirring. In addition, aeration can be performed as needed to promote high-temperature fermentation and to evaporate a large amount of water. The fermentation period is about 60 to 90 days. Although it cannot be specified because it differs depending on the mass of the moisture control material such as sludge, starch residue, miscellaneous wastewater, human manure, etc., the fermentation temperature gradually decreases. Waiting for the temperature to drop to about 40 ° C., transfer to a separate tank, and turn it back two or three times to evaporate excess heat and release heat to obtain fermented organic fertilizer. The obtained organic fertilizer is composed of an organic component in sludge, starch lees, miscellaneous wastewater, human feces and urine, and a plant fiber component of a moisture regulator, and is excellent as a good soil conditioner in addition to fertilizer.
【0009】深さ1.5m、幅3m、長さ5mのコンク
リート製の発酵槽に、コーヒー粕3m3、鋸屑5m3、米
糠1m3、藁1m3の発酵材料を前もって混合攪はんし、
予備発酵させたものを入れた、その上から終末処理汚
泥、澱粉粕、雑排水、人糞尿の混合物約300kg(こ
の混合物の水分率は約80%程度であった)を散布し
た。水分の不足を感じたので更に雑排水を100kg程
度追加して、ショベルローダーで混合攪はんした。水分
率約60%になったところでエアレーションを開始し
た。約15時間を経過した頃に発酵温度が65℃に達し
ていた。約20時間を経過する頃には75℃まで達して
いたが24時間を過ぎる頃には高温のために水分が蒸発
して水分不足状態となり温度が下降状態を示したので、
その時点で再び汚泥、澱粉粕、雑排水、人糞尿を約30
0kg追加散布した。常時発酵温度を65℃以上を維持
するよう、2カ月間同様の排水の散布と攪はん作業、エ
アレーションを繰り返した。全期間を通じて排水の処理
量は3500kgに達していた。発酵温度が徐々に下降
を始め、40℃になった時点で、発酵生成物を取り出し
て別の場所で3回の切り返しをして有機肥料として製品
化した。In a concrete fermenter of 1.5 m depth, 3 m width and 5 m length, fermentation materials of 3 m 3 of coffee grounds, 5 m 3 of sawdust, 1 m 3 of rice bran and 1 m 3 of straw are mixed and stirred in advance.
About 300 kg of a mixture of the terminally treated sludge, starch lees, miscellaneous wastewater and human manure (water content of this mixture was about 80%) containing the preliminarily fermented product was sprayed thereon. I felt that there was a shortage of water, so I added about 100 kg of miscellaneous wastewater and mixed with a shovel loader. Aeration was started when the water content reached about 60%. After about 15 hours, the fermentation temperature had reached 65 ° C. By about 20 hours, the temperature had reached 75 ° C. However, by about 24 hours, the water had evaporated due to the high temperature and the water was in a shortage state.
At that time, sludge, starch lees, miscellaneous wastewater, human excreta were again
An additional 0 kg was sprayed. In order to maintain the fermentation temperature at 65 ° C. or higher at all times, the same spraying, stirring, and aeration of wastewater were repeated for two months. Throughout the period, the amount of treated wastewater reached 3500 kg. When the fermentation temperature gradually began to fall and reached 40 ° C., the fermentation product was taken out and turned back three times in another place to produce an organic fertilizer.
【0010】[0010]
【発明の効果】本発明の汚泥、雑排水、人糞尿等の処理
方法によれば、以下の実用上の利点に加えて排水の放
出、不法投棄などによる環境汚染を防止できる。 (1)発酵熱の利用により、大部分が水分からなる終末
汚泥、澱粉粕、雑排水、人糞尿等の水分を効率的に蒸発
除去できて排水の放出は皆無となる。併せてエネルギー
消費量が少なくてすむ。従来の技術で困難であった悪臭
もコーヒー粕の作用で完全に脱臭できる。従来の排水処
理施設に比べると、設備の建設コストも約2分の1以下
でよい。 (2)得られた発酵生成物は肥料成分も高く良質の有機
肥料として有用であり、地球に優しく社会に優しく、そ
して自然に優しい処理方法でさらにリサイクルできる特
典がある。According to the method for treating sludge, miscellaneous wastewater, human manure, etc. of the present invention, in addition to the following practical advantages, environmental pollution due to discharge of wastewater, illegal dumping, etc. can be prevented. (1) By utilizing fermentation heat, water such as terminal sludge, starch cake, miscellaneous wastewater, human manure, etc., which is mostly composed of water, can be efficiently removed by evaporation, and there is no discharge of wastewater. In addition, energy consumption is small. Offensive odors that were difficult with conventional techniques can also be completely deodorized by the action of coffee grounds. Compared with a conventional wastewater treatment facility, the construction cost of the equipment may be about half or less. (2) The fermented product obtained has a high fertilizer component and is useful as a high-quality organic fertilizer.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C05F 7/00 C05F 9/04 9/04 11/00 11/00 B09B 3/00 ZABA ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI C05F 7/00 C05F 9/04 9/04 11/00 11/00 B09B 3/00 ZABA
Claims (2)
気性発酵菌で予備発酵させた水分調整材に終末処理場沈
澱汚泥、澱粉粕、雑排水、人糞尿等を混入し、水分率約
60%に調整して発酵させ約80℃の発酵熱の環境下で
2〜3カ月間継続発酵させることを特徴とする無臭発酵
処理法。[Claim 1] Mixing coffee sludge, sawdust, rice bran, and straw and preliminarily fermenting with aerobic fermentation bacterium into final treatment plant sedimentation sludge, starch lees, miscellaneous wastewater, human manure, etc. An odorless fermentation treatment method characterized in that fermentation is adjusted to about 60% and fermentation is continued for about 2 to 3 months under an environment of fermentation heat of about 80 ° C.
れる有機肥料。2. An organic fertilizer produced by the fermentation treatment method according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23835397A JPH1179873A (en) | 1997-09-03 | 1997-09-03 | Odorless fermentation treatment of miscellaneous drainage and sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23835397A JPH1179873A (en) | 1997-09-03 | 1997-09-03 | Odorless fermentation treatment of miscellaneous drainage and sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1179873A true JPH1179873A (en) | 1999-03-23 |
Family
ID=17028940
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23835397A Pending JPH1179873A (en) | 1997-09-03 | 1997-09-03 | Odorless fermentation treatment of miscellaneous drainage and sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH1179873A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003041256A (en) * | 2001-08-01 | 2003-02-13 | Tatsuya Kajikuri | Soil-conditioning material and its manufacturing method |
CN102838388A (en) * | 2012-10-08 | 2012-12-26 | 农鑫高科(北京)科技开发有限公司 | Method for producing organic fertilizer by utilizing water body bottom mud |
CN103332987A (en) * | 2013-07-10 | 2013-10-02 | 丹阳市淸云农业发展有限公司 | Organic fertilizer |
CN103739326A (en) * | 2013-12-24 | 2014-04-23 | 宁波市金穗有机肥有限公司 | Method for preparing temperature-increasing organic fertilizer and temperature-increasing organic fertilizer |
CN105152698A (en) * | 2015-08-07 | 2015-12-16 | 成都易胜科生物科技有限公司 | Preparation technology of organic fermented material |
CN108191399A (en) * | 2018-02-25 | 2018-06-22 | 上海鑫晶山建材开发有限公司 | A kind of biomass modified sludge baked brick and preparation method thereof |
-
1997
- 1997-09-03 JP JP23835397A patent/JPH1179873A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003041256A (en) * | 2001-08-01 | 2003-02-13 | Tatsuya Kajikuri | Soil-conditioning material and its manufacturing method |
CN102838388A (en) * | 2012-10-08 | 2012-12-26 | 农鑫高科(北京)科技开发有限公司 | Method for producing organic fertilizer by utilizing water body bottom mud |
CN103332987A (en) * | 2013-07-10 | 2013-10-02 | 丹阳市淸云农业发展有限公司 | Organic fertilizer |
CN103739326A (en) * | 2013-12-24 | 2014-04-23 | 宁波市金穗有机肥有限公司 | Method for preparing temperature-increasing organic fertilizer and temperature-increasing organic fertilizer |
CN105152698A (en) * | 2015-08-07 | 2015-12-16 | 成都易胜科生物科技有限公司 | Preparation technology of organic fermented material |
CN108191399A (en) * | 2018-02-25 | 2018-06-22 | 上海鑫晶山建材开发有限公司 | A kind of biomass modified sludge baked brick and preparation method thereof |
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