JPH09295000A - Anaerobic digestion of sludge or raw excretion - Google Patents

Anaerobic digestion of sludge or raw excretion

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Publication number
JPH09295000A
JPH09295000A JP13443196A JP13443196A JPH09295000A JP H09295000 A JPH09295000 A JP H09295000A JP 13443196 A JP13443196 A JP 13443196A JP 13443196 A JP13443196 A JP 13443196A JP H09295000 A JPH09295000 A JP H09295000A
Authority
JP
Japan
Prior art keywords
sludge
digestion
ppm
amount
saponin
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
Application number
JP13443196A
Other languages
Japanese (ja)
Other versions
JP3893545B2 (en
Inventor
Eiichi Tashiro
榮一 田代
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Individual
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Individual
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Priority to JP13443196A priority Critical patent/JP3893545B2/en
Publication of JPH09295000A publication Critical patent/JPH09295000A/en
Application granted granted Critical
Publication of JP3893545B2 publication Critical patent/JP3893545B2/en
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Expired - Fee Related legal-status Critical Current

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Classifications

    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently digest sludge generated in a sewage or excretion treatment plant without changing an apparatus or treatment operation and to enable the increase of treatment quantity and the miniaturization of a digestion tank. SOLUTION: In an anaerobic sludge digestion process, an extract containing 2% of quilaja saponin is added to sludge in an amt. of 2-30ppm within a medium temp. region and in an amt. of 1.5-17ppm in a high temp. region to increased the generation amt. of gas by 10% or more as compared with the case of non- addition.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、下水処理場や屎尿
処理場等で発生する汚泥や、屎尿処理場へ搬入される生
屎尿の消化を促進させる方法に係わり、汚泥や生屎尿中
にシャボンの木の抽出液を添加して処理するものに関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for promoting digestion of sludge generated in a sewage treatment plant, an excrement treatment plant, and the like, or a raw excrement carried into the excrement treatment plant. The present invention relates to the one to be treated by adding the extract of the tree.

【0002】[0002]

【従来の技術】下水処理場や屎尿処理場等に流入する排
水や屎尿は、最終的に処理水と汚泥に分離され、処理水
は河川等に放流される。一方、汚泥は、脱水後に焼却や
埋め立て処分されることもあるが、未だ多くの有機物を
含有しているので脱水後の容積を減少させるために、汚
泥消化槽等で嫌気性細菌により分解してBOD成分を減
少させ、その後に脱水して焼却や埋め立てされる場合が
多い。これに対し、生屎尿の場合は、BOD成分が1万
ppm 以上も含まれているので、これを嫌気性消化してB
OD成分を減少させてから曝気槽に送ることが一部で行
われている。
2. Description of the Related Art Wastewater and human waste that flow into a sewage treatment plant, a human waste treatment plant, etc. are finally separated into treated water and sludge, and the treated water is discharged into a river or the like. On the other hand, sludge may be incinerated or landfilled after dehydration, but since it still contains many organic substances, it is decomposed by anaerobic bacteria in a sludge digestion tank etc. in order to reduce the volume after dehydration. In many cases, BOD components are reduced and then dehydrated for incineration or landfill. On the other hand, in the case of human waste, the BOD component is 10,000
Since it contains more than ppm, anaerobically digest this and B
In some cases, the OD component is reduced and then sent to the aeration tank.

【0003】以下、主として下水処理場で発生する汚泥
の消化について説明する。嫌気性消化とは、上記したよ
うに汚泥或いは生屎尿中の有機物を嫌気性細菌や微生物
の働きによって、酵素を触媒として、酸性発酵期、
酸性減退期、アルカリ性発酵期の3段階を経て分解す
ることを言う。この有機物分解を消化と言い、は主と
して糖類、溶解性澱粉、繊維素、溶解性窒素化合物が分
解し、有機酸、硫化水素、大量の炭酸ガス、窒素及び重
炭酸塩を生成し、pHは6.8〜5.1程度まで低下する。
の段階では、窒素化合物が分解し、酸度が減少すると
ともにアンモニア性窒素が増加し、pHが6.6〜6.8程
度まで上昇する。の段階では、主として蛋白質、アミ
ノ酸、油脂等の難分解質が分解し、pHが上昇して7.0
〜7.4程度に達し、ガス中のメタン含有量が多くなり、
汚泥は安定した粗粒となる。最終ガス発生量の90%の
ガスが発生するまでの汚泥消化に要する日数は、消化温
度によって異なる。消化温度が40℃以下を中温消化
帯、40℃以上を高温消化帯と言い、両者の差異は主と
して消化に与かる嫌気性菌や微生物の違いによる。
The digestion of sludge generated mainly in a sewage treatment plant will be described below. Anaerobic digestion, as described above, the organic matter in the sludge or raw human waste by the action of anaerobic bacteria and microorganisms, the enzyme as a catalyst, the acidic fermentation period,
Decomposes through three stages of acid decline and alkaline fermentation. This decomposition of organic matter is called digestion, which mainly decomposes sugars, soluble starch, fibrin, and soluble nitrogen compounds to produce organic acids, hydrogen sulfide, large amounts of carbon dioxide, nitrogen and bicarbonate, and the pH is 6 It decreases to about 0.8 to 5.1.
In the stage, the nitrogen compound is decomposed, the acidity is decreased, the ammonia nitrogen is increased, and the pH is increased to about 6.6 to 6.8. At the stage of, the insoluble matter such as proteins, amino acids, fats and oils is mainly decomposed, and the pH rises to 7.0.
Up to about 7.4, the methane content in the gas increases,
Sludge becomes stable coarse particles. The number of days required for digesting sludge until 90% of the final amount of gas produced is different depending on the digestion temperature. A digestion temperature of 40 ° C. or lower is called a medium temperature digestion zone, and a temperature of 40 ° C. or higher is called a high temperature digestion zone. The difference between the two is mainly due to the difference in anaerobic bacteria and microorganisms involved in digestion.

【0004】[0004]

【発明が解決しようとする課題】ところが、嫌気性細菌
は好気性細菌と異なり有機物分解速度が極めて遅く、消
化には数十日(設計では50日、現実は35日程度)を
要する。一方、発生する汚泥量は極めて多く、下水道の
場合、1万人規模の町で10〜20m3 /日、100万
人規模の都市では2000〜4000m3 /日も発生す
ると言われている。従って、汚泥を完全に消化するに
は、極めて大型の消化槽を多数必要とする。現在、消化
効率の良い卵型消化槽が開発され、また40℃以上に加
温する高温消化法が採用されるなど種々改良が加えられ
ているが、改良は頭打ちの状態にある。
However, unlike aerobic bacteria, anaerobic bacteria have a very slow organic matter decomposition rate, and digestion requires several tens of days (50 days by design, 35 days in reality). On the other hand, the amount of sludge generated is extremely large, and it is said that 10 to 20 m 3 / day is generated in a town of 10,000 people and 2000 to 4000 m 3 / day in a city of 1 million people in the case of sewerage. Therefore, in order to completely digest sludge, a large number of extremely large digestion tanks are required. At present, various improvements have been made, such as the development of an egg-type digestion tank with good digestion efficiency and the adoption of a high-temperature digestion method of heating to 40 ° C. or higher, but the improvement is at a level.

【0005】そこで本発明者は、現有の消化槽や消化操
作をそのまま利用し、嫌気性細菌や微生物の活性を向上
させて消化効率を向上させることに着目して研究を続
け、本発明を完成させた。尚、消化の程度はガスの発生
量で推測される。
Therefore, the present inventor continued research by paying attention to improving the digestive efficiency by improving the activity of anaerobic bacteria and microorganisms by utilizing the existing digestive tank and digestion operation as they are, and completed the present invention. Let The extent of digestion is estimated by the amount of gas generated.

【0006】[0006]

【課題を解決するための手段】本発明は、好気性細菌や
微生物の活性化に効果があったシャボンの木の抽出液
を、汚泥中にある特定の割合で添加することを最大の特
徴とする。即ち、汚泥にシャボンの木の抽出液を添加す
る、添加量に応じてガスの発生量は増加するが、添加量
がある一定量を越えると逆に低下し、遂には無添加の場
合よりも減少することを見いだした。また、添加量は消
化温度に依存することを見いだして本発明を完成させた
ものでをある。
SUMMARY OF THE INVENTION The present invention is characterized by adding soap tree extract, which was effective in activating aerobic bacteria and microorganisms, at a specific ratio in sludge. To do. That is, when the soap tree extract is added to the sludge, the gas generation amount increases according to the addition amount, but when the addition amount exceeds a certain amount, it decreases conversely, and finally, compared to the case of no addition. I found that it decreased. Further, the present invention has been completed by finding that the addition amount depends on the digestion temperature.

【0007】キラヤサポニンは、トルペノイドサポニン
の一種で、シャボンの木をアルコールで抽出したものに
約2%(天然サポニンとして約4%)含まれている。こ
の抽出液には、20%程度の糖類と1%強の粗蛋白が含
まれている。キラヤサポニンは、その生理活性により、
微生物の反応促進作用やストレス緩和作用を示すととも
に、油脂分解作用や酸素溶解効率の向上効果をもたら
す。尚、好気処理では排水量に対しシャボンの木の抽出
液を0.5〜4ppm 、油分(ノルマルヘキサン抽出物)が
多い排水で10ppm 程度の添加で十分な効果が生じてい
る。一方、嫌気処理では、酸素溶解は不要であるし、汚
泥中には油脂分も少ない。結局、キラヤサポニンの生理
活性作用が重要と思われる。しかし、サポニンは抗菌作
用を有している。従って、あまり高濃度だと、逆に細菌
の活性を削ぐおそれがある。
Quillaja saponin is a type of torpenoid saponin, and is contained in about 2% (about 4% as natural saponin) of soap tree extracted with alcohol. This extract contains about 20% saccharides and a little over 1% crude protein. Quillaja saponin, due to its physiological activity,
It has the effect of promoting the reaction of microorganisms and the effect of alleviating stress, and also has the effect of decomposing fats and oils and improving the efficiency of oxygen dissolution. In aerobic treatment, addition of soap tree extract to 0.5 to 4 ppm relative to the amount of wastewater and addition of about 10 ppm to wastewater containing a large amount of oil (normal hexane extract) produce a sufficient effect. On the other hand, in the anaerobic treatment, it is not necessary to dissolve oxygen, and the amount of oil and fat is small in the sludge. After all, the physiologically active action of Quillaja saponin seems to be important. However, saponin has an antibacterial effect. Therefore, if the concentration is too high, the activity of bacteria may be adversely affected.

【0008】一方、本発明者は種々の経験から、微生物
の生理活性に影響を与えるのはキラヤサポニンのみでは
なく、シャボンの木の抽出液に含まれる他の成分、こと
に糖類や粗蛋白も影響を与えていると思われる。これ
は、シャボンの木の抽出液を処理してキラヤサポニン濃
度を4.5%(天然サポニンとして約10%)に高めたも
のを2種類試作し、その微生物に対する効果を測定した
ところ、前記抽出液よりも効果が劣っていることが判明
した。即ち、高濃度サポニンの一種は、糖類が約15
%、粗蛋白が0.5%含まれており、他の一種は糖類が約
30%、粗蛋白が約1.5%含まれていた。そして、この
2種類の液をキラヤサポニンが2%(なるように希釈し
て排水処理(活性汚泥)に供したところ、前者は余り効
果がなく、後者は前記抽出液と同程度あるいはそれより
幾分劣る程度の効果しか得られなかった。もし、キラヤ
サポニンの生理活性が100%であるとすると、このよ
うな結果にはならない。これは、他の成分の働きもある
ものと推察された。サポニンと同程度の極めて低い濃度
で劇的な生理活性作用を示すものは、酵素以外に考えら
れない。粗蛋白中には、この酵素或いは酵素類似物質が
含まれているものと推察される。
On the other hand, the present inventor has learned from various experiences that not only quillaja saponin affects physiological activity of microorganisms but also other components contained in the extract of soap tree, especially sugars and crude proteins. It seems to have an influence. This is the result of treating two kinds of soap tree extract with a quillaja saponin concentration increased to 4.5% (about 10% as natural saponin) and measuring the effect on the microorganism. It turned out that the effect was inferior to the liquid. That is, one type of high-concentration saponin contains about 15 sugars.
%, 0.5% of crude protein was contained, and the other one contained about 30% of saccharide and about 1.5% of crude protein. Then, when these two kinds of liquids were diluted to 2% of quillaja saponin and subjected to wastewater treatment (activated sludge), the former was not so effective, and the latter was the same as or slightly more than the extract. If the physiological activity of Quillaja saponin was 100%, this result would not be obtained, and it is speculated that this may be due to the action of other ingredients. Other than the enzyme, it is unlikely that it exhibits a dramatic physiological activity at an extremely low concentration equivalent to that of saponin, and it is presumed that this enzyme or enzyme-like substance is contained in the crude protein.

【0009】キラヤサポニン、粗蛋白のいずれがより効
果があるかは不明であるが、いずれにしても、これらを
含有する前記シャボンの木の抽出液そのものを使用し
て、汚泥の消化を行わせたところ、中温域、高温域と
も、ガス(メタンガス)の発生量が無添加の場合に比べ
て大幅な増加が見られた。究極のトータルガス発生量
は、汚泥中の有機物含有量から決まっており、ガス発生
量が増加することは、消化期間の短縮を意味する。従っ
て、消化装置内における汚泥の回転率が速くなり、引い
ては装置の小型化が可能にくなる。また、現有装置で
は、より大量の汚泥が処理できることが可能になる。
[0009] It is unknown which of Quillaja saponin and crude protein is more effective, but in any case, the soap tree extract containing them is used to digest sludge. On the other hand, in both the middle temperature range and the high temperature range, a large increase was observed in the amount of gas (methane gas) generated compared to the case without addition. The ultimate total gas generation amount is determined by the organic matter content in the sludge, and an increase in the gas generation amount means that the digestion period is shortened. Therefore, the rotation rate of the sludge in the digestion apparatus is increased, which makes it possible to downsize the apparatus. In addition, the existing device can process a larger amount of sludge.

【0010】ところで、シャボンの木の抽出液の添加に
よりガス発生量は、例えば、中温域の場合は5ppm 添加
するだけで約30%増加し、10ppm では60%増加し
た。しかし、その後は増加の割合が減少し、20ppm で
は約40%の増加にとどまった。これは、サポニンの添
加量の増加に伴って酸生成菌が増加して必要以上に低級
脂肪酸を生成させたため、メタン発酵が阻害されてされ
たものと推察される。或いは、サポニンの抗菌作用に起
因するものとも思われる。シャボンの木の抽出液の高濃
度の添加によるメタン発酵の阻害の割合は、汚泥の温度
が高くなるほど顕著に現れる。即ち、高温域では、5pp
m の添加でガス発生量は約36%増加し、10ppm では
90%増加したが、20ppm の添加では、逆に無添加の
場合よりも約25%減少した。尚、シャボンの木の抽出
液の添加コストを考慮した場合、ガス発生量が無添加の
場合と比べて30%増加すれば採用には十分な理由があ
るとされるが、増大の一途を辿る汚泥の処理に対する設
備の増強コストを考慮すれば、10%程度の増加でもそ
の効果は大きいものと思われる。
By the way, the gas generation amount by the addition of the soap tree extract increased by about 30% only by adding 5 ppm in the middle temperature range, and increased by 60% at 10 ppm. However, after that, the rate of increase decreased, and at 20 ppm, it increased to only about 40%. It is speculated that this is because methane fermentation was inhibited because the number of acid-producing bacteria increased with the increase in the amount of saponin added and produced lower fatty acids more than necessary. Alternatively, it may be caused by the antibacterial action of saponin. The rate of inhibition of methane fermentation due to the addition of a high concentration of soap tree extract becomes more pronounced as the temperature of sludge increases. That is, in the high temperature range, 5pp
The gas generation amount increased by about 36% with the addition of m, and increased by 90% at 10 ppm, but conversely with the addition of 20 ppm, it decreased by about 25% as compared with the case without addition. Considering the cost of adding soap tree extract, it is said that there is a sufficient reason for adoption if the amount of gas generated increases by 30% compared to the case where no gas is added, but it will only increase. Considering the cost of increasing the equipment for sludge treatment, even if the increase is about 10%, the effect will be great.

【0011】従って、上記結果から、ガス発生量を10
%増加させるには、中温域では前記シャボンの木の抽出
液の場合で約2ppm 〜30ppm 添加すれば良いことにな
る。また、30%増加させるには、5ppm 〜25ppm 添
加すれば良いことになる。また高温域の場合は、ガス発
生量を10%増加させるのに1.5ppm 〜17ppm 、30
%増加させるには、4ppm 〜14ppm 添加すれば良いこ
とになる。また何れの場合も、コストを考慮すれば2〜
10ppm の添加で、ガス発生量を10〜60%(高温域
では90%)増加させることができる。尚、これらは回
分式のテスト結果であるが、実際の装置では汚泥は連続
的に投入されるので、トータル発生量の増加はこれより
悪くなるが、それでも10ppm 添加で40%程度増加す
る。
Therefore, from the above results, the gas generation amount is 10
%, It is sufficient to add about 2 ppm to 30 ppm in the case of the soap tree extract in the medium temperature range. To increase the amount by 30%, it is sufficient to add 5 ppm to 25 ppm. In the high temperature range, 1.5ppm to 17ppm, 30 to increase the gas generation rate by 10%.
%, It is sufficient to add 4 ppm to 14 ppm. In any case, if cost is taken into consideration,
The addition of 10 ppm can increase the gas generation amount by 10 to 60% (90% in the high temperature range). Although these are batch-type test results, since the sludge is continuously fed in an actual device, the total production amount is worse than this, but it still increases by about 40% when 10 ppm is added.

【0012】[0012]

【実施例】以下、本発明を実施例により詳細に説明す
る。容量5L(リットル、以下同じ)の実験用嫌気性消
化槽を4組用意し、いずれにも下水処理場から採取した
生汚泥2Lと消化汚泥2Lを投入した。そして、1つの
嫌気性消化槽には何も添加せず、他の3つの嫌気性消化
槽には、それぞれシャボンの木の抽出液(キラヤサポニ
ン1.9%(天然サポニンとして約4%)、糖類(全糖)
21.6%、粗蛋白1.1%を含む)を汚泥量に対して5m
g/L(5ppm )、10mg/L(10ppm )、20m
g/L(20ppm )添加した。この4つの汚泥混合物
を、38℃(中温消化)に保ちながら、30日間ゆっく
り攪拌を続けた。各消化槽について、発生するガス量
(mL/日)を毎日測定した。その合計量を表1に示
す。 表1 抽出液添量 無添加 5ppm 10ppm 20ppm 中温消化 8,980ml 11,730ml 14,420ml 12,520ml 高温消化 8,830ml 11,985ml 16,810ml 6,670ml
EXAMPLES The present invention will be described in detail below with reference to examples. Four sets of experimental anaerobic digestion tanks each having a capacity of 5 L (liter, the same applies hereinafter) were prepared, and 2 L of raw sludge and 2 L of digested sludge collected from a sewage treatment plant were put into each of them. Nothing was added to one anaerobic digester, and soap tree extract (Quillaja saponin 1.9% (about 4% as natural saponin)) was added to each of the other three anaerobic digesters. Sugar (total sugar)
21.6%, including crude protein 1.1%) 5m against sludge amount
g / L (5ppm), 10mg / L (10ppm), 20m
g / L (20 ppm) was added. The four sludge mixtures were slowly stirred for 30 days while maintaining the temperature at 38 ° C (medium temperature digestion). The amount of gas generated (mL / day) was measured daily for each digester. The total amount is shown in Table 1. Table 1 Addition amount of extract solution No addition 5ppm 10ppm 20ppm Medium digestion 8,980ml 11,730ml 14,420ml 12,520ml High temperature digestion 8,830ml 11,985ml 16,810ml 6,670ml

【0013】表1からは、シャボンの木の抽出液を添加
したものは、ガスの発生量が増加していることがわか
る。但し、高温消化の場合、20ppm では逆に減少して
いる。これは、この嫌気性消化槽ではpHが他の場合よ
りも低くなっており、その影響と思われる。即ち、一般
的に低級脂肪酸が2000ppm 以上蓄積されるとメタン発酵
が阻害され、ガス発生は停止すると言われている。従っ
て、サポニンの添加量が多くなると、中温域、高温域を
とわず酸生成菌が活性化し、必要以上に低級脂肪酸を生
成させたため、酸性発酵とメタン発酵との動的平行が取
れなくなり、脂肪酸が高濃度に蓄積してガス発生に障害
をもたらすものと推察される。このことは、高温域の場
合ほど顕著である。これは、同じメタン発酵菌でも、中
温菌の場合は酸に対する分解能が大きいが、高温菌では
分解能が劣るためと推察される。
From Table 1, it can be seen that the amount of gas generated is increased in the case where the soap tree extract is added. However, in the case of high-temperature digestion, it decreased at 20 ppm. This is probably due to the lower pH in this anaerobic digester than in other cases. That is, it is generally said that methane fermentation is inhibited and gas generation is stopped when lower fatty acids are accumulated at 2000 ppm or more. Therefore, when the amount of saponin added is large, the acid-producing bacteria are activated regardless of the medium temperature range and the high temperature range, and since lower fatty acids are produced more than necessary, the dynamic parallelism between acidic fermentation and methane fermentation cannot be obtained, It is presumed that the fatty acid accumulates in a high concentration and causes an obstacle to gas generation. This is more remarkable in the high temperature region. This is presumably because even in the same methane-fermenting bacterium, the mesophilic bacterium has a large ability to decompose an acid, whereas the thermophilic bacterium has a poor ability to decompose an acid.

【0014】[0014]

【発明の効果】以上詳述したように、本発明の汚泥或い
は生屎尿の嫌気性消化方法は、嫌気性消化工程中におい
て、シャボンの木の抽出液を添加して消化を行わせるも
のである。そして、特に汚泥量に対して中温域で2ppm
〜30ppm 、高温域で1.5ppm〜17ppm 添加して消化
を行わせるものである。
As described above in detail, the anaerobic digestion method of sludge or human waste according to the present invention is performed by adding a soap tree extract during the anaerobic digestion step. . And, especially for sludge amount, 2ppm in the middle temperature range
-30 ppm, and 1.5 ppm-17 ppm in the high temperature range for digestion.

【0015】そのため、消化時に発生するメタンガス量
が無添加の場合に比べて約4割以上も増加し、消化が大
幅に促進されたことが判る。しかも、消化槽その他の装
置及び処理操作は従来と全く同じであり、コストは添加
剤のみであり、トータル処理費用は大幅に減少する。
Therefore, it is understood that the amount of methane gas generated during digestion increased by about 40% or more as compared with the case of no addition, and digestion was greatly promoted. Moreover, the digestion tank and other devices and processing operations are exactly the same as the conventional ones, and the cost is only the additive, and the total processing cost is greatly reduced.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 汚泥或いは生屎尿の嫌気性消化工程中に
おいて、シャボンの木の抽出液を添加することを特徴と
する汚泥或いは生屎尿の嫌気性消化方法。
1. A method for anaerobic digestion of sludge or raw human sewage, which comprises adding an extract of a soap tree during the anaerobic digestion step of sludge or raw human sewage.
【請求項2】 キラヤサポニンを2%含有するシャボン
の木の抽出液を、中温域で2ppm 〜30ppm 、高温域で
1.5ppm 〜17ppm 添加するものである請求項1記載の
汚泥或いは生屎尿の嫌気性消化方法。
2. A soap tree extract containing 2% of quillaja saponin is used in the range of 2 to 30 ppm in the medium temperature range and in the high temperature range.
The method for anaerobic digestion of sludge or raw sewage according to claim 1, which is added in an amount of 1.5 ppm to 17 ppm.
JP13443196A 1996-04-30 1996-04-30 Anaerobic digestion of sludge or ginger urine Expired - Fee Related JP3893545B2 (en)

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Application Number Priority Date Filing Date Title
JP13443196A JP3893545B2 (en) 1996-04-30 1996-04-30 Anaerobic digestion of sludge or ginger urine

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JPH09295000A true JPH09295000A (en) 1997-11-18
JP3893545B2 JP3893545B2 (en) 2007-03-14

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003112166A (en) * 2001-09-30 2003-04-15 Eiichi Tashiro Anaerobic cleaning method for soil
JP2004188406A (en) * 2002-04-02 2004-07-08 Eiichi Tashiro Anaerobic purifying method for soil
CN107299116A (en) * 2017-08-02 2017-10-27 湖南农业大学 Application of the Secondary metabolites in biomass anaerobic fermentation

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60106595A (en) * 1983-11-16 1985-06-12 Takashi Masai Treatment of sludge
JPS61118189A (en) * 1984-11-12 1986-06-05 Masazumi Takebe Method for accelerating action of microbe
JPS6242800A (en) * 1985-08-20 1987-02-24 Iwao Ueda Treatment of excess sludge
JPS63242400A (en) * 1987-03-31 1988-10-07 Maruzen Kasei Kk Treatment of excess sludge
JPH06121996A (en) * 1992-05-29 1994-05-06 Eiichi Tashiro Treatment of waste water
JPH07251187A (en) * 1993-09-30 1995-10-03 Eiichi Tashiro Solid agent for water treatment

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60106595A (en) * 1983-11-16 1985-06-12 Takashi Masai Treatment of sludge
JPS61118189A (en) * 1984-11-12 1986-06-05 Masazumi Takebe Method for accelerating action of microbe
JPS6242800A (en) * 1985-08-20 1987-02-24 Iwao Ueda Treatment of excess sludge
JPS63242400A (en) * 1987-03-31 1988-10-07 Maruzen Kasei Kk Treatment of excess sludge
JPH06121996A (en) * 1992-05-29 1994-05-06 Eiichi Tashiro Treatment of waste water
JPH07251187A (en) * 1993-09-30 1995-10-03 Eiichi Tashiro Solid agent for water treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003112166A (en) * 2001-09-30 2003-04-15 Eiichi Tashiro Anaerobic cleaning method for soil
JP2004188406A (en) * 2002-04-02 2004-07-08 Eiichi Tashiro Anaerobic purifying method for soil
CN107299116A (en) * 2017-08-02 2017-10-27 湖南农业大学 Application of the Secondary metabolites in biomass anaerobic fermentation
CN107299116B (en) * 2017-08-02 2021-05-28 湖南农业大学 Application of plant secondary metabolite in biomass anaerobic fermentation

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