JPS6017440B2 - Method for manufacturing soil improvement material using activated sludge as raw material - Google Patents

Method for manufacturing soil improvement material using activated sludge as raw material

Info

Publication number
JPS6017440B2
JPS6017440B2 JP55119204A JP11920480A JPS6017440B2 JP S6017440 B2 JPS6017440 B2 JP S6017440B2 JP 55119204 A JP55119204 A JP 55119204A JP 11920480 A JP11920480 A JP 11920480A JP S6017440 B2 JPS6017440 B2 JP S6017440B2
Authority
JP
Japan
Prior art keywords
activated sludge
water
sludge
tank
scum
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.)
Expired
Application number
JP55119204A
Other languages
Japanese (ja)
Other versions
JPS5742785A (en
Inventor
恒雄 内田
与四郎 高橋
映夫 清水
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TAKASAKI KASEI KK
Original Assignee
TAKASAKI KASEI KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TAKASAKI KASEI KK filed Critical TAKASAKI KASEI KK
Priority to JP55119204A priority Critical patent/JPS6017440B2/en
Publication of JPS5742785A publication Critical patent/JPS5742785A/en
Publication of JPS6017440B2 publication Critical patent/JPS6017440B2/en
Expired legal-status Critical Current

Links

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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Description

【発明の詳細な説明】 本発明は土壌改良材(活性腐権)の製造法に関し、更に
詳しくはパルプ製紙工場より排出する廃液中の廃繊維等
の繊維素有機物を生物処理法によって処理し、沈殿した
セルローズ・リグニン・菌体蛋白を含む活性汚泥に植物
繊維スカムを加えて搾水した後、これにフライアッシュ
を添加混和し、微生物活動に変化を与えずに脱臭させる
徴量要素を含む土壌改良材の製造法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a soil improvement material (active humus), and more specifically, it involves treating cellulose organic matter such as waste fibers in waste liquid discharged from a pulp and paper mill by a biological treatment method. Plant fiber scum is added to the activated sludge containing precipitated cellulose, lignin, and bacterial protein, and after the water is squeezed, fly ash is added and mixed to create soil that contains characteristic elements that deodorize without changing microbial activity. This invention relates to a method for producing improved materials.

従来有害物質を含有しない有機質汚泥の肥料化処理につ
いては、通常原廃水を沈澱池、シックナ一などの自然濃
縮工程を経た後、遠′○濃縮機、加圧濃縮等の構造簡単
な強制濃縮機により、水分90%程度の濃縮汚泥とし、
これを更に高性能脱水機にかけ、水分70%程度に脱水
し、次いで乾裸工程を経て含有水分50〜60%程度の
乾操汚泥とする方法が用いられているが、水分90%程
度の汚泥をさらに高性能の真空ろ過機、加圧ろ過機、遠
心脱水機などの高価な脱水機を用いて脱水するのでは、
肥料化にあたって機械設備の高負荷に加えて、製造工程
が複雑になり厄介な手間を要することになるので、経費
がかさみコスト高になり、肥料工業等では大きな課題と
なっている。
Conventionally, for processing organic sludge that does not contain harmful substances into fertilizer, raw wastewater is usually processed through a natural concentration process such as a settling tank or a thickener, and then a forced thickener with a simple structure such as a far thickener or pressure thickener is used. to make thickened sludge with a moisture content of about 90%,
This is further subjected to a high-performance dehydrator to dehydrate it to about 70% moisture, and then goes through a drying process to form dry sludge with a moisture content of about 50 to 60%, but sludge with a moisture content of about 90% is used. If you dehydrate it using an expensive dehydrator such as a high-performance vacuum filtration machine, pressure filtration machine, or centrifugal dehydrator,
In addition to the heavy load on machinery and equipment, the manufacturing process becomes complicated and requires a lot of time and effort when turning into fertilizer, resulting in increased expenses and high costs, which is a major issue in the fertilizer industry.

本発明は、前記従来の議題を解決するために提案された
ものであって、原廃水から生物処理法(好気的処理)に
より得た水分96%程度の活性汚泥に、植物繊維スカム
を適量加えることによって、構造簡単なスクリュプレス
にかけることにより、一度に水分含有率65%程度の活
性汚泥が得られる簡単で効果的搾水方法を提供すること
を第1の特徴とし、第2の特徴は上記濃縮活性汚泥に微
生物の活動(すなわち菌体増殖)に変化を与えない程度
のフライァッシュを混和した混合物を回転発酵槽等に移
送して熟成するようにした点にある。
The present invention was proposed in order to solve the above-mentioned conventional problems, and an appropriate amount of vegetable fiber scum is added to activated sludge with a water content of about 96% obtained from raw wastewater by a biological treatment method (aerobic treatment). The first feature is to provide a simple and effective water extraction method that allows activated sludge with a moisture content of about 65% to be obtained at a time by applying it to a screw press with a simple structure. The present invention is characterized in that a mixture of the concentrated activated sludge mixed with fly ash to the extent that it does not change the activity of microorganisms (ie, bacterial cell growth) is transferred to a rotary fermenter or the like and aged.

次に本発明土壌改良材の製造法を、詳しく説明するに、
パルプ製紙工場の有機廃水中の廃繊維等の有機物はその
製出工程において物理的,化学的処理が加えられており
、その性状を肥料学的にみれば、第1に炭水化物の組成
が理想的である。
Next, the method for producing the soil improvement material of the present invention will be explained in detail.
Organic substances such as waste fibers in organic wastewater from pulp and paper mills are subjected to physical and chemical treatments during the production process, and if we look at their properties from a fertilizer perspective, firstly, the composition of carbohydrates is ideal. It is.

即ち、セルローズが主体をなし、リグニンは3分の1以
下になっている。第2に形状が微細でかつ均質である。
即ち容易に微生物の分解を受け肥効を示すほか均質な製
品が得られる。
That is, cellulose is the main component, and lignin is less than one-third. Second, the shape is fine and homogeneous.
That is, it is easily decomposed by microorganisms, and a homogeneous product can be obtained that exhibits a fertilizer effect.

第3に如何なる肥料とも混合できる。即ち化学的に不活
性であって混用肥料に化学変化を及ぼさないので、どの
ような肥料でも併用できる。第4に種々の徴量要素を含
む。多量の洗撒水中に含有されている徴量要素はセルロ
ーズの吸着性により豊富に保持されている。上述したよ
うにパルプ製紙工場の廃液中の廃繊維等の繊維素有機物
は肥料製威に好適な性状を供えているうえに、工場から
多量に放出されていて、一部は回収して再使用に供され
ているものの、その70%前後が150メッシュ金網を
通過してしまうという微細繊維又は徴粉状繊維素である
から瓶そ〈が困難で、広大な沈殿池に溜め所謂沈殿池律
として排出水規制基準値に適合する上澄み水のみ河川に
放流している。例えば30000で/日の排水処理され
るパルプ製紙工場の場合沈殿池入口のSSは350〜4
0地.p.mであったとき、この沈殿池律は1日に10
〜12トンに達するので、従来から堆積している多量の
沈殿池律をも利用すれば量的にもパルプ製紙工場の廃棄
物から充分有機質肥料を工業的に製造し得るものである
Third, it can be mixed with any fertilizer. That is, it is chemically inert and does not cause any chemical changes to the mixed fertilizer, so it can be used in combination with any fertilizer. Fourth, it includes various feature elements. The constituent elements contained in a large amount of washing water are retained in abundance due to the adsorption properties of cellulose. As mentioned above, cellulose organic matter such as waste fibers in the waste water of pulp and paper mills has properties suitable for making fertilizers, and is also released in large quantities from the mills, some of which can be recovered and reused. However, around 70% of it is fine fibers or powdery cellulose that pass through a 150-mesh wire mesh, so it is difficult to bottle it, and it is stored in a vast sedimentation tank as a so-called sedimentation tank method. Only supernatant water that complies with discharge water regulation standards is released into rivers. For example, in the case of a pulp and paper mill where wastewater is treated at a rate of 30,000/day, the SS at the entrance of the settling tank is 350 to 4.
0 ground. p. m, this sedimentation pond rule is 10 m per day.
Since the amount reaches ~12 tons, it is possible to industrially produce a sufficient amount of organic fertilizer from pulp and paper mill waste by utilizing the large amount of sedimentation ponds that have been accumulated in the past.

通常下水あるいは有機廃水を生物的処理する公知の汚水
処理法においては、生成した活性汚泥は悪臭を発散させ
るので、脱水乾燥後焼却するか、土と混ぜて埋立て地等
に廃棄していたものであるが、本発明においてはパルプ
製紙工場等の有機廃水を生物処理して生じた活性汚泥を
含水率60〜70%に搾水した後、脱臭性の強力な徴粉
炭燃焼灰(フライアッシュ)を微生物活動に変化を与え
ない程度好ましくは1の重量%程度混和し、含水率50
%程度に調整し、次いでこの混合物の円滑なる腐柄化と
、品質の均一を確保するためダノウ式回転発酵槽に送入
して一定期間適当な通気,縄群を加えて微生物の繁殖を
助成し好気性発酵を進行させ、略炭素率30〜40%位
に熟成させる処理を行し、、この処理が終れば以上の操
作のまま、或は製品の保管、運搬の必要に応じて1日乃
至6日間40℃以下にて空中に放置して乾燥し微生物を
不活性又は仮死状態にして活性腐櫨を製造することであ
る。
In known sewage treatment methods that biologically treat sewage or organic wastewater, the activated sludge produced emits a bad odor, so it is either incinerated after dehydration and drying, or mixed with soil and disposed of in a landfill, etc. However, in the present invention, activated sludge produced by biological treatment of organic wastewater from pulp and paper mills, etc. is squeezed to a moisture content of 60 to 70%, and then pulverized coal combustion ash (fly ash), which has strong deodorizing properties, is used. to an extent that does not cause any change in microbial activity, preferably about 1% by weight, and the moisture content is 50%.
%, and then in order to ensure smooth rotting of this mixture and uniform quality, it is sent to a Danow-type rotary fermenter, where it is aerated for a certain period of time, and a rope is added to support the growth of microorganisms. After that, aerobic fermentation is carried out and aging is carried out to approximately 30 to 40% carbon content, and once this process is completed, the above operation can be continued or for one day depending on the need for storage and transportation of the product. The method is to dry the microorganisms by leaving them in the air at 40° C. or below for 6 days to make them inactive or in suspended animation, thereby producing active rot.

この場合空中放置に代え低温乾燥、低温保持、凍結等の
人工的処理を加え微生物を仮死状態にして能率的に活性
腐植を製造するようにしてもよい。そして、時には微生
物の全部或いは限られた割合に死滅させるため加熱、熱
線を用いるか或は紫外線等の短波照射を適宜行いうろこ
と勿論である。なお、ダノウ式回転発酵槽に送入せずに
前記活性汚泥とフライアッシュとの混合物を一定期間堆
積して炭素率30〜40%に腐熟させることもできるが
、この場合空気が堆積物の全体を透過しないので好気性
発酵は停止するか、または嫌気性発酵となるから空気及
び湿分の分布状態を均一にするため、堆積物の切り換え
しに注意しなければならない。
In this case, instead of leaving it in the air, artificial treatments such as low-temperature drying, low-temperature holding, and freezing may be applied to bring the microorganisms into suspended animation and efficiently produce active humus. Of course, heating, heat rays, or short wave irradiation such as ultraviolet rays may be used as appropriate to kill all or a limited percentage of the microorganisms. Note that the mixture of activated sludge and fly ash can be deposited for a certain period of time without being sent to the Dannow rotary fermenter, and the mixture can be matured to a carbon content of 30 to 40%. Aerobic fermentation either stops or becomes anaerobic fermentation, so care must be taken when changing the sediment to make the distribution of air and moisture uniform.

この場合少なくとも数日に1回ショベルローダ等で満べ
んなく切り換えすことを要する。
In this case, it is necessary to completely switch over using a shovel loader or the like at least once every few days.

そして活性汚泥にフライアツシュを混入することによっ
て脱臭をはかるほか、この混用によって活性汚泥に乏し
い土壌徴量要素のけし、素、鉄、ほう素、石灰、苦土、
マンガン、モリブデンなどの貴重成分が添加され良質の
土壌改良材になる。そして沈殿槽から集めた濃縮槽の活
性汚泥は96%以上水であるから、これからスクリュー
プレスで搾水する場合10〜15%の水分を取除くのが
せいぜいで、依然含水率80〜85%のスラリー状であ
るため、取扱い上にも不便であるし、堆肥の基体原料に
するには水分が多すぎるので乾燥させて水分を60〜7
0%に調整していた。然るに活性汚泥は悪臭を発するの
でこの乾燥作業は容易でなかった。そこで本発明者は濃
縮槽の活性汚泥をフロック化させて濃縮を促進するため
、繊維スカム(廃水中に浮遊する短繊維を製紙業界で通
称する)を濃縮槽において活性汚泥に添加して実験して
みたところ、驚いたことにスカムの添加量を加減するこ
とによりスクリュープレスだけで搾水量を自由に調節(
50〜70%)できることを発見し所期の目的を達成で
きた。この漏水性の向上は、スカムの添加によってスラ
リー状汚泥中の固形分が増加したことと、添加したスカ
ムの各繊維がフロツク化した汚泥の骨則ち、ろか台とな
ってスクリューの圧搾に抵抗するので搾水作用を促進す
ること及び水と共にスクリュープレスに導入されたスカ
ム繊維を芯に凝集した汚泥が、プレス胸のる水小孔に水
に議導されてスクリーン状に引っかかりる床(フィルタ
ベッド)を形成し水分をろ過排出する物理的現象に起因
するものと思われる。因みにスクリュープレスのろ過状
態をみるに、スクリュープレスろ過眼のる水小孔の略全
部が繊維スカムを芯とする汚泥フロックでおおわれてし
、て、破れたところから水が飛び出しているところから
、繊維スカムを芯とする汚泥フ。ックがろ床を形成して
いることが分かる。そして、本発明の堆肥製造の場合に
は含水率96%のスラリー状活性汚泥96部に繊維スカ
ム4部を分散させた懸濁液を活性汚泥スラリーに、その
25%重量比の割合に混合することによって含水率60
〜70%の活性汚泥が容易に得られるし、また活性汚泥
スラリーに、混合するスカム懸濁液の媒質(繊維スカム
)の量を増加させると含水率50%程度の所謂かたい汚
泥になり、廃棄又は焼却処理に適する汚泥が得られるこ
とを実験結果確認し得た。
In addition to deodorizing activated sludge by mixing fly atshu, this mixture also removes poppy, element, iron, boron, lime, magnesia, which are poor soil elements in activated sludge.
Valuable ingredients such as manganese and molybdenum are added to make it a high-quality soil improvement material. The activated sludge in the thickening tank collected from the settling tank is more than 96% water, so when water is squeezed out using a screw press, it is best to remove 10-15% of the water, leaving the water content at 80-85%. Because it is in the form of a slurry, it is inconvenient to handle, and it has too much water to be used as a base material for compost, so it is dried to reduce the water content to 60 to 70%.
It was adjusted to 0%. However, since activated sludge emits a bad odor, this drying work is not easy. Therefore, the present inventor conducted an experiment by adding fiber scum (short fibers floating in wastewater are commonly called in the paper industry) to the activated sludge in the thickening tank in order to flocculate the activated sludge in the thickening tank and promote thickening. When I tried it out, I was surprised to find that by adjusting the amount of scum added, I was able to freely adjust the amount of water expressed using just a screw press (
50-70%) I was able to discover what I could do and achieve my desired goal. This improvement in water leakage is due to the increase in the solid content in the slurry sludge due to the addition of scum, and the fact that each fiber of the added scum becomes a flocculation of the sludge bones, which acts as a filtration platform and resists the squeezing of the screw. The sludge that coagulates around the core of the scum fibers introduced into the screw press together with water is guided by water into the small water holes in the press chest and is caught in a screen-like bed (filter). This is thought to be due to the physical phenomenon of forming a bed (bed) and filtering out water. By the way, looking at the filtration condition of the screw press, almost all of the screw press filtration holes are covered with sludge flocs with fiber scum as the core, and water is coming out from the ruptures. Sludge with fiber scum as its core. It can be seen that the blocks form a filter bed. In the case of producing compost according to the present invention, a suspension in which 4 parts of fiber scum is dispersed in 96 parts of slurry activated sludge with a water content of 96% is mixed into the activated sludge slurry at a weight ratio of 25%. Possibly moisture content 60
~70% activated sludge can be easily obtained, and when the amount of scum suspension medium (fiber scum) mixed into the activated sludge slurry is increased, it becomes a so-called hard sludge with a water content of about 50%. The experimental results confirmed that sludge suitable for disposal or incineration could be obtained.

そして繊維スカムを混入した汚泥は前記したようにろ水
小孔にろ床を形成するので袷んど流出しないから、スカ
ムを混入しない汚泥が水と共に多量に流出するものに比
しスクリュープレスにおける搾水歩蟹りが極めてよく、
しかも搾水汚泥中に残留する繊維スカムは僅かであるが
、主体がセルローズであるから微生物の繁殖があればそ
のもの自体も徐々に分解して腐橘化するので活性汚泥を
基体とする堆肥の肥効を永続させることにもなる。
As mentioned above, sludge mixed with fiber scum forms a filter bed in the filtration holes, so it does not flow out. Water walking crabs are very good.
Furthermore, although there is only a small amount of fiber scum remaining in the squeezed sludge, since it is mainly made of cellulose, if microorganisms multiply, the fiber scum itself will gradually decompose and become rotten, making it difficult to use activated sludge-based compost. It will also make the effect permanent.

更に繊維スカムを混入することによって、通常汚泥を凝
集させるために添加するポリマーの添加量が略50%減
量できる。なお、パルプ製紙工場においては、別に水に
スカムを分散させた分散液を調製することなく「スカム
が浮遊している排水を適宜に調整して濃縮槽の活性汚泥
に添加してもよいこと勿論である。
Furthermore, by mixing fiber scum, the amount of polymer that is normally added to coagulate sludge can be reduced by approximately 50%. In addition, in pulp and paper mills, it is of course possible to adjust the wastewater containing floating scum and add it to the activated sludge in the thickening tank, without preparing a separate dispersion of scum in water. It is.

以上詳述したように、本発明によれば、有機廃水から生
物処理法により生成した水分96%以上の活性汚泥に植
物繊維スカムを加えることによって、構造の簡単なスク
リュープレスによる一段搾水により含水率65%程度の
活性汚泥が得られるので、従釆の肥料化汚泥の処理に使
用された二段搾水の複雑な工程と厄介な手間を要するこ
となく、かつ柊水に使用されていた高性能脱水機を使用
しないため、この種汚泥のコスト低減下をはかることが
でき「 しかも本発明においては、この活性汚泥に微生
物の活動(菌体増殖)に阻害を与えない程度のフライア
ッシュを混和し、これを回転発酵槽等に送入し熟成する
ようにしたものであるから、これを耕士に施用した場合
、生のままの汚泥よりも早く土壌中においてフミン化し
、士壌腐楯として土壌中に蓄積され、地力を増強させる
など土壌の改良を助成し、作物の生育を助ける等の効果
を奏するものである。次に実施例をあげるが、之等は本
発明の範囲を制限するものではない。
As described in detail above, according to the present invention, by adding plant fiber scum to activated sludge with a moisture content of 96% or more produced from organic wastewater by a biological treatment method, water is absorbed by one-stage water extraction using a screw press with a simple structure. Since activated sludge with a yield of about 65% can be obtained, it does not require the complicated process and troublesome two-stage water extraction process used for the treatment of fertilized sludge, and it also eliminates the need for the complicated process of two-stage water extraction and troublesome labor that was used for the treatment of fertilized sludge. Since a high-performance dewatering machine is not used, the cost of producing this type of sludge can be reduced.Moreover, in the present invention, fly ash is mixed into this activated sludge to the extent that it does not inhibit microbial activity (bacterial growth). However, since this is fed into a rotary fermentation tank or the like to mature, when this is applied to a cultivator, it becomes humic in the soil faster than raw sludge, and becomes a humic sludge in the soil. It accumulates in the soil and has effects such as enhancing soil fertility, assisting in soil improvement, and aiding the growth of crops.Examples are given below, but they do not limit the scope of the present invention. isn't it.

実施例 1 パルプ製紙工場のSS250廃液(流出廃繊維の一部を
回収した残液)を中和槽に導きP.日7に中和した後、
これに尿素とリン酸アンモニウム(微生物の栄養素)を
少量(廃液流入量12000〆/Dに対し夫々160k
9、80k9)を添加し、次いで凝集材ポリマーを0.
25%混入し、これをばつ気槽に導入いまつ気して混入
した微生物(連続運転の場合返送汚泥を種用に使用する
)による好気的処理し、次いで沈殿槽で沈殿した活性汚
泥を濃縮槽に集め、これに繊維スカム4%の懸濁水をス
ラリー状の活性汚泥の25%を混合し、この混合溶液を
ポンプでスクリュープレスに送り含水率65%の湿潤な
活性汚泥300kg/日を得た。
Example 1 SS250 waste liquid from a pulp and paper mill (residual liquid obtained by recovering a portion of spilled waste fibers) was introduced into a neutralization tank, and a P.O. After being neutralized on day 7,
Add a small amount of urea and ammonium phosphate (nutrients for microorganisms) to this (160k each for a waste liquid inflow of 12,000〆/D).
9,80k9) and then add 0.9,80k9) of agglomerate polymer.
The activated sludge is mixed with 25% of the sludge and introduced into the aeration tank, where it is aerobically treated with the mixed microorganisms (in the case of continuous operation, the returned sludge is used as seed), and then the precipitated activated sludge is collected in the settling tank. The fiber scum is collected in a thickening tank, mixed with 4% suspended water of fiber scum and 25% of slurry-like activated sludge, and this mixed solution is sent to a screw press using a pump to produce 300 kg/day of wet activated sludge with a water content of 65%. Obtained.

この湿潤汚泥に10重量%のフライアッシュを混入し、
この混合物を混練機に送入し含水率50%程度に調整し
た後、ダノウ式回転発酵槽に送込み空気を送入しながら
3日間前進熟成させ炭素率30〜40%の活性汚楯24
0kg/日を製造した。この製品の分析結果(財団法人
日本肥料検定協会分析)は第1表に示されている。第
1表 実施例 2 沈殿他律に水を加え蝿拝して分散質の濃度の濃度即ちS
S400に調整し(濃度は調節自在である)、ポンプア
ップして前記実施例1と同様の方法で活性汚泥を生成さ
せたところ300k9/日を得た。
10% by weight of fly ash is mixed into this wet sludge,
After feeding this mixture into a kneader and adjusting the water content to about 50%, it was fed into a Danow type rotary fermenter and aged for 3 days while air was fed into the activated slag 24 with a carbon content of 30 to 40%.
0 kg/day was produced. The analysis results of this product (analysis by Japan Fertilizer Inspection Association) are shown in Table 1. No.
Table 1 Example 2 Add water to the precipitation heterogeneity to determine the concentration of the dispersoid, that is, S
The activated sludge was adjusted to S400 (the concentration is adjustable) and pumped up in the same manner as in Example 1, yielding 300 k9/day.

この世来高は原料濃度(SS)を前例の略倍にしてみた
が略同量しか得られなかった、これは沈殿池律が堆積中
にけん気的分解し炭水化物がメタン、炭酸ガス等に分解
したため実施例1の生のものより減量したものとみられ
る。上記活性汚泥に1の重量%のフライアッシュを混和
し、10日間空気中に堆積し3日おきにショベルローダ
で切換えし熟成し含水率40%の活性腐楯240k9/
日を製造し得た。この結果、多少歩蟹りは良くないが多
量に堆積放棄してある沈殿池律も充分活性腐槽の原料に
なり得ることが伴明した。
I tried to increase the raw material concentration (SS) to about twice that of the previous example, but I could only obtain about the same amount. Therefore, it seems that the amount was reduced compared to the raw material of Example 1. 1% by weight of fly ash was mixed with the above activated sludge, deposited in the air for 10 days, changed over and aged with a shovel loader every 3 days, and turned into activated sludge with a moisture content of 40% 240k9/
Manufactured days. As a result, it was revealed that sedimentation ponds with a large amount of sedimentation and abandonment can be used as raw materials for active septic tanks, although the crawling rate is not good.

なお上記第1・2の実施例は、図面に示した第3実施例
に記載した廃水処理用プラントで行った経験の結果を示
す。
Note that the first and second embodiments described above represent the results of experience conducted in the wastewater treatment plant described in the third embodiment shown in the drawings.

実施例 3 図において、1は同敷地内にバルブ工場と製紙工場とを
有する廃水路からの導入水路(又は沈殿他律の導管)、
2は中和槽で、この例ではアルカリ法によりクラフトパ
ルプを製造しているので硫酸で中和するようになってい
る。
Example 3 In the figure, 1 is an introduction waterway (or a conduit for precipitation heteronomy) from a waste waterway that has a valve factory and a paper mill on the same site,
2 is a neutralization tank, and since kraft pulp is manufactured by an alkaline method in this example, neutralization is performed with sulfuric acid.

3は計量せきで単位時間に通過する廃水量によって燐酸
タンク4・尿素タンク5から流量に適合する微生物栄養
素を補給するようにしてある。
Reference numeral 3 is a metering weir which supplies microbial nutrients suitable for the flow rate from a phosphoric acid tank 4 and a urea tank 5 depending on the amount of wastewater passing per unit time.

6はばつ気槽で、中央の隔壁7で仕切り、隔壁7の下方
を蓮通させ、一次ばつ気槽6,で混入した微生物によっ
て排水中繊維素を分解し、分解の中間代謝物を利用して
合成(すなわち菌体増殖)が行われ或程度腐植化した有
機物の浮遊物が排水の流れにしたがい二次ばつ気槽62
に至り分解と合成を操り返えして排水中の有機物が活性
汚泥となって水と共に二次ばつ気槽62の溢流口63か
ら沈殿池8へ底の方から流入する。
6 is an aeration tank, which is partitioned by a partition wall 7 in the center, and a lotus is passed through the bottom of the partition wall 7. In the primary aeration tank 6, microorganisms mixed in are used to decompose cellulose in the wastewater and utilize intermediate metabolites of the decomposition. Floating organic matter that has been synthesized (i.e., bacterial cell growth) and has become humic to some extent is collected in the secondary aeration tank 62 as the wastewater flows.
By repeating the decomposition and synthesis, the organic matter in the wastewater becomes activated sludge and flows into the settling tank 8 from the bottom through the overflow port 63 of the secondary aeration tank 62 together with water.

この沈殿池8はその底中央に断面環状の沈殿溝9を備え
るとともに、該沈殿溝9中央に底から直立して流入筒1
0を設けてあつて、ばつ気槽62から活性汚泥を含む排
水が直立筒10を上昇してその上端部10′から沈殿池
8に送入される。排水は沈殿池8の周囲に設けた溢水溝
8′から河川に放流されるが、活性汚泥はそのまま沈殿
池の沈殿溝9に沈下する。11は活性汚泥濃縮槽で、沈
殿溝9に運通した配管12によりこの濃縮糟11に導き
ポンプP,によって活性汚泥を濃縮槽11に収集する。
This sedimentation tank 8 is provided with a sedimentation groove 9 having an annular cross section at the center of the bottom, and an inflow tube 1 that stands upright from the bottom at the center of the sedimentation groove 9.
0 is provided, and the wastewater containing activated sludge from the aeration tank 62 rises up the vertical cylinder 10 and is fed into the settling tank 8 from its upper end 10'. The waste water is discharged into the river from an overflow ditch 8' provided around the settling tank 8, but the activated sludge sinks as it is into the settling ditch 9 of the settling tank. Reference numeral 11 denotes an activated sludge thickening tank, and the activated sludge is introduced into the thickening tank 11 through a pipe 12 conveyed to the settling groove 9 and collected into the thickening tank 11 by a pump P.

13はスカムタンクで、水にスカムを分散させた溶液を
留めポンプP2により濃縮槽へ送り該糟の活性汚泥に適
量混入する。
Reference numeral 13 denotes a scum tank, in which a solution in which scum is dispersed in water is collected and sent to a thickening tank by a pump P2, where it is mixed in an appropriate amount into the activated sludge of the scum.

この混合液はポンプP3によりスクリュープレス14に
送入され搾水された活性汚泥にフライアッシュfを混入
して、これを混練機15に送り込み、次いでダノウ式回
転発酵槽16に送入する構成になっているから、この装
置は絶えず流入する廃水の流動をそのまま媒体として自
動的に廃水から有機物を活性汚泥として収集し、次いで
搾水、フライアッシュの混入混和、更に回転発酵槽で熟
成し、パルプ紙工場の廃液から容易に活性腐楯を得るこ
とができ、その勤作及機構を簡単且確実にすることがで
きるものである。
This liquid mixture is sent to the screw press 14 by the pump P3, and the fly ash f is mixed with the squeezed activated sludge, which is sent to the kneader 15, and then sent to the Danow type rotary fermentation tank 16. Therefore, this equipment automatically collects organic matter from the wastewater as activated sludge using the constantly flowing wastewater as a medium, then squeezes the water, mixes in fly ash, and matures it in a rotary fermenter to pulp. Activated septic can be easily obtained from paper mill wastewater, and its working mechanism can be made simple and reliable.

なお17は凝集剤ポリマータンク、18は中和槽の縄浮
羽根、19は硫酸タンク、20,21はばつ気槽の散気
機構(ェアレーション)、22は種用の返送汚泥管、2
3はスカム投入口、24は送水管、vはバルブ、25は
濃伴羽根である。
In addition, 17 is a coagulant polymer tank, 18 is a rope floating blade of a neutralization tank, 19 is a sulfuric acid tank, 20, 21 is an aeration mechanism (aeration) of an aeration tank, 22 is a return sludge pipe for seeds, 2
3 is a scum inlet, 24 is a water pipe, v is a valve, and 25 is a thickening blade.

次に本発明の実施成績は次記に示す通りである。1例、
腐槽質火山灰士に4・松菜を栽培し生育収量、窒素、燐
酸の吸収量を検討の結果である。
Next, the implementation results of the present invention are as shown below. 1 example,
These are the results of cultivating 4. Matsuna in saprophyte volcanic ash and examining the growth yield and amount of nitrogen and phosphoric acid absorbed.

草丈の平均は各区共に同程度なるも収量は本発明堆肥区
は増収を示した。
Although the average plant height was the same in each plot, the yield increased in the compost plot according to the invention.

吸収量の結果は本発明堆肥区は窒素の利用度が高く、一
般堆肥区は燐酸に多くみられたが、施肥量が多いためと
思われる。2例、標高860mの高原畑地火山灰士の大
根にについて、一般堆肥との肥効を検討の結果である。
The absorption results showed that the inventive compost plot had a high utilization of nitrogen, while the general compost plot showed a high utilization of phosphoric acid, which may be due to the large amount of fertilizer applied. These are the results of a study on the fertilizing effect of two cases, daikon radish grown in a highland field at an altitude of 860 m, with general compost.

生育途上には差はなかったが、収穫期になって本発明堆
肥区は草丈、様径、根重とも勝り増収指数は103を示
す。
There was no difference in the growth process, but at harvest time, the compost plot of the present invention was superior in plant height, seed diameter, and root weight, showing a yield increase index of 103.

収量はIQ当りである。3例 永年性植物の肥効を知る
ためカィヅカイブキ3年生について供積壌土の畑地で検
討結果である。
Yield is per IQ. 3 Examples: In order to understand the fertilizing effect of perennial plants, the following are the results of a study on 3-year-old Kaizuka Ibuki in a field with accumulated loam soil.

本発明堆肥併用区は横幹の肥大と樹高伸長共に優り新梢
生長量は1.8倍に達し、永年性植物の根部の発達が確
認される。
The plot in which the compost of the present invention was used was superior in terms of enlargement of lateral trunks and elongation of tree height, and the amount of new shoot growth reached 1.8 times, confirming the development of roots of perennial plants.

【図面の簡単な説明】[Brief explanation of drawings]

図面は、この発明を実施する装置の糠図的説明図である
。 2…・・・中和槽、3・・・・・・計量ぜき、6.・・
・・・・1次ばつ気槽、62二次ばつ気槽、8・・・・
・・沈殿池、9・・・・・・沈殿溝、10・・・・・・
流入直立稀、11・・・・・・濃縮槽、13……スカム
タンク、14……スクリュープレス、15・・・・・・
鷹練機、16・・・・・・回転発酵槽。
The drawing is a diagrammatic explanatory diagram of an apparatus for carrying out the present invention. 2... Neutralization tank, 3... Measuring girth, 6.・・・
...Primary aeration tank, 62 secondary aeration tank, 8...
... Sedimentation basin, 9 ... Sedimentation groove, 10 ...
Inflow upright rare, 11...Concentrator tank, 13...Scum tank, 14...Screw press, 15...
Hawk mixing machine, 16...Rotary fermentation tank.

Claims (1)

【特許請求の範囲】 1 パルプ製紙工場の有機廃水から生物処理法によつて
生ずるスラリー状の活性汚泥に植物繊維スカムを加えて
含水率60〜70%に搾水した後、これにフライアツシ
ユを5〜30重量%混和し含水率を50%程度に調整す
る工程と、この混合物を堆積または回転発酵槽に送入し
炭素率30〜40%に熟成する工程とよりなることを特
徴とする土壌改良材の製造法。 2 パルプ製紙工場の沈澱池滓に水を加え撹拌して分散
質の濃度を調整した有機けん濁液から製造した活性汚泥
を用いることを特徴とする特許請求の範囲第1項記載の
土壌改良材の製造法。
[Claims] 1. Vegetable fiber scum is added to slurry-like activated sludge produced by biological treatment from organic wastewater of a pulp and paper mill, and the water is squeezed to a moisture content of 60 to 70%. A soil improvement characterized by comprising a step of mixing ~30% by weight and adjusting the water content to about 50%, and a step of feeding this mixture into a pile or rotary fermenter and aging it to a carbon content of 30 to 40%. Manufacturing method of wood. 2. The soil improvement material according to claim 1, which uses activated sludge produced from an organic suspension obtained by adding water to sedimentation pond slag of a pulp and paper mill and stirring to adjust the concentration of dispersoids. manufacturing method.
JP55119204A 1980-08-29 1980-08-29 Method for manufacturing soil improvement material using activated sludge as raw material Expired JPS6017440B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55119204A JPS6017440B2 (en) 1980-08-29 1980-08-29 Method for manufacturing soil improvement material using activated sludge as raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55119204A JPS6017440B2 (en) 1980-08-29 1980-08-29 Method for manufacturing soil improvement material using activated sludge as raw material

Publications (2)

Publication Number Publication Date
JPS5742785A JPS5742785A (en) 1982-03-10
JPS6017440B2 true JPS6017440B2 (en) 1985-05-02

Family

ID=14755499

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPS6017440B2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS593089A (en) * 1982-06-29 1984-01-09 三機工業株式会社 Manufacture of organic fertilizer
IL67030A0 (en) * 1982-08-30 1983-02-23 Environmental Controls Inc Process for enhancing or fertilizing the soil using organic waste derived granulates
JPS61247675A (en) * 1985-04-22 1986-11-04 東北電力株式会社 Manufacture of organic fertilizer from organic sludge
JPH09111238A (en) * 1995-10-18 1997-04-28 Honsyu Sangyo Kk Soil modifier and its production
JP2002256266A (en) * 2001-02-15 2002-09-11 Soruteko Kk Soil-conditioning and water-controlling agent for composition using industrial waste as main component and process for preparing the same
JP2003096452A (en) * 2001-07-19 2003-04-03 Soruteko Kk Composition for soil consisting of industrial waste
CN101793403A (en) * 2010-03-15 2010-08-04 陈凤飞 Method for treating sludge
CN105198671B (en) * 2015-09-28 2018-12-25 广西壮族自治区农业科学院甘蔗研究所 A kind of acid soil improving agent and preparation method thereof
CN111592112A (en) * 2020-05-28 2020-08-28 盐城工学院 Method for remediation and recycling of organic pollution by mudflat plants

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5637285B2 (en) * 1974-06-19 1981-08-29

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5637285U (en) * 1979-08-24 1981-04-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5637285B2 (en) * 1974-06-19 1981-08-29

Also Published As

Publication number Publication date
JPS5742785A (en) 1982-03-10

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