JPS5879509A - Composition for treatment of waste liquid and sludge - Google Patents

Composition for treatment of waste liquid and sludge

Info

Publication number
JPS5879509A
JPS5879509A JP56177148A JP17714881A JPS5879509A JP S5879509 A JPS5879509 A JP S5879509A JP 56177148 A JP56177148 A JP 56177148A JP 17714881 A JP17714881 A JP 17714881A JP S5879509 A JPS5879509 A JP S5879509A
Authority
JP
Japan
Prior art keywords
sludge
waste liquid
liquid
treatment
composition
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
JP56177148A
Other languages
Japanese (ja)
Other versions
JPS6147122B2 (en
Inventor
Hachiro Tashiro
田代 八郎
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP56177148A priority Critical patent/JPS5879509A/en
Publication of JPS5879509A publication Critical patent/JPS5879509A/en
Publication of JPS6147122B2 publication Critical patent/JPS6147122B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PURPOSE:To permit easy solid-liquid sepn. of waste liquid and sludge by adding a compsn. for treatment consisting of slaked lime, etc. of specific weight ratios to said liquid and sludge and mixing and agitating the same. CONSTITUTION:A compsn. for treatment of waste liquid and sludge consists of 4.8-32.8wt% quicklime, 49.1-69.0wt% slaked lime, 3.6-4.9wt% lime silicate, 6.9-7.3wt% talc powder, 2.0-2.6wt% humic acid, and 3.3.-13.7wt% acid clay and these are mixed and agitated in gaseous nitrogen and while suppressing oxidation vulnerable to arise during mixing, the agitation is continued until the mixture has roughly uniform bulk density. Thus the surface electric charge of the molecules constituting waste liquid and sludge is changed to generate physical and chemical changes and reaction in the waste liquid and sludge and to generate the flocculation and volume shrinkage of the solids and the oxidation and clarification of water, whereby the solid-liquid sepn. is made easy.

Description

【発明の詳細な説明】 本発明は液泥状を呈する産業廃棄物に添加して廃液泥中
の1形物と水質との分離を害鳥にする廃液泥処理用組成
物#CII達する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a waste slurry treatment composition #CII which is added to industrial waste in the form of liquid slurry to harm the separation of monomorphic substances in the waste slurry from water quality.

従来、下水及び製造工業等から発生する廃液泥は、はと
んど大部分が水分で、乾物換算(2)彫物C即ち、  
Drg 8o11d )が敵量檻1であり、啼た汚泥−
一槽で物理的に濃縮した崗液泥の固形物量C約2%)に
対し塩化鉄及び消石灰を約0.4〜0.6%加えて薬注
凝沈を施し、上澄水の除去41廃液泥を固液分鳴し8発
生した脱水ケークを焼却又はそのまま埋めたてており、
或は栗注凝沈に高分子凝集剤を併用してフロックを形成
させた後固液分離を行なっている。これらの方法では。
Conventionally, waste liquid mud generated from sewage and manufacturing industries, etc., is mostly water, and the dry matter equivalent is (2) Carving C, that is,
Drg 8o11d) is the enemy quantity cage 1, and the crying sludge-
Approximately 0.4 to 0.6% of iron chloride and slaked lime are added to the solid content (C of the solid matter C of approximately 2%) of the physically concentrated clay slurry in one tank, and chemical coagulation is performed, and the supernatant water is removed.41 Waste liquid The mud is solid-liquid separated and the resulting dehydrated cake is incinerated or buried as is.
Alternatively, solid-liquid separation is performed after flocs are formed by using a polymer flocculant in combination with chestnut injection coagulation. In these methods.

最終的に残留する脱水ケークの含水率は磯ね8s%であ
り、この含水率については共存した水質が若干コロイド
状を呈しているため、脱水効率が良好でないことに原因
がある。又1M水ケークはフロック状であるため嵩高で
あり、そのためjL掛は容積も大きく、シかも−々のフ
ロックが多祉の水分を包含しているため焼却におりても
多酸の燃料が消費されて−る。fLK上記a注−沈だけ
の脱水ケークの焼却では、塩化物の生成によ石焼却炉の
腐食も@視できない。
The moisture content of the final remaining dehydrated cake is Isone 8s%, and this moisture content is due to the fact that the coexisting water has a somewhat colloidal quality, so the dehydration efficiency is not good. In addition, since the 1M water cake is in the form of flocs, it is bulky, so the volume of the JL hanger is large, and the flocs contain a lot of water, so even when incinerated, a lot of acidic fuel is consumed. It's being done. fLK Note a above - When incinerating a dehydrated cake with only sedimentation, corrosion of the stone incinerator cannot be observed due to the formation of chlorides.

又、し尿・家畜ふん尿その他の有機A廃液泥は、そのオ
會田畑に散布されたこともあり、これの禁止により海洋
投索処分も行なわれたが。
In addition, human waste, livestock manure, and other organic waste liquid mud was sometimes sprayed on the farm fields, and due to the prohibition of this, the waste was disposed of by being thrown into the ocean.

これも鵞九禁止の方向にあり、これらのIl&境は大部
分活性汚泥処理法に向かいつつある。しかしこのg&場
法では、廃液泥の汚濁濃1が活性汚泥処理法(不適当な
ほど高1111である上、アンモニアーアζンを始めと
す4憤い不快奥及び脱色困−な惜色状轢の故に、一般に
これら崗液泥は大量の水で柿、釈して活性汚泥処理をさ
れても説颯及び脱色は困峻であり、特に禽品廃WL泥の
ように油脂を共をする場合には活性汚泥処理法例えば好
気性園の能力が着しく阻害される。上記廃液泥を処理し
て残留した脱水ケークは、多分に不快夷も残しているが
その肥効成分が他の脱水ケークに比較して多いことから
有機的な補助肥料に使用することを計画されたが、沈殿
物の@巣に使う為分子凝集剤が土中のリンを無効化する
作用を有するため、一般の無害汚泥と同一に埋め立て処
分を行なってrるのが現況であるO 本発明の目的は、廃液泥状め献業廃秦物又は生tli廟
秦物等に消石灰等からなる処理用組成物を添加しかつ混
合攪拌すゐことで、廃液泥を構成する分子の表面電荷を
変t、それに伴って該廁液泥和物場的変化及び化学的反
応を生じさせ。
This is also in the direction of banning sludge, and most of these areas are moving towards activated sludge treatment methods. However, in this method, the concentration of waste liquid sludge is unsuitably high (1111) compared to the activated sludge treatment method. Therefore, in general, it is difficult to decolorize and decolorize these gray liquid muds even if they are treated with activated sludge by diluting them with a large amount of water, especially when they contain fats and oils like poultry waste WL mud. The ability of activated sludge treatment methods, such as aerobic gardening, is severely inhibited.The dewatered cake that remains after treating the waste liquid sludge described above is quite unpleasant, but its fertilizing ingredients are not absorbed by other dewatered cakes. It was planned to use it as an organic supplementary fertilizer because the amount of phosphorus in the soil is higher than that in the soil. The current situation is that sludge is disposed of in a landfill in the same way as sludge. Moreover, by mixing and stirring, the surface charge of the molecules constituting the waste liquid slurry is changed, and accordingly, a physical change and a chemical reaction are caused in the waste liquid slurry.

固形物の凝集と容噴収喝及び水質の酸化と清澄を生じさ
せて固液分離を容J6くし、含水量の低い脱水ケークに
転換させると同時に水質のrijsatを看しく低下さ
せる。、 *液部処理用組成物を提供すゐことにある。
This causes agglomeration and ejection of solids and oxidation and clarification of the water quality, thereby increasing the solid-liquid separation to a volume of J6, converting it to a dehydrated cake with a low water content, and at the same time significantly lowering the rijsat of the water quality. *An object of the present invention is to provide a composition for treating liquid parts.

本発明の崗液泥%ffi用組成物は、生石灰4J〜32
.8重量%、消石灰49.1〜694)電量%、ケイ酸
石灰3.6〜49直徽%、滑石粉6.9〜7.31量%
The composition for granite mud%ffi of the present invention comprises quicklime 4J to 32
.. 8% by weight, slaked lime 49.1-694% coulometric, silicate lime 3.6-49% by weight, talcum powder 6.9-7.31% by weight
.

腐11.0〜2β直量%及び酸性陶土1B −13,7
重量%からなり、これらを音素気流中で混合攪拌し、a
合中に発現するおそれのある酸化を抑−しつつ混合物の
嵩密實がほば均一とな4まで攪拌を続ける仁とによって
粉粒状物質として得られるものである。
Rot 11.0-2β direct weight% and acidic china clay 1B -13,7
% by weight, these are mixed and stirred in a phoneme air stream, and a
While suppressing oxidation that may occur during mixing, stirring is continued until the bulk of the mixture becomes almost uniform, resulting in a powdery granular material.

上記の廃液泥0例えば静置して余剰水をWk去した後O
含水率98%(Drg 8o1idとして2%)の下水
廃液泥を攪拌しつつ2本発明のjJ液液部処理用組成物
該廃液泥中の(2)彫物#/c対しS〜10%−加して
混合攪拌すると、比較的拡敵し菊vh#性陶土により該
廃液泥の液性は酸性11に転移し。
The above waste liquid mud 0 For example, after leaving it still and removing excess water
While stirring the sewage waste liquid mud with a water content of 98% (2% as Drg 8olid), the composition for treating the jJ liquid part of the present invention was added to (2) carvings #/c in the waste liquid mud by S to 10%. When mixed and stirred, the liquid content of the waste liquid mud changed to acidity 11 due to the relatively wide range of clay.

#嶺液泥は外−では直ちに変化な生じないが。# Mine liquid mud does not change immediately outside.

攪拌の継続により固形物がi1禰し、その膨潤体の喝@
Km細なm−固形物(8uspenslon 8o11
d )が収着し、凝集のような挙動を表わす、この時点
で攪拌を停止して静止すると、若干時間(3〜S分)経
過後膨潤凝集体はあたかも崩壊するように欺粒境に分か
れ、f!LK敵細な気泡を発生しつつ収IImを生じ、
この収一体は比較的早一連ばて沈降する。この沈降した
固形物は、初め母液との境春線では帰宅状を風している
が、1〜2分の間KtK沈降容禎の縮小が艶られ、外観
では一線を−してはっきりと引t1#まった状−を呈す
る。この時点では上澄水は全く透明になり、その着色も
ほとんど消失し、かつ下水廃液il@特有の不快夷は完
全に消失する。又、この上澄水をJIS K 0102
11業排水試験法@に基づ(分析賦鹸を行なった結蟻、
約70%のBOD &び約90%ON−へキサン抽出物
量がそれぞれ原体に比較して除去されていた。
As the stirring continues, the solid matter sludges, and the swollen solid material swells.
Km fine m-solid (8uspenslon 8o11
d) is sorbed and exhibits agglomeration-like behavior. At this point, if the stirring is stopped and the mixture is allowed to stand still, after some time (3 to S minutes), the swollen aggregates separate into deceptive grain boundaries as if collapsing. , f! LK generates small air bubbles while producing absorption IIm,
This aggregate sediments relatively quickly. At first, this settled solid material was waving in the boundary line with the mother liquor, but for 1 to 2 minutes, the reduction of the KtK sedimentation volume became noticeable, and the appearance was clearly drawn. t1# exhibits a clump-like state. At this point, the supernatant water becomes completely transparent, its coloring almost disappears, and the unpleasantness characteristic of sewage waste liquid il@ completely disappears. In addition, this supernatant water is JIS K 0102
Based on the 11 industrial wastewater test method @ (analyzed ants,
Approximately 70% BOD & 90% ON-hexane extract amounts were removed compared to the bulk, respectively.

沈降した固形物は上澄水t”除去した後、定性1紙をI
llり付けた硝子漏斗を使用して直方による(2)液分
III&を行なった結果、濾過連夜は急速であ勧、なお
r過連夜はPak通じては4均−であった。又、P@、
上の脱水ケータは5時間vkにおiで含水率80%であ
り、この脱水ケークの様相は湿った歇細な砂状であった
。又、この脱水ケークを200倍の走査形電子m敵鏡で
一察した結果、約80?クロンのほぼ球状の物体が@1
891のようKIIljKした形状を呈しており、それ
らの塊の大量さは400〜1300々クロンであった。
After removing the settled solids with supernatant water,
As a result of Nogata's (2) liquid fraction III& using a glass funnel with a 100 mm diameter, the filtration rate was rapid and recommended, and the continuous filtration rate was 4 times the Pak rate. Also, P@,
The moisture content of the upper dehydration cake was 80% at 5 hours vk i, and the appearance of this dehydration cake was moist and finely sandy. Also, as a result of looking at this dehydrated cake with a 200x scanning electronic mirror, it was about 80? Cron's almost spherical object @1
891, and the mass of these lumps was 400 to 1,300 square meters.

本発明O晩WL泥%垣用組成物の嚇液泥に対する物理的
変化及び化学的反応は、処理中の崗液泥0亭−と、磁位
差分析、ガスクc1マドグツフィー及び量光X線分析に
よる試験結果かboCのように推定される。
The physical changes and chemical reactions of the present invention's Onight WL mud composition against liquid mud during treatment were determined by magnetic potential difference analysis, gas C1 magnetic flux and quantitative X-ray analysis. It is estimated that the test result is boC.

m液部11&環用組成物は消石灰等の天−物加工品を敏
棚−合した多成分系鵡合物で4)す、これらの結晶体は
部分的には半ば複合化したものであると考えられる。従
って、鍍組成物を水中に投与すると、比較的水Kmtt
16い酸性陶土を構成する結晶がまず#l解し、それに
よって廃液部の液性がearmに急速に転移す為、その
結果として廃液部構成物質の表面帯電状lが変化し。
The liquid part 11 & ring composition is a multi-component compound made by combining natural processed products such as slaked lime (4), and these crystals are partially semi-composite. it is conceivable that. Therefore, when the coating composition is administered into water, relatively water Kmtt
The crystals constituting the 16 acidic clay first decompose into #l, and as a result, the liquid properties of the waste liquid part are rapidly transferred to the arm, and as a result, the surface charge state of the substances constituting the waste liquid part changes.

共存するカルシウム系天然物加工品の共通的挙動の凝集
効果と相俟って、魔液部の固形物粒子が相互に@集を生
じ石。この時点で、凝集体は水分を飽和しておJD、こ
れらが凝集して成る質量眼界を超えると崩壊するものと
考えられるが。
Coupled with the cohesive effect of the common behavior of calcium-based natural products that coexist, the solid particles in the magic liquid part form a mutual @ collection. At this point, the aggregates are saturated with water and are thought to disintegrate when the mass of these aggregates exceeds the visual field.

それには凝集体内部で分子約数−が生じ、それがa集体
を崩壊し、麩に細分化した凝集体を引き続いて収縮して
行くものと推定されるの腐植酸はフルボ酸とフ(ン酸か
らなる天巌物で、フルボ酸は高分子の音素を含むオ中シ
酸であり。
It is assumed that this is because a molecular divisor is generated inside the aggregate, which collapses the a aggregate, and the aggregate, which has been subdivided into wheat, is subsequently contracted. Fulvic acid is a natural substance made of acids.

投与対象物が酸性の場合は酸化力を発揮し、アルカリ性
の場合はアミン、アンモニア及び硫化水素を分解するか
ら説奥力が偵〈、これは公知の風象であろ、この腐植酸
の中核をなす物質は。
If the substance to be administered is acidic, it exerts oxidizing power, and if it is alkaline, it decomposes amines, ammonia, and hydrogen sulfide, so it has great persuasive power. What is the substance of eggplant?

未だ理論的にはm明されていなりが、該組成物が廃液部
と接触した初期から該廁植酸は腐液泥中に拡散し、a化
と説夷を行ない、酸素fs#値を向上させゐと同時に、
滑石粉を構成するケイ酸マグネシウムが電解質物質とし
て挙動することを促魂する。その結果、+11液泥のコ
ロイド状−が清澄されて固液分離効果が看しく高められ
為から、脱水ケークの含水率の低下が生じたものと推定
される。
Although it is not yet known theoretically, from the early stage when the composition comes into contact with the waste liquid, the sulfuric acid diffuses into the humic liquid mud, converts it into a, and improves the oxygen fs# value. At the same time,
Magnesium silicate, which constitutes talcum powder, acts as an electrolyte substance. As a result, the colloidal - of the +11 liquid mud was clarified and the solid-liquid separation effect was noticeably enhanced, which is presumably why the water content of the dehydrated cake decreased.

本発明の廃液・泥処理用組成物を使用する11固液泥逃
理機は、非電に簡単で、即ち従来排水浄化処理装置とし
て使用されている檗庄形反応槽。
No. 11 solid-liquid mud escape machine using the waste liquid/sludge treatment composition of the present invention is non-electrically simple, that is, a Bokusho-shaped reaction tank conventionally used as a wastewater purification treatment equipment.

シックナー及び1液分離慎だけであ石。但し攪拌機が上
下、左右及び斜め方向を同時に攪拌で龜る0回転速t 
70〜8OR/Mの円筒形攪拌機に曽几られると、目的
が6烏に達成される。又。
Thickener and 1-liquid separation are only stones. However, at 0 rotation speed t, the stirrer stirs up and down, left and right, and diagonally at the same time.
When placed in a cylindrical stirrer of 70-8 OR/M, the objective is achieved to 6. or.

脱水ケークは効率的な脱水が行なわれているものの、な
お水分が75%程t*むものと推定され。
Although the dehydrated cake has been efficiently dehydrated, it is estimated that it still contains about 75% water.

この状lでは終末処分において若干の制限を受けること
があるが、特許公開公報!S6−216801m秦廃嬌
物の高速脱水g&処理法その装置“を利用して外部より
熱を加えることなく短時間に脱水乾燥して粉末状とした
ものは、土壌改良資材として再利用できる利点を有する
。これは、。
In this situation, there may be some restrictions in the final disposition, but the patent publication publication! S6-216801m High-speed dehydration and processing method for Qin waste The product that is dehydrated and dried in a short time without applying external heat using this equipment has the advantage of being reusable as a soil improvement material. This is.

蚊組成物が土中においてリンの作用を阻害する有機高分
子凝集剤Cポリアクリル噴ア電ドが主体)を含まないの
で、土豪の破壊が回避されるからである。
This is because the mosquito composition does not contain an organic polymer flocculant C (mainly composed of polyacrylic foam) that inhibits the action of phosphorus in the soil, so destruction of the soil can be avoided.

以下本発明の廃液部処理用組成物を使用した実施例を脱
明する・ 実施例1 +1>  処理対象物− 汚泥aliI槽より採取した下水汚泥で。
Examples using the composition for treating the waste liquid part of the present invention will be explained below. Example 1 +1> Object to be treated - Sewage sludge collected from the sludge aliI tank.

その線略性状は次の通りである。Its linear properties are as follows.

(2)  処理法 上記汚泥を攪拌機付処理槽に入れ、 7fiL/Mの速
喧で攪拌機を駆動しつつ廃液泥q&堀用組成物を該汚泥
中の固形物2%に対し、S%相機量を粉粒体のt壇上紀
処城槽に投与し。
(2) Treatment method: Put the above sludge into a treatment tank equipped with an agitator, and while driving the agitator at a speed of 7fiL/M, add the waste liquid sludge q & ditch composition to 2% of the solids in the sludge, and add S% phase amount to 2% solids in the sludge. was administered into a powdered granular tank.

wLKS分間攪拌を継続した後攪拌を停止し。After continuing stirring for wLKS minutes, stirring was stopped.

沈降を行なうことなく直ちに輿空フィルターで固液分峻
を行なった。
Solid-liquid separation was immediately carried out using an empty filter without sedimentation.

(3)@珊M乗 実施例2 +11  処理対象物 工業薬品製造よむ排出した廃液部で、その傾略性状は次
の通りである。
(3) @San M power Example 2 +11 Processing target: Industrial chemical manufacturing waste liquid discharged, its slope properties are as follows.

(2) 処理法 実施例1と魂液部処理市組成物量を除き全く同じ処理法
で処理した。
(2) Treatment method The treatment was performed in exactly the same manner as in Example 1 except for the amount of the composition treated in the soul fluid section.

実施例3 (11処理対象物 粗大ゴi(@脂婦、パルプ塊等)除去後の生じ縁で、そ
の概略性状は次の通りである。
Example 3 (11) The resulting edge after removing coarse gore (@fatty, pulp lumps, etc.) to be treated, and its general properties are as follows.

(2) 処理法 実施例1の処理法と同じg&環を行なった。(2) Treatment method The same g&ring procedure as in Example 1 was carried out.

但し、処理槽は愚奥防止のため−で密閉できる処理槽で
あり、又攪拌機は攪拌軸の先端に短円筒を取付け、筒内
gに2jQK亘り3枚羽機を取付けた攪拌機である。
However, the processing tank is a processing tank that can be sealed with - in order to prevent spoilage, and the stirrer is a stirrer with a short cylinder attached to the tip of the stirring shaft and a three-blade machine installed in the cylinder g over 2JQK.

(3)  処垣緒蟻 裏111@4 +l)  処理対象物 IRs廃液泥液部その碩略性状は次の通りである。(3) Place fence ant Back 111@4 +l) Object to be treated The general properties of the IRs waste liquid slurry are as follows.

(2) 処理法 貯溜槽中の該対−物上部に浮上している粘稠油脂状物(
#h植物油の鹸化したもの)をスキζフグにより除去し
、汚濁水及び食品残漬を含む汚lAt−ディスボーfK
1m砕し、はば均一なペースト状にしたものを、実施f
llの処理法と同じ方法で処理した。
(2) Treatment method A viscous oily substance floating above the object in the storage tank (
#hSaponified vegetable oil) is removed using a blowfish, and the dirt containing contaminated water and food residue is removed.
The material was crushed into a uniform paste by 1 m, and then
The treatment was carried out in the same manner as for ll.

(3)  処理結果 実施fill (1)  処理対象物 牛ふん尿(壷金水洗水を含む)で、その峨(2)  処
理法 わら屑0毛玉その他の粗大ゴイを分−した稜の廃液部を
実施例1の@理法と同じ方法で丸環した。
(3) Implementation of treatment results (1) Processing target: Cow manure (including water for rinsing the pot); (2) Treatment method; A ring was formed in the same manner as in Example 1.

(3)  処環結襞 11m例6 +11  処理対M愉 土砂〈っさく液部で、その機略性状は次の通りである。(3) Terminal folds 11m example 6 +11 Processing vs. M-fun The mechanical properties of the liquid part of the soil are as follows.

(2) 処m法 実施例1の処理法と同じ方法で処理した。(2) Disposal method The treatment was performed in the same manner as in Example 1.

(3)  処暑結果 実施例7 (11処H1対象物 ベントナイト廃液部で、その罐略性状は次の通りである
(3) Treatment Heat Result Example 7 (11 Treatment H1 target bentonite waste liquid section, the properties of the can are as follows.

(2)  ’4511法 実施例1の@理法と同じ方法で賜壜した。(2) ’4511 Law The bottle was given in the same manner as in Example 1.

(3)  処理結果 本発明は現在膨大な発生鷲をかかえて環境上の社会問題
となっている下水fj泥、し尿1食品汚泥等の廃液部に
対して簡単かつ経済的に画処理的浄化@理を行なうこと
かで龜るもので、該処理に際して2?X公#−となり得
ることなく。
(3) Treatment results The present invention can easily and economically purify waste liquids such as sewage mud, human waste, and food sludge, which are currently generating a huge amount of environmental and social problems. 2? Without being able to become X public #-.

必要に応じて再祠用できる曖性土壊の改良材を慢ゐこと
もでき、JR境公害防止上格別の効果を奏するものであ
る。
It can also be used to improve ambiguous soil damage that can be re-shrined as needed, and is extremely effective in preventing JR environmental pollution.

手続補正書(自発) 昭和56年12月8日 特許庁長官 島 1)春 樹  殿 −事件の表示 昭和66年特許順$177148号a発
明の名称 蒜 門 屍 属 i 扇 i 晟 la補正
をする者 事件との関係  特許出願人 住  所  4門童蔽門束蓄駿笛2630番地の4氏 
 名   −−−轟 はか1名 4代 場 人 a補正の対象  明細沓の発明の詳細な説明の欄6補正
の内容   別紙のとおり L明細書第1ページ下から第2行及び第4ページ下から
第3行のrD r gJを[DryJと補正します。
Procedural amendment (spontaneous) December 8, 1980 Director General of the Japan Patent Office Shima 1) Haruki - Indication of the case 1988 Patent Order No. 177148a Name of the invention Hirumon Corpse Genus i Fan i Seki la Make amendments Relationship with the patent case Address of the patent applicant: Mr. 4, 2630, 4mon Dodamon Takashijunbue
Name --- Todoroki Haka 1 person 4 generations Place Person a Target of amendment Contents of amendment in Column 6 of Detailed explanation of the invention in the specification As shown in the appendix, L specification, second line from the bottom of page 1 and bottom of page 4 Correct rD r gJ in the third line from [DryJ].

Claims (1)

【特許請求の範囲】[Claims] 廃液泥に添加しかつ混合攪拌することで、該廃液泥中の
固形物のIll!lと容積収縮及び水質の酸化と清澄を
生じさtろことにより害鳥な向液分−が得られる組成物
で、生石灰4.8〜32Jl量%、消石灰49,1〜6
9.0重量%、ケイ酸石灰3L〜489直量%、滑石8
6.9〜′1.3重量%、腐植dR10〜161量%及
び酸性陶土3J〜13.7直置%からなることを特徴と
する膓液蛇処理用組成物。
By adding to the waste liquid mud and mixing and stirring, the solids in the waste liquid mud can be removed. It is a composition that produces harmful lyotropic components by causing volumetric contraction, oxidation and clarification of water quality, and contains quicklime 4.8-32 Jl mass%, slaked lime 49.1-6
9.0% by weight, lime silicate 3L-489% by weight, talc 8
6.9 to 1.3% by weight of humus dR, 10 to 161% by weight of humus dR, and 3J to 13.7% of acidic china clay.
JP56177148A 1981-11-06 1981-11-06 Composition for treatment of waste liquid and sludge Granted JPS5879509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56177148A JPS5879509A (en) 1981-11-06 1981-11-06 Composition for treatment of waste liquid and sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56177148A JPS5879509A (en) 1981-11-06 1981-11-06 Composition for treatment of waste liquid and sludge

Publications (2)

Publication Number Publication Date
JPS5879509A true JPS5879509A (en) 1983-05-13
JPS6147122B2 JPS6147122B2 (en) 1986-10-17

Family

ID=16026024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56177148A Granted JPS5879509A (en) 1981-11-06 1981-11-06 Composition for treatment of waste liquid and sludge

Country Status (1)

Country Link
JP (1) JPS5879509A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5415778A (en) * 1993-03-03 1995-05-16 Hydrogeo North America L.L.C. Method and related product for purification of waste water
US5491281A (en) * 1994-05-12 1996-02-13 Bhat Industries, Inc. Reactive exothermic liquid - inorganic solid hybrid process
DE19542742B4 (en) * 1995-02-16 2005-09-01 Bakelite Ag Process for the immobilization of pollutants in soils, sediments or sludges

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5415778A (en) * 1993-03-03 1995-05-16 Hydrogeo North America L.L.C. Method and related product for purification of waste water
US5491281A (en) * 1994-05-12 1996-02-13 Bhat Industries, Inc. Reactive exothermic liquid - inorganic solid hybrid process
DE19542742B4 (en) * 1995-02-16 2005-09-01 Bakelite Ag Process for the immobilization of pollutants in soils, sediments or sludges

Also Published As

Publication number Publication date
JPS6147122B2 (en) 1986-10-17

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