JPS58112096A - Purification of organic waste water or organic sludge - Google Patents

Purification of organic waste water or organic sludge

Info

Publication number
JPS58112096A
JPS58112096A JP56209354A JP20935481A JPS58112096A JP S58112096 A JPS58112096 A JP S58112096A JP 56209354 A JP56209354 A JP 56209354A JP 20935481 A JP20935481 A JP 20935481A JP S58112096 A JPS58112096 A JP S58112096A
Authority
JP
Japan
Prior art keywords
sludge
water
separated
treatment
treated
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
Application number
JP56209354A
Other languages
Japanese (ja)
Inventor
Katsuyuki Kataoka
克之 片岡
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.)
Ebara Corp
Original Assignee
Ebara Infilco Co Ltd
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 Ebara Infilco Co Ltd filed Critical Ebara Infilco Co Ltd
Priority to JP56209354A priority Critical patent/JPS58112096A/en
Publication of JPS58112096A publication Critical patent/JPS58112096A/en
Pending 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Treatment Of Sludge (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To enhance the power of dehydrating treatment without the necessity of a sludge-thickening step, by adding a ferric flocculant to treated water from the step of biological treatment, separating the treated water under an acidic condition, and subjecting the separated water to advanced treatment while dehydrating the separated sludge. CONSTITUTION:After organic waste water 1 such as night soil is treated in the step 2 of biological treatment, the biologically treated water 3 (or a mixed slurry of it with excess biological sludge) is mixed with a ferric flocculant 4, e.g. ferric chloride or poly (ferric sulfate), and optionally an alkali agent 5, e.g. slaked lime, and separated into clean separated water 7 and conc. sludge 8 by using the step 6 of capillary suction-dehydration with felt, sponge or the like. The separated water is subjected to advanced treatment, while the conc. sludge 8 is supplied to a filter press 9 provided with a pressing mechanism to obtain dehydrated cake 10 having a low water-content and a dehydration filtrate 11.

Description

【発明の詳細な説明】 本発明は4i慎性排水又り有機性汚泥の処理方法の改良
に関するものでめる0 従来、有機性排水の生物処理水をさらに高良に浄化する
ため第1凶の1つな縦東処理による三次処理法がハく実
施されている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for treating 4i wastewater or organic sludge. A tertiary treatment method with one vertical east treatment is widely practiced.

すなわち、第1−において有機性排水1の生物先埋水3
は向えは鉄糸縦粂剤4、アルカリ刑S及びホリマーsを
冷加して凝集沈駅工&20で処理され、分−水が軟P廂
上、%21で島良処塩されると共に、これらのl@から
分離δれた汚泥は畿動恢、脱水処理されている。なお−
宇、2に一1生智処堆1−@、2Bは#L粂沈駅汚泥、
24框生物学制汚泥、2iI扛汚泥脱水工伽、26L汚
泥龜輸工h127は脱水助剤でめる〇 このように従来法で龜、凝果フロックotm液分#ll
法として沈lk法区は浮上分離(転)が殊用嘔Iしてい
るので、フロックキャリオーバーなとのためFMJ敵分
IIjA5IIJ率が愚(、SSkM&に除云するため
r(4、さらに砂濾過’:L@21を設昨る必景かりる
なとプロセスの複雑化を招いている。
That is, in the first stage, organic wastewater 1 is buried in biological wastewater 3.
The other side is treated with iron thread warping agent 4, alkaline filtration agent S and holimer s by cooling and coagulation sedimentation station & 20, and the separated water is treated with soft P layer and Shimara treatment salt at % 21. The sludge separated from l@ is subjected to dehydration treatment. Note-
U, 2 to 11 Ichigodokoro 1-@, 2B is #L Kumishin Station sludge,
24-frame biological sludge, 2iI sludge dewatering technology, 26L sludge transport technology h127 are treated with a dehydration aid 〇 In this way, conventional methods are used to remove sludge, curd floc OTM liquid fraction #ll
As a law, flotation separation (transfer) is not particularly used in the sinking method, so the FMJ ratio is low due to floc carryover, and r(4 to exclude SSkM&, and sand Filtration': It is necessary to set up L@21, which complicates the process.

さらに間l@なのL生物宗鯛汚泥24、#!粂沈皺汚泥
23(又は浮上分離汚IIFO,)の88凝飄が1〜3
−機良と布滓なため、汚泥脱水1根3、Sへの供給准菖
が多くなシ、脱水機のlBI珈馳力も塩1するという大
eなm点〃)りることでめった。
In addition, @Nano L Biological Sotai Sludge 24, #! The 88 flocculation of the wrinkled sludge 23 (or flotation separation sludge IIFO) is 1 to 3.
- Because the machine was dry and the slag was sludge, there was a large amount of sludge dewatered, and there was a lot of water to be supplied to S, and the dewatering machine's IBI coffee power was also 1 salt, which was a big problem.

このため、鍛集沈歇汚泥23を脱水機に供給する剖に1
カシツクナー、遠心険紬伽、ウェッジワイヤースクリー
ンなとの汚泥機軸1楠26を敗ける分散かめ4:Iか、
シックナーはF&亀面執、遠心磯#1IaAは動力コス
ト、スクリーンロー品コスト(ホリマー龜加のたりンか
大極くなるという欠点tもつ1いた。さらに、幽紬汚託
の脱水処理時に脱水助剤217t−必嶽とするという問
題点か跣されていfc。
For this reason, it is necessary to feed the forging sedimentation sludge 23 to the dewatering machine once.
Dispersion Kame 4: I, which defeats the sludge machine shaft 1 Kusunoki 26 with Kashitsukner, centrifugal Tsumugi, and wedge wire screen,
The thickener is F&Kamemoshi, and Centrifugal Iso #1 IaA has the disadvantage of power cost and screen low product cost (the cost of Hollymer's water is extremely high).Furthermore, it is necessary to assist in dehydration during the dehydration process of Yutsumugi Firaku. 217t - The problem of making it mandatory is fc.

また、南慣性、排水、活性汚泥処J!1なとの生物処理
余剰汚泥の撫り注が勉いことか汚泥処理プロセスの最大
の問題点の一つになっており、従来のム力沈IR鎖JI
!法にかえて最近は点心蒙輪昧、浮上機m法が検討さl
−しているか、動力コストが鳥いという大右な8亀点が
解決δfしていなかった。
Also, south inertia, drainage, activated sludge plant J! One of the biggest problems in the sludge treatment process is the pouring of biologically treated surplus sludge, and the conventional method of sludge sedimentation by IR chain JI is one of the biggest problems in the sludge treatment process.
! Recently, instead of the law, the dim sum method and the levitator method have been considered.
- The 8 important points that the power cost is too high have not been resolved δf.

本発明は、こ(t)↓うな従来の有機性併水生物処塩水
の簡Ji九塩1楡、襞泉処堆工稚及び汚泥脱水1松のも
つ、畝多くの欠点を根本的に解決することのできる7゛
ロセスを提供するtのでめる01−なわb1本弗η11
愼性併水ケ生物処理工嶺°で処理し、該生物錫塩1程か
らの処理水もしくは該処理水と余剰汚泥との屁合スラリ
ー又り1機性汚泥に少なくとも獣糸?R巣剤を機態し、
毛管吸引作用を利用して敗性条汁°)で分離水と分*汚
泥にwi准分離し、駄分練水t^良九理すると共に、前
記分離汚泥tフィルタグレス蚤腕水慎にて脱水すること
t待機とする壱徐性耕水又μ壱嶺性汚耗の錫塩力紙であ
る。
The present invention fundamentally solves the many drawbacks of conventional organic co-hydrobiological treatment brine, simple treatment of organic co-water biological treatment salt water, sludge dewatering, and sludge dewatering. Provides a 7゛ process that can be used for 01-rope b1 book
The treated water from the biological tin salt or the slurry of the treated water and excess sludge is treated in a co-water biological treatment facility, and at least animal silk is added to the organic sludge. The mechanism of R nest agent,
Utilizing the capillary suction action, the septic liquid is separated into separated water and sludge, and the separated sludge is filtered into water and sludge. It is a tin-salt paper that can be slowly cultivated or soiled without being dehydrated.

しかして、本弁明の一実施瓶徐を帛2図を参湘しlがら
欧−すると、し尿などの1嶺性排水1扛生物処塩工&2
(生物学的硝化脱i!木鰍なと仕意の生物も理工*)で
処理さ扛たのち、生物処理水3(又は、これと余剰生物
汚泥との九合スラリー)に塩化第2妖、ホ94tCrl
!鉄なとの鉄系凝集剤4と、分散(PH1−緻性餉に読
振)に応じて消石灰なとのアルカリ剤6 ’k 添)J
Lして7エルト、スホンジなどによる毛11i&引脱木
工?i!(飼えはrc、p、フィルター」(曲醋名)を
急用する)6r(てm筐な分離水7と微動スラッジ8に
分離する。分離水1祉高IIIL九塩すると共1(、摂
動スラッジ8を圧搾嶺檎付のフィルタプレス9に供給し
、低含水率の脱水ケーキ1Gと脱水Faulk−得る0 本発明の最大ポイントは従来の皺集沈殿工′h2G(又
L#上分離工根)に替えて、毛11v&引脱水工機−七
配置し、かつ毛管吸引脱水によって侍られたスラッジi
フィルタ7レス9 rc供乾して史に脱水する仁とにめ
る0 また、生@宗駒汚泥なとの1憎性汚泥に対して本発明を
愈用するに抹、第3図のように1慎性汚泥30に少なく
とも鉄系IR粂剤4を絵加し、上型吸引腕水工@@4’
ごて汚泥1m細し、゛画一汚泥31を圧搾嶺構付のフィ
ルタプレス9にて脱水し、脱水ケーキ■を得るようにす
る0なおss、ms’1分離水でめる0 以上のように本発明によれhS次のようなム嶽効米を得
ることかでさ、従来プロセスの諸欠点を根本的に%医で
さる0 ψ 毛w吸引脱水工徳を生物九理水のIfIlI嵐処理
1撫に配置したので、従来のようなフロックキャクオー
パ机象、汚泥*嵐か希薄でめるという欠点力為全くない
0また、分離水はフェルト等によって一過されているた
め、ltl濾過几塩水以上に溜筺1なっており、この結
果、従来プロセスにおける砂濾過1撫か年債となる。
Therefore, in Europe, referring to the illustrations of the first embodiment of this defense, one example of this is that one wastewater such as human waste, one biological salt treatment plant, and two
(Biological nitrification removal! Biological organisms such as wood sludge are also treated with science and technology*), and then the biologically treated water 3 (or a slurry of this and surplus biological sludge) is added to the chloride 2 , Ho94tCrl
! Iron-based flocculant 4 and slaked lime alkali agent 6 depending on the dispersion (PH1-Difficulty)
L and 7 Elt, hair 11i & pull-out woodwork by Suhonji etc.? i! (Use the rc,p,filter) 6r(temperature separated water 7 and micro-moving sludge 8.Separated water 1) 8 is supplied to a filter press 9 equipped with a pressing ring to obtain 1G of dehydrated cake with a low moisture content and dehydrated Faulk. Instead, the sludge I placed in the hair 11v & dewatering machine-7 and was served by capillary suction dehydration.
Filter 7-less 9 RC drying and dehydration in the history 0 In addition, when using the present invention for 1-hateful sludge such as raw @ Munekoma sludge, as shown in Figure 3 1 Add at least iron-based IR sludge 4 to the sludge 30.
Use a trowel to reduce the sludge to 1 m, and dehydrate the sludge 31 with a filter press 9 equipped with a squeezing ridge structure to obtain a dehydrated cake. According to the present invention, it is possible to obtain the following effective rice, which fundamentally eliminates the various shortcomings of the conventional process. Because it is placed in the first stage of treatment, there is no problem with the conventional floc-crystal structure, sludge * storm, or dilution. It is more concentrated than salt water, resulting in sand filtration in the conventional process.

■ 摂動スラッジ8の5SIIjLはlO囁根藏が谷 
  易に侍られ、従来フ゛ロセスの1〜396の88龜
嵐に比べて看しく尚い0従って、恢米1aセス1(ンけ
る汚泥*継工嶺か一切不景となるoしかも脱水機の地塊
能力が向上する。
■ 5SIIjL of perturbation sludge 8 is lO whisper root Kuragadani
It is easy to handle, and it is even more beautiful than the conventional process 1 to 396 88 sludge. Improves lump ability.

■ 生物処理水に獣糸縦集剤を添加し、毛ta引脱水し
たi%lkmM泥はフィルタプレスで脱水する方法によ
って、全く脱水助剤を硝加することなく含水率50〜6
5−という着しく低含水率のケーキが得られることか判
明した0従って、脱水ケーキの乾燥、焼却島分時にム油
か不懺となり、鵬着な噛エネルキー効朱かおる。
■ The i%lkmM mud, which has been dehydrated by adding animal thread collectors to biologically treated water and dewatering it, can be dehydrated with a filter press to have a water content of 50 to 6 without adding any dehydration aid.
It has been found that a cake with a relatively low water content of 5-0 can be obtained. Therefore, when the dehydrated cake is dried and incinerated, it becomes oily or unstainable, giving off a reddish smell with an extremely chewy energy effect.

■ さらに、生@魁理水3に生智処理工根富から発生す
る生物余剰汚泥を島會ゼしめ1処塩すると生物処理水魯
のCOD、色直、りン叡、88の除去を目的として添加
される鉄系凝集剤4により1生物余剰汚泥の脱水性が着
しく改豊されることが見い出ちれた。従って、生物余剰
汚泥の脱水においても従来プロセスにおける別個の脱水
助剤270龜加ρ為不愼となり、4資源が可能になった
■ In addition, the biological surplus sludge generated from the Ikuchi treatment plant Netomi is collected in the raw @Kairui water 3 and treated with salt for the purpose of removing COD, color change, rinsing, and 88 from the biological treatment sewage. It has been found that the iron-based flocculant 4 added as a 1-organic flocculant significantly improves the dewatering properties of biological surplus sludge. Therefore, even in the dewatering of biological surplus sludge, a separate dewatering aid in the conventional process is no longer required, and four resources are now available.

■ −′*奴吸引水工@Sを生物九塩水3の島嵐九m用
#!粂工相に配置したので、従来70セスにおける&粂
沈&(゛又は浮上分履工機)、しP朧工機、汚泥111
n工樵という三つの1相か単一の1撫で達成でき、プロ
セスの簡易化、#1M1t責、設亀向徴の大−な低Jk
かWJ能となった。
■ -'*Guy suction waterworks @S for biological nine salt water 3 Shima Arashi nine meters #! Since it is located in the Kume phase, the conventional 70 cess & Kumi sink & (゛ or floating fraction excavation machine), ShiP Oboro Koki, sludge 111
It can be achieved with three steps or a single stroke of n engineer, process simplification, #1M1t responsibility, and a large low Jk
It became WJ Noh.

■ 従来プロセス1cおいて必須でめった、南分子表集
剤(ポリ・マー)が本発明6rcおいては全く不景とな
るので、11塩内子が減少し、ポリマーf#解作巣力為
不散となるなと、メンテナンスが容易になるはか、ホリ
!−の残留毒性の間組も起こり侍ない。
■ Since the southern molecule bulking agent (polymer), which is essential and rare in the conventional process 1c, is completely undesirable in the present invention 6rc, 11 Shionai decreases and the polymer f# disintegration force is reduced. It will be easier to maintain and prevent clutter! - The residual toxicity may also occur.

Φ 本発F!8を有機性汚泥の績細説水に通用する獅曾
、毛11鉄引脱水工程への流入汚泥に妖糸叙果剤t−冷
加する仁とによって、他めて容易に向形物龜[10−以
上のam汚泥か憎られ、これを71ルタルスで脱水する
ようにしたので、ム力沈敷幽縮、浮上凝縮あるいは遠心
凝縮ではとうてい得られないl1lb鏡監の員―汚泥が
鳥分子凝集剤および大きな動力を一切分散とすることな
くに鎖iiJ!!!水性の1板性汚泥が極めて合理的に
錫塩できる。
Φ Original F! 8 is a detailed explanation of organic sludge, which is commonly used for water, and 11 the sludge flowing into the iron drawing and dewatering process is cooled and easily transformed into a suitable material. [Am sludge of 10- or more is hated, so I dehydrated it with 71 Lutarus, so I couldn't get it by force sedimentation, floating condensation, or centrifugal condensation.The sludge became bird molecules. chain iiJ without any dispersion of flocculants or large forces! ! ! Tin salt can be produced from aqueous single-plate sludge in an extremely rational manner.

次1te−s本発明あ実施りylLついて記す。Next, the implementation of the present invention will be described.

*施ガ  l 側lりの水*t*するし尿t1布釈水を添加することな
く硝化a儂#L皺生物宇的佑化説輩本錫塩した。
*Water on the side*t*Natural urine T1 Nitrification without adding water *L wrinkled biological theory of natural tin salt.

島 l 懺 次に、皺生物処岬水と生物余剰汚泥との1合液(884
800〜5oooq/z、pH7,3〜7.5.ill
解! C0D500〜600WIi//l* 1!%性
色J13000’〜4000、PO4480〜560w
v/l−)に塩化纂2麩1i’ect、 t−3000
*/Lllk加したのち、消石灰cg(oH**を約1
00019/lt−加えてpH3〜4.5に鉤灸し、毛
w叙引脱水機(C,P、フィルターンに悩絽し、jlP
)2Feの水質を弔する^表地理水と88幽[1G−1
5−の鎖編スラッジを侍た01m2表 しかして、この微細スラッジ1に脱水助剤を添加するこ
となく圧搾機栴付フィル署プレスにホンブ圧送し、濾過
圧力4 kgj/a 、圧搾圧力15 kyf/ctA
にて脱水した軸糸、負′水率65.2%の脱水ケーキを
得た。この脱水ケーキの低位妬熱菫は2900に/J#
−p、 sでわり、自燃焼却が可能でめった0夷抛ガ 
 2 )水処楓@性、汚泥錫板1機から発生する缶刺油性汚泥
を下記の撫々のTIk画法を通用して九施した結果、?
Ik紬汚泥繰嵐は、^3表のとおシとなった0帛 3 
弐 また、■、■、Oのいずれのa組法に妖糸峡集剤を通用
しても、龜−汚泥画板は櫓加ぜす■、■法についてa追
に恋化した00の本発明法によるl1lIIIi!汚泥
tモーノホンノ(#lG11名) W(よってフィルタ
プレスに打込み脱水した粕来、水分64〜6bうの礁め
て低水分のケーキか倚らnた0
Shima l Senji, a mixture of Ashi Biological Treatment Misaki Water and biological surplus sludge (884
800-5oooq/z, pH 7.3-7.5. ill
Solution! C0D500~600WIi//l* 1! % color J13000'~4000, PO4480~560w
v/l-) to chloride 2 1i'ect, t-3000
*/ After adding Lllk, add slaked lime cg (oH** about 1
00019/lt-Additionally, moxibustion to pH 3-4.5, hair drying machine (C, P, filter), jlP
) Condolences for the water quality of 2Fe^ Surface geological water and 88 [1G-1
The chain-woven sludge of 5-1 was prepared in a volume of 01 m2, and this fine sludge 1 was pumped into a press with a filter press without adding any dehydration aid, and the filtration pressure was 4 kgj/a and the squeezing pressure was 15 kyf. /ctA
A dehydrated cake with a negative water content of 65.2% was obtained from the axoneme dehydrated. The low jealousy violet of this dehydrated cake is 2900/J#
- It is divided by p and s, and self-combustion is possible, which is rare.
2) As a result of applying the following TIk painting method to the canned oil-based sludge generated from one sludge tin plate,
Ik Tsumugi sludge raising storm is 3
2.Also, even if you apply the Youitokyo collection agent to any of the a combination methods of ■, ■, and O, the sludge drawing board will be added to the turret. l1lIIIi by law! Sludge T Monohonno (#1G 11 people) W (Therefore, the sludge that was poured into the filter press and dehydrated was a cake with a low moisture content of 64 to 6b.)

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

第l凶4恢米昧O糸杭胱明凶、第2凶及び帛3図は本発
明の谷実施聰様を不す系統脱明−でるる〇五・・・有機
性排水、 ト・・生物処理1租、 3・・・生qm九急
水、 4・・・妖糸献系剤、 6・・・アルカリ剤、5
′・・・ホリマー、 6・・・毛ta引腕不工掴、y、
sa、sa’・・・分融水、 ト・・−一ス2ツジ、9
・・・フィルタプレス、  14J、a2・・・脱水ケ
ーキ、11・・・脱水P液、  20・・・皺業沈振工
撫、21・・・砂P−工1、 28・・・叙粂沈駅汚泥
、  34・・・生物余剰汚泥、 16・・・汚泥脱水
1機、 26・・・汚泥鎖軸工棚、 エフ・・・脱水助
剤、 30・・・1機性汚泥、 31・・・l1lIi
IIIA汚泥。 特許出龜人  荏鳳インフイルコ株式会社代塩入 弁塩
士  港 山 五 − 同  弁塩士  千 1)  稔
Part 1, number 4, and number 3 show the results of the present invention. Biological treatment 1x, 3... Raw qm Kukyu water, 4... Youishinken type agent, 6... Alkaline agent, 5
′...Horimar, 6...Hair ta pull arm clumsiness, y,
sa, sa'...melt water, t...-1su2tsuji, 9
...Filter press, 14J, a2...Dehydrated cake, 11...Dehydrated P liquid, 20...Siye Shenzhen Technique, 21...Sand P-Technology 1, 28...Shagyishen Station Sludge, 34... Biological surplus sludge, 16... 1 sludge dewatering unit, 26... Sludge chain shaft rack, F... Dewatering aid, 30... 1 Machinery sludge, 31... l1lIi
IIIA sludge. Patent developer Eiho Infilco Co., Ltd. Daishioiri Benshioji Minato Yamago - Daishioiri Benshioji 1) Minoru

Claims (1)

【特許請求の範囲】 1、有機性排水を生物処理1伽で処堆し、該生物処理1
@からの処理水もしくa駄錫塩水と余剰汚泥との親会ス
ラリー又は有機性汚泥に少なくとも鉄糸峡東剤【松加し
、上室吸引作用をオリ用して酸性条件下で分離水と分離
汚泥に向a分際し、該分離水1に一度処理すると共に、
前記分離汚泥をフィルタプレス屋脱水慎にて脱水するこ
とt特徴とする有機性排水又は有機性汚泥の処理方法0
[Claims] 1. Treating organic wastewater with a biological treatment 1;
Treated water or a slurry of salt water and excess sludge or organic sludge is treated with at least Tetsukyoto agent [Matsuka, or separated water under acidic conditions using the suction action of the upper chamber] and the separated sludge for a minute, and the separated water 1 is treated once,
A method for treating organic wastewater or organic sludge characterized by dewatering the separated sludge in a filter press shop.
JP56209354A 1981-12-25 1981-12-25 Purification of organic waste water or organic sludge Pending JPS58112096A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56209354A JPS58112096A (en) 1981-12-25 1981-12-25 Purification of organic waste water or organic sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56209354A JPS58112096A (en) 1981-12-25 1981-12-25 Purification of organic waste water or organic sludge

Publications (1)

Publication Number Publication Date
JPS58112096A true JPS58112096A (en) 1983-07-04

Family

ID=16571552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56209354A Pending JPS58112096A (en) 1981-12-25 1981-12-25 Purification of organic waste water or organic sludge

Country Status (1)

Country Link
JP (1) JPS58112096A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5948269A (en) * 1997-08-20 1999-09-07 Stone; Michael D. Process for the removal and suppression of dissolved hydrogen sulfide and other malodorous compounds and reduction of acidity in liquid and sludge wastewater systems
CN106186639A (en) * 2016-08-16 2016-12-07 中电建水环境治理技术有限公司 Lake, river is gushed polluted bed mud and is processed remaining soil regenerative system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5948269A (en) * 1997-08-20 1999-09-07 Stone; Michael D. Process for the removal and suppression of dissolved hydrogen sulfide and other malodorous compounds and reduction of acidity in liquid and sludge wastewater systems
CN106186639A (en) * 2016-08-16 2016-12-07 中电建水环境治理技术有限公司 Lake, river is gushed polluted bed mud and is processed remaining soil regenerative system
WO2018032831A1 (en) * 2016-08-16 2018-02-22 中电建水环境治理技术有限公司 Residual soil regeneration processing system for contaminated bottom mud in rivers and lakes

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