JP3222247B2 - Sludge dewatering method - Google Patents

Sludge dewatering method

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Publication number
JP3222247B2
JP3222247B2 JP04608993A JP4608993A JP3222247B2 JP 3222247 B2 JP3222247 B2 JP 3222247B2 JP 04608993 A JP04608993 A JP 04608993A JP 4608993 A JP4608993 A JP 4608993A JP 3222247 B2 JP3222247 B2 JP 3222247B2
Authority
JP
Japan
Prior art keywords
sludge
alkaline earth
earth metal
metal salt
organic
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 - Lifetime
Application number
JP04608993A
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Japanese (ja)
Other versions
JPH06238300A (en
Inventor
勝利 田中
亮介 米本
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.)
Hymo Corp
Original Assignee
Hymo Corp
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Filing date
Publication date
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Priority to JP04608993A priority Critical patent/JP3222247B2/en
Publication of JPH06238300A publication Critical patent/JPH06238300A/en
Application granted granted Critical
Publication of JP3222247B2 publication Critical patent/JP3222247B2/en
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Expired - Lifetime legal-status Critical Current

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

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は有機性汚泥の脱水方法に
関するものであり、さらに詳しくはアルカリ土類金属塩
および特定構造の有機高分子凝集剤を組み合わせて使用
することにより経済的有利に汚泥脱水を行う方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for dehydrating an organic sludge, and more particularly to a method for economically and advantageously using an alkaline earth metal salt and an organic polymer flocculant having a specific structure in combination. The present invention relates to a method for performing dehydration.

【0002】[0002]

【従来の技術】下水処理場、屎尿処理場、各種工場にお
ける活性汚泥法などの生物処理施設から発生する有機性
汚泥は適当な脱水剤を混和した後、濾過または遠心分離
により機械脱水される。この様な有機性汚泥用の脱水剤
としてはアクリル系有機高分子凝集剤により汚泥を凝集
させた後にベルトプレスやデカンターにより脱水する方
法、あるいは塩化第2鉄および水酸化カルシウムを汚泥
に添加し真空濾過する方法が一般的である。また、ポリ
塩化アルミニウム、硫酸バンド、ポリ硫酸鉄等のアルミ
ニウム塩や鉄塩を加えた金属水酸化物含有汚泥に有機高
分子凝集剤を加える方法も公知である。
2. Description of the Related Art Organic sludge generated from biological treatment facilities such as activated sludge treatment in sewage treatment plants, human waste treatment plants, and various factories is mixed with an appropriate dehydrating agent and then mechanically dewatered by filtration or centrifugation. As such a dehydrating agent for organic sludge, a method of coagulating sludge with an acrylic organic polymer coagulant and then dehydrating with a belt press or a decanter, or adding ferric chloride and calcium hydroxide to the sludge to form a vacuum The method of filtering is common. In addition, a method of adding an organic polymer flocculant to a metal hydroxide-containing sludge to which an aluminum salt such as polyaluminum chloride, a sulfate band, and polyiron sulfate has been added, is also known.

【0003】この様な金属水酸化物含有汚泥に有効な有
機高分子凝集剤としてはアニオン性基とカチオン性基を
併せ持つ凝集剤が有効とされ、アクリル酸・アクリルア
ミド共重合物の如きアクリル系アニオン性高分子凝集剤
とポリアクリルアミドのマンニツヒ変性物あるいはジア
ルキルアミノアルキル(メタ)アクリレートまたはジア
ルキルアミノアルキル(メタ)アクリルアミドの塩また
は4級化物等のアクリル系カチオン性モノマー(共)重
合体から成るアクリル系カチオン性高分子凝集剤との混
合物が知られている。
As an organic polymer flocculant effective for such a metal hydroxide-containing sludge, a flocculant having both an anionic group and a cationic group is considered to be effective, and an acrylic anion such as acrylic acid / acrylamide copolymer is used. Acrylic based on acrylic polymer composed of acrylic polymer such as Mannich-modified polyacrylamide and dialkylaminoalkyl (meth) acrylate or dialkylaminoalkyl (meth) acrylamide salt or quaternary compound Mixtures with cationic polymeric flocculants are known.

【0004】またポリアクリル酸のヒドラジン変性物あ
るいは前述のアクリル系カチオン性モノマーおよびアク
リル酸等のアニオン性モノマーを含有するモノマーの重
合体から成るアクリル系両性高分子凝集剤も各種提案さ
れ、これら両性高分子凝集剤を他のアクリル系高分子凝
集剤と混合することも公知である。
There have also been proposed various amphoteric polymer flocculants comprising a hydrazine-modified polyacrylic acid or a polymer of a monomer containing the above-mentioned acrylic cationic monomer and an anionic monomer such as acrylic acid. It is also known to mix polymeric flocculants with other acrylic polymeric flocculants.

【0005】これら従来多用されたアクリル系有機高分
子凝集剤に対し、N−ビニルカルボン酸アミド(共)重
合体の加水分解物、ポリアクリルアミドのホフマン分解
物、ポリエチレンイミン、ポリビニルイミダゾリン等の
1級または2級アミンを含有する高分子が有機性汚泥の
脱水剤として公知である。
In contrast to these acrylic organic polymer flocculants which have been widely used in the past, a primary product such as a hydrolyzate of an N-vinylcarboxylic acid amide (co) polymer, a Hofmann decomposition product of polyacrylamide, polyethyleneimine, polyvinylimidazoline, etc. Alternatively, polymers containing secondary amines are known as organic sludge dehydrating agents.

【0006】なかでもN−ビニルカルボン酸アミド
(共)重合体の加水分解物は近年注目され、特開昭58
−23809号公報、特開昭59−39400号公報に
はポリN−ビニルカルボン酸アミドの部分加水分解物、
また特開昭59−39399号公報、特開昭62−74
902号公報、特開昭63−218718号公報にはN
−ビニルカルボン酸アミドと他のモノマーの共重合体の
加水分解物が開示されている。
Among them, a hydrolyzate of an N-vinylcarboxylic acid amide (co) polymer has recently attracted attention and has been disclosed in
-23809 and JP-A-59-39400 disclose partial hydrolysates of poly (N-vinylcarboxylic acid amide).
JP-A-59-39399 and JP-A-62-74.
No. 902 and JP-A-63-218718 disclose N
-Hydrolysates of copolymers of vinyl carboxylic acid amides with other monomers are disclosed.

【0007】[0007]

【発明が解決しようとする課題】1級および/または2
級アミンを含有する高分子凝集剤は汚泥に対する吸着性
が良く、脱水ケーキの含水率を低下させる効果が強い。
しかしながら、上記凝集剤は多価アニオン塩やアルカリ
の影響を受け易く、消化汚泥の如く重炭酸イオンを多量
に含む有機性汚泥に対しては凝集力が弱く、酸添加によ
りpHを低下させる汚泥の調質法は酸の取り扱いが危険
であり、発泡によるスカム発生の恐れがある。これを改
善するため、汚泥調質のために従来公知の鉄塩やアルミ
ニウム塩を有機性汚泥に添加しても汚泥の脱水性は改善
されず、1級および/または2級アミンを有する高分子
凝集剤の効果を広範囲の汚泥に対し発揮させる方法が望
まれていた。
SUMMARY OF THE INVENTION Grade 1 and / or 2
A polymer coagulant containing a secondary amine has good adsorptivity to sludge and has a strong effect of lowering the water content of the dewatered cake.
However, the above flocculant is easily affected by polyvalent anion salts and alkalis, and has a weak flocculating power against organic sludge containing a large amount of bicarbonate ions, such as digested sludge. In the refining method, handling of acid is dangerous, and scum may be generated by foaming. In order to improve this, even if a conventionally known iron salt or aluminum salt is added to the organic sludge for sludge conditioning, the dewatering property of the sludge is not improved, and a polymer having a primary and / or secondary amine is used. There has been a demand for a method of exerting the effect of the flocculant on a wide range of sludge.

【0008】[0008]

【課題を解決するための手段】本発明者らは上記課題を
解決するために鋭意検討を行った結果、水溶性のアルカ
リ土類金属塩とビニルアミン構造単位および/またはア
ミジン構造単位が全繰り返し単位の35モル%以上であ
るカチオン性有機高分子凝集剤を組み合わせて汚泥に添
加することにより極めて優れた汚泥の脱水効果が発現す
ることを見い出し本発明に到達した。
Means for Solving the Problems The inventors of the present invention have made intensive studies to solve the above-mentioned problems, and as a result, have found that a water-soluble alkaline earth metal salt and vinylamine structural unit and / or
Midine structural unit is at least 35 mol% of all repeating units
The present inventors have found that an extremely excellent sludge dewatering effect is exhibited by adding a cationic organic polymer flocculant to the sludge in combination.

【0009】本発明の請求項1の発明は、有機性汚泥に
水溶性のアルカリ土類金属塩とビニルアミン構造単位お
よび/またはアミジン構造単位が全繰り返し単位の35
モル%以上であるカチオン性有機高分子凝集剤を添加す
ることを特徴とする汚泥の脱水方法である。
[0009] The invention of claim 1 of the present invention relates to a water-soluble alkaline earth metal salt and a vinylamine structural unit for organic sludge .
And / or the amidine structural unit is 35 of all repeating units.
A sludge dewatering method characterized by adding a cationic organic polymer flocculant of not less than mol% .

【0010】本発明の請求項2の発明は、アルカリ土類
金属塩を添加した後、ビニルアミン構造単位および/ま
たはアミジン構造単位が全繰り返し単位の35モル%以
上であるカチオン性有機高分子凝集剤を添加することを
特徴とする請求項1に記載の汚泥の脱水方法である。
According to a second aspect of the present invention, an alkaline earth
After adding the metal salt, the vinylamine structural unit and / or
Or the amidine structural unit is at least 35 mol% of all repeating units.
2. The method for dewatering sludge according to claim 1, wherein said cationic organic polymer flocculant is added .

【0011】本発明で使用する水溶性のアルカリ土類金
属塩はカルシウムまたはマグネシウムの塩であり、特に
限定されるものではないが、経済的見地からは塩化カル
シウムあるいは塩化マグネシウムを選ぶことができ、中
でも塩化カルシウムは特に好ましく用いられる。これら
アルカリ土類金属塩は、有機性汚泥1リットルあたり1
00〜5000mg添加混合して調質した後にカチオン
性有機高分子凝集剤を添加する方法が望ましい。
The water-soluble alkaline earth metal salt used in the present invention is a calcium or magnesium salt, and is not particularly limited. From an economic viewpoint, calcium chloride or magnesium chloride can be selected. Among them, calcium chloride is particularly preferably used. These alkaline earth metal salts are contained in an amount of 1 to 1 liter of organic sludge.
It is desirable to add a cationic organic polymer flocculant after adding and mixing 100 to 5000 mg, and then tempering.

【0012】アルカリ土類金属塩とカチオン性有機高分
子凝集剤を同時にあるいは混合して汚泥に添加しても有
効ではあるが、アルカリ土類金属塩を先に添加した方が
濾水性が良くなり含水率も低下する。アルカリ土類金属
塩を添加した後に攪拌を行うが、その目的は添加した金
属塩と有機性汚泥を十分に接触させて反応を行うことで
あり、攪拌の方法は攪拌羽根を用いてもよく、配管中の
流れによるものでもよい。
Although it is effective to add the alkaline earth metal salt and the cationic organic polymer flocculant to the sludge simultaneously or in a mixture, it is effective to add the alkaline earth metal salt first to improve the drainage. The water content also decreases. Stirring is performed after the addition of the alkaline earth metal salt, but the purpose is to sufficiently contact the added metal salt and organic sludge to carry out the reaction, and the stirring method may use a stirring blade, It may be due to the flow in the piping.

【0013】発明において還元粘度とは被験高分子化
合物を1規定の食塩水に0.1g/dlとなるように溶
解し、25℃で測定した還元粘度を意味する。
In the present invention, the reduced viscosity means the reduced viscosity measured at 25 ° C. by dissolving a test polymer compound in 1N saline at a concentration of 0.1 g / dl.

【0014】−ビニルホルムアミドはアクリロニトリ
ルとの交互共重合性比が良く、N−ビニルホルムアミド
構造単位とアクリロニトリル構造単位が隣接し易い。こ
の結果、N−ビニルホルムアミド構造単位の加水分解に
より生成したビニルアミン構造単位と隣接するアクリロ
ニトリル構造単位が分子内化学変性により、環状のアミ
ジン構造単位を生成する。該アミジン化反応は、酸性条
件下80〜150℃、好ましくは90〜120℃の加熱
条件で行われる。
[0014] N - vinylformamide may have alternating copolymerization ratios of acrylonitrile, easy to adjacent N- vinylformamide structural units and acrylonitrile structural units. As a result, the acrylonitrile structural unit adjacent to the vinylamine structural unit generated by the hydrolysis of the N-vinylformamide structural unit generates a cyclic amidine structural unit by intramolecular chemical modification. The amidination reaction is carried out under heating conditions of 80 to 150 ° C, preferably 90 to 120 ° C under acidic conditions.

【0015】本発明においては、ビニルアミン構造単位
とアミジン構造単位を合わせたカチオン性構造単位の比
率が全繰り返し単位中の35モル%以上を有する水溶性
高分子を用いる。アミジン構造単位の比率が大きいほど
汚泥脱水剤としての性能は向上する傾向にあるが、全官
能基が環化反応によりアミジン化することは非現実的で
あり、未反応の官能基や副反応により生成した官能基で
あるN−ビニルホルムアミド、ビニルアミン、アクリロ
ニトリル、アクリルアミド、アクリル酸等の構造単位も
分子内に有する。本発明において上記カチオン性高分子
凝集剤は汚泥中の懸濁固体に対し0.2〜2重量%添加
混合される。上記アミン・アミジン構造を有する高分子
凝集剤と前述の各種アクリル系高分子凝集剤を併用添加
することもできる。
In the present invention, a water-soluble polymer having a ratio of a cationic structural unit, which is a combination of a vinylamine structural unit and an amidine structural unit, of 35 mol% or more of all the repeating units is used. Although the performance as a sludge dehydrating agent tends to improve as the ratio of amidine structural units increases, it is impractical to convert all functional groups into amidines by a cyclization reaction. The resulting functional group also has structural units such as N-vinylformamide, vinylamine, acrylonitrile, acrylamide, and acrylic acid in the molecule. In the present invention, the cationic polymer flocculant is added and mixed in an amount of 0.2 to 2% by weight based on the suspended solids in the sludge. The polymer flocculant having an amine / amidine structure and the various acrylic polymer flocculants described above can be added in combination.

【0016】本発明においては、消臭の目的等で過酸化
水素等の酸化剤や防腐剤、香料等を併用することもでき
る。またアルカリ土類金属塩の効果に悪影響を及ぼさな
い範囲で鉄塩・アルミニウム塩・亜鉛塩等を併用するこ
ともできる。汚泥pHがアルカリ性となることは好まし
くないが、調質後の汚泥pHが6以下に留まる場合には
アルカリ性物質の添加も許される。
In the present invention, an oxidizing agent such as hydrogen peroxide, a preservative, a fragrance and the like can be used in combination for the purpose of deodorizing. In addition, iron salts, aluminum salts, zinc salts, and the like can be used in combination as long as the effects of the alkaline earth metal salts are not adversely affected. It is not preferable that the sludge pH is alkaline, but if the sludge pH after refining stays at 6 or less, the addition of an alkaline substance is also allowed.

【0017】[0017]

【作用】本発明におけるアルカリ土類金属塩の作用は、
重炭酸イオン等の凝集阻害物質を不活性化し汚泥の凝集
性を高める効果が主たるものと推測されるが、定かでは
ない。
The action of the alkaline earth metal salt in the present invention is as follows.
It is presumed that the main effect is to inactivate the coagulation inhibitor such as bicarbonate ions and to increase the cohesiveness of sludge, but it is not clear.

【0018】[0018]

【実施例】次に実施例により本発明をさらに詳細に説明
するが、本発明はこれらの例によって、なんら制限され
るものではない。なお、実施例、比較例で用いたポリマ
ーを表1に示す。
Next, the present invention will be described in more detail by way of examples, which should not be construed as limiting the present invention. Table 1 shows the polymers used in Examples and Comparative Examples.

【0019】[0019]

【表1】 [Table 1]

【0020】(実施例1〜、比較例1〜) A市下水処理場から発生した消化洗浄汚泥(pH:7.
0、固形物濃度:17800mg/l)200mlを3
00mlのビーカーに入れ、これに10%水溶液に溶解
した塩化カルシウム及び塩化マグネシウムを所定量添加
混合し、次に表1に示す汚泥脱水剤を0.2重量%の水
溶液状で所定量添加した後、TRITON社製のCST
測定装置の攪拌機で1000r.p.m.の回転速度で
10秒間攪拌した。攪拌により生じた凝集フロックの大
きさを測定した後、60メッシュのナイロン濾布を付し
た円筒に移し、重力濾過により凝集汚泥を濾過し、10
秒後の濾水量を測定した。重力濾過後の汚泥を30cm
角のポリエチレン製モノフィラメント濾布(日本フィル
コン社製)2枚に挟み、更にこれを水抜け溝を有するホ
リ塩化ビニル製の板に挟み、2kg/cm2 の圧力で6
0秒間圧搾脱水した後、常法により脱水汚泥ケーキの含
水率を測定した。以上の結果を表2に示す。
(Examples 1 to 8 , Comparative Examples 1 to 6 ) Digestion and washing sludge (pH: 7.
0, solids concentration: 17800 mg / l)
In a 00 ml beaker, a predetermined amount of calcium chloride and magnesium chloride dissolved in a 10% aqueous solution was added and mixed, and then a predetermined amount of a sludge dewatering agent shown in Table 1 in the form of a 0.2% by weight aqueous solution was added. , TRITON CST
1000 r. p. m. The mixture was stirred at a rotation speed of 10 seconds. After measuring the size of the flocculated floc generated by the stirring, the flocculated sludge was transferred to a cylinder having a 60-mesh nylon filter cloth and filtered by gravity filtration.
After 2 seconds, the amount of drainage was measured. 30cm sludge after gravity filtration
A square polyethylene monofilament filter cloth (manufactured by Nippon Filcon Co., Ltd.) is sandwiched between two sheets, and this is further sandwiched between polyvinyl chloride plates having water drainage grooves, and pressed at a pressure of 2 kg / cm 2.
After pressing and dewatering for 0 seconds, the water content of the dewatered sludge cake was measured by an ordinary method. Table 2 shows the above results.

【0021】[0021]

【表2】 [Table 2]

【0022】(実施例9〜16、比較例7〜8) T市下水処理場の消化汚泥(pH:7.7、固形物濃
度:23600mg/l)を用いて実施例1〜と同様
の方法で試験を実施した。結果を表3に示す。
(Examples 9 to 16 and Comparative Examples 7 to 8 ) The same as Examples 1 to 8 using digested sludge (pH: 7.7, solids concentration: 23600 mg / l) from the T municipal sewage treatment plant. The test was performed by the method. Table 3 shows the results.

【0023】[0023]

【表3】 [Table 3]

【0024】(実施例17〜19、比較例9〜13) F市下水処理場の混合生汚泥(pH:6.0、固形物濃
度:16500mg/l)を用い実施例1〜と同様の
方法で試験を実施した。結果を表4に示す。
(Examples 17 to 19 , Comparative Examples 9 to 13 ) The same as Examples 1 to 8 using mixed raw sludge (pH: 6.0, solids concentration: 16500 mg / l) from the municipal wastewater treatment plant in the F city. The test was performed by the method. Table 4 shows the results.

【0025】[0025]

【表4】 [Table 4]

【0026】[0026]

【発明の効果】本発明は有機性汚泥の脱水方法に関する
ものであり、アルカリ土類金属塩および特定構造の有機
高分子凝集剤を組み合わせて汚泥に添加することによ
り、極めて優れた汚泥の脱水効果を得ることができる。
本発明の有機性汚泥の脱水方法は、例えば、消化汚泥の
如く重炭酸イオンを多量に含む有機性汚泥に対しても極
めて効果的に汚泥の脱水を行うことができるので産業上
の利用価値が高い。
The present invention relates to a method for dewatering organic sludge, and provides an extremely excellent sludge dewatering effect by adding an alkaline earth metal salt and an organic polymer flocculant having a specific structure to the sludge in combination. Can be obtained.
The method for dewatering organic sludge of the present invention is extremely effective for dewatering sludge even for organic sludge containing a large amount of bicarbonate ions such as digested sludge. high.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭59−230700(JP,A) 特開 昭53−15277(JP,A) 特開 昭52−30777(JP,A) 特開 平3−118804(JP,A) 特開 昭59−39400(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 11/00 - 11/20 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-59-230700 (JP, A) JP-A-53-15277 (JP, A) JP-A-52-30777 (JP, A) JP-A-3-3 118804 (JP, A) JP-A-59-39400 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C02F 11/00-11/20

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 有機性汚泥に水溶性のアルカリ土類金属
塩とビニルアミン構造単位および/またはアミジン構造
単位が全繰り返し単位の35モル%以上であるカチオン
性有機高分子凝集剤を添加することを特徴とする汚泥の
脱水方法。
An alkaline earth metal salt soluble in organic sludge and a vinylamine structural unit and / or an amidine structure.
A method for dewatering sludge, comprising adding a cationic organic polymer coagulant whose unit is at least 35 mol% of all repeating units .
【請求項2】 アルカリ土類金属塩を添加した後、ビニ
ルアミン構造単位および/またはアミジン構造単位が全
繰り返し単位の35モル%以上であるカチオン性有機高
分子凝集剤を添加することを特徴とする請求項1に記載
の汚泥の脱水方法。
2. The method according to claim 1, wherein the alkaline earth metal salt is added.
All ruamine and / or amidine structural units
High cationic organic content of at least 35 mol% of the repeating units
The sludge dewatering method according to claim 1, wherein a molecular coagulant is added .
JP04608993A 1993-02-12 1993-02-12 Sludge dewatering method Expired - Lifetime JP3222247B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04608993A JP3222247B2 (en) 1993-02-12 1993-02-12 Sludge dewatering method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04608993A JP3222247B2 (en) 1993-02-12 1993-02-12 Sludge dewatering method

Publications (2)

Publication Number Publication Date
JPH06238300A JPH06238300A (en) 1994-08-30
JP3222247B2 true JP3222247B2 (en) 2001-10-22

Family

ID=12737267

Family Applications (1)

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

Country Link
JP (1) JP3222247B2 (en)

Cited By (1)

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JP3772287B2 (en) * 1997-05-16 2006-05-10 ハイモ株式会社 Sludge dewatering method
JP5117228B2 (en) * 2008-03-12 2013-01-16 ダイヤニトリックス株式会社 Sewage sludge treatment method
JP6186944B2 (en) * 2012-07-02 2017-08-30 三菱ケミカル株式会社 Papermaking wastewater treatment method
JP7427535B2 (en) * 2020-06-11 2024-02-05 オルガノ株式会社 Sludge dewatering method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102318287B1 (en) * 2019-09-02 2021-10-28 엘지전자 주식회사 A vacuum cleaner

Also Published As

Publication number Publication date
JPH06238300A (en) 1994-08-30

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