JPS6015670B2 - Plant medium adjustment method - Google Patents

Plant medium adjustment method

Info

Publication number
JPS6015670B2
JPS6015670B2 JP57200002A JP20000282A JPS6015670B2 JP S6015670 B2 JPS6015670 B2 JP S6015670B2 JP 57200002 A JP57200002 A JP 57200002A JP 20000282 A JP20000282 A JP 20000282A JP S6015670 B2 JPS6015670 B2 JP S6015670B2
Authority
JP
Japan
Prior art keywords
group
flocculant
polymer
flocculants
groups
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
JP57200002A
Other languages
Japanese (ja)
Other versions
JPS5891787A (en
Inventor
英俊 土田
徳 武田
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.)
Moriroku KK
Original Assignee
Moriroku 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 Moriroku KK filed Critical Moriroku KK
Priority to JP57200002A priority Critical patent/JPS6015670B2/en
Publication of JPS5891787A publication Critical patent/JPS5891787A/en
Publication of JPS6015670B2 publication Critical patent/JPS6015670B2/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

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)
  • Fertilizers (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Description

【発明の詳細な説明】 本発明は植物塔地調整方法に関するものである。[Detailed description of the invention] TECHNICAL FIELD The present invention relates to a method for adjusting plant soil.

本発明者は以前からホスホニトリル系化合物の研究を行
なってきたのであるが、該化合物のうちの或特定の構造
のものは分解性を有し、この分解性が、この化合物を工
業材料等として使用する場合には欠点となることが判明
したのであるが、この性質を逆に利用し、そしてまた、
別の研究すなわち凝集剤の研究を基にして本発明が完成
されたのである。
The present inventor has been researching phosphonitrile compounds for some time, and found that a certain structure of these compounds has degradability, and this decomposition property makes it possible to use this compound as an industrial material. It turned out to be a drawback when using it, but this property can be used to the contrary, and
The present invention was completed based on another study, that is, research on flocculants.

炭素原子を含む主鏡を有する有機高分子凝集剤は公知で
つて、現在盛んに使用されている。
Organic polymer flocculants having a primary mirror containing carbon atoms are well known and currently widely used.

本発明者は、上記の炭素系主鏡を有する公知高分子凝集
剤とは実質的に異なる燐−窒素系主鎖を有する高分子凝
集剤を見出した。このものはいわゆるホスホニトリル系
(PN系)重合体に属するものであって、すなわちこれ
は一般式(ここにR1、R2、R3、R4はカチオン含
有基、アニオン含有基、水素結合性の基、ハロゲンまた
は不活性有機基であり、ただしR1、R2、R3、R4
の少なくとも1つはカチオン含有基、アニオン含有基ま
たは水素結合性の基である)のユニットからなる重合体
である。
The present inventors have discovered a polymer flocculant having a phosphorus-nitrogen main chain that is substantially different from the known polymer flocculants having a carbon-based primary mirror. This product belongs to the so-called phosphonitrile-based (PN-based) polymer, and has the general formula (where R1, R2, R3, and R4 are cation-containing groups, anion-containing groups, hydrogen-bonding groups, halogen or inert organic group, provided that R1, R2, R3, R4
at least one of which is a cation-containing group, an anion-containing group, or a hydrogen-bonding group.

このホスホニトリル系重合体は、上記の公知有機凝集剤
とは単に主鎖原子の種類が異なるのみでなく、下記の如
き独特な大きい長所を有するものである。すなわち、こ
のPN系重合体凝集剤の独特な特長は、液中特に水中で
、もしくは湿潤士嬢中で徐徐に分解し、簡単な低分子量
化合物たとえば燐酸、燐酸アンモニウム、他の燐酸塩等
に変わり、これらの分解生成物が微生物の栄養源として
役立つことである。
This phosphonitrile polymer differs not only in the type of main chain atoms from the above-mentioned known organic flocculants, but also has the following unique advantages. In other words, the unique feature of this PN-based polymer flocculant is that it gradually decomposes in a liquid, especially water, or in a humidifier, and converts into simple low-molecular weight compounds such as phosphoric acid, ammonium phosphate, and other phosphates. , these decomposition products serve as a nutritional source for microorganisms.

ただし、このときの分解速度はかなり遅く、湿潤土壌中
での木材、枯草の分解(腐食)速度と同程度にすること
ができる。この分解は、主としてPN主鎖の加水分解に
よるものであるが、また、微生物によるPN主鎖の分解
すなわち生物化学的分解も起り得るのである。
However, the decomposition rate at this time is quite slow, and can be made comparable to the decomposition (corrosion) rate of wood and dried grass in wet soil. This decomposition is mainly due to hydrolysis of the PN main chain, but decomposition of the PN main chain by microorganisms, that is, biochemical decomposition can also occur.

また、化学的分解(加水分解)と生物化学的分解との両
者が起ることもある。このPN系高分子凝集剤のもう1
つの大きい長所は、その主鎖形成原子(PおよびN)の
相互反溌力により主鎖が液中で実質的に糠状に伸びてお
り、そのために、主鎖に付いている活性基が極めて効果
的に水中懸濁粒子または漆存物と接触することである。
Additionally, both chemical (hydrolysis) and biochemical degradation may occur. Another one of this PN polymer flocculant
The major advantage of the main chain is that the main chain essentially stretches like a bran in the liquid due to the mutual repulsion of the atoms forming the main chain (P and N), and as a result, the active groups attached to the main chain are extremely active. Effective contact with suspended particles in water or lacquer particles.

これに反し、従来の高分子凝集剤は一般に液中で大きく
曲がって存在、すなわち「糸まり」状であるために、こ
の「糸まり」の中央部に存在する活性基は有効に作用し
ない。参考のために、上記の2つの型の重合体の液中存
在状態を模式的に示す。したがって本発明は、前記一般
式を有するホスホニトリル系重合体を凝集剤として用い
て固液分離操作を行うことによって得られる凝集生成物
を、±壌または土壌改良剤として使用することを特徴と
する楯物培地調整方法に関するものである。
On the other hand, conventional polymer flocculants generally exist largely bent in the liquid, that is, in the form of a "string", and therefore the active groups present in the center of this "string" do not work effectively. For reference, the state of existence of the above two types of polymers in liquid is schematically shown. Therefore, the present invention is characterized in that a flocculation product obtained by performing a solid-liquid separation operation using a phosphonitrile polymer having the above general formula as a flocculant is used as a soil or soil conditioner. The present invention relates to a method for adjusting a shield culture medium.

凝集沈降法とか生物処理法にて生成したスラツジ、活性
汚泥等は、従来、焼却処理、埋立あるいは海洋投棄等を
行なっているのであるが、最近では、有用な資源として
有効利用が行なわれようとしている。
Sludge, activated sludge, etc. produced by coagulation-sedimentation methods or biological treatment methods have traditionally been incinerated, landfilled, or dumped into the ocean, but recently, efforts have been made to effectively utilize them as useful resources. There is.

すなわち、有機肥料とか±穣改良剤として使用するもの
である。凝集沈降法において、凝集沈降剤を使用して得
られた沈降物(スラッジ)とか、生物処理法により生成
した余剰活性汚泥等は、高含水率であるため、炉過、乾
燥等の処理を行なって取り扱い易い形態とするものであ
るが、炉過工程で脱水を促進するため、炉過促進剤を使
用している。
That is, it is used as an organic fertilizer or a grain improver. In the coagulation-sedimentation method, the sediment (sludge) obtained by using a coagulation-sedimentation agent and the surplus activated sludge produced by the biological treatment method have a high moisture content, so they must be treated by filtration, drying, etc. Although it is made into a form that is easy to handle, a furnace filtration accelerator is used to promote dehydration in the furnace filtration process.

これら使用した公知凝集剤とか炉過促進剤等は、分離せ
ずに残留して土壌汚染の原因となり、種々の障害をもた
らすことが認められている。これに対し、本発明に従っ
て凝集沈降剤とか炉過促進剤として前記ホスホニトリル
系重合体を使用することにより凝集沈降、炉過促進の効
果を発揮することは勿論のこと、或時点で分解して燐と
かアンモニウム化合物の如き肥料成分となる特長を有す
る。すなわち、この凝集剤は、凝集操作とか炉過操作の
実施後に凝縮物に吸着残留し、そして該凝縮物を保存中
とか土中に埋めたときに本凝集剤は徐々に分解し、土壌
の肥沃化に役立つ。これに対し、従来の炭素主鏡を有す
る合成有機高分子凝集剤は土壌中でも分解し難く、土壌
の肥沃化には役立たず、むしろ土壌内残留に伴う公害問
題が起ることもあり得るのである。このPN系高分子凝
集剤は、側鎖の種類を種々変えることにより種々の形式
の凝集剤になり得るものであって、すなわちカチオン凝
集剤、アニオン凝集剤、ノニオン凝集剤または両性凝集
剤になり得るものであるが、この点については、炭素主
鏡を有する公知の有機高分子凝集剤の場合と大体同じで
ある。
It has been recognized that the known flocculants, furnace filtration accelerators, etc. used remain without separation and cause soil contamination, causing various problems. In contrast, by using the above-mentioned phosphonitrile polymer as a flocculating sedimentation agent or a furnace accelerating agent according to the present invention, it not only exhibits the effects of coagulating sedimentation and accelerating furnace accelerating, but also decomposes at a certain point. It has the characteristics of being a fertilizer component like phosphorus and ammonium compounds. In other words, this flocculant remains adsorbed in the condensate after flocculation operation or furnace filtration operation, and when the condensate is stored or buried in the soil, the flocculant gradually decomposes and improves soil fertility. It is useful for In contrast, conventional synthetic organic polymer flocculants with carbon primary mirrors are difficult to decompose in the soil, are not useful for soil fertilization, and may even cause pollution problems if they remain in the soil. . This PN-based polymer flocculant can be made into various types of flocculants by changing the type of side chain, that is, it can be a cationic flocculant, an anionic flocculant, a nonionic flocculant, or an amphoteric flocculant. However, in this respect, it is almost the same as in the case of known organic polymer flocculants having a carbon primary mirror.

たとえば、側鎖としてアミン基、第4アンモニウム基、
イミン基等を有するPN系重合体はカチオン凝集剤であ
り、カルボキシル基、カルボキシレート基等を有するP
N系重合体はァニオン凝集剤であり、水酸基、アクリル
アミド基、メタクリルアミド基等を有するPN系重合体
は/ニオン凝集剤であり、アミノ酸基等を有するPN系
重合体は両性凝集剤である。
For example, as a side chain, an amine group, a quaternary ammonium group,
PN polymers having imine groups, etc. are cationic flocculants, and PN polymers having carboxyl groups, carboxylate groups, etc.
N-type polymers are anionic flocculants, PN-type polymers having hydroxyl groups, acrylamide groups, methacrylamide groups, etc. are /ionic flocculants, and PN-type polymers having amino acid groups, etc. are amphoteric flocculants.

これらのPN系重合体は、たとえば次式で表わされる。These PN-based polymers are represented by the following formula, for example.

上式においてRは有機基、Rc■はカチオン含有基、R
^eはアニオン含有基を表わす。nは、炭素系主鏡を有
する公知高分子凝集剤の場合と同機に、かなり大きい数
である。前記公知高分子凝集剤の場合には一般にnの値
の代りに分子量が文2献に記載されることが多いので、
本発明においても分子量で示せば、このPN系重合体の
分子量は一般に10万以上、好ましくは30万一300
万またはそれ以上である(後記参考例参照)。なお、上
記の式では、記載の簡略化のために各イオンの相手3方
イオンの記載は省略してある。本来の活性基であるカチ
オン基、アニオン基、/ニオン基等が単独に結合した構
造を有する凝集剤に加えて、カチオン基またはアニオン
基とノニオン基とを併有する凝集剤、およびカチオン基
ま3たはアニオン基と疎水性結合基または水素結合基と
を併有する凝集剤の如き、複合性能を持つ凝集剤も容易
に得られるが、このことも本発明の大きな特徴の1つで
ある。
In the above formula, R is an organic group, Rc■ is a cation-containing group, R
^e represents an anion-containing group. n is a considerably large number, as in the case of a known polymer flocculant having a carbon-based primary mirror. In the case of the above-mentioned known polymer flocculants, the molecular weight is generally described in literature 2 instead of the value of n, so
In the present invention, the molecular weight of the PN polymer is generally 100,000 or more, preferably 300,000 to 300,000.
10,000 or more (see reference examples below). Note that in the above formula, the description of the three-way partner ion of each ion is omitted to simplify the description. In addition to flocculants having a structure in which cationic groups, anionic groups, /ionic groups, etc., which are original active groups, are individually bonded, flocculants having a combination of cationic groups or anionic groups and nonionic groups, and cationic groups or 3 It is also possible to easily obtain a flocculant having multiple properties, such as a flocculant having both an anionic group and a hydrophobic bonding group or a hydrogen bonding group, and this is also one of the major features of the present invention.

本発明において使用できるPN系高分子凝集剤は多数あ
るが、そのうちの若干のものを以下に示す。
There are many PN-based polymer flocculants that can be used in the present invention, some of which are shown below.

カチオン系: fNP(OCH2CH2N由・Me3・Xe)2 ナn
fNP(OCH2CH2N・Me2)2チntNP(O
CH2CH2NH・Me)2ナn→NP(OCH2CH
2NH2)2チntNP(NHCH2C比N・Me3N
e)2ナnfNP(NHCH2C比N・Me2)2ナn
fNP(NHCH2C比NH・Me)2ナnfNP(N
HCH2C比NH2)2チn→NP(NH2)2チn fNP(NHCH3)2ナn および上記のユニットと、別のユニットたとえばtNP
fOR)2ナまたはNP(OROH)2との共重合体;
上記ユニットと、さらに別のユニットたとえば十NPキ
CI2)2ナとの共重合体または三元共重合体。
Cationic system: fNP(OCH2CH2N/Me3/Xe)2nan
fNP(OCH2CH2N・Me2)2 ntNP(O
CH2CH2NH・Me)2nan→NP(OCH2CH
2NH2) 2chintNP (NHCH2C ratio N・Me3N
e) 2nnfNP (NHCH2C ratio N・Me2) 2nn
fNP (NHCH2C ratio NH・Me) 2nnfNP (N
HCH2C ratio NH2)2chin → NP(NH2)2chin fNP(NHCH3)2nan and the above unit and another unit such as tNP
copolymer with fOR)2 or NP(OROH)2;
A copolymer or terpolymer of the above unit and another unit such as 10 NP x CI2) 2).

アニオン系: fNP(OCH2000‐)2ナn てNP(OC6ACOO‐)2チn tNP(SCH2COO‐)2チn fNP(OC6伍S03‐)2ナn tNP〔CH(COO‐)2〕2チn fNP〔OC3日(COO‐)2〕チn および上記ユニットと他のユニットとの共重合体。Anion type: fNP(OCH2000-)2nan teNP(OC6ACOO-)2chin tNP(SCH2COO-)2chin fNP(OC655S03-)2n tNP[CH(COO-)2]2chin fNP [OC3 days (COO-)2] Chin and copolymers of the above units and other units.

/ニオン系: てNPf○(CH2C比○ナ,H〕2ナnfNPt○C
H2COO(CH2CH20ナ,H〕2 チnfNPf
NH(CH2C&0チIH〕2 ナnfNPfNHCH
2COO(CH2CQOナ,H〕2 ナn* および上
記のユニットと他のユニットとの共重合体。
/Nion system: NPf○ (CH2C ratio ○na, H) 2nnfNPt○C
H2COO(CH2CH20na,H]2 chinnfNPf
NH (CH2C & 0chi IH) 2 nfNPfNHCH
2COO(CH2CQOna,H)2nan* and copolymers of the above units and other units.

両性系: fNP(NHCH2C00‐)2チn fNP(NHCH2C4COO‐)2ナn→NP(N(
CH3)C比COO‐)2ナnfNP〔NHCH(CO
O‐)・CH2CH2COO‐〕2チnfNP(NHC
6鶴S03‐)2ナnおよび上記のユニットと他のユニ
ットとの共重合体。
Amphipathic system: fNP(NHCH2C00-)2n fNP(NHCH2C4COO-)2n→NP(N(
CH3)C ratio COO-)2nnfNP [NHCH(CO
O-)・CH2CH2COO-]2chinnfNP(NHC
6 Tsuru S03-) 2nan and a copolymer of the above unit and other units.

本発明に使用されるPN系重合体は、ホスホニトリルジ
クロライド重合体キPNC12ナnの塩素原子またはそ
の一部をアニオン基、ノニオン基、カチオン基または両
性基で置換するか、またはこれらの基と疎水性結合基ま
たは水素結合基とにて置換したものである。
The PN polymer used in the present invention is a phosphonitrile dichloride polymer in which the chlorine atom or a part thereof is substituted with an anionic group, a nonionic group, a cationic group, or an amphoteric group, or is substituted with these groups. Substituted with a hydrophobic bonding group or a hydrogen bonding group.

本重合体の合成法としては、環状トリホスホニトリルヘ
キサクロラィド(PNC12)3を閉環重合して直鎖状
ホスホニトリルジクロライド重合体fPNC12ナnを
作り、これを所望基で置換するか、または環状トリホス
ホニトリルヘキサクロラィドを予じめ所望基で置換し、
次いでこれを開環重合して所望重合体を得る方法がある
The method for synthesizing this polymer includes ring-closing polymerization of cyclic triphosphonitrile hexachloride (PNC12)3 to produce a linear phosphonitrile dichloride polymer fPNC12nan, which is then substituted with a desired group, or Cyclic triphosphonitrile hexachloride is substituted with a desired group in advance,
There is a method in which this is then subjected to ring-opening polymerization to obtain the desired polymer.

いずれにしても、出発原料は環状トリホスホニトリルヘ
キサクロラィドであるが、このものは通常は五塩化燐と
塩化アンモニウムとを溶媒中で反応させ、次いで精製す
ることにより得られる。
In any case, the starting material is cyclic triphosphonitrile hexachloride, which is usually obtained by reacting phosphorus pentachloride and ammonium chloride in a solvent, followed by purification.

また、環状テトラホスホニトリルオクタクロラィド(P
NC12)4を出発原料として単独に、または環状トリ
ホスホニトリルヘキサクロライドーこ混合して使用する
ことも多い。なお、其他の多くの合成法も提案されてい
る。
In addition, cyclic tetraphosphonitrile octachloride (P
NC12)4 is often used as a starting material alone or in combination with cyclic triphosphonitrile hexachloride. Note that many other synthesis methods have also been proposed.

前記の環状トリホスホニトリルヘキサクロラィドは、2
50−350qoの温度に加熱すると関環重合する。そ
の1例をあげると、この環状トリホスホニトリルヘキサ
ク。ラィドをパィレックスガラス管に入れ、真空にした
後アルゴンあるいは窒素ガスを導入して封管し、加熱す
ることにより重合させて、分子量の大きいホスホニトリ
ルジクロライド重合体を得るのである。得られた重合体
をテトラヒドロフラン(THF)等の溶剤で分離精製し
て、可溶性部分より得られた重合体が、架橋のない所望
重合体である。この重合体の塩素原子は非常に大きい反
応性を有する。ェステル化反応、アミノ化反応、フリー
デルークラフッ反応等は容易に行なわれ、これらの反応
を利用して該重合体にアニオン基、カチオン基またはノ
ニオン基を有する化合物、もしくはカチオン基とアニオ
ン基とを有する化合物、および/または其他の基を有す
る化合物を作用させると、所望置換基を有するPN系重
合体が得られる。前許PN系重合体を用いる凝集操作や
炉過操作を実施する場合には、慣用装置が使用でき、特
殊な器具は一般に不必要である。
The cyclic triphosphonitrile hexachloride is 2
When heated to a temperature of 50-350 qo, ring polymerization occurs. One example is this cyclic triphosphonitrile hexac. The lyde is placed in a Pyrex glass tube, the tube is evacuated, argon or nitrogen gas is introduced, the tube is sealed, and the tube is polymerized by heating to obtain a phosphonitrile dichloride polymer with a large molecular weight. The obtained polymer is separated and purified using a solvent such as tetrahydrofuran (THF), and the polymer obtained from the soluble portion is the desired polymer without crosslinking. The chlorine atoms in this polymer have very high reactivity. Esterization reactions, amination reactions, Friedel-Klaff reactions, etc. are easily carried out, and these reactions can be used to add compounds having an anionic group, a cationic group, or a nonionic group, or a combination of a cationic group and an anionic group to the polymer. A PN-based polymer having a desired substituent group can be obtained by reacting with a compound having this group and/or a compound having another group. When carrying out flocculation operations and filtration operations using the aforementioned PN-based polymers, conventional equipment can be used and special equipment is generally unnecessary.

本凝集剤は希薄水溶液(または水中懸濁液)の形で用い
るのが有利であり、たとえば0.1−1%水溶液の形で
使用できる。ここで注意すべきことは、本凝集剤は使用
直前に溶解すべきであって、水溶液の状態で保存するこ
とは避けなければならない。本凝集剤の使用量は懸濁物
の種類、濃度、液のpH、温度其他の条件により種々変
わるが、簡単な予備試験により容易に決定できる。後記
実施例の記載もまた、個個の場合における使用量決定の
ための1つの目安になり得るであろう。この凝集剤は他
種凝集剤と一緒に使用してもよい。前許?N系高分子重
合体は、公知の有機高分子凝集剤の場合と同様に、その
種類に応じて種々の分野において有利に使用できるもの
であり、しかも前記の如き独特な効果を奏する。
The present flocculants are advantageously used in the form of dilute aqueous solutions (or suspensions in water), for example in the form of 0.1-1% aqueous solutions. It should be noted here that the present flocculant should be dissolved immediately before use, and storage in the form of an aqueous solution should be avoided. The amount of the flocculant to be used varies depending on the type of suspension, concentration, pH of the liquid, temperature and other conditions, but can be easily determined by a simple preliminary test. The description of the examples below may also serve as a guide for determining the usage amount in individual cases. This flocculant may be used together with other flocculants. Forgive me? Like the known organic polymer flocculants, N-based polymers can be advantageously used in various fields depending on their type, and they also exhibit the unique effects described above.

たとえばカチオン凝集剤は有機コロイド懸濁物、イオン
性有機化合物の凝集、スラッジの脱水、炉過促進等のた
めに使用でき、たとえば都市の下水処理、床処理、抄紙
工場排水処理、パルプ工場排水処理、アルキルベンゼン
スルホン酸ナトリウムの除去、染料および染色工場排水
処理等における凝集促進、炉過促進のために本凝集剤が
有利に使用できる。なお、本凝集剤の前記特性にかんが
み、これが活性汚泥法等において非常に有利に使用でき
るものであることは勿論である。ァニオン凝集剤は、正
電荷を有する重金属酸化物の沈降促進、蛋白質其他の懸
濁物質の凝集等のために使用でき、たとえばアルミナ工
場における赤泥の分離、苛性ソーダ製造時の不純物の除
去、魚肉、畜肉の水さらし後の排水からの可食性組蛋白
質の回収、上水道水の原水の処理、金属イオンの分離・
回収等のために使用できる。
For example, cationic flocculants can be used for organic colloidal suspensions, flocculation of ionic organic compounds, sludge dewatering, furnace filtration acceleration, etc., such as urban sewage treatment, floor treatment, paper mill effluent treatment, pulp mill effluent treatment. The present flocculant can be advantageously used to remove sodium alkylbenzenesulfonate, promote flocculation in dye and dye factory wastewater treatment, and accelerate furnace filtration. In view of the above characteristics of the present flocculant, it goes without saying that it can be used very advantageously in activated sludge methods and the like. Anion flocculants can be used to promote the precipitation of positively charged heavy metal oxides, to flocculate proteins and other suspended substances, and for example, to separate red mud in alumina factories, to remove impurities during caustic soda production, to fish meat, Recovery of edible protein from wastewater after soaking livestock meat, treatment of raw tap water, separation of metal ions,
It can be used for collection, etc.

ノニオン凝集剤は比較的粗大な粒子懸濁物の凝集等のた
めに使用でき、たとえば粉状鉱物買物質の凝集、製鉄所
の高炉ガス洗浄排水の浄化、石綿スレート工場の排水処
理、クレーの沈降促進、燐酸製造時の不純物の凝集、亜
鉛製錬時の不純物の除去、マグネシア製造時の水酸化マ
グネシウムの沈降促進、苛性ソーダ製造時の不純物の除
去、石油化学工場における油分の分離および懸濁物質の
除去、パルプ工場の排水処理、抄紙工場の排水処理、ヱ
マルジョン塗料製造工場の排水処理、土木工事現場にお
ける懸濁物凝集等のために使用できる。
Nonionic flocculants can be used to flocculate relatively coarse particle suspensions, such as flocculation of powdered mineral substances, purification of blast furnace gas cleaning wastewater in steel plants, wastewater treatment of asbestos slate factories, and sedimentation of clay. Accumulation of impurities during phosphoric acid production, removal of impurities during zinc smelting, acceleration of precipitation of magnesium hydroxide during magnesia production, removal of impurities during caustic soda production, separation of oil and removal of suspended solids in petrochemical plants. It can be used for removal, wastewater treatment of pulp mills, wastewater treatment of paper mills, wastewater treatment of emulsion paint manufacturing plants, suspended matter aggregation at civil engineering construction sites, etc.

両性凝集剤は、公知の水溶性蛋白質型凝集剤(たとえば
ゼラチン)の場合と同様な使用分野において使用できる
Amphoteric flocculants can be used in the same fields of use as known water-soluble protein type flocculants (eg gelatin).

カチオン活性基、ノニオン活性基、アニオン活性基、両
性活性基に加えて、疎水性結合基または水素結合基を併
せもつ凝集剤は、その効果を増強すると共に、使用分野
を拡大し得る。
A flocculant having a hydrophobic bonding group or a hydrogen bonding group in addition to a cationic active group, a nonionic active group, an anionic active group, an amphoteric active group can enhance its effectiveness and expand the field of use.

上記の如くして得られた凝集生成物は一般にかなりの水
分を含んでいるから、これに脱水操作を行うのがよい。
Since the agglomerated product obtained as described above generally contains a considerable amount of water, it is preferable to subject it to a dehydration operation.

脱水は常法に従って実施でき、たとえば遠心分離機で脱
水した後に熱風乾燥を行うことができる。乾燥粉末の形
にすると保管、輸送に便利であり、かつ現場施用も行い
易い。また、前記凝集生成物の脱水、乾燥の実施前、実
施中または実施後に、他の物質たとえば肥料、土壌、有
機廃物(たとえばおがくず)、農薬等を混合することも
できる。
Dehydration can be carried out according to a conventional method, for example, after dehydration with a centrifuge, hot air drying can be carried out. When it is in the form of a dry powder, it is convenient to store and transport, and it is also easy to apply on-site. It is also possible to mix other substances such as fertilizers, soil, organic waste (eg sawdust), pesticides, etc. before, during or after the dehydration and drying of the agglomerated product.

現場施用は常法に従って、たとえば肥料施用や客士施用
等の場合と同様な施用方法に従って行うことができる。
Field application can be carried out according to conventional methods, for example according to the same application methods as in the case of fertilizer application, customer application, etc.

有害性の重金属とか無機または有機化合物の混在の場合
には使用しないことは勿論である。参考例 1 ポリホスホニトリルジクロライドてPNC12チnとメ
チルアミンとの反応により得られるポリ〕ビス(メチル
イミ/)ホスフアゼン〕は、それ自体公知の重合体化合
物であり、これは次式で表わすことができる。
Of course, it should not be used if it contains harmful heavy metals or inorganic or organic compounds. Reference Example 1 Poly[bis(methylim/)phosphazene] obtained by the reaction of polyphosphonitrile dichloride PNC12tin with methylamine is a known polymer compound, and can be represented by the following formula. .

これは水中では少し不安定で、水中では約30日以内に
分解する。このィミノ化合物風(分子量約550000
)を用いて次の凝集実験を行なった。
It is somewhat unstable in water and decomposes within about 30 days. This imino compound style (molecular weight approximately 550,000
) was used to conduct the following aggregation experiment.

微粉状カオリンを水中に懸濁し、1晩放置し、沈降しな
い部分を採取し、上記凝集剤化合物のを1%水溶液の形
で添加し、充分に瀦拝、混合した。
Finely powdered kaolin was suspended in water, left to stand overnight, the part that did not settle was collected, and the flocculant compound described above was added in the form of a 1% aqueous solution, and thoroughly mixed.

2ぴ分後に上燈液を調べ、「実質的に透明な上燈液(無
添加の場合を濁度100%とした場合の比濁度10%以
下の液)を得るのに必要な凝集剤の最低所要量」を調べ
た。
After 2 minutes, check the top lighting solution and find out the flocculant necessary to obtain a substantially transparent top lighting solution (liquid with a nephelometric turbidity of 10% or less when the turbidity is 100% without additives). The minimum required amount of

この場合の最低所要量は5.1脚であった。一方、対照
試料である硫酸アルミニウムの場合には、その最低所要
量は189血であり、市販のカチオン型有機高分子凝集
剤の最低所要量は13奴であった。参考例 2 てPNC12チnにアルコールを反応させて完全置換ェ
ステル体を得る方法自体は公3印である。
The minimum requirement in this case was 5.1 legs. On the other hand, in the case of aluminum sulfate, which is a control sample, the minimum required amount was 189 blood, and the minimum required amount of a commercially available cation type organic polymer flocculant was 13 blood. Reference Example 2 The method itself of reacting PNC12tin with alcohol to obtain a fully substituted ester is a public 3rd seal.

1価アルコールとして塩化コリンを用いて、この公知反
応により次式のェステル体‘B}を製造した分子量は約
450000。
Using choline chloride as the monohydric alcohol, an ester body 'B} of the following formula was produced by this known reaction.The molecular weight was about 450,000.

このェステル体‘B似第4級アンモニウム基を含んでい
るために、カチオン凝集剤として使用できるものであっ
た。有機質および無機質の種々の浮遊物を含んでいる下
水を1時間放置し、沈降しない部分を採取して沈降管に
入れ、凝集剤を添加した。
Since it contained a quaternary ammonium group similar to this ester 'B, it could be used as a cation flocculant. The sewage containing various suspended organic and inorganic substances was allowed to stand for one hour, and the portion that did not settle was collected and placed in a sedimentation tube, and a flocculant was added thereto.

凝集剤の量を種々変えて、「5分後に清澄液を得るのに
必要な凝集剤の最低所要量」を調べた。この実験の結果
は次の通りであった。* 市販品X・・・ポリアクリル
アミドのカチオン化変性物である凝集剤。
The amount of flocculant was varied and the "minimum amount of flocculant required to obtain a clear liquid after 5 minutes" was investigated. The results of this experiment were as follows. *Commercial product X: A flocculant that is a cationized modified product of polyacrylamide.

参考例 3 ポリホスホニトリルジクロライドfPNC12チnとO
H基含有化合物との反応であるェステル化反応自体は公
知である。
Reference example 3 Polyphosphonitrile dichloride fPNC12tin and O
The esterification reaction itself, which is a reaction with an H group-containing compound, is known.

OH基含有化合物としてグリコール酸HOCH2COO
日のナトリウム塩を用いて上記公知反応を行って次式の
カルボン酸ナトリウム基含有化合物{C}を製造した。
Glycolic acid HOCH2COO as an OH group-containing compound
A sodium carboxylate group-containing compound {C} of the following formula was prepared by carrying out the above-mentioned known reaction using the sodium salt of 100%.

化合物【C}の分子量は340000であった。この化
合物‘qをアニオン系凝集剤として用いて凝集実験を行
なった。酸化鉄の5%水中懸濁液を作成して沈降管に入
れ、凝集剤を0.1%水溶液の形で10脚添加し5時間
後の沈降物容積を測定した。
The molecular weight of compound [C} was 340,000. A flocculation experiment was conducted using this compound 'q as an anionic flocculant. A 5% suspension of iron oxide in water was prepared and placed in a sedimentation tube, 10 flocculants were added in the form of a 0.1% aqueous solution, and the volume of the sediment after 5 hours was measured.

この実験の結果を次表に示す。参考例 4 環状ホスホニトリルクロラィド(ヘキサクロラィドとオ
クタクロラィドとの混合物(PNC12)3.4)を2
50−30ぴ0に加熱して開環重合させ、鎖状重合体キ
PNC12ナnを得た。
The results of this experiment are shown in the table below. Reference Example 4 Cyclic phosphonitrile chloride (mixture of hexachloride and octachloride (PNC12) 3.4)
Ring-opening polymerization was carried out by heating to 50-30 mm to obtain a chain polymer (PNC12).

上記鎖状重合体にグリコールおよびエチレンオキサイド
を作用させ、次式の重合体化合物を得た。
The above chain polymer was treated with glycol and ethylene oxide to obtain a polymer compound of the following formula.

この重合体化合物■の分子量は約2500000であつ
た。
The molecular weight of this polymer compound (1) was about 2,500,000.

上記化合物血をノニオン系凝集剤として用いて凝集実験
を行なった。
A flocculation experiment was conducted using the above compound blood as a nonionic flocculant.

この化合物血を水で希釈して0.1%水溶液として用い
た。クレー排水(固型分0.80%)の清澄化処理を行
なった。
This compound blood was diluted with water and used as a 0.1% aqueous solution. Clarification treatment of clay wastewater (solid content 0.80%) was carried out.

水温は約20℃、軸は約3.0一4.0であった。容量
100ccの比色管を用いて清澄水の光線透過率を調べ
た。実験結果を次表に示す。実施例 1 下水処理場の消化汚泥(軸=7.5:蒸発残澄=5.9
0%;懸濁園型物=5.40%:懸濁団型物の強熱銭澄
=62.5%)に各種凝集剤を添加し、ゆるやかに蝿拝
し、汚泥凝集により分離した自由水を除去し、プレスバ
キューム炉過脱水菱直において脱水処理した。
The water temperature was about 20°C and the axis was about 3.0-4.0. The light transmittance of clear water was examined using a colorimetric tube with a capacity of 100 cc. The experimental results are shown in the table below. Example 1 Digested sludge from a sewage treatment plant (axis = 7.5: evaporation residue = 5.9
Various flocculants were added to suspension aggregate type 0%; suspended aggregate type material = 5.40%; various flocculants were added to suspension aggregate type ignited liquid = 62.5%), and the mixture was gently stirred and separated by sludge flocculation. Water was removed and dehydration was carried out in a press vacuum furnace.

本実験に使用された凝集剤および実験結果を次表に示す
The flocculant used in this experiment and the experimental results are shown in the table below.

率20%の乾燥物とした。It was made into a dry product with a ratio of 20%.

他に、ポリアクリルァミドのカチオン化変性物(第1表
参照)を使用して同様に得られたものを対照試料として
栽培試験を行なった。各々を細土壌に対し20%配合し
、2ケ月間放置した後整地してハクサイを播種し、その
生育状況を観察した。播種7日後の発芽数では本発明の
場合には95%に達し、対照は83%であり、30日後
の生体重量は本発明の場合が87夕であったに対し、対
照は62夕であった。
In addition, a cultivation test was conducted using a control sample obtained in the same manner using a cationized modified polyacrylamide (see Table 1). 20% of each was mixed into fine soil, left for 2 months, the ground was leveled, Chinese cabbage was sown, and the growth status was observed. The number of germination after 7 days of sowing reached 95% in the case of the present invention and 83% in the control, and the live weight after 30 days was 87 in the case of the present invention and 62 in the control. Ta.

また別に、セロリを定植して収穫時の生体重量を測定し
たが、本発明の場合は230夕であり、対照は185夕
であった。実施例 2 陸砂利洗浄作業のときの排水を2畑時間静遣した。
Separately, celery was planted and the live weight at the time of harvest was measured, and in the case of the present invention it was 230 days, and in the control it was 185 days. Example 2 Drainage from land gravel cleaning work was allowed to stand for two hours in the field.

沈降しない部分を含む上液を、参考例3のアニオン凝集
剤に)および公知のポリアクリルアミド系アニオン凝集
剤とで別々に処理した。各凝集剤凝集剤{B)を用いる
前記凝集操作により得られた脱水ケーキ(第1表参照)
を熱風乾燥により含水の使用量はそれぞれIQ蚊であっ
たが、本発明の凝集剤を用いた場合の浮遊物凝集沈澱速
度は、対照凝集剤を使用した場合の該速度の約3倍であ
った。各々の場合において、得られた沈澱と、最初の静
層により得られた沈澱とを混合し乾燥した。
The supernatant containing the non-sedimented portion was treated separately with the anionic flocculant of Reference Example 3) and a known polyacrylamide-based anionic flocculant. Dehydrated cake obtained by the above flocculation operation using each flocculant flocculant {B) (see Table 1)
The amount of water used by hot air drying was IQ mosquitoes, but the flocculant flocculation rate when using the flocculant of the present invention was about three times the rate when using the control flocculant. Ta. In each case, the precipitate obtained was mixed with the precipitate obtained by the first static layer and dried.

これを±壌として使用した。育苗箱に各々の土壌を充填
し栽培床とした。
This was used as a material. Seedling boxes were filled with each type of soil and used as cultivation beds.

これに催芽した種籾を播種した後、所定の育苗操作を行
ない、25日後の結果を調べた。本発明に従って操作を
行なった場合には平均草丈16.7伽、平均重量2.5
夕であったが、これに対し対照では平均草丈12.5弧
、平均重量1.7のこすぎなかった。実施例 3亜硫酸
パルプ蒸簾廃液に対して、参考例2記載のカチオン凝集
剤曲を、廃液重量を基準として5%添加して、50qo
に1時間加熱しながら縄拝した。
After sowing the germinated rice seeds thereon, prescribed seedling-raising operations were performed, and the results were examined 25 days later. When operated according to the invention, the average plant height was 16.7, and the average weight was 2.5.
It was evening, but in contrast, in the control, the average plant height was 12.5 arcs, and the average weight was 1.7 arcs. Example 3 5% of the cationic flocculant described in Reference Example 2 was added to the sulfite pulp distillation waste liquid, based on the weight of the waste liquid, to give 50 qo.
I worshiped the rope while heating it for an hour.

次いで静遣し、生成した沈澱を炉別後に遠心脱水および
熱風乾燥した。別に、同じ廃液の直接乾燥物を用意した
(対照試料)。これらの乾燥物を土壌に混合して栽培試
験を行なった。砂壌土に上記廃液乾燥物を20%の割合
で配合し、湿潤状態で2ケ月間放置後栽培に供した。ワ
グネルポットに充填し、各々にカリ月巴料を加えた後、
コカプを播種して、その生育状況を調べた。40日後の
調査結果は、本発明の場合には根重65夕、全重量14
3夕であり、一方、対照では根重47夕、全軍量104
夕であった。
The mixture was then allowed to stand still, and the resulting precipitate was separated in a furnace, centrifugally dehydrated, and dried with hot air. Separately, a directly dried product of the same waste liquid was prepared (control sample). Cultivation tests were conducted by mixing these dried substances into soil. The dried waste liquid was mixed with sandy loam at a ratio of 20%, and the soil was left in a moist state for 2 months before cultivation. After filling the Wagner pots and adding potash to each one,
Kokapu was sown and its growth status was investigated. The results of the investigation after 40 days showed that in the case of the present invention, the root weight was 65 yen, and the total weight was 14 yen.
On the other hand, in contrast, the net weight was 47 nights, and the total army was 104 days.
It was evening.

Claims (1)

【特許請求の範囲】 1 一般式 ▲数式、化学式、表等があります▼ (ここにR^1、R^2、R^3、R^4はカチオン含
有基、アニオン含有基、水素結合性の基、ハロゲンまた
は不活性有機基であり、ただしR^1、R^2、R^3
、R^4の少なくとも1つはカチオン含有基、アニオン
含有基または水性結合性の基である)のユニツトからな
る重合体を凝集剤として用いて固液分離操作を行うこと
によって得られる凝集生成物を、土壌または土壌改良剤
として使用することを特徴とする植物培地調整方法。
[Claims] 1 General formula▲ Numerical formula, chemical formula, table, etc.▼ (Here, R^1, R^2, R^3, R^4 are cation-containing groups, anion-containing groups, hydrogen bonding groups group, halogen or inert organic group, with the proviso that R^1, R^2, R^3
, at least one of R^4 is a cation-containing group, an anion-containing group, or an aqueous-binding group) is an agglomerated product obtained by performing a solid-liquid separation operation using a polymer as a flocculant. A method for adjusting a plant medium, which comprises using the following as soil or a soil conditioner.
JP57200002A 1982-11-15 1982-11-15 Plant medium adjustment method Expired JPS6015670B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57200002A JPS6015670B2 (en) 1982-11-15 1982-11-15 Plant medium adjustment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57200002A JPS6015670B2 (en) 1982-11-15 1982-11-15 Plant medium adjustment method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP53108839A Division JPS5814805B2 (en) 1978-09-05 1978-09-05 Solid-liquid separation method

Publications (2)

Publication Number Publication Date
JPS5891787A JPS5891787A (en) 1983-05-31
JPS6015670B2 true JPS6015670B2 (en) 1985-04-20

Family

ID=16417157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57200002A Expired JPS6015670B2 (en) 1982-11-15 1982-11-15 Plant medium adjustment method

Country Status (1)

Country Link
JP (1) JPS6015670B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2003240532A1 (en) * 2002-06-03 2003-12-19 Parallel Solutions, Inc. Sulfonated polyphosphazenes, uses thereof, and methods for preparing same
US20060193820A1 (en) * 2005-02-18 2006-08-31 Andrianov Alexander K Immunostimulating polyphosphazene compounds
EP1874729B1 (en) * 2005-04-15 2011-11-16 Parallel Solutions, Inc. Biodegradable polyphosphazenes containing pyrrolidone side groups

Also Published As

Publication number Publication date
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