Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0510386B2 - - Google Patents
[go: Go Back, main page]

JPH0510386B2 - - Google Patents

Info

Publication number
JPH0510386B2
JPH0510386B2 JP6582584A JP6582584A JPH0510386B2 JP H0510386 B2 JPH0510386 B2 JP H0510386B2 JP 6582584 A JP6582584 A JP 6582584A JP 6582584 A JP6582584 A JP 6582584A JP H0510386 B2 JPH0510386 B2 JP H0510386B2
Authority
JP
Japan
Prior art keywords
polymer
acrylamide
water
weight
soluble vinyl
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
JP6582584A
Other languages
Japanese (ja)
Other versions
JPS60210657A (en
Inventor
Kozo Hayashi
Yoshiaki Ito
Atsuhiko Nitsuta
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP6582584A priority Critical patent/JPS60210657A/en
Publication of JPS60210657A publication Critical patent/JPS60210657A/en
Publication of JPH0510386B2 publication Critical patent/JPH0510386B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、熱分解に対して安定化されたアクリ
ルアミド系重合体の製造方法に関する。 アクリルアミド系重合体は、凝集剤、製紙用薬
剤、土質改良剤、増粘剤、石油回収剤等の多くの
産業分野に於いて広く利用されている。この様
に、多岐にわたる用途面でアクリルアミド系重合
体は期待に応える成果を挙げているのであるが、
しかしこの重合体には重大な欠点があつて、その
本来有する能力を充分に発揮しえない場合があ
る。すなわち、この欠点とは、この重合体は他の
重合体に比較して熱分解を起し易いということで
ある。例えば、アクリルアミド系重合体の水溶液
を室温下に放置する場合にも水溶液粘度値は短時
間しか維持されないという現象がしばしば認めら
れ、特に比較的高温においては、この性能劣化の
傾向は加速されて、甚だしい場合には目的とする
用途への使用が不可能となる場合もある。特に、
原油の強制回収剤として水溶液の形で地下に圧入
する場合には、地下の油層温度は約40〜100℃で
あり、しかも圧入されたアクリルアミド系重合体
水溶液は注入井から生産井に至るまで地下の油層
に数カ月〜数10カ月に及ぶ長期にわたつて存在す
るために、その期間中のアクリルアミド系重合体
の品質面の保証がユーザーから要求される。従つ
て、この温度領域での重合体品質の経時劣化をで
きるだけ小さくすることがアクリルアミド系重合
体メーカーに課せられた問題である。従来、この
ような問題を解決するために、劣化防止剤の検討
が行なわれてきた。例えば、特開昭54−83048に
は2−メルカプトベンゾイミダゾール及びその誘
導体、特公昭49−27662にはチオ尿素及びその誘
導体、特開昭57−159839にはメトキシフエノール
等が有効であると記載されている。また、米国特
許第3357356号及び同第3493539号明細書には紫外
線吸収剤として2−(0−アミドフエニル)−2,
1,3−ベンゾトリアゾールや2−(2−ヒドロ
キシフエニル)ベンゾトリアゾールが有効である
と記載されている。 しかしながら、このような劣化防止剤の添加な
しで、重合体自体に熱安定性を付与し得ることが
望まれる。本発明の目的は、熱時安定性の良好な
水溶性の高分子量アクリルアミド系重合体の製造
方法の提供にある。 本発明によつて、次の安定化されたアクリルア
ミド系重合体の製造方法が提供される。 アクリルアミド系重合体に、少なくともそれの
0.5重量%の水溶性ビニルモノマーを添加するこ
とを特徴とする安定化されたアクリルアミド系重
合体の製造方法。 本発明方法により処理されるアクリルアミド重
合は、アクリルアミド、メタアクリルアミド若し
くはこれらの混合物、またはこれらの1種と他の
共重合可能なビニル系単量体、例えば(メタ)ア
クリル酸又はその塩、(メタ)アクリロニトリル、
2−アクリルアミド−2−メチルプロパンスルホ
ン酸またはその塩、(メタ)アクリル酸ジメチル
アミノエチル、アクリル酸低級アルキルエステ
ル、ビニルピリジン、ジアルキルアミノアルキル
(メタ)アクリレートの酸性塩もしくは4級塩又
はジアルキルアミノアルキル(メタ)アクリルア
ミドの酸性塩もしくは4級塩などの50重量%以下
との混合物を周知の方法で重合若しくは共重合し
て得られる優位量の(メタ)アクリルアミド部分
を含む重合体、共重合体若しくはこれらの混合物
である。また、例えば(メタ)アクリルアミド単
独重合体などのアミド基の一部を加水分解、メチ
ロール化またはマンニツヒ化などの高分子反応に
よつて他の官能基に変換して得られた共重体をも
含む。これらの重合体の分子量は、特には限定さ
れない、本発明の効果がより良く発現されるの
は、比較高い分子量をもつた重合体においてであ
る。具体には、少なくとも500万の重量平均分子
量を持つことが好ましい。重量平均分子量の測定
は光散乱法または固有粘度[η]法([η]の値
は1N−硫酸ナトリウム水溶液を用い、30℃の恒
温槽中でウベローデ型粘度計またはキヤノンフエ
ンスケ型粘度計を用いて測定した値であり、アク
リルアミドホモポリマーの場合の重量平均分子量
は [η]=3.73×10-4[MW]0.66
30℃、1N−NaNO3) によつて求めた数値である。)による。 これらのアクリルアミド系重合体またはその水
溶液に、重合体の少くとも0.5重量%、好ましく
は1.0〜5.0重量%の水溶性ビニルモノマーが添加
される。0.5%よりも少ない添加量では熱時安定
性の改善が充分ではなく、5.0重量%を越えても
それ以上の安定性の改善を望めないばかりではな
く、単位有効成分あたりの粘度特性の低下をおこ
す。前記の量の水溶性ビニルモノマーをアクリル
アミド系重合体またはその溶液に添加する方法
は、種々の方法により実施することができる。 その一つの方法は、この重合体水溶液(重合体
の分子量ないし濃度によつてはゲル状となつてい
ることがある)に本発明水溶性ビニルモノマーを
そのまま、あるいは溶液ないし分散液として添加
することである。この重合体水溶液を固体重合体
の溶解によつてつくるべきときはあらかじめ水溶
性ビニルモノマーを固体重合体(ゲルまたは粉
末)にミキサ、ブレンダ等によつて混合しておく
か、またはあらかじめ溶媒の水に水溶性ビニルモ
ノマーを溶解させておくかである。アクリルアミ
ド系重合体水溶液は重合終了後のものでも、また
はこれを濃縮または稀釋したものでも、或いは使
用の際に固体重合体を溶解して得られたものでも
よい。水溶性ビニルモノマーとしては、アクリル
アミド、メタクリルアミド(メタ)アクリル酸ま
たはその塩、(メタ)アクリロニトリル、2−ア
クリルアミド−2−メチル−プロパンスルホン酸
またはその塩、(メタ)アクリル酸ジメチルアミ
ノエチル、アクリル酸低級アルキルエステル、ビ
ニルピリジンその他の水溶性ビニルモノマーを例
示することができる。これらのビニルモノマー
は、単独でも、混合物として用いることもでき
る。また、重合に用いた単量体と同じ種類のもの
でも、異なる種類のものでもよい。 本発明方法によつて得られる重合体の分子量
は、特には限定されないが、本発明の効果がより
良く発現されるのは、比較的高い分子量をもつた
重合体においてである。具体的には、少なくとも
500万の重量平均分子量を持つことが好ましい。
重量平均分子量の測定は光散乱法または固有粘度
[η]法([η]の値は1N−硫酸ナトリウム水溶
液を用い、30℃の恒温槽中でウベローデ型粘度計
またはキヤノンフエンスケ型粘度計を用いて測定
した値であり、アクリルアミドホモポリマーの場
合の重量平均分子量は [η]=3.73×10-4[MW]0.66(30℃、1N−
NaNO3) によつて求めた数値である。)による。 本発明方法により得られたアクリルアミド系重
合体は凝集剤、製紙用薬剤、土質改良剤、増粘
剤、石油回収剤などの分野に広く用いられるが、
これらの適用場面においては重合体は水溶液とし
て用いられる。この重合体の溶解に用いられる水
は市水、工業用水、河川水、地下水のほかに、各
種の可溶性物質が溶存したものであつてもよい
(溶存物質の種類および量は、アクリルアミド系
重合体の析出を生ずる様なものであつてはならな
いことはいうまでもない)。その様な水の例とし
ては油田において得られる“produced water”
及び“fresh water”が挙げられる。本発明で対
象としている安定化すべきアクリルアミド系重合
体水溶液の濃度は分子量によつて変化するが、
500万以上の分子量の重合体の場合には約0.01〜
約1.0重量%であることが通常である。 使用時における水溶液状態の、アクリルアミド
系重合体の品質低下の原因は明らかでないが、重
合体中に含まれる酸化性物質又は、溶存酸素の関
与するラジカル反応に基づく重合体の崩壊と考え
られ、発生したラジカルが添加された水溶性ビニ
ルモノマーに連鎖移動を起して、重合体自身の分
解を防ぐものと推察できる。 本発明によれば、アクリルアミド系重合体に水
溶ビニルモノマーを少くとも0.5重量%、好まし
くは1.0〜5.0重量%(重合体に対して)添加する
ことにより熱安定性効果が得られる。そして本発
明による安定化効果は室温近傍においてのみなら
ず、90℃という高温であつても得られる。以下に
実施例を示して、さらに本発明を具体的に説明す
る。 実施例1および比較例1 公知のラジカル重合法を用いて得られた、アク
リルアミド82モル%とアクリル酸Na18モル%か
らなるアクリルアミド系重合体粉末品(0.1重量
%の濃度で1N−naCl水溶液中、25℃ブルツクフ
イールド回転粘度計B8L型アダプター付で60rpm
の条件で6.0cpsのもの)を“Texaco Redu
Water”に溶解させて、0.1重量%の重合体水溶
液を調製した後、この溶液の粘度を測定して初期
粘度(AO)とし、この水溶液の一部を採つて本
発明の水溶性ビニルモノマーを添加し耐熱試験瓶
に入れ密栓し、90℃処理後粘度(A)を測定して、経
時変化を粘度保持百分率(A/Ao×100)で表−
1及び表−2に示した。なお、水溶性ビニルモノ
マー無添加のものの粘度保持百分率をも併せて表
−1に示した。 “Texaco Redu Water”の組成 NaCl 0.1714(重量%) CaCl2 0.0039( 〃 ) Na2SO4 0.0083( 〃 ) MgCl2 0.00636( 〃 ) NaHCO3 0.1553( 〃 ) Na2CO3 0.00378( 〃 )
The present invention relates to a method for producing an acrylamide-based polymer stabilized against thermal decomposition. Acrylamide-based polymers are widely used in many industrial fields such as flocculants, paper-making agents, soil conditioners, thickeners, and oil recovery agents. In this way, acrylamide-based polymers have achieved promising results in a wide variety of applications.
However, this polymer has serious drawbacks and may not be able to fully demonstrate its inherent ability. That is, this disadvantage is that this polymer is more susceptible to thermal decomposition than other polymers. For example, even when an aqueous solution of an acrylamide polymer is left at room temperature, it is often observed that the aqueous solution viscosity value is maintained only for a short time, and especially at relatively high temperatures, this tendency of performance deterioration is accelerated. In extreme cases, it may become impossible to use it for the intended purpose. especially,
When injecting crude oil underground in the form of an aqueous solution as a forced recovery agent, the temperature of the underground oil layer is approximately 40 to 100°C, and the injected acrylamide polymer aqueous solution flows underground from the injection well to the production well. Because acrylamide-based polymers remain in the oil layer for a long period of time, ranging from several months to several tens of months, users demand that the quality of acrylamide-based polymers be guaranteed during that period. Therefore, the challenge faced by acrylamide polymer manufacturers is to minimize the deterioration of polymer quality over time in this temperature range. Conventionally, in order to solve such problems, studies have been conducted on anti-deterioration agents. For example, 2-mercaptobenzimidazole and its derivatives are described as effective in JP-A-54-83048, thiourea and its derivatives in JP-A-49-27662, and methoxyphenol etc. are described as effective in JP-A-57-159839. ing. In addition, U.S. Pat.
It is described that 1,3-benzotriazole and 2-(2-hydroxyphenyl)benzotriazole are effective. However, it would be desirable to be able to impart thermal stability to the polymer itself without the addition of such antidegradants. An object of the present invention is to provide a method for producing a water-soluble high molecular weight acrylamide polymer with good thermal stability. The present invention provides the following method for producing a stabilized acrylamide polymer. Acrylamide-based polymers, at least
A method for producing a stabilized acrylamide polymer, which comprises adding 0.5% by weight of a water-soluble vinyl monomer. Acrylamide polymerization processed by the method of the present invention involves acrylamide, methacrylamide or a mixture thereof, or one of these and other copolymerizable vinyl monomers, such as (meth)acrylic acid or its salts, (meth) ) acrylonitrile,
2-acrylamido-2-methylpropanesulfonic acid or its salt, dimethylaminoethyl (meth)acrylate, lower alkyl acrylate, vinylpyridine, acid salt or quaternary salt of dialkylaminoalkyl (meth)acrylate, or dialkylaminoalkyl A polymer, copolymer or copolymer containing a predominant amount of (meth)acrylamide moiety obtained by polymerizing or copolymerizing a mixture with 50% by weight or less of an acid salt or quaternary salt of (meth)acrylamide by a well-known method. It is a mixture of these. It also includes copolymers obtained by converting a part of the amide group into other functional groups through polymer reactions such as hydrolysis, methylolation, or Mannitz formation, such as (meth)acrylamide homopolymers. . The molecular weight of these polymers is not particularly limited, and the effects of the present invention are better expressed in polymers with relatively high molecular weights. Specifically, it is preferable to have a weight average molecular weight of at least 5 million. The weight average molecular weight can be measured by the light scattering method or the intrinsic viscosity [η] method (the value of [η] is determined using a 1N sodium sulfate aqueous solution and an Ubbelohde viscometer or Canon Fuenske viscometer in a constant temperature bath at 30°C. The weight average molecular weight for acrylamide homopolymer is [η]=3.73×10 -4 [MW] 0.66 (
This is a value obtained using 1N−NaNO 3 ) at 30°C. )by. A water-soluble vinyl monomer is added to these acrylamide-based polymers or their aqueous solutions in an amount of at least 0.5% by weight of the polymer, preferably 1.0 to 5.0% by weight. If the amount added is less than 0.5%, the improvement in thermal stability will not be sufficient, and if it exceeds 5.0% by weight, not only will no further improvement in stability be expected, but the viscosity properties per unit active ingredient will decrease. cause The above amount of water-soluble vinyl monomer can be added to the acrylamide polymer or its solution by various methods. One method is to add the water-soluble vinyl monomer of the present invention as it is or as a solution or dispersion to this aqueous polymer solution (which may be in the form of a gel depending on the molecular weight or concentration of the polymer). It is. When this aqueous polymer solution is to be prepared by dissolving a solid polymer, the water-soluble vinyl monomer must be mixed with the solid polymer (gel or powder) in advance using a mixer, blender, etc., or water as a solvent must be prepared in advance. The solution is to dissolve the water-soluble vinyl monomer in the water. The acrylamide polymer aqueous solution may be a solution obtained after completion of polymerization, a solution obtained by concentrating or diluted solution, or a solution obtained by dissolving a solid polymer at the time of use. Water-soluble vinyl monomers include acrylamide, methacrylamide (meth)acrylic acid or its salt, (meth)acrylonitrile, 2-acrylamido-2-methyl-propanesulfonic acid or its salt, dimethylaminoethyl (meth)acrylate, acrylic Examples include acid lower alkyl esters, vinyl pyridine and other water-soluble vinyl monomers. These vinyl monomers can be used alone or as a mixture. Furthermore, the monomer may be of the same type as the monomer used in the polymerization, or may be of a different type. Although the molecular weight of the polymer obtained by the method of the present invention is not particularly limited, the effects of the present invention are better expressed in a polymer having a relatively high molecular weight. Specifically, at least
Preferably, it has a weight average molecular weight of 5 million.
The weight average molecular weight can be measured by the light scattering method or the intrinsic viscosity [η] method (the value of [η] is determined using a 1N sodium sulfate aqueous solution and an Ubbelohde viscometer or Canon Fuenske viscometer in a constant temperature bath at 30°C. In the case of acrylamide homopolymer, the weight average molecular weight is [η] = 3.73×10 -4 [MW] 0.66 (30℃, 1N-
This is the numerical value obtained by NaNO 3 ). )by. Acrylamide-based polymers obtained by the method of the present invention are widely used in fields such as flocculants, paper-making agents, soil conditioners, thickeners, and oil recovery agents.
In these applications, the polymer is used as an aqueous solution. The water used for dissolving this polymer may be city water, industrial water, river water, underground water, or water containing various soluble substances dissolved therein (the type and amount of the dissolved substances are determined based on the acrylamide-based polymer). It goes without saying that the material must not be of a type that would cause the precipitation of An example of such water is “produced water” obtained from oil fields.
and “fresh water”. The concentration of the acrylamide polymer aqueous solution to be stabilized, which is the object of the present invention, varies depending on the molecular weight, but
Approximately 0.01~ for polymers with a molecular weight of 5 million or more
It is usually about 1.0% by weight. The cause of the quality deterioration of acrylamide-based polymers in an aqueous solution state during use is not clear, but it is thought that the deterioration of the polymer is due to radical reactions involving oxidizing substances contained in the polymer or dissolved oxygen. It can be inferred that this radical causes chain transfer to the added water-soluble vinyl monomer, thereby preventing the polymer itself from decomposing. According to the invention, a thermal stability effect is obtained by adding at least 0.5% by weight, preferably 1.0 to 5.0% by weight (based on the polymer) of a water-soluble vinyl monomer to the acrylamide-based polymer. The stabilizing effect of the present invention can be obtained not only near room temperature but also at a high temperature of 90°C. EXAMPLES The present invention will be explained in more detail with reference to Examples below. Example 1 and Comparative Example 1 An acrylamide polymer powder product consisting of 82 mol% acrylamide and 18 mol% Na acrylate obtained using a known radical polymerization method (in a 1N-naCl aqueous solution at a concentration of 0.1% by weight, 25℃Brutskfield rotational viscometer B8L type with adapter 60rpm
6.0cps under conditions of “Texaco Redu
After preparing a 0.1% by weight aqueous polymer solution, the viscosity of this solution was measured to determine the initial viscosity (AO), and a portion of this aqueous solution was taken to prepare the water-soluble vinyl monomer of the present invention. Add it, put it in a heat-resistant test bottle, seal it, measure the viscosity (A) after treatment at 90℃, and show the change over time as viscosity retention percentage (A/Ao x 100).
1 and Table 2. Note that Table 1 also shows the viscosity retention percentage of those without the addition of water-soluble vinyl monomer. Composition of “Texaco Redu Water” NaCl 0.1714 (wt%) CaCl 2 0.0039 (〃) Na 2 SO 4 0.0083 (〃) MgCl 2 0.00636 (〃) NaHCO 3 0.1553 (〃) Na 2 CO 3 0.00378 (〃)

【表】【table】

【表】 表−1の結果から明らかになるように、特に
1.0重量%以上のアクリルアミドおよびアクリル
酸ソーダの添加によりアクリルアミド系重合体の
熱安定性が改良される。 実施例 2 実施例1において用いられた水溶性ビニルモノ
マーを表−2に示した各種のビニルモノマーに代
えて実施例1を繰返した。
[Table] As is clear from the results in Table 1, especially
The addition of 1.0% by weight or more of acrylamide and sodium acrylate improves the thermal stability of acrylamide-based polymers. Example 2 Example 1 was repeated except that the water-soluble vinyl monomer used in Example 1 was replaced with various vinyl monomers shown in Table 2.

【表】 表−2から明らかになるように、重合体の構成
モノマー以外の水溶性ビニルモノマーの添加も、
アクリルアミド系重合体の熱安定性改善に寄与す
る。
[Table] As is clear from Table 2, the addition of water-soluble vinyl monomers other than the constituent monomers of the polymer also
Contributes to improving the thermal stability of acrylamide polymers.

Claims (1)

【特許請求の範囲】 1 アクリルアミド系重合体に、少なくともそれ
の0.5重量%の水溶性ビニルモノマーを添加する
ことを特徴とする安定化されたアクリルアミド系
重合体の製造方法。 2 該水溶性ビニルモノマーを該重合体の1.0〜
5.0重量%添加する特許請求の範囲第1項記載の
方法。 3 該アクリルアミド系重合体の水溶液に該水溶
性ビニルモノマーが添加される特許請求の範囲第
1項または第2項記載の方法。
[Claims] 1. A method for producing a stabilized acrylamide polymer, which comprises adding at least 0.5% by weight of a water-soluble vinyl monomer to the acrylamide polymer. 2 The water-soluble vinyl monomer is added to the polymer in a proportion of 1.0 to
The method according to claim 1, wherein 5.0% by weight is added. 3. The method according to claim 1 or 2, wherein the water-soluble vinyl monomer is added to the aqueous solution of the acrylamide polymer.
JP6582584A 1984-04-04 1984-04-04 Production of stabilized acrylamide polymer Granted JPS60210657A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6582584A JPS60210657A (en) 1984-04-04 1984-04-04 Production of stabilized acrylamide polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6582584A JPS60210657A (en) 1984-04-04 1984-04-04 Production of stabilized acrylamide polymer

Publications (2)

Publication Number Publication Date
JPS60210657A JPS60210657A (en) 1985-10-23
JPH0510386B2 true JPH0510386B2 (en) 1993-02-09

Family

ID=13298188

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6582584A Granted JPS60210657A (en) 1984-04-04 1984-04-04 Production of stabilized acrylamide polymer

Country Status (1)

Country Link
JP (1) JPS60210657A (en)

Also Published As

Publication number Publication date
JPS60210657A (en) 1985-10-23

Similar Documents

Publication Publication Date Title
US4694046A (en) Hydrophobically associating terpolymers of acrylamide, salts of acrylic acid and alkyl acrylamide
US5089578A (en) Hydrophobically associating terpolymers containing sulfonate functionality
US5990233A (en) Rheology modifiers for use in aqueous compositions
US4730028A (en) Process for preparing hydrophobically associating terpolymers containing sulfonate functionality
US4040967A (en) Method of fracturing subterranean formations penetrated by a well
US4042529A (en) Composition and method for enhancing dispersibility of water soluble polymers
US3897382A (en) Method for the acid hydrolysis of acrylonitrile containing polymers, hydrogels and fibers of products prepared by said method
US3234163A (en) Aqueous solutions of polyacrylamide stabilized with thiocyanates
CN107759738B (en) Water-soluble thermal tackifying copolymer, preparation method and application
CN101205281A (en) Water-soluble hydrophobically associating copolymer and its preparation method
CN1148432C (en) Method for preparing oil-displacing agent of high-tack-producing hydrophobic association polymer
US5100953A (en) Solutions of hydrophobically associating terpolymers containing sulfonate functionality
JPS6239622B2 (en)
CN101225144A (en) Water-soluble hydrophobically associating copolymer and its preparation method
CN106749836B (en) Copolymer suitable for filtrate reducing with temperature resistance anticalcium ability and its preparation method and application and drilling fluid and its application
US4481316A (en) Method for inhibiting the degradation of an aqueous solution of an acrylamide polymer in a petroleum recovery process
JPH0510386B2 (en)
JPS6011516A (en) Intramolecular polymer composite body-acid, base and viscosity rendering agent for salt solution
US4393163A (en) Method for stabilizing an acrylamide polymer in a petroleum recovery process
DE69818426T2 (en) METHOD FOR PRODUCING POLYACRYLAMIDE DISPERSIONS
US4579926A (en) Process for the formation of novel acrylamide acrylate copolymers
KR870010096A (en) Low molecular weight copolymer of vinyl halide / vinylacetate prepared by water soluble polymerization
CN106543352B (en) A kind of hydrophobic associated polymer and its preparation method and application
US3396154A (en) Sodium borohydride as a polymerization inhibitor for a redox system
US3663490A (en) Acrylic acid-acrylamide-diacetone acrylamide terpolymer