[go: up one dir, main page]

JPS61102995A - Polymer composition for recovering petroleum - Google Patents

Polymer composition for recovering petroleum

Info

Publication number
JPS61102995A
JPS61102995A JP22414384A JP22414384A JPS61102995A JP S61102995 A JPS61102995 A JP S61102995A JP 22414384 A JP22414384 A JP 22414384A JP 22414384 A JP22414384 A JP 22414384A JP S61102995 A JPS61102995 A JP S61102995A
Authority
JP
Japan
Prior art keywords
polymer
oil
weight
parts
salt
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP22414384A
Other languages
Japanese (ja)
Other versions
JPH0410557B2 (en
Inventor
細谷 好夫
羊一 細川
新田 敦彦
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 Cyanamid Ltd
Original Assignee
Mitsui Cyanamid 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 Mitsui Cyanamid Ltd filed Critical Mitsui Cyanamid Ltd
Priority to JP22414384A priority Critical patent/JPS61102995A/en
Publication of JPS61102995A publication Critical patent/JPS61102995A/en
Publication of JPH0410557B2 publication Critical patent/JPH0410557B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は石油強制回収(E OR)に使用する圧入液に
関するものであり、少量の使用量で石油回収率を向上さ
せる石油回収用重合体組成物に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to an injection fluid used in forced oil recovery (EOR), and is a polymer composition for oil recovery that improves oil recovery with a small amount of use. Regarding.

従来の技術 石油採掘技術は、現在までに大きく3つの段階を経て発
展して来た。第1段階は現在−次回取決と云われ油層の
もつ自然のエネルギーで自噴するままに油を回収するも
ので、回収率は埋蔵量の局程度と云われる。第2段階は
、自噴能力の減退した油田に、地表から人工的に水ある
いはガスを圧入して油を押し出すもので二次回収法と云
われる。
Conventional Technology Petroleum extraction technology has evolved through three major stages to date. The first stage is called the current-next agreement, in which oil is recovered as it self-gushes using the natural energy of the oil layer, and the recovery rate is said to be at a local level of reserves. The second stage is called the secondary recovery method, in which water or gas is artificially injected from the ground into oil fields where the artesian ability has diminished to push out the oil.

これらの回収法によっては、貯溜岩の孔隙に油滴として
存在する油、岩石表面に油膜として付着している油、二
次回収法のガス又は水に全く接触しない領域に存在する
油は、未回収となり、原油の局〜%が地下に残存すると
考えられている。
Depending on these recovery methods, oil that exists as oil droplets in the pores of reservoir rocks, oil that adheres to the rock surface as an oil film, and oil that exists in areas that do not come into contact with gas or water in secondary recovery methods may be untreated. It is believed that up to 50% of the crude oil remains underground after recovery.

加圧水又は加圧ガスを使用する第2次回収方法では(1
)圧入流体が低浸透率層または低浸透本領域を回避する
こと、(2)フィンガーリングを起こすこと、(3)粘
度の高い原油の下あるいは土を走ること、(0割れ目を
通してチャネリングすること等が回収率を低くする原因
とされている。そこで更に石油回収率を向上することを
目的として圧入水の流動抵抗を増すことが考えられ、こ
の手段としてポリマー水溶液を使用することが知られて
おり、合成ポリマーとしてポリアクリルアミド、バイオ
ポリマーとしてザンサンガム等が実用に供されている。
In the secondary recovery method using pressurized water or pressurized gas (1
) the injected fluid avoids low permeability layers or low permeability zones, (2) causes fingering, (3) runs under or through soil with high viscosity, (channeling through zero cracks, etc.) is said to be the cause of low recovery rates.In order to further improve the oil recovery rate, it is considered to increase the flow resistance of the injection water, and it is known that an aqueous polymer solution is used as a means for this purpose. , polyacrylamide as a synthetic polymer, and xanthan gum as a biopolymer are in practical use.

この残存油を回収する技術が第3段階であって、Enh
anced Oil Recovery  (EOR)
と呼ばれている。
The technology to recover this residual oil is the third step,
anced Oil Recovery (EOR)
It is called.

本発明はEOR方法に関するものである。The present invention relates to an EOR method.

発明が解決しようとする問題点 前述の如く、ポリアクリルアミドを用いて圧入液の流動
抵抗を増加させることは既に知られているが、アクリル
アミド重合体自体の改質については未だ充分検討されて
いない0本発明においては、アクリルアミド系重合体に
少量の添加物を添ズ       加することによりさ
らにすぐれた圧入液特性を発現させる石油回収用薬剤を
提供しようとするものである。
Problems to be Solved by the Invention As mentioned above, it is already known that polyacrylamide can be used to increase the flow resistance of injection fluid, but the modification of the acrylamide polymer itself has not yet been sufficiently investigated. The present invention aims to provide an oil recovery agent that exhibits even better injection fluid properties by adding a small amount of additives to an acrylamide polymer.

問題点を解決するための手段・作用 本発明の構成は、 1、 アクリルアミド系重合体100重量部と、2− 
 ・メルカプトベンゾイミダゾール又はその塩・0.5
〜2重量部とからなる抵抗ファクターおよび残存抵抗フ
ァクターの改良された石油回収用重合体組成物、ならび
に 2、 アクリルアミド系重合体100重量部、2−メル
カプトベンゾイミダゾール又はその塩を0.5〜2.0
重量部、およびチオ尿素類0.05〜5.0重量部から
なる抵抗ファクターおよび残存ファクターの改良された
石油回収用重合体組成物である。
Means/Function for Solving the Problems The composition of the present invention is as follows: 1. 100 parts by weight of an acrylamide polymer;
・Mercaptobenzimidazole or its salt ・0.5
100 parts by weight of an acrylamide polymer, 0.5 to 2 parts by weight of 2-mercaptobenzimidazole or a salt thereof; .0
This is a polymer composition for oil recovery with improved resistance factor and residual factor, which comprises 0.05 to 5.0 parts by weight of a thiourea.

次に本発明の石油回収用重合体組成物の組成し二ついて
更に詳細に説明する。
Next, the composition of the oil recovery polymer composition of the present invention will be explained in more detail.

前述の加圧水による石油回収方法においては置換流体す
なわち加圧水と、被置換流体すなわち原油との易動度の
比が回収率に大きく影響することは古くから知られてい
る。
In the aforementioned oil recovery method using pressurized water, it has been known for a long time that the mobility ratio between the displacement fluid, ie, pressurized water, and the fluid to be replaced, ie, crude oil, greatly influences the recovery rate.

易動度比CM)は次のように定義される。The mobility ratio CM) is defined as follows.

M= (Kw/牌W) / (K oZ用0)・串・C
1)ここに、 Kwは不動水飽和率における水の相対浸透率KOは不動
水飽和率における袖の相対浸透車用Wは水の粘度 JLoは油の粘度 通常の加圧水の場合Mがlθ〜30と非常に高い価をと
り、水の方が油より動き易い性質を示すことが低い油回
収率と関連するもので、何らかの手段によりMを1〜2
に低下させれば、油を押し出す作用がスムースに行われ
る。
M= (Kw/Tile W) / (0 for K oZ)・Skewer・C
1) Here, Kw is the relative permeability of water at the immobile water saturation rate KO is the relative permeability of the sleeve at the immobile water saturation rate W is the viscosity of water JLo is the viscosity of oil For normal pressurized water M is lθ ~ 30 The fact that water exhibits a property of being more mobile than oil is associated with a low oil recovery rate.
If the temperature is lowered to 100%, the action of pushing out the oil will be carried out smoothly.

ポリマー攻法においては上記水をポリマー溶液に読み替
えるわけであるが、このMを低下させるためのポリマー
溶液の性能を知るために、抵抗ファクターRFが測定さ
れる。
In the polymer attack method, the above-mentioned water is replaced with a polymer solution, and in order to know the performance of the polymer solution for reducing M, the resistance factor RF is measured.

RF= (Kw/pw)/ (Kp/pp) 番・(2
)ここに、 Kpは不動水飽和率におけるポリマー溶液の相対浸透率 ルPはポリマー溶液の粘度 このRFはポリマーの濃度、ポリマーの分子量および溶
媒の性質等に影響されるが、このRFの値が大きければ
石油回収用溶液として好ましいことは(1)式とその説
明から容易に理解される。
RF= (Kw/pw)/(Kp/pp) No.・(2
) Here, Kp is the relative permeability of the polymer solution at the immobile water saturation rate. P is the viscosity of the polymer solution. This RF is influenced by the concentration of the polymer, the molecular weight of the polymer, the properties of the solvent, etc., but the value of this RF is It is easily understood from equation (1) and its explanation that the larger the value, the better the solution for oil recovery.

次にアクリルアミド系重合体溶液のもう一つの特徴は、
一度ポリマー溶液を岩石に通過させることによって、そ
の岩石の浸透率を半永久的に低下させることである。こ
の浸透率の低下を表示するものが残存抵抗ファクターR
RFである。
Next, another feature of the acrylamide polymer solution is that
By passing a polymer solution through a rock, the permeability of the rock is semi-permanently reduced. The factor that indicates this decrease in penetration rate is the residual resistance factor R.
It is RF.

このRRFが大きくなればポリマー溶液通過後の岩石の
浸透率は小さくなり、原理的には原油層をポリマー溶液
層で押し、ポリマー溶液層を水層で押して原油を採掘す
るポリマー攻法にとっては好ましい現象である。
As this RRF increases, the permeability of the rock after passing through the polymer solution decreases, which is, in principle, preferable for the polymer exploration method in which crude oil is mined by pushing the crude oil layer with the polymer solution layer, and pushing the polymer solution layer with the water layer. It is a phenomenon.

なお、上記(2)及び(3)式は、   QL ル A・ΔP ただし、A:コアの断面積 L:コアの長さ Q:流量 であることから、次の(4)及び(5)式のようになる
Note that the above equations (2) and (3) are as follows: QL A・ΔP However, since A: cross-sectional area of the core L: core length Q: flow rate, the following equations (4) and (5) are obtained. become that way.

= (QW/ΔPw)(ΔPp/Qp)=(ΔPp/Q
p)/(ΔP W/QW) −e 6 (4)RRF=
 (Qw/ΔPw) (ΔPw’/Qw’)=(ΔP’
w/Qw’)/(ΔPw/Qw)・・(5)発明者はこ
れら2つの抵抗ファクターから本発明の石油回収用重合
体組成物の組成を特定の範囲に限定したものであって、
アクリルアミド系重合体100重量部に対し2−メルカ
プトベンゾイミダゾール(1’lBIと略記することが
ある。)又はその塩の添加量がMBI &算0.5重量
部未満であれば上述の2つの抵抗ファクターの上昇効果
は期待できず、またMBI又はその塩の添加量がMHI
換算2.0重量%を超えると、かえって上述の2つの抵
抗71     ″−がKTt6. tfZh % 2
 Q(7)l!;)*7 y 9ターは、上記限定範囲
内で極大値を有するものである。
= (QW/ΔPw) (ΔPp/Qp) = (ΔPp/Q
p)/(ΔP W/QW) −e 6 (4) RRF=
(Qw/ΔPw) (ΔPw'/Qw')=(ΔP'
w/Qw')/(ΔPw/Qw) (5) The inventor limited the composition of the oil recovery polymer composition of the present invention to a specific range based on these two resistance factors,
If the amount of 2-mercaptobenzimidazole (sometimes abbreviated as 1'lBI) or its salt added to 100 parts by weight of the acrylamide polymer is less than MBI & 0.5 parts by weight, the above two resistances will be met. No effect of increasing the factor can be expected, and the amount of MBI or its salt added may be lower than MHI.
If it exceeds 2.0% by weight, the above two resistors 71''- will actually become weaker than KTt6.tfZh%2
Q(7)l! ;) *7y9ter has a maximum value within the above-mentioned limited range.

さらにこれらNBI又はその塩の上記範囲内にある組成
物に、アクリルアミド系重合物100部に対し0.05
重量部〜5.0重量部の範囲のチオ尿素類を添加するこ
とにより上述の2つの抵抗ファクターがさらに増大する
が、これら範囲外のチオ尿素類の添加はかえって2つの
抵抗ファクターは低下する。
Furthermore, 0.05 parts of NBI or a salt thereof is added to the composition within the above range, based on 100 parts of the acrylamide polymer.
By adding thioureas in the range of 5.0 parts by weight to 5.0 parts by weight, the above-mentioned two resistance factors are further increased, but addition of thioureas outside these ranges actually decreases the two resistance factors.

なお1本発明において、アクリルアミド系重合体とは、
アクリルアミド成分を含む全ての水溶性重合体を包含す
る。
Note that in the present invention, the acrylamide polymer is
Includes all water-soluble polymers containing an acrylamide component.

具体的には、アクリルアミドとアクリル酸(塩)、メタ
アクリル酸(塩)、2−アクリルアミド−2−メチルプ
ロパンスルホン酸(塩)等の共重合物、あるいは、これ
らの7ニオン性重合体に水溶性を損なわない範囲でメタ
アクリルアミド、7クリロニトリル、ジメチルアミノエ
チルメタアクリレート3級塩、4級化物、アクリル酸低
級アルキルエステル等を含む重合物。
Specifically, copolymers of acrylamide and acrylic acid (salt), methacrylic acid (salt), 2-acrylamide-2-methylpropanesulfonic acid (salt), etc., or water-soluble in these 7-ionic polymers A polymer containing methacrylamide, 7-crylonitrile, dimethylaminoethyl methacrylate tertiary salt, quaternized product, lower alkyl acrylic acid ester, etc. within a range that does not impair properties.

また所謂共重合反応に依ったものに限らず、重合抜挿々
の化学反応により、アミド基を他の官能基に変換したも
の、例えばアルカリにより加水分解したり、メチロール
化したものを包含する。
Furthermore, it is not limited to those based on so-called copolymerization reactions, but also includes those in which an amide group is converted into another functional group by chemical reactions in and out of polymerization, such as those in which an amide group is hydrolyzed with an alkali or converted into a methylol group.

また、上記の2種以上の重合体の混合物を包含する。It also includes mixtures of two or more of the above polymers.

又見掛の重合度は10000以上のものが好ましい。Further, the apparent degree of polymerization is preferably 10,000 or more.

次に2−メルカプトベンゾイミダゾール又はその塩とは
、下記一般式で示される水溶性の化合物である。
Next, 2-mercaptobenzimidazole or a salt thereof is a water-soluble compound represented by the following general formula.

(但しXは水素、アルカリ金属またはアンモニウムを示
す。) Xが水素のときは、溶解性が悪いので通常はナトリウム
塩、カリウム塩、アンモニウム塩の形で使用する場合が
多い。
(However, X represents hydrogen, an alkali metal, or ammonium.) When X is hydrogen, it has poor solubility, so it is usually used in the form of sodium salt, potassium salt, or ammonium salt.

又、本発明でいうチオ尿素類とは次の一般式%式% て炭素および水素からなる有機の基を、またR3は主と
して炭素お、よび水素からなる有機の基をあられす)で
示される構造部分を少なくとも1個有する化合物である
In addition, the thioureas referred to in the present invention are represented by the following general formula (% formula % (%) represents an organic group consisting of carbon and hydrogen, and R3 represents an organic group mainly consisting of carbon and hydrogen). A compound having at least one structural moiety.

たとえば、このようなチオ尿素類としては、チオ尿素、
N、N”−ジフェニルチオ尿素、ジオルト−トリルチオ
尿素、エチレン尿素などが挙げられる。
For example, such thioureas include thiourea,
N,N''-diphenylthiourea, diortho-tolylthiourea, ethyleneurea, and the like.

また本発明の重合体組成物は、アクリルアミド系重合体
と、MHI又はその境、8よびチオ尿素類が混合されて
固体状をなす場合のみならず、使用状態において実質的
に上記3者が共存していればよく1例えば溶液状、スラ
リー状、ゲル状等の場合も含むものである。なおこれら
王者の混合方法については1通常知られている何れの方
法をも採用することができる。
Furthermore, the polymer composition of the present invention is not limited to the case where the acrylamide-based polymer, MHI or its boundary, 8, and thioureas are mixed to form a solid state, but also when the above three components substantially coexist in the state of use. For example, it may be in the form of a solution, slurry, gel, etc. As for the method of mixing these champions, any commonly known method can be employed.

しかして、本発明の重合体組成物が石油回収に効果を発
揮する濃度は約1100pp 〜50,000Ppm水
溶液であり、特に1ooppa+ 〜to、ooopp
lの濃度が好すI9い− 実施例 アクリルアミド80モル%、アクリル酸ナトリウム20
モル%からなる重合体で、その分子量が約15.000
,000であるアクリルアミド系重合体を、食塩Q、1
4g/i、塩化カルシウム無水物0.18g/nを含む
塩水(溶媒)を用いて溶液中のアクリルアミド重合体の
濃度が3009P!lになるごとく調製し、 )IBI
、千オ尿素を所定量加えて攪拌溶解し、第1表に示すご
とき組成の異るサンプルlロケを得た。
Therefore, the concentration at which the polymer composition of the present invention is effective for oil recovery is about 1100 ppm to 50,000 ppm aqueous solution, particularly 1ooppa+ to to, ooopp
The preferred concentration is I9 - Example acrylamide 80 mol%, sodium acrylate 20
A polymer consisting of mol%, whose molecular weight is approximately 15,000
,000 of an acrylamide-based polymer, salt Q, 1
Using salt water (solvent) containing 4g/i and 0.18g/n of calcium chloride anhydride, the concentration of acrylamide polymer in the solution was 3009P! )IBI
, 1,000 urea was added in a predetermined amount and dissolved with stirring to obtain samples having different compositions as shown in Table 1.

これら重合体組成物溶液サンプルについて油層岩のモデ
ルとして浸透率900〜1000ミリダルシーのベレア
砂岩を用いてコアテストを行った。
A core test was conducted on these polymer composition solution samples using Berea sandstone with a permeability of 900 to 1000 millidarcy as a model of oil reservoir rock.

1サンプル毎に新しいコアに次の順序で流体を流し、流
量Qとコア前後の圧力差ΔPを求め、(4)式、(5)
式により抵抗ファクターRFおよび残存抵抗ファクター
RRFを求めた。
For each sample, flow the fluid into a new core in the following order, find the flow rate Q and the pressure difference ΔP before and after the core, and use equations (4) and (5)
The resistance factor RF and the residual resistance factor RRF were determined using the formula.

なお、液温は25℃±1℃に保持した。Note that the liquid temperature was maintained at 25°C±1°C.

測定順序   流体   流量  差圧1     溶
媒   Qw   Δpw2    サンプル  Qp
   ΔPp3    13媒   Q’W   Δp
’wRF= (ΔPp/Qp)、/(ΔPw/Qw)・
・・(4)RRF= (ΔP’W/QW’)/(ΔPW
/QW)・・(5)得られた結果を第1表に示す。
Measurement order Fluid Flow rate Differential pressure 1 Solvent Qw Δpw2 Sample Qp
ΔPp3 13 medium Q'W Δp
'wRF= (ΔPp/Qp), /(ΔPw/Qw)・
...(4) RRF= (ΔP'W/QW')/(ΔPW
/QW)...(5) The results obtained are shown in Table 1.

本アクリルアミド重合体100重量部に対する添加重量
部発明の効果 本発明の石油回収用重合体組成物によれば、従来ホリマ
ー攻法に使用されているポリアクリルアミドの使用量の
削減あるいは石油回収率の向上を図ることができ、その
経済効果はきわめて大きい。
Part by weight added to 100 parts by weight of the present acrylamide polymer Effect of the invention According to the polymer composition for oil recovery of the present invention, the amount of polyacrylamide used conventionally used in the polymer attack method can be reduced or the oil recovery rate can be improved. The economic effect is extremely large.

Claims (1)

【特許請求の範囲】 1、アクリルアミド系重合体100重量部と、2−メル
カプトベンゾイミダゾール又はその塩0.5〜2重量部
とからなる抵抗ファクターおよび残存抵抗ファクターの
改良された石油回収用重合体組成物。 2、アクリルアミド系重合体100重量部、2−メルカ
プトベンゾイミダゾール又はその塩を0.5〜2.0重
量部、およびチオ尿素類0.05〜5.0重量部からな
る抵抗ファクターおよび残存ファクターの改良された石
油回収用重合体組成物。
[Scope of Claims] 1. An oil recovery polymer with improved resistance factor and residual resistance factor, comprising 100 parts by weight of an acrylamide polymer and 0.5 to 2 parts by weight of 2-mercaptobenzimidazole or its salt. Composition. 2. Resistance factor and residual factor consisting of 100 parts by weight of acrylamide polymer, 0.5 to 2.0 parts by weight of 2-mercaptobenzimidazole or its salt, and 0.05 to 5.0 parts by weight of thioureas. Improved oil recovery polymer compositions.
JP22414384A 1984-10-26 1984-10-26 Polymer composition for recovering petroleum Granted JPS61102995A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22414384A JPS61102995A (en) 1984-10-26 1984-10-26 Polymer composition for recovering petroleum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22414384A JPS61102995A (en) 1984-10-26 1984-10-26 Polymer composition for recovering petroleum

Publications (2)

Publication Number Publication Date
JPS61102995A true JPS61102995A (en) 1986-05-21
JPH0410557B2 JPH0410557B2 (en) 1992-02-25

Family

ID=16809218

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22414384A Granted JPS61102995A (en) 1984-10-26 1984-10-26 Polymer composition for recovering petroleum

Country Status (1)

Country Link
JP (1) JPS61102995A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5927828A (en) * 1982-08-05 1984-02-14 Seikagaku Kogyo Co Ltd Preparation of amebocyte lysate

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5927828A (en) * 1982-08-05 1984-02-14 Seikagaku Kogyo Co Ltd Preparation of amebocyte lysate

Also Published As

Publication number Publication date
JPH0410557B2 (en) 1992-02-25

Similar Documents

Publication Publication Date Title
CA1178040A (en) Enhanced oil displacement processes and compositions
CA2459672C (en) Organosilicon containing compositions for enhancing hydrocarbon production and method of using the same
EP0115836B1 (en) Polymeres useful in the recovery and processing of natural resources
US7182136B2 (en) Methods of reducing water permeability for acidizing a subterranean formation
CA1217589A (en) Crosslinking composition and method of preparation
US4439332A (en) Stable emulsion copolymers of acrylamide and ammonium acrylate for use in enhanced oil recovery
US4120361A (en) Method for reducing the permeability of subterranean formations to brines
US5922653A (en) Compositions and processes for treating subterranean formations
US5270382A (en) Compositions and applications thereof of water-soluble copolymers comprising an ampholytic imidazolium inner salt
US4487265A (en) Acidizing a subterranean reservoir
EP0180406B1 (en) Method of treating a subterranean formation
Moradi-Araghi et al. The application of gels in enhanced oil recovery: Theory, polymers and crosslinker systems
CN110452326B (en) Coating agent for water-based drilling fluid and preparation method thereof
CA1239921A (en) Composition for and method of altering the permeability of a subterranean formation
EP0447967B1 (en) Gelation of acrylamide-containing polymers with furfuryl alcohol and water dispersible aldehydes
CN113698534A (en) Polymer for high-performance environment-friendly borehole wall stabilizer for water-based drilling fluid
US4637467A (en) Permeability contrast correction
US20110263465A1 (en) Use Of Vinyl Phosphonic Acid For Producing Biodegradable Mixed Polymers And The Use Thereof For Exploring And Extracting Petroleum And Natural Gas
CA1320303C (en) Aminoalkylated polyacrylamide aldehyde gels, their preparation and use in oil recovery
US4163476A (en) Secondary recovery process utilizing an acrylamido alkanesulfonic acid polymer
US3927717A (en) Secondary recovery process utilizing polyvinylpyrrolidones
Hsieh et al. Water‐soluble polymers for hostile environment enhanced oil recovery applications
EP0136773A2 (en) Composition for cross-linking carboxyl polymers and the use thereof in treating subterranean formations
US3247900A (en) Method and composition for well treatment
US4210205A (en) Secondary recovery process

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term