Terpolymers based on sulfobetaines, processes for their...

Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Polymers from only ethylenic monomers or processes of...

Reexamination Certificate

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C526S219600, C526S263000, C526S265000, C526S287000

Reexamination Certificate

active

06346588

ABSTRACT:

The present invention relates to terpolymers based on sulfobetaines, processes for their preparation and their use as thickeners for aqueous salt solutions, in particular in the form of highly saline so-called completion and workover brines in the oilfield sector. Completion brines are understood as meaning, for example, aqueous solutions of CaCl
2
, CaBr
2
or ZnBr
2
up to saturation and mixtures thereof having a density range of from 1.3 to 2.3 g/ml. It is generally difficult to thicken such brines since conventional thickening agents based on anionic polymers or hydroxyethylcellulose (HEC) no longer have a thickening effect in concentrated salt solutions and moreover are insoluble or only very poorly soluble, so that, for example, the preparation of premixes, heating or high stirring speeds are required.
According to the prior art, mainly HEC has been used to date as a thickener for highly saline completion and workover brines in oilfields, but it is necessary in each case to prepare special mixtures in order to obtain HEC in solution.
WO 97/26310 describes premixes of HEC with a prehydrating alcohol, an alcoholic solvent and an inorganic salt, WO 97/13578 describes premixes of HEC with propylene glycols and polyether glycols and U.S. Pat. No. 4,350,601 describes polysaccharides which have been treated with formaldehyde and/or with aliphatic dialdehydes. Their advantage is improved dissolution behavior and hence improved efficiency as thickeners for zinc-containing brines.
However, a disadvantage of these thickeners is that HEC is thermally stable only up to max. 135° C. and does not have a thickening effect in brines having densities of between 1.45 and 1.75 g/ml at room temperature (thickening gap). In addition, it was found that HEC is precipitated from the brines at temperatures as high as above 650C. (cf. R. M. Hodge, SPE Drilling & Completion, June 1998).
Poly(sodium acrylamidomethylpropane)sulfonate, hydrolyzed polyacrylamides and poly(vinypyrrolidone) and copolymers thereof are water-soluble polymers which are described in the literature and are used as thickeners of aqueous solutions. The effect as thickener is based on the combination of high molecular weight and chain extension, which is due to the mutual repulsion of identically charged ionic groups along the polymer chain or to hydrogen bridge bonds. These polymers are however known to be sensitive to the action of salts and their use in highly saline systems is therefore limited.
U.S. Pat. No. 5,480,863 discloses a process for increasing the viscosity of zinc-containing brines (up to 1.8 g/ml) with acrylamide/AMPS copolymer in the presence of a surfactant, and U.S. Pat. No. 4,619,773 discloses a thickened brine stable at high temperature (200° C.) and containing AMPS/vinylamide and optionally acrylamide.
Betaines are a particular type of zwitterions. They neutralize themselves and contain no opposite ions. In addition, the positive and negative charges are separated from one another by alkyl groups. Polymers which contain betaine monomers show antipoly-electrolytic behavior in salt solutions, i.e. they swell up instead of contracting.
Carboxymethacrylate-betaine monomers and polymers are known and are disclosed in U.S. Pat. No. 2,777,872, U.S. Pat. No. 2,834,758 and U.S. Pat. No. 2,846,417. Carboxybetaines are sensitive to divalent ions, such as, for example, calcium. However, calcium salts are the basis of the customary completion brines.
Methacrylate-based sulfobetaine monomers and polymers have already been disclosed in German Auslegeschrift 1,207,630. The reaction solutions obtained in the synthesis examples are already highly viscous at a solids content of only 5% by weight (100,000 to 400,000 cP, Brookfield viscosity). Sulfobetaine copolymers with hydroxyethyl methacrylate (HEMA) are described, for example, by J. M. Rego et al. in Polym. J., 23(12), 1425-34, the polymer being reacted with a crosslinking agent and a hydrogel being obtained, which is optimized with respect to its material properties.
Sulfobetaine copolymers as thickeners for salt solutions are disclosed, for example, in U.S. Pat. Nos. 5,153,289 and 4,650,848. According to U.S. Pat. No. 5,153,289, an N-3(3-sulfopropyl)-N-methacryloyloxyethyl-N, N-dimethylammonium betaine (SPE)/N-vinyl-pyrrolidine (NVP) copolymer is recommended as a thickener in up to 20% strength NaCl solution. U.S. Pat. No. 4,650,848 describes a terpolymer of acrylamide (AM), a hydrophobic acrylamide and a sulfobetaine monomer and its use as a thickener in up to 20% strength NaCl solution. Said sulfobetaine-containing polymers are always obtained as solids.
However, in the thickening of highly saline aqueous systems, the problem of bringing a thickener into solution generally occurs since the water is bound in the solution by the high salt content and is thus no longer available for dissolving the polymer. This often leads to agglomeration and to incomplete dissolution of the thickener. Consequently, the producing rock formations may be blocked and thus damaged. It is therefore often necessary to prepare premixes of the thickeners or to use expensive technical mixing devices (for example with high shear load, high temperature, etc.) in order to increase the viscosity in salt solutions (such as, for example, in the case of HEC).
It was therefore the object of the present invention to develop a terpolymer which can be used as a thickener for highly saline systems, which terpolymer simultaneously
has a thickening effect over a wide density range (1.2-2.5 g/ml)
remains stable at high temperatures (up to at least 200° C.) over a period of at least 48 h
is stable to polyvalent ions (e.g. Ca
2+
, Zn
2+
)
can be prepared and used without great technical complexity (e.g. with high shear load, high temperature, etc.).
This object was achieved, according to the invention, by the terpolymers according to claim
1
.
Surprisingly, it was found that sulfobetaine polymers which contain a monomer having a pendant OH group thicken salt solutions to a substantially greater extent than conventional sulfobetaine polymers.
The terpolymers corresponding to the present invention are composed of three structural units altogether. The first structural unit a) corresponds to the general formula I
in which R
1
denotes H or CH
3
,
R
2
and R
3
, independently of one another, denote H, a C
1-4
-alkyl (linear or branched) or phenyl radical.
The second structural unit b) corresponds to the general formula II
in which R
1
represents H or CH
3
and m represents 1 to 4
The third structural unit c) finally corresponds to the general formula III
in which X is selected from the group consisting of
in which R
4
denotes —(CH
2
)
m
—,
m denotes 1 to 4 and
n denotes 0 to 3 and R
1
, R
2
and R
3
have the abovementioned meaning.
It is to be regarded as essential to the invention that the terpolymers corresponding to the present invention are composed of from 5 to 79 mol % of the structural unit a), from 20 to 94 mol % of the structural unit b) and from 1 to 75 mol % of the structural unit c).
A particular advantage of the terpolymers according to the invention is that they are thermally stable in aqueous solution up to at least 200° C.
In addition, the synthesis of these sulfobetaine polymers can be controlled so that the aqueous reaction solution formed during their preparation and having a preferred solids content of from 5 to 60% by weight and a preferred viscosity from 50 to 500,000 cP at 20° C. can—if desired and technically expedient—be used without further working up as a liquid thickener for highly saline systems. This is a significant advantage since the full thickening effect can be obtained without special technical equipment or prior treatment of a thickener powder within a very short time.
In the case of all thickeners used to date for highly saline systems, either expensive premixes have to be prepared or additional auxiliary agents have to be added in order to bring the active substances into solution in the respective systems. The efficiency of the respective active substance can

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