Polymers which exhibit thermothickening properties and process making same

Inactive Publication Date: 2005-01-04
RHODIA OPERATIONS SAS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

In accordance the present invention, an improvement to the process for producing thermothickening polymers which overcomes the problems as discussed above, and provides novel products which can be used for multiple applications is provided. More specifically, the improvement comprises producing the thermothickening polymers by utilizing an inverse emulsion (water-in-oil) synthesis technique.

Problems solved by technology

These synthesis methods are limited in that highly concentrated polymer solutions cannot be easily produced.
It is further believed that polymers having a molecular weight of greater than 2,000,000 daltons (using a size exclusion chromatograhpy method) cannot be synthesized using the above-mentioned methods.

Method used

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  • Polymers which exhibit thermothickening properties and process making same
  • Polymers which exhibit thermothickening properties and process making same
  • Polymers which exhibit thermothickening properties and process making same

Examples

Experimental program
Comparison scheme
Effect test

Example

EXAMPLE 1

Into a first vessel, an aqueous phase is prepared containing 243.7 parts of distilled water (a), 160.0 parts of 2-acrylamido-2-methylpropanesulfonic acid (b) (AMPS from Lubrizol), 40.0 parts of acrylic acid (c), 66.7 parts of Polyglycol B11 / 700 (d) (from Hoechst) and 12.0 parts of 50% NaOH (e). This phase is formed by dissolving AMPS and acrylic acid in water, mixing in NaOH solution and then adding Polyglycol B11 / 700.

Into a second vessel, an oil phase is prepared by mixing 12.0 parts of sorbitan monooleate (f), 10.0 parts of C12-C15 alcohols ethoxylated with 3 moles of ethylene oxide (g) and 6.0 parts of Hypermer B246 (h) (commercially available from ICI) in 170.0 parts of mineral spirits Shell Sol 151 (i) (commercially available from Shell). The aqueous phase is poured slowly into the oil phase while mixing, and the resulting mixture is homogenized in a blender for 15-25 seconds. The obtained monomer emulsion is then transferred to a reaction vessel equipped with an agit

Example

EXAMPLE 47

This example describe the characterization of thermothickening properties of the polymers thus made.

The thickening properties of the polymer are characterized by measuring the viscosity against salt concentration (salt thickening), temperature (thermal thickening) or shear rate (shear thickening). Polymer solution is either prepared with the above isolated solid product or with the inverted emulsion by nonyl phenol ethoxylated with 9 mols of ethylene oxide. The inversion of the emulsion is done by mixing 10.0 parts of the emulsion with 0.50 parts of nonyl phenol ethoxylated with 9 mol of ethylene oxide. The mixture is then diluted with 40.0 parts of water and neutralized with 1.14 parts of 50% (by weight) sodium hydroxide. This solution is then used for thickening characterization.

Sodium carbonate is used as the salt to show salt thickening. An 1.0% polymer solution is prepared either by diluting inverted emulsion or by dissolving the isolated solid in water. The viscosity is

Example

EXAMPLE 48

This example demonstrates that the non-ionic surfactants enhance the thermothickening of the polymer synthesized in Examples #1-45.

Polymer solution (0.5-1% by weight) is prepared by dissolving the isolated polymer in distilled water. To this solution is mixed in nonionic surfactant (0-2% by weight of Rhodasurf LA-7). If required, Ca(OH)2 is added to saturate the solution. The solution is heated and its viscosity at different temperature is recorded on a Brookfield LV viscometer at 60 rpm (shear rate 76.3 s−1). Polymers from Examples #1, #21, #32 (polymerized at 45, 55° C.), #34 (polymerized at 40° C.), #39 and #43 are tested with one or more of the nonionic surfactants, which are C12-15 alcohols ethoxylated with 3, 7 or 9 mols of ethylene oxide (an example of a representative surfactant having 7 mols of ethylene oxide is shown in FIG. 7).

TABLE 1Lubricant 50-HB-3520Polyglycol B11 / 700Example(MW 3520)(MW 5000)320.040.0430.030.0540.020.0660.0—

TABLE 2ExampleAmount of Components

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Abstract

A polymer produced by polymerizing via water-in-oil emulsion polymerization one or more water soluble monomers with one or more polyalkoxylated monomers wherein said one or more polyalkoxylated monomers contains at least 25 alkylene oxide units and wherein said product demonstrates thermothickening properties, its method of manufacture and use thereof is disclosed.

Description

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Claims

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Application Information

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Owner RHODIA OPERATIONS SAS
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