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Dispersions of polymer oil additives

A technology of dispersions and polymers, applied in the directions of additives, fuel additives, lubricating compositions, etc., can solve the problems of unsatisfactory efficacy of additives, unsatisfactory long-term stability of dispersions, insufficient miscibility, etc.

Inactive Publication Date: 2013-08-21
CLARIANT FIANCE (BVI) LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The problems in the proposed prior art solutions are above all the unsatisfactory long-term stability of the dispersion over several weeks to months, and the often unsatisfactory efficacy of the additive, which is caused above all by Caused by the incorporation of emulsifying monomer units, followed by insufficient miscibility of hydrophobic active substances from their hydrophilic carrier medium into the mineral oil to be treated

Method used

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  • Dispersions of polymer oil additives
  • Dispersions of polymer oil additives
  • Dispersions of polymer oil additives

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0209] 14 g of an ethylene-vinyl acetate copolymer having a vinyl acetate content of 25% by weight and an average molecular weight of 100,000 g / mol (measured by GPC in THF relative to poly(styrene) standards), 21 Solvesso 150ND (ExxonMobil), and a mixture of 0.4 g diethanolammonium resinate and 1.1 g diethanolammonium tall oil fatty acid salt, were homogenized with stirring and heating to 80 to 85°C. With further stirring, 10 grams of monoethylene glycol was slowly added to the solution at 80 to 85° C., followed by 14 grams of water. A white, low-viscosity dispersion is formed here. After cooling to 50°C, use the Ultra- T45 sheared the dispersion for 2 minutes at 10000 rpm.

[0210] The dispersion thus obtained had an average particle size of 1.6 microns and a viscosity (25° C.) of 625 mPa·s. After storage of an aliquot of the sample at room temperature or at 50° C. for 5 weeks, the sample was homogeneous and unchanged in viscosity.

Embodiment 2

[0212] 0.5 g of diethanolammonium resinate and 1.5 g of diethanolammonium tall oil fatty acid salt were dissolved in 13 g of monoethylene glycol and heated to 60°C. Subsequently, 36 g of a 50% solution of poly(octadecyl acrylate) having a K value of 32 (measured according to Fikentscher in a 5% solution) in xylene were added in portions with stirring over a period of 15 minutes. After homogenization, 13 g of water containing 2.5 g / l xanthan gum and 1.0 g / l biocide were added, during which time the temperature of the microdispersion formed was kept constant at 60°C. After cooling the reaction solution to 40°C, with the help of Ultra- T2B sheared it for 2 minutes at 20000 rpm.

[0213] The dispersion thus obtained had a viscosity of 140 mPa·s. After an aliquot of the sample was stored at room temperature or at 50°C for 6 weeks, the sample was homogeneous with no change in viscosity.

Embodiment 3

[0215] 33 g of behenyl acrylate grafted in a 4:1 weight ratio with a vinyl acetate content of 28% by weight and an MFI of 7 g / 10 min 190 A solution of ethylene-vinyl acetate copolymer in 22 grams of xylene was blended with 0.8 grams of diethanolammonium resinate and 2.2 grams of diethanolammonium tall oil fatty acid salt and heated to 85°C with stirring. With further stirring, 19 grams of monoethylene glycol was slowly added to the solution at 80 to 85°C, followed by 23 grams of water. A white, low-viscosity suspension formed here. After cooling to 50°C, use the Ultra- T45 sheared the suspension at 10000 rpm for 2 minutes.

[0216] The dispersion thus obtained had an average particle size of 1.7 microns and a viscosity of 270 mPa·s. After storage of an aliquot of the sample at room temperature or at 50° C. for 5 weeks, the sample was homogeneous and unchanged in viscosity.

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Abstract

Dispersion comprises at least one effective oil soluble polymer as cold-flow improver for mineral oil; at least one water-insoluble organic solvent; water; at least one alkanol amine salt of polycyclic carboxylic acid; and optionally at least one water-soluble organic solvent. An independent claim is included for a preparation of the dispersion.

Description

Background technique [0001] Crude oil and the products made from it are complex mixtures of different types of substances, some of which can cause problems during production, transportation, storage and / or further processing. For example, crude oil and its derived products, such as middle distillates, heavy fuel oil, bunker oil, bunker oil, or resid, contain hydrocarbon waxes that precipitate at low temperatures and form a three-dimensional network of flakes and / or fine needles. At low temperatures, this especially impairs the fluidity of the oil, for example, when transported in pipelines, and in storage tanks, where considerable quantities of oil are enclosed between paraffin wax crystallized out especially on the tank walls. [0002] Therefore, various types of additives are added to paraffinic mineral oil for transportation and storage. These additives are mainly synthetic polymers. So-called wax inhibitors improve the low-temperature fluidity of oils, for example by mod...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10M169/04C10L1/14C09K8/524
CPCC10L1/2335C10M2207/281C10M2207/18C10M2207/021C10L1/1981C10L1/198C10L1/1886C10M2207/16C10L1/1616C10L1/125C10L1/19C10L1/1826C10M2207/20C10L1/1824C10M2209/103C10M169/044C10M2205/028C10N2230/04C10M2205/02C10M2207/022C10L1/1885C10M2205/022C10L1/1966C10L1/1973C10L1/1857C10M173/02C10L1/1641C10L1/1963C10L1/1985C10M2207/08C10L1/1855C10N2220/023C10L1/2225C10L10/16C10N2230/08C10L1/1608C10L1/10C10L1/1888C10M2209/101C10N2250/12C10N2020/011C10N2030/08C10N2030/04C10N2050/015C10M2209/062C10M2209/084C10M2209/08C10M169/04C10M129/68C10M129/52C10N2030/02
Inventor M·福伊斯特尔M·克鲁尔C·凯瑟尔M·楼
Owner CLARIANT FIANCE (BVI) LTD