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Transparent nanometer calcium carbonate oil phase dispersion and its preparation method by supergravity method

A nano-calcium carbonate, super-gravity method, which is applied in the petroleum industry, dyeing low-molecular-weight organic compounds, fibrous fillers, etc., can solve the problems of difficult dispersion and poor stability of nano-calcium carbonate.

Active Publication Date: 2017-10-10
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The first technical problem to be solved in the present invention is to provide a kind of transparent nano-calcium carbonate oil phase dispersion; It is the oil-soluble reverse micellar core-shell structure of wrapping calcium carbonate, and the core area is nano-CaCO 3 Dispersion, the shell layer is a single-layer reverse micelle structure of anionic surfactant, the solid content is 40-60wt%, the one-dimensional size is 0.5-15nm, the polydispersity index PDI is 0.05-0.3, and the base value is 400-550mgKOH / g; The present invention solves the problem of difficult dispersion and poor stability of nano-calcium carbonate in the organic matrix, and successfully prepares a transparent nano-calcium carbonate white oil phase dispersion with high solid content, high transparency and high stability

Method used

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  • Transparent nanometer calcium carbonate oil phase dispersion and its preparation method by supergravity method
  • Transparent nanometer calcium carbonate oil phase dispersion and its preparation method by supergravity method
  • Transparent nanometer calcium carbonate oil phase dispersion and its preparation method by supergravity method

Examples

Experimental program
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Effect test

Embodiment 1

[0100] (1) Surfactant synthesis section

[0101] 1) Put 410g of petroleum sulfonic acid into the stirring tank at one time, pump 95ml of sodium hydroxide (70wt%) in the lye storage tank into the stirring tank at a flow rate of 120ml / min, start the stirring tank at the same time to start stirring, and carry out the neutralization reaction. The reaction temperature is controlled by a constant temperature water tank at 50°C, and the pH at the end point is 8.2;

[0102] 2) Pump 500g of ethanol into 1) the stirring tank at a flow rate of 200ml / min, and stir evenly until the reactants are completely dissolved;

[0103] 3) Pour the above mixture into the extraction and separation tank, and after standing for 18 hours, keep the clear liquid;

[0104] 4) Pour the clear liquid into a vacuum distillation tank, the distillation temperature is 65° C., and the pressure is 0.08 MPa, and the solvent is removed to obtain a petroleum sulfonate surfactant. The fraction can be recycled and then ...

Embodiment 2

[0122] (1) Surfactant synthesis section

[0123] 1) Put 480g of alkylbenzenesulfonic acid into the stirred tank at one time, pump 100ml of ammonia water (analytical pure) in the lye storage tank into the reactor at a flow rate of 120ml / min, and start the reactor to stir at the same time, and carry out the neutralization reaction. The reaction temperature is controlled by a constant temperature water tank at 60°C, and the final pH is 8.6;

[0124] 2) Pump 550g of ethanol into 1) the stirring tank at a flow rate of 200ml / min, and stir evenly until the reactants are completely dissolved;

[0125] 3) Pour the above mixture into the extraction and separation tank, and leave the clear liquid after standing for 24 hours to separate layers;

[0126]4) Pour the clear liquid into a vacuum distillation tank, the distillation temperature is 60° C., and the pressure is 0.08 MPa, and the solvent is removed to obtain an alkylbenzene sulfonate surfactant. The fraction can be recycled and fra...

Embodiment 3

[0143] (1) Surfactant synthesis section

[0144] 1) Put 800g of petroleum sulfonic acid into the stirred tank at one time, pump 200ml of ammonia water (analytical pure) in the lye storage tank into the reactor at a flow rate of 150ml / min, start the reactor at the same time to start stirring, and carry out the neutralization reaction. The water tank controls the reaction temperature to 60°C, and the final pH is 8.3;

[0145] 2) Pump 850g of n-butanol into 1) the stirring tank at a flow rate of 200ml / min, and stir evenly until the reactants are completely dissolved;

[0146] 3) Pour the above mixture into the extraction and separation tank, and leave the clear liquid after standing for 20 hours for stratification;

[0147] 4) Pour the clear liquid into a vacuum distillation tank, the distillation temperature is 85° C., and the pressure is 0.09 MPa, and the solvent is removed to obtain a petroleum sulfonate surfactant. The fraction can be recycled and then fractionated into n-bu...

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Abstract

The invention discloses a transparent nano calcium carbonate oil-phase dispersion which is a calcium-carbonate-coated oil-soluble reverse micelle core-shell structure, wherein the core area is a nano CaCO3 dispersion, and the shell is a single-layer reverse micelle structure of an anionic surfactant. The solid content is 40-60 wt%, the one-dimensional size is 0.5-15nm, the polydispersity index (PDI) is 0.05-0.3, and the alkali number is 400-550 mgKOH / g. The transparent nano calcium carbonate oil-phase dispersion has the characteristics of high solid content, high transparency and high stability. The invention also discloses a preparation method of the transparent nano calcium carbonate oil-phase dispersion by a hypergravity process.

Description

technical field [0001] The invention belongs to the field of chemical technology and process strengthening. More specifically, it relates to a transparent nano-calcium carbonate oil phase dispersion and a method for preparing it by a high gravity method. Background technique [0002] Nano-calcium carbonate is an important alkaline component and inorganic nano-particles in industry, and its dispersion can be obtained after treatment to be used as a lubricating oil additive. The basic component nano-calcium carbonate in lubricating oil additives can effectively neutralize the inorganic acid (H 2 SO 4 / SO 2 ,HNO 3 / NO X ) and organic acids to prevent corrosion of the engine, and can be adsorbed on solid particles such as soot and sludge to make it colloidally dissolved in lubricating oil to play a role in cleaning and solubilizing; at the same time, it can also penetrate into the metal subsurface Or rub the surface, carry out physical adsorption and tribochemical reaction...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10M125/10C09C1/02C09C3/08C10N30/04C10N30/06
Inventor 陈建峰康芳王洁欣
Owner BEIJING UNIV OF CHEM TECH