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Preparation method of high-magnesium-content alkylbenzene magnesium sulfonate

A technology of magnesium alkyl benzene sulfonate and content, applied in the petroleum industry, additives, lubricating compositions, etc., can solve the problems of low flash point and inconvenience of products

Inactive Publication Date: 2018-09-14
XINXIANG RICHFUL LUBE ADDITIVE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the addition of fuel oil at the later stage of the production process results in a low flash point of the product, which is inconvenient to be used in the field of engine oil with high flash point requirements.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0020] The preparation method of the present invention mainly uses the following raw materials to prepare magnesium alkylbenzene sulfonate with high magnesium content, wherein each raw material is calculated by mass parts: 40-70 parts of base oil, 1.5-2.5 parts of α-olefin, 1-2.0 parts of maleic anhydride 20-25 parts of sulfonic acid, 5-10 parts of methanol, 30-45 parts of magnesium oxide, 100-300 parts of diluent oil, 3-6 parts of acids, 20-30 parts of water, and 40-45 parts of carbon dioxide.

[0021] The distillation range of the above base oil is 250-350°C, the molecular weight of α-olefin is 168-252, the magnesium content of magnesia is 96%-98%, and magnesia is added in two times, the magnesia added for the first time The amount of magnesium oxide added is 5-10 parts, and the amount of magnesium oxide added for the second time is 25-35 parts. Sulfonic acid is one of heavy alkylbenzenesulfonic acid, long-chain linear alkylbenzenesulfonic acid or a mixture of both. The dis...

no. 1 example

[0023] First add 61g of base oil, 2g of α-olefin (average molecular weight 252), 1.5g of maleic anhydride in the reaction flask, and then react for 300 minutes at a temperature of 190-200°C. During the reaction, the stirring speed of the materials in the reaction flask 400r / min. After the completion of the reaction, cool the reacted material to 45°C and continue to add 25g of heavy alkylbenzenesulfonic acid, 10g of methanol and 10g of magnesium oxide with a magnesium content of 96% in the reaction flask, then react for 30 minutes and increase the stirring speed to 600r / m Min, continue to add toluene 150g, alkyl salicylic acid 5g in above-mentioned reaction bottle, and continue to add surplus magnesia 30g, water 26g, then begin to pass into 40g carbonic acid gas at a constant speed continuously in reaction bottle for 5 hours and carry out carbonation reaction, And control the temperature in the reaction bottle to keep at 45-50°C until the carbonation reaction ends.

[0024] Af...

no. 2 example

[0027] First add 58g of base oil, 1.5g of α-olefin (average molecular weight 168), and 1.0g of maleic anhydride to the reaction flask, and then react at a temperature of 180-190°C for 200 minutes. During the reaction, the materials in the reaction flask are stirred The speed is 400r / min. After the reaction was completed, the reacted material was cooled to 45° C., then continued to add 30 g of long-chain linear alkylbenzenesulfonic acid, 7 g of methyl alcohol and 5 g of magnesium oxide with a magnesium content of 98% in the reaction flask for 30 minutes, and the stirring speed was increased. to 600r / min, then continue to add 200g of isobutanol, 5g of formic acid in the above-mentioned reaction flask, and continue to add surplus magnesium oxide 33g, water 28g, then start to feed 40g of carbon dioxide into the reaction flask at a constant speed for 5 hours continuously for carbonation React, and control the temperature in the above-mentioned reaction bottle to remain at 50-53° C....

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Abstract

The invention discloses a preparation method of a high-magnesium-content alkylbenzene magnesium sulfonate. The preparation method comprises, firstly, adding base oil, alpha-olefin and maleic anhydrideinto a reaction flask for reaction at 180-200 DEG C for 150-300 minutes; secondly, adding sulfonic acid, methanol and magnesium oxide into the reaction flask for reaction at 40-60 DEG C for 30-90 minute; thirdly, adding cutback oil and acids into the reaction flask, then adding in magnesium oxide and water, continuously inletting carbon dioxide for carbonation reaction, and controlling the temperature inside the reaction flask to be 45-60 DEG C until the carbonation reaction is completed; fourthly, distilling methanol, water and a part of cutback oil out of the materials inside the reaction flask; lastly, performing centrifugal slag removal and reduced pressure distillation on the materials to remove the cutback oil to obtain finished products. The prepared high-magnesium-content alkylbenzene magnesium sulfonate has the advantages of being high in alkali value, magnesium content, flashing point and stability.

Description

technical field [0001] The invention relates to the technical field of preparation of metal detergents and dispersants, in particular to a preparation method of magnesium alkylbenzene sulfonate with high magnesium content. Background technique [0002] Magnesium alkylbenzene sulfonate is a sulfonate metal detergent and dispersant product, which is characterized by high base value, low ash content, strong neutralization ability, and good detergency and rust resistance. It is not only used as a medium and high-grade internal combustion engine oil It is a detergent and dispersant, and it can also be used as an inhibitor in some fuel oils, so it has a wide range of application scenarios. [0003] Patent No. CN1229840 discloses a process of using alkylbenzenesulfonic acid and other additives to form a neutral salt with high-activity magnesium oxide at room temperature, and disperse magnesium oxide at high temperature to form an oil-soluble anti-vanadium additive. The magnesium co...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10M159/24C10N20/02
CPCC10M159/24C10M2219/046C10N2020/02
Inventor 卜卫元李学文范金凤乔庆文
Owner XINXIANG RICHFUL LUBE ADDITIVE CO LTD