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Delaying coking non-silicon defoaming agent with multiple active components and preparation method thereof

A non-silicon defoamer, delayed coking technology, applied in chemical instruments and methods, foam dispersion/prevention, chemical/physical process, etc., can solve the problem of low efficiency, slow penetration and diffusion, and high temperature resistance of non-silicon defoamer It can achieve the effect of large spreading coefficient, small dosage and good compatibility

Active Publication Date: 2010-07-21
JIANGSU SAIOUXINYUE DEFOAMER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN1919439 directly compounded polymethylsiloxane with polyether fatty acid ester and organosilicon compound, which can achieve a defoaming rate of more than 50% in the coking tower, but still has the problem of high silicon content
The defoamer does not contain any silicon element, and will not affect the downstream hydrogenation process and the quality of the final light oil product, but its disadvantage is that the active components are not enough, and the penetration and diffusion in the tower are slow, so it must be processed under high pressure ( 100 ~ 200ppm) to achieve a high defoaming rate, while poor high temperature resistance
[0004] From the existing patent information and the information on delayed coking defoamers on the market, it can be seen that silicon-containing defoamers will inevitably affect the subsequent hydrofining process and the quality of the final light oil product, while non-silicon defoamers have low efficiency , large dosage, low defoaming rate at high temperature, etc.

Method used

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  • Delaying coking non-silicon defoaming agent with multiple active components and preparation method thereof
  • Delaying coking non-silicon defoaming agent with multiple active components and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Add the starter ethanol and the catalyst sodium hydroxide into the autoclave, feed ethylene oxide and propylene oxide at a temperature of 130°C and a pressure of 0.5 MPa, and the molar ratio of ethylene oxide to propylene oxide is 50 : 100, keep warm for 5h, cool, filter and refine to obtain polyether.

[0026] Mix isooctyl alcohol and stearyl alcohol at a weight ratio of 80:20 at room temperature for 15 minutes to obtain a higher carbon alcohol mixture.

[0027] Weigh 30g of polyether, 35g of higher alcohol mixture, 15g of octadecyl stearate and 20g of paraffin into the reaction kettle, stir, slowly raise the temperature to 50°C, react for 2 hours, and finally end the stirring, cool and filter to remove The solid impurities are the defoamer product with a viscosity of 350cs.

Embodiment 2

[0029] The preparation of polyether is the same as in Example 1.

[0030] Weigh 40g of polyether, 35g of higher alcohol mixture, 10g of octadecyl stearate and 15g of hydrogenated diesel oil into the reaction kettle, stir, slowly raise the temperature to 100°C, react for 1 hour, and finally end the stirring, after cooling Filter to remove solid impurities to obtain a defoamer product with a viscosity of 380cs.

Embodiment 3

[0032] The preparation of polyether is the same as in Example 1.

[0033] Add polyether, stearic acid and toluenesulfonic acid into the reaction kettle, react at 160°C for 4 hours under stirring, lower the temperature to 50°C, adjust the pH value to neutral with potassium hydroxide aqueous solution, and finally use saturated chlorination The sodium solution extracts and removes the salt impurities to obtain the modified polyether.

[0034] Mix 3-heptanol and cetyl alcohol at a weight ratio of 70:30 at room temperature for 15 minutes to obtain a mixture of higher alcohols.

[0035]Weigh 50g of modified polyether, 25g of higher carbon alcohol mixture, 10g of ethylene bisstearamide and 15g of kerosene into the reaction kettle, stir, slowly raise the temperature to 80°C, react for 1.5 hours, and finally stop the stirring, cool and filter to remove The solid impurity namely obtains the defoamer product that viscosity is 480cs.

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Abstract

The invention discloses a delaying coking non-silicon defoaming agent with multiple active components and a preparation method thereof, and the defoaming agent is formed by compounding 30-50 parts by weight of polyether or modified polyether polymer, 25-35 parts by weight of high-carbon alcohol mixture, 10-15 parts by weight of high-carbon alcohol fatty acid ester or fatty acyl amide and 15-20 parts by weight of alkymer. The preparation method of the defoaming agent comprises the following steps: adding the polyether or the modified polyether polymer, the high-carbon alcohol mixture, the high-carbon alcohol fatty acid ester or the fatty acyl amide and the alkymer into a reaction kettle according to the proportion, stirring, slowly increasing the temperature to 50-100 DEG C, carrying out reaction for 1-2h, finally stopping stirring, cooling, filtering for removing solid impurities and finally preparing the delaying coking non-silicon defoaming agent. The defoaming agent can effectively suppress and eliminate the formation of bubbles in a delayed coking reaction tower, improve the treatment capacity of the reaction tower, prolong the coking time of coke and prevent clogging phenomenon.

Description

technical field [0001] The invention relates to a defoamer and a preparation method thereof, in particular to a delayed coking non-silicon defoamer with multiple active components and a preparation method thereof. Background technique [0002] Delayed coking technology is one of the most important processing methods for the lightening of residual oil. It has the characteristics of low investment and operating costs, strong adaptability to different raw materials, and mature technology. Over the years, my country's crude oil has generally been heavy in oil quality, high in wax content, and low in diesel yield, resulting in a prominent contradiction between the supply and demand of diesel-gasoline ratio. At present, my country imports about 80×10 4 tons of diesel, while having to export 30×10 4 tons of gasoline in order to balance domestic supply and demand. The light oil product of delayed coking technology has a high diesel-gasoline ratio (1.94 for delayed coking and 0.56...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01F17/42B01F17/34B01F17/22B01F17/08B01D19/04C09K23/42C09K23/08C09K23/22C09K23/34
Inventor 杨柏忠
Owner JIANGSU SAIOUXINYUE DEFOAMER
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