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Effective non-polymeric and non-fouling additives for inhibiting high temperature naphthenic acid corrosion and methods of use thereof

A non-polymer, corrosion-inhibiting technology, applied in the composition of drilling holes, corrosion/fouling inhibition of treatment equipment, separation methods, etc., can solve problems such as side-stream contamination of distillates

Inactive Publication Date: 2016-09-07
DORF KETAL CHEM (I) PTE LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, its high oil solubility raises the risk of contamination of distillate side draws by phosphorus-containing compounds

Method used

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  • Effective non-polymeric and non-fouling additives for inhibiting high temperature naphthenic acid corrosion and methods of use thereof
  • Effective non-polymeric and non-fouling additives for inhibiting high temperature naphthenic acid corrosion and methods of use thereof
  • Effective non-polymeric and non-fouling additives for inhibiting high temperature naphthenic acid corrosion and methods of use thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0066] To a clean four necked round bottom flask kept in a 30°C oil bath was added 733.4 gm of 2-ethyl-hexanol and a nitrogen purge was initiated. A total of 266.5 gm of phosphorus pentoxide was added to the flask in six portions. After adding phosphorus pentoxide to the flask, an exotherm was observed. After the phosphorus pentoxide addition was complete, the temperature of the reaction mixture was raised to 99°C and maintained at this temperature for 4 hours.

[0067] The reaction mixture was cooled to 30°C-35°C, filtered, and analyzed for acid number and phosphorus content by inductively coupled plasma (ICP) method.

[0068] The acid number was found to be in the range of 280 to 330 mg KOH / gm. Typical acid value is 308mgKOH / gm. Phosphorus content is in the range of 10 to 12%. A typical phosphorus content value is 11.65%. The reaction mixture obtained in Example 1 is a prior art naphthenic acid corrosion inhibiting additive. The test results of Example 1 are given in T...

Embodiment 2

[0070] Into a clean four necked round bottom flask kept in an oil bath at 30°C was added 200 gm of the reaction mixture of Example 1. 150 gm of butylene oxide was slowly added to the reaction mixture. An exotherm was observed and the temperature was maintained below 40°C until a total of 150 gm of butylene oxide addition was complete. Samples of the resulting chemical mixture were taken intermittently and analyzed for acid value. The reaction was continued until the acid number was 10 mgKOH / gm.

[0071] The resulting reaction mixture was then heated to a temperature of 60° C. and kept at this temperature for 2 hours.

[0072] The resulting reaction mixture was cooled to 30°C-35°C, filtered, and analyzed by ICP method for acid value and phosphorus content.

[0073] The acid number was found to be less than 10 mg KOH / gm. A typical acid number is 1 mg KOH / gm. Phosphorus content is in the range of 5 to 7%. A typical phosphorus content value is 6.53%. The reaction mixture ob...

Embodiment 3

[0075] To a clean four necked round bottom flask kept in a 30°C oil bath was added 486 gm of 2-ethyl-hexanol and a nitrogen purge was initiated. A total of 265 gm of phosphorus pentoxide was added to the flask in six portions. After adding phosphorus pentoxide to the flask, an exotherm was observed. After the phosphorus pentoxide addition was complete, the temperature of the reaction mixture was raised to 99°C and maintained at this temperature for 4 hours.

[0076] The reaction mixture was cooled to room temperature of 30°C, filtered, and analyzed by ICP method for acid value and phosphorus content.

[0077] The acid number was found to be in the range of 320 to 350 mg KOH / gm. Typical acid value is 331mgKOH / gm. Phosphorus content is in the range of 14 to 16%. A typical phosphorus content value is 15.408%. The reaction mixture obtained in Example 3 is a prior art naphthenic acid corrosion inhibiting additive. The test results of Example 3 are given in Table 1.

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Abstract

The present invention relates to a method of inhibiting high temperature naphthenic acid corrosion that occurs in hydrocarbon processing equipment. The present invention provides effective novel non-polymeric and non-fouling additives for inhibiting high temperature naphthenic acid corrosion comprising an effective corrosion inhibiting amount of a second phosphoric acid ester, wherein the second phosphoric acid ester is obtained by combining the first phosphoric acid ester with The alkylene oxide compound selected from butylene oxide, ethylene oxide, propylene oxide or any other alkylene oxide compound or their combination is preferably obtained by reaction with butylene oxide which is capable of producing a compound having structure A or B The second phosphoric acid ester, in formula (A) and (B), wherein R 1 and R 2 Each is independently selected from moieties having 1 to 20 carbon atoms, and R 1 and R 2 Can be the same or different, X is H, CH 3 or C 2 h 5 and n can vary between 1 and 20, wherein the first phosphate has structure I or II, in formulas (I) and (II), wherein R 1 and R 2 Each is independently selected from moieties having 1 to 20 carbon atoms, and R 1 and R 2 Which may be the same or different, said first phosphate is obtained as a reaction product of an alcohol and phosphorus pentoxide.

Description

technical field [0001] This invention relates to inhibiting the corrosion of metals in acidic hot hydrocarbons, in particular to inhibiting the corrosion of ferrous metals in hot acidic hydrocarbons, especially when the acidity is derived from the presence of naphthenic acids, and more particularly to achieving corrosion Inhibitory effective non-polymeric and non-staining additives and methods of use thereof. Background technique [0002] It is well known in the art that the processing of crude oil and its various fractions causes damage to pipelines and other associated equipment due to naphthenic acid corrosion. These are corrosive to equipment used to distill, extract, transport and process crude oil. In general, naphthenic acid corrosion occurs when the neutralization number or total acid number (TAN) (expressed as the number of milligrams of potassium hydroxide required to neutralize the acid in 1 gram of sample) of the crude oil being treated exceeds 0.2 . It is als...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G7/10C02F5/14C10L1/26C10L1/04C23F11/167
CPCC02F2303/08C09K8/524C09K8/54C10G7/00C10G7/10C10G75/02C10G2300/1033C10G2300/203C10G2300/4075C10G2300/80B01D3/34C23F11/04
Inventor 马赫什·苏布拉马尼亚姆
Owner DORF KETAL CHEM (I) PTE LTD