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A kind of isopropanol urea dewaxing method

A technology of isopropanol and dewaxing, which is applied in the recovery/refining of mineral wax, petroleum industry, and only multi-stage serial refining process treatment, etc. It can solve the problems of low water temperature requirements, pipeline blockage, and reduced heat exchange effect. To achieve the effect of simplifying the process, good protection, and saving low-temperature water resources

Active Publication Date: 2016-02-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Due to the isopropanol aqueous solution urea dewaxing technology, when water is used as the refrigerant, the reaction system needs a large amount of cooling water, and the water temperature requirement is also low, and the heat exchange method is indirect heat exchange, which will cause the reactor directly in contact with the cooling medium water The wall temperature is lower than the temperature inside the reactor, the urea and the normal alkanes in the raw oil will react on the wall to form a complex, and attach to the tube wall to form a wall phenomenon, which reduces the heat transfer effect. It is easy to block the pipeline for a long time and affect the normal production

Method used

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  • A kind of isopropanol urea dewaxing method
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  • A kind of isopropanol urea dewaxing method

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Embodiment 1

[0023] The raw material oil used in the present embodiment is the second-line distillate oil of Daqing, and the properties of the raw material are beneficial to Table 1, and the cooling medium is one of the urine composition isopropanol, and the urine composition and reaction process conditions are as Table 2 and Table 3,

[0024] The washing oil is distillate oil with a distillation range of 120-160 DEG C, and the complex is washed under the final temperature condition of the complex reaction. Then the complex is heated to 60-70°C to decompose into wax liquid and urine, the wax liquid is washed with water, and the urine is circulated back to the urine tank. The specific results are shown in Table 4.

[0025] Table 1 Raw Oil Properties

[0026]

[0027] Table 2 Composition of isopropanol urine solution

[0028]

[0029] Table 3 reaction process conditions

[0030]

[0031] Table 4 embodiment result

[0032]

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Abstract

The invention relates to a dewaxing method of isopropanol urea. The dewaxing method specifically comprises the following steps: mixing raw material oil with an isopropanol urea water solution, adding the mixed solution into a reactor, carrying out complexation, operating the reactor under a reduced pressure condition, circulating gaseous effluent on the top of the reactor back to the reactor after cooling, returning partial reactants obtained at the bottom of the reactor to the reactor, and carrying out subsequent separation on the rest reactants by virtue of a decomplexation settling and washing tower. According to the dewaxing method, by virtue of reduced pressure operation, heat released by complexation of n-alkanes in the urea and the raw martial oil is absorbed when isopropanol and water in the isopropanol urea water solution are converted from a liquid state to a gas state by virtue of gasification, so that the requirement of complexation to the temperature is met; other cooling mediums do not need to be introduced, so that the defect that the reaction temperature is controlled by virtue of a large amount of underground water in the prior art is overcome, and the underground water resource is saved; the technique can be further applied to areas which are relatively deficient in water resources.

Description

technical field [0001] The invention relates to a dewaxing method, in particular to an isopropanol urea aqueous solution complexation reaction dewaxing method. Background technique [0002] The urea dewaxing technology uses the basic principle of contacting urea molecules with n-alkane to form helical hexagonal crystals around n-alkane to form a complex that is immiscible with oil, thereby separating n-alkane from oil. The pore size of the helical hexagonal crystal is 0.525nm, which can also be regarded as an organic molecular sieve with a single pore size. [0003] Isopropanol urea dewaxing is to mix urea with a certain proportion of water and isopropanol, and heat the mixture until the urea is completely dissolved to form a uniform solution. After the contact of alkanes, the temperature of the reaction mixture is gradually reduced, and the urea and n-alkanes react to form an oil-insoluble complex, so that the n-alkanes (wax) are released from the oil. As the reaction tem...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G73/22C10G53/04
CPCC10G53/04C10G73/22C10G2300/20
Inventor 苏重时姚春雷李景斌刘灏
Owner CHINA PETROLEUM & CHEM CORP
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