Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Gasoline deep desulfurization method, and equipment used for gasoline deep desulfurization

A technology for deep desulfurization and gasoline, applied in the petroleum industry, processing hydrocarbon oil, hydrocarbon oil treatment products, etc., can solve the problems of hydrogenation catalyst poisoning and coking, unfavorable hydrotreating, reducing solvent extraction sulfide, etc.

Active Publication Date: 2018-05-08
CHINA PETROLEUM & CHEM CORP +1
View PDF10 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, studies have found that the sulfur-rich materials produced during the lye extraction process usually carry a small amount of alkali and colloids, which can easily lead to poisoning and coking of the hydrogenation catalyst when entering the hydrogenation system, while the sulfur-containing materials produced during the solvent extraction process Materials often also contain unstable impurities, which are not conducive to direct hydrogenation treatment, especially under high-temperature hydrogenation conditions in pursuit of higher desulfurization rates; on the other hand, conventional liquid-liquid solvent extraction is usually not suitable for all The sulfides are selective, and when the extracted material is separated from the extraction solvent, it is often entrained with each other (usually requires further follow-up treatment, such as washing the extracted material with water, etc.), while the positive pressure ( Above the standard atmospheric pressure), distillation of the solvent with the extracted material is difficult to recover the extraction solvent, and even leads to side reactions such as high temperature degradation of the extraction solvent, reducing the ability of the solvent to continue to extract sulfides

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Gasoline deep desulfurization method, and equipment used for gasoline deep desulfurization
  • Gasoline deep desulfurization method, and equipment used for gasoline deep desulfurization
  • Gasoline deep desulfurization method, and equipment used for gasoline deep desulfurization

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0137] This embodiment adopts figure 1 The equipment shown in Table 1 performs advanced desulfurization treatment on the gasoline feedstock A.

[0138] The gasoline raw material A is subjected to a pre-hydrogenation reaction, and the conditions of the pre-hydrogenation reaction are: use a pre-hydrogenation catalyst Cat2, the reaction temperature is 80°C, the reaction pressure is 1.0MPa, and the liquid hourly volume space velocity is 4.0h -1 , the volume ratio of hydrogen to oil is 5, and the gasoline raw material after prehydrogenation is obtained.

[0139] The aforementioned pre-hydrogenated gasoline raw material is fractionated into light fraction, middle fraction and heavy fraction. The fractionation temperature of light fraction and middle fraction is 60°C, and the fractionation temperature of middle fraction and heavy fraction is 120°C. The yields (by mass fraction) of light fraction, middle fraction and heavy fraction after fractionation are about 20%, 45%, and 35%, res...

Embodiment 2

[0166] This embodiment adopts figure 1 The equipment shown is for advanced desulfurization of gasoline feedstock E.

[0167] The gasoline raw material E is subjected to a pre-hydrogenation reaction, and the conditions of the pre-hydrogenation reaction are: use a pre-hydrogenation catalyst Cat2, the reaction temperature is 100°C, the reaction pressure is 1.2MPa, and the liquid hourly volume space velocity is 5.0h -1 , the volume ratio of hydrogen to oil is 5, and the gasoline raw material after prehydrogenation is obtained.

[0168] The aforementioned pre-hydrogenated gasoline raw material is fractionated into light fraction, middle fraction and heavy fraction. The fractionation temperature of light fraction and middle fraction is 55°C, and the fractionation temperature of middle fraction and heavy fraction is 120°C. The yields (in terms of mass fraction) of light fraction, middle fraction and heavy fraction after fractionation are about 25%, 35%, and 40%, respectively.

[01...

Embodiment 3

[0183] This embodiment is carried out with the same raw material oil E and the same combined desulfurization process and the same process parameters as in Example 2, the difference is:

[0184] The extraction solvent used in the solvent extraction process of this example does not contain additives, and the rest are the same as in Example 2. As a result, the sulfur content in the middle fraction after solvent extraction is ≯10 μg / g.

[0185] After selective hydrogenation, the hydrogenated heavy fraction is obtained, and the sulfur content in the hydrogenated heavy fraction is ≯10 μg / g.

[0186] Mix light distillate, solvent extracted middle distillate and hydrogenated heavy distillate to form low-sulfur gasoline product H; or mix etherified distillate and hydrogenated heavy distillate to produce low-sulfur, low-olefin gasoline product I.

[0187] The properties of gasoline product H and gasoline product I are shown in Table 4.

[0188] It can be seen from Table 4 that the desu...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
boiling pointaaaaaaaaaa
Login to View More

Abstract

The invention belongs to the field of hydrocarbons refining, and discloses a gasoline deep desulfurization method and equipment used for gasoline deep desulfurization. The gasoline deep desulfurization method comprises following steps: 1, gasoline raw material is subjected to pre-hydrogenation so as to obtain pre-hydrogenated gasoline raw materials; 2, the pre-hydrogenated gasoline raw materials are subjected to fractionation so as to obtain light fractions, medium fractions, and heavy fractions; 3, the medium fractions are contacted with an extraction solvent so as to obtain a sulfur-containing solvent and solvent-extracted medium fractions, separation is adopted to separate the sulfur-containing solvent from sulfides contained by the sulfur-containing solvent so as to obtain a solvent extracted sulfur-containing material and a recycled sulfide-free solvent; 4, the heavy fractions are subjected to selective hydrogen desulfurization reaction so as to obtain hydrogenated heavy fractions; and 5, the light fractions, the solvent extracted medium fractions, and the hydrogenated heavy fractions are mixed so as to obtain gasoline products. The gasoline deep desulfurization method is capable of obtaining gasoline products lower in sulfur content without large reduction of octane value.

Description

technical field [0001] The present invention relates to the refining field of hydrocarbon materials, in particular, to a method for deep desulfurization of gasoline and a device for deep desulfurization of gasoline, and more specifically, to a kind of sulfur-containing gasoline through hydrogenation and non-hydrogenation A combination of deep desulfurization process. Background technique [0002] As we all know, the emission of toxic and harmful substances in automobile exhaust seriously affects the air quality. For this reason, countries all over the world have set stricter and stricter standards for the quality of oil used as engine fuel. From January 1, 2013, my country has implemented No. IV emission standards nationwide, and has implemented No. V emission standards in Beijing, Shanghai and other major cities. No. Ⅳ and No. Ⅴ emission standards respectively stipulate that the sulfur content in motor gasoline shall not exceed 50 μg / g and 10 μg / g. [0003] The sulfur in ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/04C10G67/10C10G67/14
CPCC10G67/0418C10G67/10C10G67/14C10G2300/104C10G2300/1044C10G2300/202C10G2300/305C10G2400/02
Inventor 潘光成李涛赵杰赵丽萍习远兵唐文成褚阳常春艳吴明清陶志平田龙胜李明丰胡志海
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products