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

Method for comprehensive oil gas recovery

A recovery method, oil and gas technology, applied in the direction of liquid hydrocarbon mixture recovery, separation methods, chemical instruments and methods, etc., can solve the problems of high investment and operating costs of regeneration equipment, high feed temperature, high vacuum degree, etc., and achieve operating costs Low, high absorption efficiency, efficient recovery effect

Active Publication Date: 2013-02-06
CHINA PETROLEUM & CHEM CORP +1
View PDF3 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] For the oil and gas absorption process using special absorbents, there is generally a regeneration process of the absorbent after absorbing oil and gas (absorbents after absorbing oil and gas are called rich absorbents); Diesel oil can not be regenerated, and can be further processed in downstream processing procedures, such as hydrotreating or entering a fractionation tower. Since the absorbed oil and gas are also hydrocarbons, it does not affect the normal operation of downstream processing, but some occasions do not have the source of gas oil. , such as gasoline transportation, sales and other enterprises, so the scope of application of gas oil as the absorbent has certain limitations; for the absorption process using commercial diesel as the absorbent, since the absorbed oil gas belongs to the low-carbon hydrocarbons in gasoline , the rich absorbent is highly volatile, and if the rich absorbent is not regenerated, the indicators such as the flash point and distillation range of the diesel oil will be unqualified, but to completely desorb the oil gas entering the diesel oil, a higher degree of Vacuum degree and higher feed temperature, regeneration equipment investment and operating costs are higher

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
  • Method for comprehensive oil gas recovery
  • Method for comprehensive oil gas recovery

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] In this example, the source of oil and gas is the oil and gas produced during the loading process of gasoline. The volume content of light hydrocarbons in the oil and gas is 30%. Commercial diesel oil No. 10 is used as the absorbent for absorption treatment. The measured flash point is 69°C. use as figure 1 the process described. The working fluid of the liquid ring compressor is commercial diesel oil at 5°C refrigerated by the refrigeration unit, and the working fluid of the liquid ring compressor is operated in one pass. 40% to 60% (volume) of oil and gas can be recovered in the steps of liquid ring compressor and outlet oil and gas condensation. The commercial diesel absorbent entering the absorption packing tower is cooled to 5°C by the refrigerating unit. The operating condition of the absorption packing tower is that the volume ratio of fresh absorbent diesel to oil and gas is 0.2, and the design value of the volume flow space velocity of oil gas to packing at th...

Embodiment 2

[0036] In this example, the source of oil and gas is the oil and gas produced by volatilization of gasoline storage tanks. The volume content of hydrocarbons in the oil and gas is 25%. Commodity diesel-20 diesel oil is used as the absorbent for absorption treatment. The measured flash point is 63°C. The commercial diesel absorbent entering the absorption packing tower is cooled to -10°C by the refrigerating unit (the working fluid of the liquid ring compressor is also the -10°C commercial diesel oil), and the operating condition of the absorption packing tower is that the volume ratio of fresh absorbent diesel to oil gas 0.04, the design value of the volume flow space velocity of the oil gas at the inlet of the packed tower to the packing is 500h -1 , The operating pressure of the absorption packed tower is 0.2MPa (gauge pressure). After absorption, the exhaust gas oil and gas content is lower than 12g / m 3 .

[0037] After heat exchange and temperature rise of the rich absor...

Embodiment 3

[0040] In this example, the source of oil and gas is the oil and gas produced by the volatilization of gasoline storage tanks. The volume content of hydrocarbons in the oil and gas is 25%, and commercial diesel No. 0 diesel oil is used as the absorbent for absorption treatment. The temperature is 270°C. The commercial diesel absorbent entering the absorption packing tower is cooled to 10°C by the refrigerating unit (the working fluid of the liquid ring compressor is also the 10°C commercial diesel oil). The operating condition of the absorption packing tower is that the volume ratio of fresh absorbent diesel to oil gas is 0.1 The design value of the volume flow space velocity of the oil gas to the filler at the inlet of the packed tower is 600h -1 , The operating pressure of the absorption packed tower is 0.6MPa (gauge pressure). After absorption, the exhaust gas oil and gas content is lower than 10g / m 3 .

[0041] After heat exchange and temperature rise, the rich absorben...

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
Flash pointaaaaaaaaaa
Flash pointaaaaaaaaaa
Login to View More

Abstract

The present invention discloses a method for comprehensive oil gas recovery, including an oil gas absorption process and a rich absorbent regeneration process. Commercial diesel oil is used as the oil gas absorbent for the oil gas absorption process. The temperature of the absorbent entering an absorption tower is -20 to 20 DEG C. The oil gas is compressed to 0.2-1MPa via a liquid ring compressor. The liquid ring compressor-pressurized oil gas exchanges heat with the rich absorbent discharged from the absorption tower for cooling. Oil gas condensed to be liquid phase is recovered, while un-condensed oil gas is fed into the absorption tower and in countercurrent contact with the absorbent in the absorption tower. The rich absorbent absorbed the oil gas is discharged from the absorption tower; and is desorbed after being heated via heat exchange. Commercial diesel oil is used as operating fluid for the liquid ring compressor, and the operating fluid is once-through. The operating fluid discharged from the liquid ring compressor, together with the rich absorbent discharged from the absorption tower, is desorbed by means of appropriate vacuum, and then is fed into a commercial diesel tank. Compared with the prior art, the method of the present invention has advantages of a reasonable technological process, high oil gas recovery efficiency, low investment in equipment and operating costs, etc.

Description

technical field [0001] The invention provides a comprehensive oil gas recovery method, in particular a gasoline or light hydrocarbon oil gas recovery method using commercial diesel oil as an absorbent. Background technique [0002] In the process of crude oil extraction, transportation, storage, transfer, processing and crude oil processing products (gasoline, kerosene, diesel oil, etc.) , which generally contain air and other components) escape into the atmosphere, and in some chemical solvents such as benzene, toluene, xylene production workshops, paints and other organic solvents, there are also light hydrocarbons with similar properties and high volatility point. [0003] On the one hand, the oil and gas dissipated into the air waste a lot of energy, causing huge economic losses, and on the other hand, reduce the quality of oil products. Moreover, since the explosion limit of oil and gas is 1%~6% (volume), the concentration of oil and gas around the escaped oil and gas...

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
IPC IPC(8): C10G5/04B01D53/14
Inventor 刘忠生方向晨朴勇郭兵兵王海波
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