Unlock instant, AI-driven research and patent intelligence for your innovation.

A method for catalytic reaction rectification separation and cracking of carbon five and its catalytic reaction rectification tower

A catalytic reaction, rectification separation technology, applied in distillation purification/separation, fractionation, addition of unsaturated hydrocarbons to hydrocarbons, etc., can solve the problems of low conversion rate and short residence time, and achieve higher yield and easier reaction , the effect of increasing the reaction speed

Active Publication Date: 2018-01-02
HEBEI UNIV OF TECH
View PDF9 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to provide a method for catalytic reaction rectification separation and cracking of carbon five and a catalytic reaction rectification tower for the problems of short residence time and low conversion rate in the application of current reactive distillation technology to the separation process of carbon five
This method adds a high-efficiency catalyst on the basis of the original reactive distillation to form a catalytic reactive distillation. By installing a preset bolt assembly on the tray, a fixed ring, and the catalyst is packaged in the fixed frame, and the height of the catalyst is adjusted through the nut, Thereby solving the problem of catalytic reaction and rectification separation and segmentation, as well as the problem of catalyst installation and fixation

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
  • A method for catalytic reaction rectification separation and cracking of carbon five and its catalytic reaction rectification tower
  • A method for catalytic reaction rectification separation and cracking of carbon five and its catalytic reaction rectification tower
  • A method for catalytic reaction rectification separation and cracking of carbon five and its catalytic reaction rectification tower

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 300kg. The operating conditions are: tower top pressure 0.25MPa, tower top temperature 55.6°C, tower bottom temperature 87°C, reflux ratio 8, space velocity 4h -1 . After running normally, the measured test results are shown in Table 2.

[0045] Table 2

[0046] component name

[0047]...

Embodiment 2

[0054] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 300kg. The operating conditions are: tower top pressure 0.2MPa, tower top temperature 47.8°C, tower bottom temperature 82°C, reflux ratio 6, space velocity 5h -1 . After running normally, the measured test results are shown in Table 4.

[0055] Table 4

[0056] Composition

[0057] ...

Embodiment 3

[0060] The method and device thereof of present embodiment catalytic reaction rectification separation cracking carbon five are as above-mentioned, and concrete operation parameter is: catalytic reaction rectification tower, tower diameter 2m, rectifying section 2m packing (equivalent to 30 theoretical trays ), 2m packing (equivalent to 30 theoretical trays) in the stripping section, 30 layers of catalytic reaction rectification trays in the catalytic reaction section, the number of hoods on the trays in the catalytic reaction section is 24, and the total number of catalyst bags in each layer The area is 1.25m 2 , with a volume of 0.15m 3 , The quality of each layer of catalyst is 250kg. The operating conditions are: tower top pressure 0.3MPa, tower top temperature 62.5°C, tower bottom temperature 93°C, reflux ratio 4, space velocity 6h -1 . After running normally, the measured test results are shown in Table 5.

[0061] table 5

[0062] Composition

[0063] Res...

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
diameteraaaaaaaaaa
lengthaaaaaaaaaa
heightaaaaaaaaaa
Login to View More

Abstract

The invention relates to a catalytic reaction rectification method for separating and cracking carbon five and a catalytic reaction rectification tower thereof. The method comprises the following steps: (1) Adding cracked C5 raw materials into the catalytic reaction section of the catalytic reaction rectification tower, contacting with the catalyst installed on the tray for catalytic reaction, the dicyclopentadiene and piperylene produced And other heavy components in the raw material are concentrated downward through the stripping section and enter the tower kettle, and the dicyclopentadiene product is obtained through the piperylene separation tower and the carbon six separation tower; (2) light isoprene-based The components are refined from the catalytic reaction section upwards through the rectification section and enter the top condenser. After condensation, they are extracted and separated by the extraction tower to obtain the isoprene product. The addition of the high-efficiency catalyst of the invention reduces the reaction conditions, makes the reaction easier, and the reaction speed increases rapidly. Under the same conditions, compared with the ordinary rectification column: the conversion rate increased by 5.57%, and the yield increased by 5.49%.

Description

technical field [0001] The invention relates to a method for catalytic reaction rectification, separation and cracking of carbon five and a catalytic reaction rectification tower. Background technique [0002] In the process of producing ethylene from petroleum cracking, a large number of by-product C5 fractions will be produced. These C5 fractions can account for 15% to 20% of the ethylene production. The C5 fractions are rich in isoprene, cyclopentadiene and piperylene Alkenes and other diolefins account for about 40% to 60% of the C5 fraction. These diolefins are active in chemical properties and are important chemical raw materials. With the continuous increase of ethylene production, making full use of this part of resources is of great significance to reduce the cost of ethylene plants and comprehensively utilize petroleum resources. [0003] The traditional process for separation of C5 fractions usually starts with the thermal dimerization of cyclopentadiene to conve...

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 Patents(China)
IPC IPC(8): C07C13/61C07C11/20C07C11/18C07C7/04C07C2/52B01D3/14
Inventor 刘继东刘国成吕建华边超刘爽李扬
Owner HEBEI UNIV OF TECH