A method for preparing needle coke raw material
A technology for needle coke raw materials and raw materials, which can be applied to coking carbon-containing materials, coke ovens, petroleum industry, etc., can solve problems such as affecting the quality of needle coke, difficulty in needle coke products, and large investment.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
preparation example Construction
[0017] According to the method for preparing needle coke raw material of the present invention, the method comprises injecting part of the delayed coking raw material and catalytic cracking oil slurry into the lower part of the coking fractionation tower, and injecting the fractionation tower bottom containing the partial delayed coking raw material and catalytic cracking oil slurry into The oil is injected into the upper part of the coke tower, and another part of the delayed coking raw material is injected into the bottom of the coke tower after being heated by the radiant section of the heating furnace, and the delayed coking reaction is carried out, and the oil and gas produced by the delayed coking reaction are fractionated to obtain the wax oil component, and the obtained The wax oil component is steam stripped to obtain needle coke raw materials; wherein, during the delayed coking reaction process, cooling oil and / or cooling water are injected into the top of the coke tow...
Embodiment 1
[0052] This example is used to illustrate the preparation method of the needle coke raw material provided by the present invention.
[0053] This embodiment adopts figure 1 process shown. The ratio of vacuum residue 1 (i.e. delayed coking raw material, whose relevant parameters are shown in Table 1) to catalytic cracking oil slurry 9 (related parameters are shown in Table 1) is 75:25; in addition, the vacuum residue 1 Based on the total weight of the heating furnace, the convection section 4 and the radiation section 5 are heated successively, and then the consumption of the vacuum residue 1 entering the bottom of the coke drum is 90% by weight.
[0054] After heat exchange between delayed coking raw material 1 and coker diesel oil, coker wax oil and coker heavy wax oil ( figure 1 (not marked in ) is divided into two paths, one path passes through the convection section 4 and the radiation section 5 of the heating furnace in turn to be heated to 500°C, and then enters the bo...
Embodiment 2
[0060] This example is used to illustrate the preparation method of the needle coke raw material provided by the present invention.
[0061] Adopt the method of embodiment 1 to carry out, difference is: the ratio of vacuum residue oil and catalytic cracking oil slurry is 70:30; 501°C; the pressure of the coke tower is 0.16MPa; the sum of the non-catalytic cracking oil slurry and delayed coking raw material components in the fractionation tower bottom oil and the catalytic cracking oil slurry and delayed coking raw material components contained in the fractionation tower bottom oil The weight ratio is 0.25: 1; the length of the feed position on the coke drum from the lower end of the cylinder accounts for 9 / 10 of the entire cylinder length; replace the cooling oil with the same amount of cooling water (the same amount of cooling water contains desulfurization and denitrification catalysts in the same amount as the cooling oil), so that the weight ratio of the total amount of co...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


