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Method for preventing or retarding salt deposition of delayed coking fractionator

A technology of coking fractionation tower and delayed coking, which is applied in the field of preventing or slowing down salt accumulation in delayed coking fractionation tower, and can solve problems such as inability to completely eradicate salt formation, complex methods, and salt formation in fractionation towers

Active Publication Date: 2016-08-17
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] (1) Water washing is a more effective solution to solve the salt accumulation on the top tray of the fractionation tower. For the salt accumulation on the top tray of the fractionation tower, the fractionation towers of domestic coking units and catalytic cracking units basically use water washing treatment, but this method It can only be an emergency treatment when salt builds up in the fractionation tower, but cannot completely eradicate the salt buildup. After a period of time, the fractionation tower will still accumulate salt, and it needs to be washed again
[0007] (2) By increasing the top circulation dehydration tank and continuous desalination, the salt scale in the top circulation pipeline and fractionation tower is dissolved into the sulfur-containing sewage and sent to the acidic water stripping device, finally forming the betaine at the top of the coking fractionation tower and the top circulation pipeline The open-circuit treatment is a measure to reduce the salt accumulation of the fractionation tower from the process operation. This method is relatively complicated
[0008] For example, Zhang Jinxian [Zhang Jinxian. Treatment measures for salt accumulation on top trays of coking towers. Oil Refining Technology and Engineering. 2009.3 (3): 25-26] thinks that water washing is a more effective solution to solve salt accumulation on top trays of fractionation towers. For fractionation towers Salt build-up on the top tower tray, domestic coking units and catalytic cracking unit fractionation towers are basically treated with water washing, although the details of washing are different, for example, some use deoxygenated water and some use fresh water, etc., but the principle and process are roughly similar , but this method can only be used as an emergency treatment when the fractionation tower accumulates salt, but cannot completely eradicate the salt formation. After a period of time, the fractionation tower will still accumulate salt, and it needs to be washed again
[0009] For example, Wang Bin et al [Wang Bin, Fu Qiang, Guo Shouxue. Analysis and Treatment of Delayed Coking Unit Top-cycle Salt Condensation. Guangzhou Chemical Industry, January 2013, Vol. , dissolve the salt scale in the top circulation pipeline and the fractionation tower into the sulfur-containing sewage and send it to the sour water stripping device, and finally form the open-circuit treatment of the betaine at the top of the coking fractionation tower and the top circulation pipeline, and reduce the knot in the fractionation tower from the process operation salt measures, the method is more complex

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  • Method for preventing or retarding salt deposition of delayed coking fractionator

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Example 1, the processing capacity of a delayed coking unit is 2.1 million tons per year, the circulation ratio is 0.2:1, the operating pressure of the delayed coking coke tower is 0.18MPa, and the temperature of coking oil gas generated by the reaction in the delayed coking coke tower is 450-460°C , the coking oil and gas flow into the large oil and gas pipeline at the top of the coke tower through the top of the delayed coke tower, and the circulating oil at the top of the coking and fractionating tower is injected into the large oil and gas pipeline 3 at the top of the coking and fractionating tower through the first injection port, and the injection speed of the circulating oil at the top of the coking and fractionating tower is 28- 30 tons per hour, the temperature of the coking oil and gas in the large oil and gas pipeline 3 at the top of the coking tower is lowered to 415-425 ° C. The effect is that no salt formation is found in the delayed coking and fractionating...

Embodiment 2

[0040] Example 2, the processing capacity of a delayed coking unit is 1.6 million tons per year, the outlet temperature of the coking furnace is 500°C, the operating pressure of the coke tower is 0.16MPa, the circulation ratio is 0.3:1, and the temperature of the coking oil gas generated by the reaction in the coke tower is The temperature is 445-455°C. The coking oil and gas flow into the large oil and gas pipeline at the top of the coke tower through the top of the coke tower. The temperature of the coking oil and gas in the top oil and gas pipeline is cooled. After cooling, the temperature of the oil and gas in the top oil and gas pipeline of the coke tower is reduced to 420-425°C. %, the effect is that no salt formation has been found in the delayed coking fractionation tower for 14 months.

Embodiment 3

[0043] Example 3 A delayed coking treatment capacity is 1.2 million tons per year, the operating pressure of the coke tower is 0.15MPa, the circulation ratio is 0.15:1, the temperature of the coking oil gas generated by the reaction in the coke tower is 440-450°C, and the coking oil gas is passed through the coke The top of the tower flows into the large oil and gas pipeline at the top of the coke tower, and the middle circulating oil is injected into the large oil and gas pipeline at the top of the coke tower through the first injection port. , after cooling down, the temperature of the coking oil gas is 415-420°C. Before the cooled coking oil gas enters the delayed coking fractionation tower, the top circulating oil of the coking fractionation tower is injected into the large oil and gas pipeline at the top of the coke tower through the second injection port, and the coking top circulating oil The injection rate is 8 tons / hour, and its effect is that the coking fractionation ...

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Abstract

The invention provides a method for preventing or retarding salt deposition of a delayed coking fractionator; a mixture of one or more of coking fractionator top circulating oil, a coker gasoline fraction and a light diesel fraction is used as specific fraction oil, and the specific fraction oil is injected into a coke tower top large oil-gas pipeline through a first injection port, so as to reduce the temperature of coked oil gas in the coke tower top large oil-gas pipeline; or / and the specific fraction oil is injected to the coke tower top large oil-gas pipeline through a second injection port, and the specific fraction oil and the coked oil gas are mixed as a feeding material for the delayed coking fractionator to enter the delayed coking fractionator.

Description

technical field [0001] The invention relates to a delayed coking method, in particular to a method for preventing or slowing down salt formation in a delayed coking fractionation tower. Background technique [0002] Delayed coking is a petroleum secondary processing technology, which refers to the deep thermal cracking and condensation reaction at high temperature (about 500°C) using hydrogen-poor heavy oil as raw material to produce gas, gasoline, diesel oil, wax oil, and coke technology. The so-called delayed coking means that the coking raw materials (raw oil and circulating oil) are heated to the coking reaction temperature quickly through the heating furnace, and then quickly enter the coke tower. No coke is formed in the heating furnace tube, but enter the coke tower and then carry out the coking reaction. There is a delayed effect, called delayed coking technology. [0003] As crude oil becomes heavier and society's demand for light oil products continues to increas...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G75/00
Inventor 杨长文刘海澄李京辉相养冬王宏德于洋张永翰徐鲁燕张华
Owner PETROCHINA CO LTD
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