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Delayed coking system and delayed coking process

A delayed coking and process technology, applied in non-catalytic thermal cracking, cracking, petroleum industry and other directions, can solve the problems of complex improvement, easy coking in the wax oil section, and insufficient liquid recovery effect, and achieve the effect of improving product quality.

Active Publication Date: 2016-04-20
SINOPEC ENG GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The equipment and method can improve the poor quality of wax oil products in the conventional delayed coking process, the heavy wax oil section of the fractionation tower is easy to coke, the coke tower reaction oil gas pipeline is easy to coke, and the device circulation ratio is not easy to adjust. However, the invention is mainly from the fractionation tower. The equipment has been improved, the improvement is more complicated, and the effect of increasing liquid collection is not significant enough
[0010] To sum up, in the prior art, in order to improve the economic benefits of the delayed coking unit, technicians mostly start from the perspectives of increasing material handling equipment, adding liquid increasing or coke suppression additives, improving the heating furnace process, and improving fractionation tower equipment. These methods Both have a certain effect on improving the economy of the delayed coking unit, but there are still certain problems in each

Method used

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  • Delayed coking system and delayed coking process
  • Delayed coking system and delayed coking process
  • Delayed coking system and delayed coking process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] figure 1 The delayed coking system 100 provided by Embodiment 1 of the present invention is shown, including a coke tower 101, an oil and gas flash tank 102, a fractionation tower 103, a first oil and gas pipeline 104 and a second oil and gas pipeline 105, and the coke tower 101 passes through the first oil and gas pipeline 104 communicates with the oil-gas flash tank 102, and the oil-gas flash tank 102 communicates with the fractionation tower 103 through the second oil-gas pipeline 105. The oil-gas flash tank 102 is provided with a quenching system 106, and the quenching system 106 is used to provide Quenching oil, the quenching oil is used to cool and wash the oil and gas generated by the coke tower 101 and enters the oil-gas flash tank 102 .

[0033] In the present embodiment, one end of the first oil and gas pipeline 104 communicates with the top of the coke tower 101, and the other end communicates with the bottom of the oil and gas flash tank 102 (limited by 1 / 2 ...

Embodiment 2

[0042] figure 2 Shown is the delayed coking system 200 provided by Embodiment 2 of the present invention. The setting of the second oil-gas pipeline 201 of this embodiment is different from that of Embodiment 1, and the spraying amount of the quenching oil in the oil-gas flash tank 102 is related to the delayed Except that the mass ratio of the feed amount of the coking system 200 is 0.3:1.0, other settings are the same as in the first embodiment.

[0043] In this embodiment, the second oil and gas pipeline 201 includes a tank top pipeline 202 and a tank bottom pipeline 203. The top of the oil and gas flash tank 102 communicates with the upper part of the fractionation tower 103 through the tank top pipeline 202, and the bottom of the oil and gas flash tank 102 passes through the tank. The bottom line 203 communicates with the lower part of the fractionation column 103 . The "upper part" and "lower part" mentioned here are bounded by 1 / 2 of the vertical height of the oil and...

Embodiment 3

[0047] Embodiment 3 of the present invention provides a delayed coking system, wherein the mass ratio of the spraying amount of the quenching oil in the oil-gas flash tank 102 to the feed amount of the delayed coking system 200 is 0.1:1, except that other settings and implementation Example 2 is the same. In addition, the gauge pressure of the oil-gas flash tank 102 is preferably 10-170 kPa, and in this embodiment, the gauge pressure is 130 kPa.

[0048] The temperature of the oil that enters the oil-gas flash tank 102 from the coke tower 101 is higher, and the pressure is also larger, and in the present embodiment, the pressure inside the oil-gas flash tank 102 is controlled within a small range, so that the oil-gas flash tank 102 The total pressure is small, so the partial pressure of the oil and gas is also small. Under the condition of constant reaction temperature and circulation ratio, this setting can reduce the residual amount of heavy hydrocarbons, reduce the coke yie...

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Abstract

The invention provides a delayed coking system. The delayed coking system comprises a coke tower, an oil gas flash tank, a fractionating tower, a first oil gas pipeline and a second oil gas pipeline, wherein the coke tower is communicated with the oil gas flash tank through the first oil gas pipeline; the oil gas flash tank is communicated with the fractionating tower through the second oil gas pipeline; the oil gas flash tank is provided with a quenching system; the quenching system is used for providing quenching oil for the interior of the oil gas flash tank; the quenching oil is used for cooling and washing the oil gas which is generated by the coke tower and enters the oil gas flash tank; the final boiling point of the quenching oil is lower than that of the oil which is introduced into the oil gas flash tank. According to the delayed coking system provided by the invention, the content of coke powder in a coked light product can be effectively reduced, and the quality of the product can be improved. The invention further provides a delayed coking process used by the delayed coking system.

Description

technical field [0001] The invention relates to the technical field of petroleum refining, and in particular to a delayed coking system and a delayed coking process. Background technique [0002] Due to the non-renewable nature of petroleum resources, its efficient utilization has become a common concern of scientific and technological workers. [0003] At present, the delayed coking process has developed into an important means of heavy oil processing due to its mature technology, strong adaptability, thorough decarburization, and simple process. However, with the continuous deterioration of crude oil properties, the heavy oil processed by the delayed coking process also shows a trend of inferior quality, which brings certain challenges to the economical efficiency of heavy oil processed by the delayed coking process and makes the operation of the coking unit difficult. The product quality deteriorates, the yield of low value-added products coke and gas increases, and the ...

Claims

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Application Information

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IPC IPC(8): C10G9/00
CPCC10G9/005C10G2400/02C10G2400/04
Inventor 王洪彬李节宋业恒江莉黄新龙刘淑芳张瑞风张晓燕陈小民赵智刚
Owner SINOPEC ENG GRP CO LTD
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