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Liquid-phase hydrogenation feed preheating system and process

A liquid-phase hydrogenation and liquid-phase technology, which is used in the liquid-phase hydrogenation feed preheating system and the liquid-phase hydrogenation feed preheating field, can solve the problem of product coking in the tube, furnace tube scaling, harsh feeding conditions, etc. problems, to achieve the effect of reducing coking and scaling, ensuring recycling, and small temperature differential pressure

Inactive Publication Date: 2020-10-30
张家港保税区慧鑫化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the heating furnace is an important key equipment in any liquid-phase hydrogenation reaction. Since the liquid-phase reactor requires a higher reaction temperature, and the feed needs to be mixed with hydrogen, the partial pressure of hydrogen in the furnace tube of the heating furnace is relatively high. , the pipe wall temperature and total pressure are correspondingly high, which will limit the raw materials of the liquid phase hydrogenation process
[0003] In addition, because the heating feed includes multiphase flow of gas, liquid and solid, there are great uncertainties in the design of the heating furnace, the calculation of pressure loss and heat transfer, and the high temperature and easy wear are very unfavorable to the use of the heating furnace
[0004] Due to the harsh feeding conditions, the heating furnace is likely to cause scaling inside the furnace tube and coking of products in the tube. The heating time of the feeding material in the heating furnace is limited, and it is easy to cause the furnace tube to break, etc., and the safety of the process operation is poor.

Method used

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  • Liquid-phase hydrogenation feed preheating system and process
  • Liquid-phase hydrogenation feed preheating system and process
  • Liquid-phase hydrogenation feed preheating system and process

Examples

Experimental program
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Embodiment 1

[0035] Choose the vacuum residue of Arabian light crude oil as raw material, mix 1wt% solid additive / catalyst, the hydrogen-oil ratio at the inlet of the liquid phase reactor is 750 Nm / ton of oil, the operating temperature of the liquid phase reactor is 470°C, and the gas phase reactor is operated The temperature is 370-390°C, the operating temperature of the hot high fraction of the liquid phase reactor is 460°C, the operating temperature of the second hot separator is 270°C, and the operating temperature of the cold separator is 40°C. The process parameters are shown in Table 1.

[0036] Table 1 process parameter list

[0037] logistics 1 2 3 4 5 6 temperature C 180 40 157 411 40 480 pressure BARG 210.0 210.0 210.0 208.5 210.0 207.5 flow KG / HR 10100 202 10302 10302 722 722

[0038] logistics 7 8 9 10 11 12 temperature C 423 460 460 390 270 270 pressure BARG 207.5 206.0 206.0 ...

Embodiment 2

[0043] Select the vacuum residue of Arabian light crude oil as raw material, mix 1wt% solid additive / catalyst, the hydrogen-oil ratio at the inlet of the liquid phase reactor is 750 Nm / ton of oil, the operating temperature of the liquid phase reactor is 450°C, and the gas phase reactor is operated The temperature is 360-380°C, the operating temperature of the hot high fraction of the suspended bed is 460°C, the operating temperature of the second hot separator is 270°C, and the operating temperature of the cold separator is 40°C. The process parameters are shown in Table 2.

[0044] Table 2 process parameter list

[0045] logistics 1 2 3 4 5 6 temperature C 180 40 157 396 40 510 pressure BARG 210.0 210.0 210.0 208.5 210.0 207.5 flow KG / HR 10100 202 10302 10302 722 722

[0046] logistics 7 8 9 10 11 12 temperature C 416 440 440 380 270 270 pressure BARG 207.5 206.0 206.0 205.0 ...

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Abstract

The invention relates to a liquid-phase hydrogenation feeding preheating system and process. The system is characterized in that the top end of a first thermal separator is in reflux connection with athird liquid-phase heat exchanger and a third gas-phase heat exchanger; the third gas-phase heat exchanger is connected to a gas-phase reactor; the top end of the gas-phase reactor is connected to asecond liquid-phase heat exchanger and a second gas-phase heat exchanger; the second gas-phase heat exchanger is connected to a second heat separator, the top end of the second heat separator is connected to a first liquid-phase heat exchanger and the first gas-phase heat exchanger, the first gas-phase heat exchanger is connected to a cold separator, and the top end of the cold separator is connected to a liquid-phase feeding pipe and a gas-phase feeding pipe through a compressor. The system is scientific and reasonable in structural design and safe to operate, liquid-phase feeding and gas-phase feeding can be subjected to countercurrent heat exchange preheating respectively to reach the required temperature, technological parameters are guaranteed, damage to a heating furnace is small, the phenomena of coking, scaling and the like are avoided, and operation safety is guaranteed; meanwhile, heat and hydrogen can be effectively recycled, and the energy utilization rate is increased.

Description

technical field [0001] The invention belongs to the technical field of liquid-phase heavy oil hydrogenation, relates to liquid-phase hydrogenation feed preheating, in particular to a liquid-phase hydrogenation feed preheating system. Background technique [0002] For the hydrogenation process of liquid-phase feed such as heavy oil from oil shale and tar sands, atmospheric residue, coal tar or bitumen, the feed needs to be heated to the temperature required by the liquid-phase reactor through a heating furnace. Therefore, the heating furnace is an important key equipment in any liquid-phase hydrogenation reaction. Since the liquid-phase reactor requires a higher reaction temperature, and the feed needs to be mixed with hydrogen, the partial pressure of hydrogen in the furnace tube of the heating furnace is relatively high. , the pipe wall temperature and total pressure are correspondingly high, which will limit the raw materials for the liquid-phase hydrogenation process. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/00C10G47/00
CPCC10G45/00C10G47/00
Inventor 刘哲昝大鑫吕云飞王鑫邓宏达
Owner 张家港保税区慧鑫化工科技有限公司
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