Hydrocarbon oil hydrotreating method

Patent metadata

Field	Value
Publication number	US-9862896-B2
Application number	US-201314430499-A
Country	US
Kind code	B2
Filing date	Sep 18, 2013
Priority date	Sep 21, 2012
Publication date	Jan 9, 2018
Grant date	Jan 9, 2018

Abstract

Provided is a hydrocarbon oil hydrotreating method, comprising the following steps: (1) injecting hydrogen into the hydrocarbon oil via an opening having a nanoscale average diameter, so as to obtain hydrocarbon oil containing hydrogen; and (2) under a liquid phase hydrotreating condition, feeding into a reactor the hydrocarbon oil containing hydrogen to contact a catalyst having a hydrogenation catalysis effect. The method of the present invention can quickly and efficiently disperse and dissolve the hydrogen into the hydrocarbon oil even without the aid of a diluent or circulating oil, so as to obtain stable hydrogen-containing hydrocarbon oil with a high hydrogen content, and obtain an hydrotreating effect equivalent to or even better than the existing hydrotreating methods.

First claim

The invention claimed is:

1. A method for hydroprocessing hydrocarbon oil, comprising:
feeding a first hydrocarbon oil feedstock into an inlet of a first mixing device having pores with an average pore diameter in a nanometer size range,
injecting hydrogen gas into the first hydrocarbon oil feedstock through the pores in the first mixing device to obtain a first hydrogen-containing hydrocarbon oil feedstock from an outlet of the first mixing device;
feeding the first hydrogen-containing hydrocarbon oil feedstock into an inlet of a first hydrogenation reactor to contact a first catalyst having a hydrogenation catalytic action disposed in the first hydrogenation reactor under a first liquid-phase hydroprocessing condition; and
obtaining a first product stream from an outlet of the first hydrogenation reactor;
feeding the first product stream into an inlet of a second mixing device having pores with an average pore diameter in a nanometer size range;
injecting hydrogen gas into the first product stream through the pores in the second mixing device to obtain a hydrogen-containing first product stream from an outlet of the second mixing device;
feeding the hydrogen-containing first product stream into an inlet of a second hydrogenation reactor to contact a second catalyst having a hydrogenation catalytic action disposed in the second hydrogenation reactor under a liquid-phase hydroprocessing condition; and
obtaining a second product stream from an outlet of the second hydrogenation reactor.

2. The method according to claim 1 , wherein the pores have an average pore diameter in a range of 1 nm to 1,000 nm.

3. The method according to claim 2 , wherein a percentage of the pores with a pore diameter in a range of 50 nm to 500 nm to a total number of the pores is 95% or higher.

4. The method according to claim 1 , wherein the hydrogen gas is injected into the hydrocarbon oil in a flowing state at a rate of v 1 by g·h −1 ·m −2 , the hydrocarbon oil has a flow rate of v 2 by kg·h −1 ·m −2 , and a ratio of v 1 /v 2 is in a range of 0.000625 to 0.09.

5. The method according to claim 1 , wherein the first mixing device comprises at least one liquid passage for accommodating the first hydrocarbon oil and at least one gas passage for accommodating the hydrogen gas, the liquid passage is separated from the gas passage by a component having a porous area containing the pores.

6. The method according to claim 5 , wherein the porous area has a porosity in a range of 5-28%.

7. The method according to claim 1 , wherein the first hydrogenation reactor is a fixed-bed reactor, a volume space velocity of the first hydrocarbon oil is in a range of 0.5 h −1 to 20 h −1 ; the liquid-phase hydroprocessing condition comprises a temperature in a range of 120° C. to 500° C. and a pressure in a range of 1 MPa to 20 MPa by gage pressure.

8. The method according to claim 1 , wherein the first hydrogenation reactor is a tubular reactor.

9. The method according to claim 7 , wherein the tubular reactor has a ratio of length to inner diameter in a range of 5-50:1.

10. The method according to claim 9 , wherein the tubular reactor has an inner diameter in a range of 20 nm to 1,000 mm.

11. The method according to claim 1 , wherein the hydroprocessing of the first hydrocarbon oil feedstock is one or more selected from the group consisting of hydrodeolefin, hydrodesulfurization, hydrodenitrogenation, hydrodeoxygenation, and hydrodemetalization.

12. The method according to claim 1 , wherein the first hydrocarbon oil feedstock is one or more selected from the group consisting of gasoline, reformate, aviation fuel, and diesel oil.

13. The method according to claim 12 , wherein the hydrogen gas is injected in an amount for 0.1 to 4 times of a saturated solubility of the hydrogen gas in the first hydrocarbon oil feedstock, and the saturated solubility is measured under the liquid-phase hydroprocessing condition.

14. The method according to claim 1 , further comprising contacting the first hydrogen-containing hydrocarbon oil feedstock with the first catalyst without the presence of a diluent or a circulating oil.

15. A method for hydroprocessing hydrocarbon oil, comprising:
feeding a first hydrocarbon oil feedstock into an inlet of a first mixing device having pores with an average pore diameter in a nanometer size range,
injecting hydrogen gas into the first hydrocarbon oil feedstock through the pores in the first mixing device to obtain a first hydrogen-containing hydrocarbon oil feedstock from an outlet of the first mixing device;
feeding the first hydrogen-containing hydrocarbon oil feedstock into an inlet of the first hydrogenation reactor to contact a first catalyst having a hydrogenation catalytic action disposed in the first hydrogenation reactor under a first liquid-phase hydroprocessing condition;
obtaining a first product stream from an outlet of the first hydrogenation reactor;
injecting hydrogen gas into a second hydrocarbon oil feedstock through a second mixing device having pores with an average pore diameter in a nanometer size range to obtain a second hydrogen-containing hydrocarbon oil feedstock;
feeding the second hydrogen-containing hydrocarbon oil feedstock into a second hydrogenation reactor to contact a second catalyst having a hydrogenation catalytic action disposed in the second hydrogenation reactor under a liquid-phase hydroprocessing condition;
obtaining a second product stream; and
combining the first product stream and the second product stream.

16. The method of claim 1 , wherein the first catalyst and the second catalyst are the same.

17. The method of claim 15 , wherein the wherein the first mixing device comprises at least one liquid passage for accommodating the first hydrocarbon oil and at least one gas passage for accommodating the hydrogen gas, the liquid passage is separated from the gas passage by a component having a porous area containing the pores.

18. The method of claim 15 , wherein the hydroprocessing of the first hydrocarbon oil feedstock is one or more selected from the group consisting of hydrodeolefin, hydrodesulfurization, hydrodenitrogenation, hydrodeoxygenation, and hydrodemetalization.

19. The method of claim 15 , wherein the first hydrocarbon oil feedstock is one or more selected from the group consisting of gasoline, reformate, aviation fuel, and diesel oil.

Assignees

• China Petroleum & Chem Corp
• Hunan Changling Petrochemical Science And Tech Development Co Ltd

Inventors

• Li Hua
• Liu Jianping
• She Xichun
• He Xiaojun
• Li Qinghua
• Chen Qingling
• Jiang Lei
• Zeng Zhiyu
• Liu Chengli
• Yang Qingpin

Classifications

• C10G45/60

  characterised by the catalyst used · CPC title

• C10G45/22 Primary

  with hydrogen dissolved or suspended in the oil · CPC title

• C10G2400/04

  Diesel oil · CPC title

• C10G3/42

  Catalytic treatment · CPC title

• C10G45/04

  characterised by the catalyst used · CPC title