INTEGRATED SYSTEM FOR WET DESULFURIZATION USING A SUSPENSION BED AND REGENERATION

• US 20180296977A1
• Filed: 01/19/2018
• Published: 10/18/2018
• Est. Priority Date: 04/12/2017
• Status: Active Grant

• Current Assignee: Beijing Huashi United Energy Technology and Development Co., Ltd .
• Original Assignee: Beijing Huashi United Energy Technology and Development Co., Ltd .
• Inventors: Lin, Ke, Li, Lin, Guo, Lixin, Zhao, Gang, Song, Jun
• Granted Patent: US 10,449,491 B2
• Time in Patent Office: Days
• CPC Class Codes: B01D 2251/602 Oxides
• CPC Class Codes: B01D 2251/604 Hydroxides
• CPC Class Codes: B01D 2257/304 Hydrogen sulfide
• CPC Class Codes: B01D 53/52 Hydrogen sulfide
• CPC Class Codes: B01D 53/80 Semi-solid phase processes, i.e. by using slurries
• CPC Class Codes: B01D 53/96 Regeneration, reactivation or recycling of reactants
• CPC Class Codes: C10L 2250/06 Particle, bubble or droplet size
• CPC Class Codes: C10L 2290/12 Regeneration of a solvent, catalyst, adsorbent or any other component used to treat or prepare a fuel
• CPC Class Codes: C10L 2290/541 Absorption of impurities during preparation or upgrading of a fuel
• CPC Class Codes: C10L 2290/542 Adsorption of impurities during preparation or upgrading of a fuel
• CPC Class Codes: C10L 2290/545 Washing, scrubbing, stripping, scavenging for separating fractions, components or impurities during preparation or upgrading of a fuel
• CPC Class Codes: C10L 3/103 Sulfur containing contaminants

Abstract

Provided is an integrated system for wet desulfurization using a suspension bed and regeneration, comprising a suspension bed reactor, a gas liquid separation tank, a flash evaporation tank and an oxidation regeneration tank that are connected in sequence. The integrated system is adapted to reduce the sulfur content in the hydrogen sulfide containing gas from 2.4-140 g/Nm³ to 50 ppm or less by using a suspension bed, so that the desulfurization efficiency is 98% or more. The present invention is adapted to realize regeneration of a spent desulfurizer by reacting an oxygen-containing gas with the rich solution, and the barren solution may be recycled for being used as the desulfurization slurry, without generating secondary pollution. Therefore, a process using the integrated system is simple and reasonable, with high desulfurization and regeneration efficiency, simple equipment, little occupation of land and low investment, which is very suitable for industrial promotion.

Claims

1. An integrated system for wet desulfurization using a suspension bed and regeneration, comprising:

a suspension bed reactor, provided with a feed inlet at bottom thereof and a discharge outlet at top thereof, the suspension bed reactor being filled with a mixture of a desulfurization slurry and a hydrogen sulfide containing gas, wherein the mixture has a dwell time of 5-60 mins in the suspension bed reactor;

a gas liquid separation tank, in connection with the discharge outlet of the suspension bed reactor, and provided with a rich solution outlet at bottom thereof and an exhaust port at top thereof;

a flash evaporation tank, in connection with the rich solution outlet of the gas liquid separation tank, and provided with a saturated liquid outlet at bottom thereof; and

an oxidation regeneration tank, in connection with the saturated liquid outlet of the flash evaporation tank, and provided with a barren solution outlet arranged at bottom thereof and in connection with the feed inlet of the suspension bed reactor.

2. The integrated system of claim 1, wherein the suspension bed reactor has an empty tower gas velocity of 0.03-0.3 m/s, preferably 0.05-0.2 m/s.

3. The integrated system of claim 1, wherein the desulfurization slurry has a desulfurizer concentration of 1-5 wt %, preferably 2-3 wt %.

4. The integrated system of claim 1, wherein, the suspension bed reactor has a first sprinkler means provided therein and disposed adjacent to the discharge outlet of the suspension bed reactor;

the gas liquid separation tank has a second sprinkler means provided therein and disposed adjacent to the exhaust port of the gas liquid separation tank;

the flash evaporation tank has a third sprinkler means provided therein and disposed adjacent to a light hydrocarbon discharge outlet at the top of the flash evaporation tank; and

the oxidation regeneration tank has a fourth sprinkler means provided at an upper portion thereof.

5. The integrated system of claim 4, further comprising

a solid liquid separator, in connection with a saturated liquid outlet arranged in a lower portion of the oxidation regeneration tank, and provided with an water outlet which is connected with an water inlet of each of the first sprinkler, the third sprinkler and the fourth sprinkler respectively.

6. The integrated system of claim 1, wherein, the oxidation regeneration tank is provided with an aeration device therein and a blower and an aeration pump outside thereof, wherein the blower and the aeration pump are respectively connected with the aeration device, and the aeration pump is connected with a liquid outlet arranged in a lower portion of the oxidation regeneration tank.

7. The integrated system of claim 6, further comprising

a venturi mixer having an outlet connected to a slurry inlet arranged in an upper portion of the oxidative regeneration tank, and a water inlet connected to the water outlet of the solid liquid separator.

8. The integrated system of claim 1, further comprising

a coalescer having an exhaust port communicating with the feed inlet of the suspension bed reactor.

9. The integrated system of claim 1, wherein, the flash evaporation tank has a pressure drop of 0.1-0.4 MPa.

10. The integrated system of claim 1, wherein, the desulfurization apparatus comprises

one suspension bed reactor, or

at least two suspension bed reactors connected in series and/or in parallel.

12. The integrated system of claim 2, wherein the desulfurization slurry has a desulfurizer concentration of 1-5 wt %, preferably 2-3 wt %.

13. The integrated system of claim 2, wherein,

the suspension bed reactor has a first sprinkler means provided therein and disposed adjacent to the discharge outlet of the suspension bed reactor;

the gas liquid separation tank has a second sprinkler means provided therein and disposed adjacent to the exhaust port of the gas liquid separation tank;

the flash evaporation tank has a third sprinkler means provided therein and disposed adjacent to a light hydrocarbon discharge outlet at the top of the flash evaporation tank; and

the oxidation regeneration tank has a fourth sprinkler means provided at an upper portion thereof.

14. The integrated system of claim 13, further comprising

a solid liquid separator, in connection with a saturated liquid outlet arranged in a lower portion of the oxidation regeneration tank, and provided with a water outlet which is connected with a water inlet of each of the first sprinkler, the third sprinkler and the fourth sprinkler respectively.

15. The integrated system of claim 2, wherein, the oxidation regeneration tank is provided with an aeration device therein and a blower and an aeration pump outside thereof, wherein the blower and the aeration pump are respectively connected with the aeration device, and the aeration pump is connected with a liquid outlet arranged in a lower portion of the oxidation regeneration tank.

16. The integrated system of claim 15, further comprising

a venturi mixer having an outlet connected to a slurry inlet arranged in an upper portion of the oxidative regeneration tank, and a water inlet connected to the water outlet of the solid liquid separator.

17. The integrated system of claim 2, further comprising

a coalescer having an exhaust port communicating with the feed inlet of the suspension bed reactor.

18. The integrated system of claim 2, wherein, the flash evaporation tank has a pressure drop of 0.1-0.4 MPa.

19. The integrated system of claim 2, wherein, the desulfurization apparatus comprises

one suspension bed reactor, or

at least two suspension bed reactors connected in series and/or in parallel.

11. An integrated system for wet desulfurization using a suspension bed and regeneration, comprising:

a suspension bed reactor, provided with a feed inlet at bottom thereof and a discharge outlet at top thereof;

a gas liquid separation tank, in connection with the discharge outlet of the suspension bed reactor, and provided with a rich solution outlet at bottom thereof and an exhaust port at top thereof;

a flash evaporation tank, in connection with the rich solution outlet of the gas liquid separation tank, and provided with a saturated liquid outlet at bottom thereof; and

an oxidation regeneration tank, in connection with the saturated liquid outlet of the flash evaporation tank, and provided with a barren solution outlet arranged at bottom thereof and in connection with the feed inlet of the suspension bed reactor.