Regenerative and integrative hydrogen sulfide liquid phase oxidation absorption method of sulphur separation/desulfuration solution

A technology of desulfurization solution and liquid phase oxidation, which is applied in the direction of refining with oxygenated compounds, can solve the problems of increasing the loss of desulfurization agent, unsatisfactory separation effect, etc., and achieves the effect of high separation efficiency

Active Publication Date: 2010-10-27
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the prior art, the sedimentation ratio of sulfur is increased by adding methods such as dispersing and flocculants, so that the sulfur settles at the bottom of the regeneration reactor or the inner circulation bubble tower, and then the sedimentation liquid is discharged, and then the sulfur is separated by methods such as filtration. The sulfur content in the sedimentation liquid is low, so that a large amount of solution is circulated between the filter unit and the reactor, which not only increases the energy consumption and the loss of desulfurization agent, but also the separation effect is still not ideal

Method used

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  • Regenerative and integrative hydrogen sulfide liquid phase oxidation absorption method of sulphur separation/desulfuration solution
  • Regenerative and integrative hydrogen sulfide liquid phase oxidation absorption method of sulphur separation/desulfuration solution

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] The absorption tower is a bubbling tower with an effective volume of 12L; the volume of the bubbling reaction section of the regeneration-separation tower is 25L, the diameter of the bubbling reaction section: the diameter of the gas-liquid separation section: the diameter of the foam collecting section = 1:1:1.43, the height of the bubbling reaction section : The height of the gas-liquid separation section: the height of the foam collection section=1: 0.4: 0.8 (the volume of the foam collection section can be calculated to be 160% of the bubbling reaction section). The diameter ratio of the overflow tank weir in the foam collection section to the foam collection section is 1:1.2, and the ratio of the overflow tank weir height to the total height of the foam collection section is 0.4:1. The flow rate of the purified gas is 0.5m 3 / h (standard condition), H 2 The content of S is 1.0% (volume fraction); the concentration of complexed iron ions in the desulfurization solu...

Embodiment 2

[0026] The device is the same as in Example 1. The flow rate of the purified gas is 0.8m 3 / h (standard condition), H 2 The content of S is 2.0% (volume fraction); the concentration of complexed iron ions in the desulfurization solution is 30mol / m 3 , the circulating flow rate of the desulfurization solution between the two towers is 60L / h. The amount of desulfurization solution in the regeneration-separation tower is kept at 26-28L (it can be seen that the residence time of the desulfurization solution containing 1g of sulfur powder in the regeneration-separation tower is 1.2h), and the superficial gas velocity is 1.7cm / s. SDBS is used as the active agent, and the flow rate is as follows: 0.012g of surfactant is newly added for every desulfurization solution containing 1g of sulfur entering the regeneration-separation tower. After the system runs stably, the pH is maintained at 9.0-9.5, and the H in the gas at the outlet of the absorption tower 2 The S content is less tha...

Embodiment 3

[0028] The absorption tower is a bubble tower with an effective volume of 12L; the volume of the bubble reaction section of the regeneration-separation tower is 27L, the diameter of the bubble reaction section: the diameter of the gas-liquid separation section: the diameter of the foam collection section = 1:1:1.7, the height of the bubble reaction section : The height of the gas-liquid separation section: the height of the foam collection section=1: 0.25: 0.4 (the volume of the foam collection section can be calculated to be 120% of the bubbling reaction section). The diameter ratio of the overflow tank weir in the foam collection section to the foam collection section is 1:1.4, and the ratio of the overflow tank weir height to the total height of the foam collection section is 0.2:1. H in the purified gas 2 The content of S is 1.0% (volume fraction), the gas flow rate is 1m 3 / h (standard condition); the concentration of complexed iron ions in the desulfurization solution i...

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Abstract

The invention relates to a regenerative and integrative hydrogen sulfide liquid phase oxidation absorption method of sulphur separation / desulfuration solution, comprising a regeneration-separation tower composed of a bubbling reaction section, an air liquid separation section and a foam collection section. Desulfuration solution used for absorbing H2S flows out of a self-absorption tower and enters into the regeneration-separation tower, and then is oxidized and regenerated by a catalyst at the bubbling reaction section so as to enrich sulphur granules on a bubble interface; at the air liquidseparation section, the regeneration / desulfuration solution is separated from foams and is returned to an absorption tower for recycling, and sulphur is carried to the foam collection section by foams and is recovered by collecting foams; 0.008-0.012g of surfactant is added when per desulfuration solution containing 1g of sulphur enters into the tower; air dose introduced in the desulfuration solution containing 1g of sulphur is no less than 34L, and empty tower gas velocity is 0.8-2.5cm / s; and the sulphur granule separation rate and regenerative reaction rate are high, the energy consumptionand catalyst consumption are low, and the method can be applicable to the process of absorbing H2S gas in medium-size sulphur throughputs.

Description

technical field [0001] The invention relates to a sulfur separation / desulfurization solution regeneration integrated hydrogen sulfide absorption method for complex iron liquid phase oxidation and absorption of hydrogen sulfide gas. Background technique [0002] Hydrogen sulfide gas is one of the main gases that affect product quality and cause environmental pollution in natural gas, oil refining and chemical industry. H in natural gas and refinery gas with medium latent sulfur content (100kg / d to 30t / d elemental sulfur) 2 Among the S absorption processes, the complex iron liquid-phase oxidation absorption process has the advantages of fast absorption speed, high desulfurization efficiency, less side reactions, low cost, and environmental friendliness, and has the most industrial application value. The process uses trivalent complex iron ions as a catalyst to convert the H dissolved in the desulfurization solution 2 S is oxidized to elemental sulfur, and the catalyst is red...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G27/10
Inventor 蒋国强常宏岗江盛阳何金龙赵洲洋张伍丁富新黄瑛
Owner PETROCHINA CO LTD
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