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Suspended bed and fixed bed combined desulfurization technology

A desulfurization process and suspended bed technology, applied in the field of desulfurization, can solve the problems of low desulfurization efficiency, complicated process flow and equipment, etc., and achieve the effects of high desulfurization efficiency, low price and simple equipment

Active Publication Date: 2018-10-23
BEIJING HUASHI UNITED ENERGY TECH & DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem solved by the present invention is to overcome the defects of low desulfurization efficiency, complex process flow and equipment existing in the existing desulfurization process, and then provide a desulfurization efficiency high, simple process flow, low equipment investment, which can convert the Combined desulfurization process of suspended bed and fixed bed that directly converts hydrogen sulfide into sulfur without secondary pollution

Method used

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  • Suspended bed and fixed bed combined desulfurization technology

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0047] The combined desulfurization process of a suspended bed and a fixed bed provided in this embodiment includes the following steps:

[0048] (1) Mix magnetic iron oxide with a particle size of 1 to 20 μm and water evenly in a certain proportion, and prepare a desulfurization slurry with a concentration of 1 wt %;

[0049] (2) H 2 The S content is 71.2g / Nm 3 The biogas mixed with the desulfurization slurry enters the first-stage suspended bed reactor with a superficial gas velocity of 0.3m / s from bottom to top, and the residence time of the desulfurization slurry in the first-stage suspended bed reactor is controlled to 5-7min The mixture discharged from the top of the first-stage suspended bed reactor enters the second-stage suspended-bed reactor with a superficial gas velocity of 0.3m / s from the bottom again, and the residence time of the desulfurization slurry in the second-stage suspended-bed reactor is controlled to be 5min. To make the biogas and the desulfurizatio...

Embodiment 2

[0053] The combined desulfurization process of a suspended bed and a fixed bed provided in this embodiment includes the following steps:

[0054] (1) Mix ferric hydroxide with a particle size of 5-15 μm and water uniformly in a certain proportion, and prepare a desulfurization slurry with a concentration of 2wt%;

[0055] (2) H 2 S content is 2.4g / Nm 3 The coke oven gas mixed with the above-mentioned desulfurization slurry enters from bottom to top into the suspension bed reactor with a superficial gas velocity of 0.15m / s, and the residence time of the desulfurization slurry in the suspension bed reactor is controlled to be 6-8min. Make the coal gas and the desulfurization slurry fully contact and react in the suspended bed reactor;

[0056] (3) Carry out gas-liquid separation to the gas-solid-liquid three-phase mixture discharged from the top of the suspended bed reactor, collect the gas phase and the rich liquid respectively, and measure the H in the gas phase 2 The S con...

Embodiment 3

[0059] Such as figure 1 As shown, the combined desulfurization process of a suspended bed and a fixed bed provided in this embodiment includes the following steps:

[0060] (1) Mixing amorphous iron oxyhydroxide with a particle size of 5-20 μm and water uniformly in a certain proportion to prepare a desulfurization slurry with a concentration of 2.5 wt %;

[0061] (2) H 2 S content is 140g / Nm 3 The natural gas from the coalescing tank is sent to the coalescing tank to remove heavy components above C5. The natural gas from the coalescing tank is mixed with the desulfurization slurry and then enters the suspension bed reactor with a superficial gas velocity of 0.2m / s from bottom to top. Control the residence time of the desulfurization slurry in the suspended bed reactor to 30-35 minutes, so that the natural gas and the desulfurization slurry can fully contact and react in the suspended bed reactor;

[0062] (3) Carry out gas-liquid separation to the gas-solid-liquid three-ph...

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Abstract

The invention provides a suspended bed and fixed combined desulfurization technology. A hydrogen sulfide-containing gas and a desulfurization slurry are mixed and then enter a suspended bed reactor from bottom to top, the residence time of the desulfurization slurry in the reactor is controlled to be 5-60 min to ensure full contact of the hydrogen sulfide-containing gas and the desulfurization slurry in order to carry out a reaction, and a gas phase separated after gas-liquid separation of the above obtained reaction mixture enters a fixed bed reactor and undergoes secondary desulfurization toobtain a purified gas. The technology can reduce the sulfur content of the hydrogen sulfide-containing gas to 50 ppm or less from 2.4-140 g / N.m<3> by using the suspended bed, a fixed bed is also usedto further reduce the sulfur content to 10 ppm or less, so the serial connection combination of the suspended bed and the fixed bed realizes high-efficiency desulfurization; and the technology has the advantages of simple and reasonable flow, high desulfurization efficiency, simplicity in required devices, small occupied land and low investment, and is very suitable for industrial promotion.

Description

technical field [0001] The invention belongs to the technical field of desulfurization, and in particular relates to a high-efficiency desulfurization process utilizing a series combination of a suspension bed reactor and a fixed bed reactor. Background technique [0002] H 2 The removal of S, the desulfurization methods that have been industrialized at present are mainly divided into two types: dry method and wet method. [0003] The dry desulfurization process and regeneration method use solid adsorbent to remove hydrogen sulfide and organic sulfur in the gas. The operation is simple and reliable, and the desulfurization purification degree is high. It is suitable for the treatment of low hydrogen sulfide gas. The main desulfurizer is iron oxide, while other desulfurizers such as activated carbon, molecular sieve, manganese oxide, zinc oxide, etc. are more expensive and less used. [0004] Wet desulfurization process and regeneration method can be divided into physical a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/80B01D53/75B01D53/52B01D53/96C10L3/10
CPCB01D53/52B01D53/75B01D53/80B01D53/96C10L3/101C10L3/103C10L2290/545C10L2290/12C10L2250/06C10L2290/542C10L2290/541B01D53/82B01D2253/1124B01D2253/304B01D2255/20738B01D2255/20761B01D2255/20792B01D2256/24B01D2258/05B01D2257/304B01D2251/602B01D2251/604B01D53/8612C01B17/04
Inventor 林科李林郭立新赵刚
Owner BEIJING HUASHI UNITED ENERGY TECH & DEV
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