A method and system for recovering elemental sulfur and regenerating catalysts loaded with sulfur

A technology of catalyst and recovery sheet, which is applied in the field of recovery of elemental sulfur and regeneration of sulfur-loaded catalysts. It can solve the problems of difficult control of by-products, high energy consumption, and influence of operating temperature, and achieve simple system equipment and production processes. Safe and reliable, good energy saving and safety effect

Active Publication Date: 2022-01-14
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Usually, the external conditions required for elemental sulfur recovery and catalyst regeneration are very high. For example, the temperature required for hot soaking and charcoal burning process is as high as 450-500 °C, which requires high energy consumption, and it is necessary to prevent carbon deposition and accelerated aging of the catalyst; the hot soaking process catalyst Sulfur condensation may occur on the surface. Although these problems can be avoided after special operation, the sulfur recovery rate of the device at this time is lower than that achieved by normal operation.
The sulfur recovery process has been widely studied at home and abroad, but there are still many technical problems in the process including the direct oxidation reactor. The formation process of liquid sulfur in the catalyst is affected by the operating temperature, or the formed by-product H 2 The generation of S is difficult to control
At present, the methods for recovering elemental sulfur and regenerating catalysts after loading sulfur are all dry methods, and there is no mention of wet methods using solution leaching.

Method used

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  • A method and system for recovering elemental sulfur and regenerating catalysts loaded with sulfur

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Effect test

Embodiment 1

[0037]A system for recovering and regenerating elemental sulfur by catalysts loaded with sulfur, comprising ammonia sulfide storage tank 1, sulfur leaching reactor 2, ammonia polysulfide storage tank 3, elemental sulfur stripping reactor 4, solid-liquid separator 5, elemental sulfur Sulfur drier 6, sulfur storage tank 7, catalyst drier 8, catalyst storage tank 9, cooling tower 10, tail gas purification tower 11, lye tank 15, waste liquid tank 16; The top of the reactor 2 is connected, and a three-way solenoid valve 12 and a two-way electric valve 13 are arranged between the pump 14 and the sulfur leaching reactor 2. The three-way solenoid valve 12 is also connected with the distilled water inlet, and the top of the sulfur leaching reactor 2 is provided with Sulfur-loaded catalyst inlet; the bottom of the sulfur leaching reactor 2 is connected to the ammonia polysulfide storage tank 3 through a pump, the ammonia polysulfide storage tank 3 is connected to the elemental sulfur gas...

Embodiment 2

[0047] Adopt the system of embodiment 1, after carrying out carrying out sulfur, catalyst reclaims elemental sulfur and regenerates, concrete steps are as follows:

[0048] (1) Efficient normal temperature and pressure immersion extraction of sulfur in ammonium sulfide solution:

[0049] The catalyst is Co 15 Mo 10 / Al 2 o 3 catalytic reduction of SO 2 For the subsequent catalyst, the sulfur-loaded catalyst is added to the sulfur leaching reactor 2 from the sulfur-loaded catalyst inlet, the two-way electric valve 13 is opened, the three-way solenoid valve 12 is connected to the pump 14 and the sulfur leaching reactor 2, and the sulfurized The ammonia sulfide solution in the ammonia storage tank 1 is pumped into the sulfur leaching reactor 2. The mass fraction of the ammonia sulfide solution is 18%. The volume ratio is 1:5, under normal temperature and pressure, let the leaching reaction stand for 8 hours, wait for the leaching to be completed, pump the leaching solution, ...

Embodiment 3

[0056] Adopt the system of embodiment 1, after carrying out carrying out sulfur, catalyst reclaims elemental sulfur and regenerates, concrete steps are as follows:

[0057] (1) Efficient normal temperature and pressure immersion extraction of sulfur in ammonium sulfide solution:

[0058] The catalyst is Co 15 Mo 10 / Al 2 o 3 catalytic reduction of SO 2 For the subsequent catalyst, the sulfur-loaded catalyst is added to the sulfur leaching reactor 2 from the sulfur-loaded catalyst inlet, the two-way electric valve 13 is opened, the three-way solenoid valve 12 is connected to the pump 14 and the sulfur leaching reactor 2, and the sulfurized The ammonia sulfide solution in the ammonia storage tank 1 is pumped into the sulfur leaching reactor 2. The mass fraction of the ammonia sulfide solution is 20%. The volume ratio is 1:6, under normal temperature and pressure, let the leaching reaction stand for 10 hours, wait until the leaching is completed, pump the leaching solution, ...

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Abstract

The invention discloses a method and system for recovering elemental sulfur and regenerating a sulfur-loaded catalyst. The sulfur-loaded catalyst is soaked in an ammonia sulfide solution. time; after the two leaching solutions of the steps are combined, high-temperature nitrogen gas is used to strip elemental sulfur, and the gas stripping tail gas is condensed and discharged after purification treatment. The elemental sulfur is obtained by drying; the catalyst after twice soaking and extraction is washed and dried to become a regenerated catalyst; the invention can avoid the high temperature and high pressure conditions of the traditional desulfurization method, and the sulfur on the catalyst is thoroughly leached with high efficiency, and the reaction device is simple and convenient. It is safe and reliable, and the low temperature and low pressure reaction conditions are conducive to energy saving. Using this method to recover elemental sulfur, the sulfur extraction rate of ammonia polysulfide solution can reach more than 98%.

Description

technical field [0001] The invention belongs to the technical field of catalyst regeneration and sulfur recovery, and in particular relates to a method and system for recovering and regenerating elemental sulfur from a catalyst loaded with sulfur. Background technique [0002] Catalytic reduction of SO by CO 2 The generated elemental sulfur will be deposited on the catalyst, and harsh conditions are required to extract the generated elemental sulfur from the catalyst. Usually, the external conditions required for elemental sulfur recovery and catalyst regeneration are very high. For example, the temperature required for hot soaking and charcoal burning process is as high as 450-500 °C, which requires high energy consumption, and it is necessary to prevent carbon deposition and accelerated aging of the catalyst; the hot soaking process catalyst Sulfur condensation may occur on the surface, although these problems can be avoided after special operation, but the sulfur recover...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B17/033B01J23/882B01J23/94B01J38/48
CPCC01B17/033B01J23/882B01J23/94B01J38/48B01J38/66C01B17/0205C01B17/027Y02P20/584
Inventor 张秋林张腾祥宁平张亚青王慧敏
Owner KUNMING UNIV OF SCI & TECH
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