Process and system for producing ammonium sulfate by deaminizing coke oven gas with ammonium sulfite method

The technology of ammonium sulfite and coke oven gas is applied in the field of coal chemical industry, which can solve the problems of long process, high operation cost and high investment, and achieve the effects of low energy consumption, low investment and simple process flow

Pending Publication Date: 2019-03-26
DALIAN HAOTONG ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The purpose of the present invention is to propose a method for the problems of long process flow, high investment and high operating costs in the current coke oven gas desulfurization slurry acid production process, and the need to add purchased sulfuric acid in the coke oven gas production ammonium sulfate process. Coke oven gas ammonium sulfite deamination process to produce ammonium sulfate. This process uses ammonium sulfite solution as a solvent to absorb ammonia in coke oven gas. Ammonium sulfite solution absorbs sulfur slurry or acid vapor incineration to produce flue gas The sulfur dioxide can be regenerated, and the ammonium sulfite produced by absorbing ammonia and sulfur dioxide is oxidized and converted into ammonium sulfate, which effectively improves the utilization rate of resources.

Method used

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  • Process and system for producing ammonium sulfate by deaminizing coke oven gas with ammonium sulfite method

Examples

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Effect test

Embodiment 1

[0052] This embodiment discloses a coke oven gas ammonium sulfite method to produce ammonium sulfate system, its structure is as follows figure 1 As shown, it includes combustion furnace 1, waste heat boiler 2, cooling tower 3, desulfurization tower 4, ammonia washing tower 5, oxidation tank 6, cooling water pump 7, desulfurization upper circulation pump 8, desulfurization lower circulation pump 9, ammonium sulfate solution circulation pump 10. Ammonia washing circulating fluid pump 11. Desulfurization tower cooler 12:

[0053] The desulfurization tower 4 is a multi-stage packed tower.

[0054] The oxidation tank 6 has a built-in microporous air distribution pipe, and a cobalt sulfate fixed-bed catalyst is set.

[0055] The sulfur slurry or acid steam pipeline, fuel gas pipeline and air pipeline are connected to the inlet of the combustion furnace 1, and combustion generates flue gas containing sulfur dioxide;

[0056] The flue gas outlet of the combustion furnace 1 is conne...

Embodiment 2

[0085] This embodiment discloses a coke oven gas ammonium sulfite deamination process for producing ammonium sulphate, using the coke oven gas ammonium sulfite deamination system described in Example 1 to produce ammonium sulphate.

[0086] 1.1 million tons of coking plant gas treatment capacity of 55,000m 3 / h, the gas contains ammonia 6g / m 3 , containing hydrogen sulfide 4g / m 3 . Gas dehydrogen sulfide adopts vacuum carbonate desulfurization technology, and carbonate desulfurization rich liquid is vacuum desorbed to produce acid vapor containing hydrogen sulfide.

[0087] In the ammonia washing tower, the coal gas is in countercurrent contact with the ammonium sulfite lean solution sprayed on the top of the tower from bottom to top, the ammonia in it is absorbed, and the ammonia reacts with ammonium bisulfite to form ammonium sulfite, which forms ammonium sulfite at the bottom of the tower Rich liquid; the operating temperature of the ammonia washing tower is 30°C, and th...

Embodiment 3

[0091] This embodiment discloses a coke oven gas ammonium sulfite deamination process for producing ammonium sulphate, using the coke oven gas ammonium sulfite deamination system described in Example 1 to produce ammonium sulphate.

[0092] 1.1 million tons of coking plant gas treatment capacity of 55,000m 3 / h, the gas contains ammonia 7g / m 3 , containing hydrogen sulfide 5g / m 3 . Hydrogen sulfide removal from coal gas adopts ammonia wet oxidation technology to convert hydrogen sulfide removed from coal gas into sulfur slurry.

[0093] In the ammonia washing tower, the coal gas is in countercurrent contact with the ammonium sulfite lean solution sprayed on the top of the tower from bottom to top, the ammonia in it is absorbed, and the ammonia reacts with ammonium bisulfite to form ammonium sulfite, which forms ammonium sulfite at the bottom of the tower Rich liquid; the operating temperature of the ammonia washing tower is 30°C, and the pressure is 20kPa; the pH value of t...

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Abstract

The invention provides a process and a system for producing ammonium sulfate by deaminizing coke oven gas with an ammonium sulfite method. The process for producing the ammonium sulfate by deaminizingthe coke oven gas with the ammonium sulfite method comprises the following steps of using ammonia in the coke oven gas and sulfur dioxide generated by sulfur paste, generated by the wet oxidative desulfurization on the gas with an ammonia method, or an acid gas, generated by desulfurization with an absorptive method, through incineration as raw materials, absorbing the ammonia in the coke oven gas by adopting an ammonium sulfite solution as a solvent, regenerating the ammonium sulfite solution through absorbing the sulfur dioxide in flue gas generated by the incineration of the sulfur paste or the acid gas, and converting ammonium sulfite generated by absorbing the ammonia and the sulfur dioxide into ammonium sulfate through oxidation. The problem that a device in a process of washing theammonium with sulfuric acid is seriously corroded is solved. According to the process, cooling water absorbs sulfur trioxide to generate the sulfuric acid which can be used for replacing sulfuric acid which is needed to be purchased when the ammonium sulfate is produced; and the resource is comprehensively utilized. The invention also discloses the system for producing the ammonium sulfate by deaminizing the coke oven gas with the ammonium sulfite method. The system has the advantages of being low in investment, low in energy consumption and easy to popularize.

Description

technical field [0001] The invention relates to coal chemical technology, in particular to a process and system for producing ammonium sulfate by deammonization of coke oven gas with ammonium sulfite. Background technique [0002] The gas produced in the coking production of coke ovens contains harmful impurities such as ammonia and hydrogen sulfide, which need to be purified to remove harmful impurities and recover chemical products; the purified coke oven gas is used as industrial fuel or chemical synthesis raw material gas. At present, sulfuric acid absorption method is mainly used for deammonization of coke oven gas, and sulfuric acid is used to absorb ammonia to produce ammonium sulfate. This process is characterized by simple process flow and wide application of ammonium sulfate products; Purchased sulfuric acid increases production costs. Coke oven gas dehydrogen sulfide mainly adopts absorption method and ammonia wet oxidation method. The absorption method is to wa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10K1/00C10K1/10C01C1/24B01D53/96B01D53/78B01D53/50F27D17/00
CPCB01D53/502B01D53/78B01D53/96B01D2258/0283C01C1/24C10K1/002C10K1/103F27D17/001F27D17/008Y02P10/25Y02P20/129
Inventor 王英丽张卫东
Owner DALIAN HAOTONG ENVIRONMENTAL PROTECTION ENGINEERING TECHNOLOGY CO LTD
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