System for preparing sulfuric acid from sulfur foam and desulfurization waste liquid by semi-dry method and acid preparation method

A technology for desulfurization waste liquid and sulfur foam, which is applied in the system field of semi-dry production of sulfuric acid from sulfur foam and desulfurization waste liquid, can solve the problem of inability to separate sulfur foam impurities and pulverized coal, inability to rapidly burn and release heat, and affect the quality of dilute acid. and other problems, to achieve the effect of satisfying thermal balance, low volatility, and low production of dilute acid

Active Publication Date: 2020-06-16
江苏康茂环保工程有限公司
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Problems solved by technology

[0005] 1. It is impossible to separate the pulverized coal in the sulfur foam. If the pulverized coal has poor fluidity and is brought into the pipeline, it will block the pipeline. After being brought into the incineration system, it cannot be decomposed. After high temperature, carbon knots block the fire tube of the waste heat boiler. Dilute acid affects the quality of dilute acid
[0006] 2. The above two process routes cannot separate the impurities and coal powder in the sulfur foam. The mixing of elemental sulfur and coal powder impurities together causes the particles to increase and contain crystal water. After entering the incinerator, they cannot burn quickly. In this case, in order to Rapid and complete combustion in the incinerator can only increase the combustion temperature (usually the combustion temperature is controlled at 1150 ° C) to avoid the genera...

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  • System for preparing sulfuric acid from sulfur foam and desulfurization waste liquid by semi-dry method and acid preparation method

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Embodiment 1

[0048] Such as figure 1 As shown, the waste liquid comes from the coking chemical desulfurization process, and the desulfurization liquid mainly generates S, NH 4 CNS, (NH 4 ) 2 S 2 o 3 , and other salts and sulfur. 100 cubic meters of desulfurization waste liquid from coking (ammonium thiocyanate 140 g / L, ammonium thiosulfate 100 g / L, ammonium sulfate 10 g / L, and suspended sulfur 1.5 g / L) are intercepted by filters , of which 60 cubic meters are lowered from the bottom of the sulfur paste filter to the sulfur foam storage tank, and 40 cubic meters of clear liquid after filtration are returned to the desulfurization system; the sulfur foam delivery pump delivers 6 cubic meters of sulfur foam per hour under a pressure of 12 kg to multiple Separator, the internal pressure of multiple separators is maintained at 0.4MPa, and 150°C steam is used to heat the coil to keep the separator at 130°C. After the sulfur foam stays in the tower for 10 hours, 60% of the sulfur containing ...

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Abstract

The invention discloses a system for preparing sulfuric acid from sulfur foam and desulfurization waste liquid by a semi-dry method and an acid preparation method. The system is formed by sequentiallyconnecting a separation unit, an incineration unit, a purification unit, a dry absorption unit and a tail absorption unit. Sulfur is extracted from sulfur foam, mixed with salt and sent to an incinerator to be incinerated for acid making, and dissolved clear liquid obtained after the sulfur is extracted and mixed with salt meets the requirement for returning to a desulfurization section to be recycled or entering a cold drum section.

Description

technical field [0001] The invention relates to the field of recovery and reuse of solid waste and liquid waste resources, in particular to a system and method for producing sulfuric acid by a semi-dry method of sulfur foam and desulfurization waste liquid. Background technique [0002] In the existing sulfur foam and desulfurization waste liquid acid production, there are mainly two types: dry acid production and wet acid production. The dry acid production process is: sulfur foam—filter—dryer—screening—crushing—incinerator—waste heat boiler—power wave scrubber—cooling scrubber—dry suction tower—electric demister—fan—converter—absorption Tower (two suctions) - sulfuric acid storage tank. Although the amount of dilute acid produced by the dry method is small, the dilute acid is of poor quality and contains too many impurities and cannot be used in the ammonium sulfate section. The drying pretreatment process causes the decomposition of salts, which makes it difficult to tre...

Claims

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Application Information

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IPC IPC(8): C01B17/80C01B17/765C01B17/54
CPCC01B17/54C01B17/7655C01B17/80C01B17/806Y02P20/129
Inventor 陈建康
Owner 江苏康茂环保工程有限公司
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