Nitrosyl sulfuric acid production method and system

A technology of nitrosyl sulfuric acid and production methods, applied in chemical instruments and methods, inorganic chemistry, non-metallic elements, etc., can solve the problems of incomplete tail gas absorption, increased energy consumption, emissions, cumbersome processes, etc., and reduce tail gas treatment Cost and raw material cost, reduction of raw material cost, effect of increasing reaction rate

Active Publication Date: 2018-04-27
ZHEJIANG DIBANG CHEM
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The Chinese patent literature with the publication number CN106379875A discloses a production method and application of nitrosyl sulfuric acid. The patent first uses mixed acid to absorb tail gas, but due to the high content of volatile nitric acid and nitrogen oxides in the mixed acid, the absorption of tail gas At the same time, there will be new tail gas, which needs to be absorbed by sodium hydroxide aqueous solution. After the absorption, acid and alkali adjustment and evaporation crystallization are required. Although the resource-based products of sodium nitrate and sodium chloride are obtained, the process is cumbersome and consumes more energy. high
[0005] Nitric acid mist, sulfur dioxide, sulfur trioxide, water, nitrogen oxides and other exhaust gases are produced during the production of nitrosyl sulfuric acid. Mixed acid is generally used for pre-absorption in the treatment of these exhaust gases. Strong, so the absorption of exhaust gas is not complete, and the follow-up exhaust gas still needs other treatment methods, which will increase energy consumption and emissions
And the reaction raw materials lost in the tail gas will cause the loss of products

Method used

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  • Nitrosyl sulfuric acid production method and system

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Effect test

Embodiment 1

[0045] A kind of production method of nitrosyl sulfuric acid, comprises the following steps:

[0046] (1) waste acid is concentrated waste acid that obtains sulfuric acid mass fraction as 30% through concentration;

[0047] (2) flow is that the concentrated waste acid of 1.0t / h is passed into absorption tower continuously from top to bottom, absorbs the mixed tail gas that produces in the production process of nitrosyl sulfuric acid, and mixed tail gas enters absorption tower from bottom to top, obtains absorption sulfuric acid, The massfraction of sulfuric acid at the outlet of the absorption tower is 31.5%;

[0048]The absorption tower is a packed tower reactor, and the filler is aluminum silicate. The absorption tower is vented on the top of the absorption tower and connected to the waste gas treatment device for treatment; absorption sulfuric acid storage tank, sulfuric acid storage tank, nitric acid storage tank, and sulfuric acid configuration pot , The mixed acid confi...

Embodiment 2

[0052] A kind of production method of nitrosyl sulfuric acid, comprises the following steps:

[0053] (1) waste acid is concentrated waste acid that obtains sulfuric acid mass fraction as 85% through concentration;

[0054] (2) Concentrated waste acid is continuously fed into the absorption tower from top to bottom with a flow rate of 355kg / h to absorb the mixed tail gas produced in the production process of nitrosyl sulfuric acid, and the mixed tail gas enters the absorption tower from bottom to top to obtain absorbed sulfuric acid. The massfraction of sulfuric acid is 87.5%;

[0055] The absorption tower is a packed tower reactor, and the filler is aluminum silicate. The absorption tower is vented on the top of the absorption tower and connected to the waste gas treatment device for treatment; absorption sulfuric acid storage tank, sulfuric acid storage tank, nitric acid storage tank, and sulfuric acid configuration pot , The mixed acid configuration pot, the reaction tower...

Embodiment 3

[0059] A kind of production method of nitrosyl sulfuric acid, comprises the following steps:

[0060] (1) the waste acid is pretreated and concentrated to obtain a concentrated waste acid with a mass fraction of 60%;

[0061] (2) Concentrated waste acid is continuously fed into the absorption tower from top to bottom with a flow rate of 555kg / h to absorb the mixed tail gas produced in the production process of nitrosyl sulfuric acid, and the mixed tail gas enters the absorption tower from bottom to top to obtain absorbed sulfuric acid. The massfraction of sulfuric acid is 61.6%;

[0062] The absorption tower is a packed tower reactor, and the filler is aluminum silicate. The absorption tower is vented on the top of the absorption tower and connected to the waste gas treatment device for treatment; absorption sulfuric acid storage tank, sulfuric acid storage tank, nitric acid storage tank, and sulfuric acid configuration pot , The mixed acid configuration pot, the reaction tow...

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Abstract

The invention discloses a green continuous production method of nitrosyl sulfuric acid. The production method includes the steps: (1) condensing waste acid to obtain condensed waste acid; (2) continuously leading the condensed waste acid in an absorption tower to absorb mixed tail gas generated in the production of the nitrosyl sulfuric acid to obtain absorbed sulfuric acid; (3) preparing the absorbed sulfuric acid and water and/or concentrated sulfuric acid into sulfuric acid solution with demand concentration, and mixing the sulfuric acid solution and the concentrated sulfuric acid into mixed acid; (4) continuously feeding the mixed acid and gas with sulfur dioxide into a reaction tower to perform reaction to obtain a nitrosyl sulfuric acid finished product. The invention further discloses a production system of the nitrosyl sulfuric acid. The tail gas generated in the production process of the nitrosyl sulfuric acid is absorbed and recycled by the aid of the condensed waste acid, the mixed acid is preheated by the nitrosyl sulfuric acid finished product, and the nitrosyl sulfuric acid is synthesized in a continuous and automatic chain control manner. According to automatic chaincontrol, heat exchange and tail gas resource utilization, emission reduction of tail gas is achieved, energy is saved, consumption is reduced, and yield is improved.

Description

technical field [0001] The invention relates to the field of dye intermediate production, in particular to a green production method and system for dye intermediate nitrosyl sulfuric acid. Background technique [0002] Nitrosyl sulfuric acid is an important diazotization raw material. Compared with sodium nitrite, it has higher activity and can carry out diazotization reaction with some low activity amino groups. And no salt will be generated during the diazotization process, which is convenient for subsequent processing. [0003] Because nitrosyl sulfuric acid is easy to decompose, concentrated sulfuric acid is used as a solvent for storage and transportation in industry (some production processes also directly use sulfuric acid as a raw material to participate in the reaction). Since the reaction raw materials have volatile components and gaseous components, they will produce waste gases such as nitric acid mist, nitrogen oxides, sulfur dioxide, and sulfur trioxide durin...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B21/094
CPCC01B21/094
Inventor 傅伟松赵小敏冯彦博
Owner ZHEJIANG DIBANG CHEM
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