Production device and production process of EL-grade sulfuric acid

A technology of production equipment and production process, applied in the field of production equipment of EL grade sulfuric acid, can solve the problems of high cost, energy consumption, not suitable for large-scale production, etc., and achieve the effect of good elasticity and low energy consumption

Pending Publication Date: 2020-08-14
上海六谦工程科技股份有限公司
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Problems solved by technology

The rectification operating temperature of this method reaches more than 300 degrees Celsius, which requires high material requirements for related equipment, and consumes energy. It is difficult to remove individual impurities. At the same time, waste gas and acid mist will be generated during the process, which has a certain impact on environmental protection and is not suitable. mass production
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  • Production device and production process of EL-grade sulfuric acid

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Embodiment Construction

[0024] The principles and features of the present invention are described below in conjunction with the accompanying drawings, and the examples given are only used to explain the present invention, and are not intended to limit the scope of the present invention.

[0025] A kind of production method of EL grade sulfuric acid, its production process is as follows:

[0026] S1, SO from niacin plant 3 The gas is liquefied by the first condenser (1) and then enters the first vaporizer (2), heated by hot water (about 60°C) and vaporized, and then SO 3 Enter the second condenser (3) and the second gasifier (4) for secondary condensation and secondary gasification to achieve sufficient purification of SO 3 The goal;

[0027] More specifically, in the above step S2, in order to prevent small particles of dust from entering the subsequent process, a gas filter (5) is installed after the secondary gasifier, and the intercepted particle size range is below 1 micron;

[0028] S2, purif...

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Abstract

The invention relates to a production device of EL-grade sulfuric acid. The production device comprises a first condenser, a second condenser, a first gasifier and a second gasifier which are connected in sequence. The first condenser is communicated with a falling film evaporator in the nicotinic acid evaporation process and is used for receiving evaporated sulfur trioxide gas; the second gasifier is connected with an EL-grade sulfuric acid absorption tower, the EL-grade sulfuric acid absorption tower is tower-tank integrated equipment and comprises an absorption tower body and an acid tank,the acid tank is connected with a circulating acid cooler through a circulating acid pump, and the outlet of the circulating acid cooler is divided into three paths which are respectively communicatedwith the acid tank, the absorption tower body and a diluter; the diluter is communicated with the water treatment device and is used for receiving high-purity water; the diluter is communicated withthe finished product acid cooler and is used for cooling to prepare finished product acid. The production device has the advantages of low energy consumption and no pollution. The invention also provides a production process of EL-grade sulfuric acid.

Description

technical field [0001] The invention relates to the field of sulfuric acid production devices, in particular to a production device of EL grade sulfuric acid and a production process thereof. Background technique [0002] At present, domestic EL grade sulfuric acid production methods mainly include rectification method and ultrapure water or ultrapure dilute sulfuric acid gas absorption method. [0003] The rectification method is to use industrial sulfuric acid to distill in a rectification tower to obtain higher purity sulfuric acid. However, since the raw materials used in this method contain a large amount of metal impurity ions, sulfur dioxide, acid radical ions and other organic matter, etc., they need to be pretreated before entering the device, and the relevant impurities must be oxidized by oxidizing agents to become sulfuric acid and sulfur dioxide. The pretreated sulfuric acid finally enters the rectification tower of special materials for rectification. Metal i...

Claims

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Application Information

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IPC IPC(8): C01B17/74C01B17/90
CPCC01B17/74C01B17/90Y02P20/10
Inventor 丁云朋鲁建国王颖
Owner 上海六谦工程科技股份有限公司
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