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Sodium hydrosulfite synthesizing and continuous producing method

A production method and technology of hydrosulfite, which is applied in the field of continuous production of hydrosulfite synthesis, can solve problems such as non-continuous, etc., and achieve the effects of improving production efficiency, improving efficiency, and balancing exhaust gas emissions

Active Publication Date: 2017-03-22
CHIFENG RUIYANG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In October 2013, China Salt Anhui Hongsifang Co., Ltd. applied for a patent for synthesis of continuous large droplet addition (application number 201310501782.2). From the disclosed content, the core is that after each large droplet addition is completed, the small droplet When adding the pot and transferring the material, the material that has completed the large dropwise addition operation is left with a certain volume (2m) by limiting the volume of the transferred material 3 ) material as the base material, and then perform the operation of adding AE and ME dropwise in the process of synthetic large dropwise addition, which cannot be regarded as continuous in the true sense.

Method used

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  • Sodium hydrosulfite synthesizing and continuous producing method
  • Sodium hydrosulfite synthesizing and continuous producing method
  • Sodium hydrosulfite synthesizing and continuous producing method

Examples

Experimental program
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Effect test

Embodiment 1

[0047] Getting the raw materials ready: the configuration mass fraction is 98% HCOONa, and the preparation mass fraction is 62% sodium pyrosulfite concentration with SO 2 Gauge, SO 2 -CH 3 OH,SO 2 Concentration ≥ 370g / L, carrier methanol, mass fraction is 78%;

[0048] Bottom feeding: use inert gas to press into the storage tank, open the flow meter and feed AE of about 1.8m³ into the synthetic large dripping pot, and start to heat up;

[0049] Value adjustment: Turn on the steam when the temperature rises to 76°C, the pressure is at 0.1MPa, and at the same time open the flow meter valve to add SO to the large dripping pot 2 -CH 3 OH solution 25L, a certain amount of ethylene oxide, and adjust the pH to 4.3;

[0050] Large dripping: After adjusting the value for 10min~20min, when the temperature rises to 81℃~82℃, start adding AE and ME to stabilize the pH at 4.4~4.5, and the pressure is 0.2MPa~0.25MPa. After reaching 80% (one batch of materials), the bottom tubes in the ...

Embodiment 2

[0055] Getting the raw materials ready: the configuration mass fraction is 99% HCOONa, and the preparation mass fraction is 64% sodium metabisulfite concentration (in the form of SO 2 Count), SO 2 -CH 3 OH,SO 2 Concentration ≥ 370g / L, carrier methanol, mass fraction is 79%;

[0056] Bottom feeding: use inert gas to press into the storage tank, open the flow meter and feed about 2m³ of AE to the synthetic large dripping pot, and start to heat up;

[0057] Value adjustment: Turn on the steam when the temperature rises to 80°C, the pressure is between 0.15MPa and 0.2MPa, and at the same time open the flow meter valve to add SO to the large dripping pot 2 -CH 3 OH solution 25L, a certain amount of ethylene oxide, and adjust the pH to 4.4;

[0058] Large drop: After adjusting the value for 10min~20min, when the temperature rises to 82°C~83°C, start adding AE and ME to stabilize the pH at 4.3~4.4, and the pressure is 0.15MPa~0.2MPa. After reaching 80% (one batch of materials),...

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Abstract

The invention discloses a sodium hydrosulfite synthesizing and continuous producing method. The sodium hydrosulfite synthesizing and continuous producing method comprises the following steps: taking a synthesizing pot as a tubular reactor; after preparing raw materials AE and ME, transferring the raw materials AE and ME into AE and ME storage tanks via inert gas; adding the raw materials AE and ME in a large synthesis dropwise adding pot; opening the pot and inserting a bottom tube into the large synthesis dropwise adding pot to transfer the materials into a small synthesis dropwise adding pot; keeping the liquid level of the materials in the large dropwise adding pot to be stable relatively in a material transferring process; continuing adding the raw materials AE and ME into the large synthesis dropwise adding pot continuously and uniformly; after the small synthesis dropwise adding pot receives a first batch of materials, enabling a second small dropwise adding pot to begin to receive the material from the large synthesis dropwise adding pot, and enabling the rest dropwise adding pot to begin to receive the material from the large synthesis dropwise adding pot in the same way; continuously adding a SO2-CH3OH solution as a raw material at a suitable speed to an end point by the small dropwise adding pots from the time when the small dropwise adding pots begin to receive the material to the time when reaction reaches the end point; and after insulating and ripening are completed, placing the material in a drying process for subsequent use. A repeated operation process of a reaction process is omitted, so that a synthesis process is continuous, and while the efficiency of the device is improved, consumption of sodium formate and sodium pyrosulfite is reduced.

Description

technical field [0001] The invention belongs to the technical field of production technology of sodium hydrosulfite, and in particular relates to a synthetic and continuous production method of hydrosulfite. Background technique [0002] Hydrosulfite, also known as sodium dithionite, is a white sandy crystal or light yellow powder chemical. Since sulfur is in an intermediate valence state, sodium dithionite has both strong reducing and oxidizing properties. It is mainly used as a bleaching agent in the textile industry and paper industry. It will release a large amount of heat and toxic gases such as hydrogen dioxide and hydrogen sulfide after contacting with water. It is widely used in reduction dyeing, reduction cleaning, bleaching and organic synthesis, wood pulp and paper making and other fields in the textile industry. [0003] Since the method of adding sodium metabisulfite to the production process of sodium formate sodium hydrosulfite was successful in Guangdong Zh...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B17/66
CPCC01B17/66
Inventor 肖琳董华荣李万忠李权全宏冬李鸿雁
Owner CHIFENG RUIYANG CHEM
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