Wet decomposition evaporation alkali production technique for NaHCO3 alkali halide

A process, the technology of alkali brine, which is applied in the field of wet decomposition and evaporation of alkali brine containing NaHCO3, can solve the problems of high process cost, environmental pollution, environmental pollution, etc., shorten the process flow, solve environmental pollution problems, and reduce production costs Effect

Active Publication Date: 2009-08-12
HENAN ZHONGYUAN CHEM
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Problems solved by technology

After 7 years of experiments, 47,000 tons of soda ash were produced, and 50,000 tons of caustic mud (on a dry basis) were produced at the same time. Three large pools were piled up, which seriously polluted the environment and could not be expanded.
The cost of this process is high, and a large amount of causticized mud will be produced in the production process, which will seriously pollute the environment

Method used

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  • Wet decomposition evaporation alkali production technique for NaHCO3 alkali halide

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Embodiment Construction

[0014] The wet decomposition and evaporation soda production process of the present invention is completed by the following steps:

[0015] a. The refined brine in the refining process enters the clear liquid storage tank, and is pumped by the refined brine to the first, second, and third stage preheaters. The preheating temperature rises to above 90°C and enters the first effect wet decomposition evaporator;

[0016] b. The first-effect evaporation liquid enters the second-effect wet decomposition evaporator through the material guide pump. The raw steam used by the first-effect wet decomposition evaporator is 0.45MPa (absolute pressure) back pressure steam, and the condensed water produced enters the first-level clear liquid The preheater returns to the boiler after preheating; the secondary steam generated during the second-effect evaporation process enters the three-effect heating chamber as the heat source of the next effect;

[0017] c. The second-effect wet decompositio...

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Abstract

The invention discloses an alkali preparing process for wetly decomposing and evaporating alkali halide containing NaHCO3, which comprises the following steps: adding purified brine in the refining process into a clear liquid storage tank; successively adding the brine into a first effective wet decomposition evaporator, a second effective wet decomposition evaporator, a third effective evaporator and a fourth effective crystallizer after the brine is sent to a primary preheater, a secondary preheater and a tertiary preheater in sequence by using a purified brine pump; and obtaining a crystal in the fourth effective crystallizer; and then sending the crystal to the filtering process. Primary steam used by the first effective wet decomposition evaporator adopts back pressure steam of 0.45 MPa (absolute pressure); condensed water generated after being preheated by a primary clear liquid preheater is returned to a boiler; secondary steam generated by each effective evaporator is used as a next effective heat source; and secondary steam generated during the fourth effective evaporation process is emptied after passing through a surface condenser. By adopting the production technology of the wet decomposition and evaporation process, the process flow of natural alkali preparing pure alkali is shortened, the production cost is reduced, the problem of environmental pollution in the traditional art is solved, and the production of the pollution-free natural alkali preparing pure alkali is achieved.

Description

Technical field [0001] The present invention relates to the field of soda making technology, more specifically, relates to a kind of 3 Alkali brine wet decomposition evaporation alkali production process. Background technique [0002] After Tongbai Anpeng soda mine was discovered in Henan Oilfield in the early 1980s, detailed exploration was carried out, and a 10kt / a heavy soda ash pilot plant was built in 1990. The monohydrate soda processing technology, that is, the causticization method, was used to produce light caustic lye. Neutralization of NaHCO in brine 3 , Evaporate and crystallize to obtain alkali monohydrate, separate and calcinate to obtain heavy soda ash. After 7 years of experiments, 47,000 tons of soda ash were produced, and 50,000 tons of caustic mud (on a dry basis) were produced at the same time. Three large ponds were piled up, which seriously polluted the environment and could not be expanded. The cost of this process is high, and a large amount of cau...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01D7/12
Inventor 丁喜梅王胜利李山岭齐铁新孔涛李守刚刘二明郭爱贵贺锦荣
Owner HENAN ZHONGYUAN CHEM
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