Method for preheating canalization molten-salt section during producing alumina

A production process and pipeline technology, applied in the direction of alumina/hydroxide, etc., can solve the problems of high investment cost and replacement cost, easy damage of electric heating wire, damage of electric heat tracing, etc., and achieve low investment and operation cost , low failure rate and short heating time

Active Publication Date: 2010-06-02
中铝矿业有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 1. The electric heating wire is easily damaged, and the pipeline cleaning adopts hydraulic cleaning. If water enters the electric heating wiring during cleaning, it will cause damage to the electric heating wire and affect the life of the electric heating wire
[0006] 2. It is difficult to replace the electric heating wire. The insulation of the whole pipe must be removed first, and then the electric heating wire can be replaced. It takes about 2 days
[0007] 3. The cost of the electric heating wire is high, the value of the electric heating wire in the molten salt heating section is more than 200,000 yuan, and the investment cost and replacement cost are high
[0008] 4. The heating time of the electric heating wire is long, and it takes about 20 hours for the pipeline in the molten salt heating section to be heated to above 180°C required for the start-up of the device, which causes the start-up time of the entire pipeline device to be prolonged

Method used

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Examples

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Effect test

Embodiment

[0024] The exhaust steam of the self-evaporation system is to connect the eighth-stage self-evaporator with the exhaust steam heat exchange section corresponding to the tenth section with exhaust steam pipes. The temperature and pressure of the exhaust steam heat exchange section are the highest in the first stage, and the lowest in the eighth stage. The new steam process is added to the first-stage exhaust steam pipe, and high-temperature gas is introduced after the device is cleaned and overhauled to increase the temperature of the inner pipe of the first-stage exhaust steam heat exchange section, and the temperature is transferred by using the heat transfer of the inner pipe. For the molten salt heating section, so that the pipeline in the molten salt heating section reaches the temperature required for the start-up of the device. The temperature of the high-temperature steam is 330°C-350°C, the steam pressure is 3.1-3.3MPa, and the steam flow rate is 6t / h.

[0025] The heat...

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Abstract

The invention discloses a method for preheating a canalization molten-salt section during producing alumina and relates to a method for preheating a molten-salt heating section before pump starting of canalization molten-salt during producing alumina. The method is characterized in that the preheating of the canalization molten-salt section is realized in such a way that dead steam in a self-evaporation system is adopted to heat ore pulp in a canalization stripping pipe and molten salt in an interlayer of the canalization stripping pipe is preheated through the heated ore pulp. Compared with the prior art, the method for preheating a canalization molten-salt section during producing alumina adopts steam heating, low fault compared with electric tracing cords, lower investment and running cost than electric tracing, short heating time, can achieve temperature needed for the start of the canalization device in short time, can preheat the whole system through self-evaporation systems of a canalization system at all levels and is beneficial to establishing heat balance after the canalization device starts.

Description

technical field [0001] The invention relates to a preheating method for a pipelined molten salt section in an alumina production process, and relates to a method for preheating a molten salt heating section before starting a pipelined dissolution salt pump for alumina production. Background technique [0002] Pipeline dissolution is an important link in the Bayer alumina production process. The slurry heating process is divided into three processes. The molten salt heating section is the most important heating stage. It uses heat-carrying molten salt to heat the slurry. To the required dissolution temperature, the heat-carrying molten salt used is made of KNO 3 、NaNO 3 、NaNO 2 Composed of three components, in order to prevent the molten salt from solidifying, the pipeline device must go through the preheating process of the molten salt heating section before starting the pipeline device in a cold state after cleaning and maintenance. It is required that the temperature of ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F7/02
Inventor 茹红伟胡秋华田雷梅永峰
Owner 中铝矿业有限公司
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