Hydrometallurgical process for nickel oxide ore

Abstract

The hydrometallurgical Process for a nickel oxide ore, which is capable of preventing inevitable operation shutdown of a leaching step and maintaining high operation efficiency as a whole process, in a trouble of the steps other than the leaching step, in a hydrometallurgical Process for a nickel oxide ore using a High Pressure Acid Leach.It is characterized in that, the hydrometallurgical Process for a nickel oxide ore using a High Pressure Acid Leach equipment equipped with the following means (a) to (c), in a trouble of the steps other than the above leaching step, the leached slurry discharged from the means (c), which is used in the above High Pressure Acid Leach equipment, is subjected to self-circulation inside the High Pressure Acid Leach equipment, by transferring to the means (a), which is used in the above High Pressure Acid Leach equipment, as well as by shutdown of receiving the ore slurry and the addition of sulfuric acid, in the above leaching step:means (a) to preliminarily increase temperature and pressure of the ore slurry;means (b) to form the leached slurry, by the addition of sulfuric acid to the ore slurry with preliminarily increased temperature and pressure, and leaching under blow of high-pressure steam and high-pressure air;means (c) to eliminate a pressurized state of the leached slurry formed.

Description

BACKGROUND OF THE INVENTION[0001]1. Field of the Invention[0002]The present invention relates to a hydrometallurgical Process for a nickel oxide ore, in more detail, in a hydrometallurgical Process for a nickel oxide ore using a High Pressure Acid Leach including a preparation step of ore slurry for making a slurry of a nickel oxide ore, a leaching step for obtaining leached slurry by transferring the relevant ore slurry to a High Pressure Acid Leach equipment for leaching nickel and cobalt, and a solid-liquid separation step of the relevant leached slurry, the present invention relates to a hydrometallurgical Process for a nickel oxide ore, which is capable of preventing inevitable operation shutdown of the above leaching step and maintaining high operation efficiency as a whole process basis, in a trouble of the steps other than the above leaching step.[0003]2. Description of the Prior Art[0004]A High Pressure Acid Leach using sulfuric acid has been noticed in recent years, as a w...

AI Technical Summary

Benefits of technology

[0017]In view of the above conventional technological problems, it is an object of the present invention to provide a hydrometallurgical Process for a nickel oxide ore, which is capable of preventing inevitable operation shutdown of the above leaching step, and maintaining high operation efficiency as a whole process basis, in a hydrometallurgical Process for a nickel oxide ore, using the High Pressure Acid Leach including: a preparation step of ore slurry for making the slurry of a nickel oxide ore; a leaching step for obtaining leached slurry by transferring of the ore slurry to a High Pressure Acid Leach equipment, for leaching nickel and cobalt; and a solid-liquid separation step of the leached slurry, and in a trouble of the steps other than the above leaching step.

[0019]means (a) to preliminarily increase temperature and pressure of the ore slurry;

[0024]means (a) to preliminarily increase temperature and pressure of the ore slurry;

[0032]means of (c): a multistage flash tank for decreasing temperature and pressure of the leached slurry stepwise.

[0035]The hydrometallurgical Process for a nickel oxide ore of the present invention, in a hydrometallurgical Process for a nickel oxide ore using the above High Pressure Acid Leach, and in a trouble of the steps other than the above leaching step, is capable of preventing inevitable operation shutdown of the above leaching step, by self-circulation of the leached slurry inside the High Pressure Acid Leach equipment by shutdown of receiving of the above ore slurry and the addition of sulfuric acid, in the above leaching step, as well as by shutdown of transfer of the leached slurry discharged from the means of (c), which is used in the above High Pressure Acid Leach equipment, to the above solid-liquid separation step, and transferring to the means of (a), which is used in the above High Pressure Acid Leach equipment, and is capable of maintaining operation, by restart operation soon, if necessary, as well as by no generation of discharged water due to no use of industrial water, and still more by preventing corrosion troubles of apparatuses such as a heater or pump of the High Pressure Acid Leach equipment, under suitable control of pH of the leached slurry to be circulated, and thus industrial value thereof is extremely high.

Problems solved by technology

It should be noted that, at this stage, because temperature is still low and suitable operation condition has not been attained, the ore slurry as a raw material cannot be supplied.

That is, in the case where they are connected at a temperature of below 150° C., for example, use amount of industrial water to be supplied instead of the ore slurry increases, resulting in generation of a large amount of discharged water.

In this sense, it is desirable that they are connected at a temperature side as higher as possible near 180° C. However, in the case where they are connected at a temperature of over 180° C., for example, at equal to or higher than 200° C., difference between vapor pressure in the autoclave and vapor pressure in the flash tank becomes large, and thus pressure-like impact generates onto the flash tank in connection, and in the worst case, a valve or inner-lining brick of the flash tank are damaged.

In the former case, due to use of industrial water, discharged water generates in that amount, however, cooling rate is fast and thus temperature can be decreased in a shorter time.

In addition, in the latter case, although there is no discharged water generation, cooling rate is slow and thus a longer time is required in temperature decrease.

It should be noted here that the situation leading to inevitable shutdown of the above High Pressure Acid Leach equipment includes, other than shutdown accompanied with the above scheduled inspection and repair, the generation of emergency such as a process trouble, which could give tremendously bad influence on safety or environment; or the case of generation of a relatively small scale trouble such as off specifications of intermediate products in the ore slurry preparation step of a prior step of the leaching step, or the neutralization step or the sulfurization step and the like of the subsequent steps.

However, in a trouble of the steps other than the above leaching step using the High Pressure Acid Leach equipment, the above relatively small scale troubles generate in many cases, and in such troubles, because of no failure in the High Pressure Acid Leach equipment itself, there was required that, by maintaining operation of the High Pressure Acid Leach equipment as longer as possible, operation shutdown time shall be shortened, and decrease in operation efficiency shall be suppressed, as well as frequency of shutdown and start-up of the equipment shall be decreased.

However, even by such countermeasures, shutdown of the leaching step was necessary, in the case of over limitation.

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