Process for the production of alumina

Abstract

A process for the production of alumina comprising:

Description

[0001] The present invention relates to a process for the production of aluminum hydroxide containing material in particular for use in the preparation of catalyst carriers.

BACKGROUND OF THE INVENTION

[0002] The state of the art methods for preparing alumina include use of raw materials produced by precipitation as exemplified by mixing bases such as alkaline aluminate and alkaline hydroxide bases with an acid such as HNO3, H2SO4 and H3PO4, in addition to Al (NO3) and A12(SO4)3. Useful carriers for refinery processing catalysts are produced from alumina and intermediate products like pseudo boehmite owing their large surface area and high porosity.

[0003] The known methods for preparing alumina catalyst carriers are costly in terms of purchase of the acid and basic raw materials being employed in the preparation process and, furthermore, expense to pH adjustments, washing steps and wastewater treatment.

[0004] The general object of this invention is, thus, to provide an improved process for the production of alumina such as aluminum oxide and pseudo boehmite for use in the preparation of catalyst carriers, wherein production of alumina is carried out by simplified and inexpensive steps. Compared to the known methods, the advantages of the invention includes, furthermore, high product yield through reduced loss of material during the processing.

SUMMARY OF THE INVENTION

[0005] The process of this invention comprises the following steps:

[0006] a) dissolution of Gibbsite (A12O3, 3H2O) in nitric acid providing an acid solution of Al(NO3)3 by reaction (i)

A12O3, 3H2O+6HNO3→2Al (NO3)3+6H2O

[0007] b) thermal decomposition of the acid solution into aluminum hydroxides and NOx gases by reaction (ii):

2 Al(NO2)3+6H2O→A12O3; Z H2O+6NO2+(6−Z) H2O+3/2O2;

[0008]  and

[0009] c) regeneration of NOx gasses in one or a series of absorption towers to concentrated nitric acid according to reaction (iii):

6 NO2+3H2O+3/2 O26HNO3

[0010] The overall reaction, i.e. (i)+(ii)+(iii) is then:

A12O3, 3H2O+3H2O Al2O3, Z H2O+(6−Z) H2O,

[0011] wherein

Z=0.5-3

[0012] In a specific embodiment of the invention, NO2 being formed in the above reaction (i) is partly regenerated in absorption towers. Reaction (ii) results in formation of nitric acid that is recycled and utilised for dissolution of Gibbsite, which is the sole raw material in the process.

[0013] Though, due to minor loss of the nitric acid to be recycled, occasionally small amounts of nitric acid in addition to what is being currently regenerated have to be added, to maintain or enhance dissolution of the Gibbsite raw material.

[0014] Decomposition in the above step (b) may be performed by spraying the acidic solution from step (a) onto the inner surface of one or more rotary kilns with free supply of air at 300-700° C. However, by using this method, measures may be taken in order to prevent sticking of the product to the inner surface of the rotary kiln, e.g. by means of one or more sliding chains. In order to be efficient, the chains must be relatively heavy and are to be present inside each kiln in such a way that they slide down on surface, while the kiln rotates, and thereby prevent the solid material from adhering to the surface.

[0015] Adhesion of the prepared material from the decomposed acid solution to the inner side of said kiln may also be prevented by other physical or chemical means known in the art.

[0016] The alumina product can be further improved by addition of an organic compound capable of reducing nitrates. Those components can be glucose or similar compounds. The reaction between the organic compound and the nitrate will then generate a faster decomposition of the nitrates through minor local explosions, and, thus, reduce the size of the formed particles.

EXAMPLE

[0017] Preparation of alumina from aluminium nitrate (Al(NO3)39H2O).

[0018] 225 g Al (NO3)3.9H2O) are dissolved in 100 g water and 1 g 65% by weight HNO3. The solution is clear without any remaining crystallites.

[0019] The solution is then pumped into a preheated rotating furnace (length 1.5 m inclination 1°), rotating at 30 rpm. The temperature in the furnace is 350° C.

[0020] The pumping speed is around 5-20 ml/min. Alumina in its boehmite form starts to form when the solution comes into contact with the walls of the furnace by decomposition of the nitrates.

[0021] The formed product is in shape of very porous foam that can easily be grinded to a powder suitable for further processing.

Claims

1. A process for the production of alumina comprising: (a) dissolution of Gibbsite (A12O3, 3H2)) in nitric acid providing an acid solution of aluminum nitrate products; (b) decomposition at 300-700° C. with free air supply of the acid solution to alumina and NoX; (c) regeneration of the formed NOX to concentrated nitric acid and recycling of produced nitric acid to step (a); and (d) recovery of the alumina product formed in step (b) by means selected from spraying onto the inner surface of one or more rotary kilns, drying in a fluid bed, and drying in a steel band conveyor furnace.

2. A process according to claim 1, wherein decomposition of the acid solution in step (b) is enhanced by addition of an organic compound being active in reduction of nitrates.

3. A process according to claim 1, wherein the rotary kiln is equipped with one or more chains of a heavy material, which slide on the inner surface of the kiln, while rotating the kiln.