Process for the removal of metals from carbon black

The invention relates to a process for the removal of metals, especially of iron and/or nickel and/or vanadium or their compounds, from carbon black. To this end, the invention provides for an aqueous carbon black suspension to be heated to a temperature of about 30.degree. to 90.degree. C., for chlorine to be passed therethrough with agitation. The chlorine gas is used in a stoichiometric excess, based on the metal content of the aqueous carbon black suspension. Next, the carbon black is separated from the aqueous suspension and dried.

The invention relates to a process for the removal of metals from carbon 
black by treating an aqueous carbon black suspension with an agent 
suitable for dissolving the metals, if appropriate at an elevated 
temperature, separating off the carbon black from the suspension and 
recovering the carbon black so purified. 
The combustion or partial gasification of oil or heavy oil, with the use of 
air or oxygen and, if appropriate, stem, results in the formation of 
carbon black which partially contains substantial amounts of metals or 
metal compounds originating from the metal(s) contained in the fuel or 
gasification raw material. Typical metal components are iron, vanadium and 
nickel, which are present in the carbon black in a proportion of between 
about 0.1 and 10% by weight, for example, in those cases in which the fuel 
subjected to combustion or gasification is a residue originating from the 
distillation of crude oil under vacuum. Carbon black obtained upon the 
combustion of such an oil is difficult to dispose of as metal(s) contained 
therein is (are) liable to corrode the combustion chamber. Apart from 
this, the carbon black contains metals which are rendered valuable by 
their price so that it is desirable for the metals or metal compounds 
contained therein to be removed and utilized. 
On the other hand, it is also desirable to have pure carbon black which has 
properties highly desirable for certain uses. In fact, it is not allowable 
for carbon black intended for further uses to contain more than a certain 
maximum of metal contaminants, in order to avoid harmful side-effects of 
the metals, for example catalytic effects or corrosion. 
It is therefore highly desirable to have a process permitting metals to be 
removed from carbon black originating from the combustion or gasification 
of oil, the metals and purified carbon black being suitable for further 
use. 
German Offenlegungsschrift No. 2,717,303 discloses a process for the 
recovery of metals, such as vanadium, from carbon black obtained on 
combustion of oil, the carbon black being extracted by means of an 
alkaline liquor and the metals being recovered from the alkaline liquor, 
preferably by liquid-liquid extraction. In this process, the carbon black 
is extracted with an aqueous sulfuric acid solution, having a pH value of 
1 to 2, and a portion of the metal is extracted. Next, the carbon black so 
treated is subjected to combustion in a furnace at 600.degree. to 
1,200.degree. C. The combustion residue is extracted with an aqueous 
solution of sulfuric acid, having a pH value of 0 to 2, in order to 
recover additional metal from the combustion residue. 
It is a disadvantage of this known process that two process steps are 
required to remove the metals from the carbon black. Furthermore, in the 
second process step the carbon black is subjected to combustion for as 
long as necessary to obtain an ash residue whereby further use of the 
carbon black is rendered impossible. In other words, this is a process 
relating exclusively to metal recovery. 
In those cases in which the carbon black used as feed material is one which 
is obtained in the form of an aqueous suspension containing 0.5 to 4% by 
weight of solid matter, the suspension being obtained by subjecting heavy 
oil or liquid or gaseous hydrocarbons to combustion at temperatures of 
between 1,200.degree. and 2,000.degree. C. and pressures of between 1 and 
80 bar, with admission of air or oxygen and steam, if desired, and 
scrubbing the carbon black-containing gas stream with water (compare 
German Auslegeschrift No. 2,515,633), it is customary for such suspensions 
to be treated with sulfuric acid at pH 1 and 90.degree. C. for 24 hours, 
with agitation. This treatment in fact permits 90% by weight of the 
vanadium to be removed from the carbon black isolated from the suspension, 
but only permits about 50% by weight of the iron and 30% by weight of the 
nickel to be removed therefrom. The replacement of sulfuric acid by 
hydrochloric acid or nitric acid, or the addition of an oxidizing agent, 
such as hydrogen peroxide or potassium permanganate, to the sulfuric acid 
solution, could not be found to add to improving the solubility of these 
metals. 
The present invention now unexpectedly provides a process wherein the 
carbon black suspension described above is treated with chlorine gas at an 
elevated temperature with the resultant removal, by dissolution, inter 
alia of 90 to 98% by weight of the nickel from the carbon black. 
The invention relates more particularly to a process for the removal of 
metals, especially of iron and/or nickel and/or vanadium or their 
compounds, from carbon black by treating an aqueous suspension of the 
carbon black with an agent suitable for dissolving the metals or their 
compounds, at an elevated temperature, if desired, and separating the 
carbon black from the suspension, which comprises passing chlorine gas 
with agitation through the aqueous carbon black suspension, having a 
temperature of about 30.degree. to 90.degree. C., separating the carbon 
from the aqueous suspension and drying it, the chlorine being used in a 
stoichiometric excess, based on the metal content of the carbon black. 
The carbon black used in accordance with this invention may contain about 
0.05 to 3% of iron and/or about 0.05 to 2% nickel and/or about 0.05 to 5% 
of vanadium or compounds of these elements. 
In those cases in which the feed material used in the process of this 
invention is carbon black which has been obtained by thermal conversion of 
hydrocarbons which are liquid or gaseous under normal conditions, in the 
presence of oxygen or an oxygen-containing gas and optionally of steam, at 
temperatures of about 1,200.degree. to 2,000.degree. C. and under 
pressures of about 1 to 80 bar, the separation, in accordance with this 
invention, of the carbon black from the carbon black-containing gas stream 
by means of water, invariably results in the formation of an aqueous 
suspension containing about 0.5 to 4% by weight of solid matter. This is a 
carbon black suspension permitting chlorine gas to be passed therethrough 
in an excess which amounts to about 10 to 100 times the amount 
stoichiometrically required, based on the metal content of the carbon 
black, the chlorine gas being passed through the aqueous soot suspension 
over a period within the range about 15 to 180 minutes. This processing 
step is based on the assumption that the highly reducing environment 
causes the metals to be present in the carbon black in their zero-valency 
state, that is to say in elementary form, and that they are oxidized by 
the chlorine supplied. 
More specifically, Fe is oxidized to Fe.sup.3+, V to V.sup.5+ and Ni to 
Ni.sup.2+. Even in the evant of only a portion of the metals being present 
in elementary form and another portion in the form of compounds, for 
example as sulfides, it is necessary to use an excess of Cl.sub.2. 
The process of this invention has also been found to produce technically 
beneficial results in all those cases in which the carbon black directly 
isolated from the gasification process or combustion off-gases are 
obtained in the form of pulverulent free-flowing material of which the 
metal content is too high to permit further use. 
In this event, it is merely necessary for the carbon black to be suspended 
in water and preferable for the resulting suspension to contain 5 to 30 
g/l of solid matter. Suspensions with higher concentrations of solid 
matter therein present a high viscosity. They are naturally considerably 
more difficult to stir or to convey by pumping, and it is difficult for 
chlorine to be passed therethrough. 
A further preferred embodiment of the process according to the invention 
provides for a straight-chain alcohol, preferably n-amyl alcohol, or a 
methyl ester or ethyl ester of an aliphatic monocarboxylic acid with 2 to 
4 C-atoms to be added to the aqueous carbon black suspension, in a 
proportion of 5 to 15 g of alcohol or ester per gram of suspended carbon 
black, so as to separate the carbon black in the form of granular 
material. After stirring for 1 to 3 minutes, the carbon black floats as a 
granular material on the water surface from which it can readily be 
recovered, for example by filtration. The material thus obtained contains 
about 10% by weight of carbon black, 30 to 40% by weight of water and 50 
to 60% by weight of alcohol. Next, it is heated to about 
150.degree.-350.degree. C. to evaporate alcohol and water, vaporous matter 
is condensed, the aqueous and alcoholic phases are separated and the 
alcohol, which is now saturated with water, is re-used for separation of 
further carbon black. Condensed water, which always contains some 
dissolved alcohol, is disposed of. Next, the filtrate coming from the 
carbon black separation stage is treated in conventional manner, for 
example by liquid-liquid extraction (compare C. HANSON: "Pecent Advances 
in Liquid-Liquid Extraction", Pergamon Press, Oxford 1971) so as to 
recover the metals or metal compounds therefrom. 
The process of the invention may be carried out discontinuously, for 
example in an agitator-provided vessel, or continuously, in which case it 
is advantageous to use a bubble column or packed scrubbing tower for 
passing chlorine gas through the aqueous suspension and a suitable 
agitator-provided vessel for the subsequent separation of the carbon 
black. 
The process of the invention compares favorably with the prior art methods 
inasmuch as it permits 90 to 95% of the iron and vanadium and 98% of the 
nickel to be removed from the carbon black, in a single processing stage. 
Furthermore, it permits the recovery of carbon black, whose favorable 
properties make it suitable for a variety of uses. Finally, the use of 
certain alcohols and esters to effect the separation of carbon black from 
the aqueous carbon black suspension results in the formation of a granular 
product which can be separated from the organic/aqueus phase without 
difficulties, for example by filtration.

EXAMPLE 1 
(Comparative Example) 
An aqueous carbon black suspension which contained 0.6% by weight of carbon 
black and was obtained on subjecting heavy oil to gasification at 
1,500.degree. C. and 60 bar by scrubbing the resulting carbon 
black-containing gas stream, and which contained 4,500 ppm of Fe, 3,200 
ppm of V and 6,500 ppm of Ni, was mixed with an amount of sulfuric acid 
sufficient for the resulting suspension to contain 10% by weight of 
sulfuric acid. After heating the carbon black suspension to 90.degree. C., 
it was stirred at this temperature for 24 h, and the carbon black was then 
separated from the water by adding 10 g of n-amyl alcohol/g of carbon 
black. Next, the whole was filtered. Alcohol and water were expelled from 
the filter residue, and carbon black which still contained 2,100 ppm of 
Fe, 290 ppm of V and 4,500 ppm of Ni was obtained,. 
EXAMPLE 2 
(Invention) 
4 liters of an aqueous carbon black suspension which contained 0.6 % by 
weight of solid matter, 6,300 ppm of Fe, 2,500 ppm of V and 5,800 ppm of 
Ni, were heated to 70.degree.-80.degree. C., and 20 liters of chlorine 
gas, corresponding to a 90-fold stoichiometric excess of chlorine, were 
passed therethrough with agitation and within one hour, and the carbon 
black was then separated from the aqueous phase by adding 10 g of n-amyl 
alcohol/g of carbon black. The carbon black was filtered, alcohol and 
water were expelled at a temperature of 200.degree. C., and carbon black 
which contained 200 ppm of Fe, 300 ppm of V and 170 ppm of Ni was 
obtained. 
EXAMPLE 3 
(Invention) 
The procedure was analogous to Example 2 except that the n-amyl alcohol was 
replaced by 8 g of methyl acetate/g of carbon black. The carbon black, 
freed from ester and water, contained 220 ppm of Fe, 350 ppm of V and 180 
ppm of Ni. 
EXAMPLE 4 
(Invention) 
The procedure was analogous to Example 2 save that the 20 liters/h of 
chlorine gas were replaced by 10 liters/h, corresponding to an about 
45-fold stoichiometric excess, which was passed through the carbon black 
suspension; the carbon black, freed from alcohol and water, contained 440 
ppm of Fe, 330 ppm of V and 190 ppm of Ni. 
EXAMPLE 5 
(Invention) 
The feed material was 4 liters of an aqueous carbon black suspension which 
contained 15 g/l of solid matter. It was prepared by stirring carbon black 
into water. It was carbon black which had been isolated as a free-flowing 
material from a stream of gas originating from the gasification of heavy 
oil. The carbon black contained 0.42% of Fe, 1.05% of V and 0.77% of Ni. 
Chlorine gas, corresponding to a 10-fold stoichiometric excess, was passed 
into the suspension over one hour at 80.degree. C. Next, 15 g of n-amyl 
alcohol/g of carbon black were added and the carbon black was separated as 
a granular material by filtration. The product, freed from water and 
alcohol at a temperature of 200.degree. C., contained 240 ppm of Fe, 540 
ppm of V and 110 ppm of Ni. 9n