 |
Description  |
|
|
This invention is concerned with improvements in and relating to the
manufacture of porous carbon.
Porous carbon may be used, inter alia, as a catalyst support, for example
for catalyst systems used for purifying the exhaust gases of automobile
engines. There are two principal requirements for such catalyst supports,
namely that they have adequate physical strength to withstand mechanical
and thermal stresses encountered in use whilst at the same time having as
high a specific surface area as practically possible.
It has now been found, in accordance with the present invention, that
porous carbon, suitable for use for example as a catalyst support, may be
produced from pitch and/or coal by a two-stage carbonisation process using
different pitch fractions separated from the pitch and/or coal by solvent
extraction.
According to the invention, therefore, there is provided a process for the
production of a porous carbon which comprises carbonising a first, solid
fraction (obtained from pitch and/or coal by solvent extraction) to
produce a first porous carbon, absorbing a second liquid fraction
(obtained from pitch and/or coal by solvent extraction) into the first
porous carbon, and carbonising the porous carbon containing absorbed
liquid fraction to produce a second porous carbon having a higher specific
surface area than the first.
The basic starting materials for use in the present invention are pitch
and/or coal.
Pitches and coals comprise a complex mixture of various hydrocarbons
(generally having a high content of aromatic materials-e.g. up to 80% by
weight in the case of coke oven coal tar pitches and from 50 to 60% by
weight in the case of petroleum derived pitches) and for use in the
present invention the pitch and/or coal is separated into fractions. by a
solvent extraction process using a succession of solvents and the
solubility or otherwise of the fractions in various solvents also serves
to characterise the fractions.
It will be a matter of choice as to which solvents are employed to separate
the pitch and/or coal into fractions, the basic principle underlying the
selection of the solvents being that the solvents have a range of
capabilities of dissolving the components of the starting material. We
have found that four convenient solvents for use in separating the
starting material into fractions, and by reference to which the fractions
may be defined are, in increasing order of solvent power for the
components of the starting material:
methanol,
n-heptane,
toluene, and
quinoline.
With reference to these four solvents, five fractions of pitch may be
defined, namely:
an .alpha.-fraction--solid insoluble fraction-insoluble in methanol,
n-heptane, toluene and quinoline;
a .beta.-fraction--solid fraction-insoluble in methanol, n-heptane and
toluene; soluble in quinoline;
a .gamma.-fraction--liquid/solid fraction-insoluble in methanol and
n-heptane; soluble in toluene and quinoline;
a .delta.-fraction--liquid fraction insoluble in methanol; soluble in
n-heptane, toluene and quinoline.
an .epsilon.-fraction--liquid fraction-soluble in methanol, n-heptane,
toluene and quinoline.
The principal fractions of interest for use in accordance with the
invention are the .beta.-fraction, which is preferably used as the solid
fraction carbonised to produce the first porous carbon; the
.delta.-fraction, which is preferably the liquid fraction used in the
production of the second porous carbon; and the .gamma.-fraction which,
when a liquid, may also be used alone or in conjunction with the
.delta.-fraction, as the liquid fraction used in the production of the
second porous carbon.
The .alpha.-fraction is an essentially insoluble residue and may be
discarded. However in the case of the ethylene cracker residue pitches, it
has been found that the content of .alpha.-fraction is low, e.g. of the
order of less than 2% by weight, so that it is not necessary to separate
out this fraction but it may be used in admixture with the
.beta.-fraction. Where, however, the .alpha.-fraction content is greater,
say 5% or more, as in the case of coals or coal tar pitches, then it is
desirable to separate out and discard the .alpha.-fraction. The
.gamma.-fraction, depending on the nature of the starting materal, may be
solid, semisolid or liquid in nature and when liquid may be combined with
the .delta.-fraction.
The solvent extraction is conveniently effected by contacting the starting
material with the various solvents in order.
Two procedures are possible. The starting material may be first contacted
with the most powerful solvent (e.g. quinoline) to dissolve out the
.beta.-, .gamma.-, .delta.- and .epsilon.- fractions. The resultant
solution is separated from the .alpha.-fraction, e.g. by filtration, and
then contacted with the next most powerful (e.g. toluene) to precipitate
out the .beta.-fraction which is separated out, e.g. by filtration. This
procedure is repeated using the solvents of decreasing solvent power to
separate out the .gamma.- and .delta.-fractions.
Alternatively, the starting material may be first contacted with the
solvent of the lowest solvent power (e.g. methanol) and then successively
with solvents of increasing solvent power. The procedure is conveniently
carried out in a vessel having a porous or perforated bottom, thereby to
obtain a solution of the fraction soluble in a particular solvent. The
fraction may then be removed from the solution by conventional means, e.g.
by distilling off the solvent, preferably under reduced pressure in the
case of higher boiling solvents such as quinoline.
The latter approach is preferred and a preferred mode of carrying out the
solvent extraction is summarised in the table below which also indicates
preferred temperature conditions for each step.
______________________________________
Solvent
Extraction
step Solvent Solute Residue Temperatures
______________________________________
1 Methanol .epsilon.-fraction
.alpha.-,.beta.-,.gamma.-
Warm, (e.g.
and 50-60.degree. C.)
.delta.-fractions
2 n-Heptane .delta.-fraction
.alpha.-,.beta.-and
Warm,(e.g.
.gamma.-fractions
50-60.degree. C.)
3 Toluene .gamma.-fraction
.alpha.-,and .beta.-
hot (e.g.
fractions
90-110.degree. C.)
4 Quinoline .beta.-fraction
.alpha.-fraction
hot (e.g.
90-110.degree. C.
______________________________________
As will be appreciated various pitches or coals will contain the various
fractions in varying proportions and it will be a matter of simple trial
to establish the relative fraction content of any particular pitch or coal
and it may, in some cases be desirable to employ a mixture of pitches
and/or coals as starting material in order to obtain the desired balance
of final fractions.
The pitches used as starting material may be coal tar pitches or pitches
derived from the distillation of petroleum refinary residues. The latter
are generally preferred in view of their more ready commercial
availability and their content of the desired fractions and an especially
preferred pitch is that derived from ethylene cracker residues. The coals
used as starting material are generally middle range coals and, as will be
appreciated, will generally be employed in finely divided or powered form
in order to expedite the solvent extraction process.
It may be noted that when using an ethylene cracker residue pitch, in which
the .alpha.-fraction content is low, the last step (using quinoline) may
be omitted and the combined .alpha.- and .beta.-fractions (obtained as
residues from step 3) used as first solid fraction.
When using the four solvents with ethylene cracker residue pitch, the
following fractions are obtained in the following approximate yields,
based on the weight of starting material:
.alpha.-fraction--1-2%
.beta.-fraction--20-35%
.gamma.-fraction--3-10%
.delta.-fraction--5-15%
As indicated above, the process of the invention is not limited to the use
of the four above solvents in the solvent extraction process--clearly
combinations of solvents having relative solvent powers for pitch and/or
coal fractions comparable to those of the four listed above may be
employed. The four listed solvents are however preferred in view of their
ready avialability. As a guide to the selection of other solvents two
criteria may be mentioned. Firstly the solid fraction (e.g. the
.beta.-fraction metioned above) should be capable of producing a
relatively coarse porous carbon (e.g. having a specific surface area of
50-250 m.sup.2 /gm).
Secondly, as an approximate guide, it is believed that the fractions noted
above have the following approximate average molecular weights (it being
appreciated of course that each is a mixture of compounds).
.alpha.-fraction-->400
.beta.-fraction--400-350
.gamma.-fraction--300-250
.delta.-fraction--<250.
The amount of liquid fraction added or absorbed in the first porous carbon
is suitably from 5-25% by weight, based on the weight of the first porous
carbon, and it has been found that amounts of this order are wholly
absorbed by the first porous carbon at temperatures of about 100.degree.
C.
The carbonisation of the solid fraction to produce the first porous carbon
is suitably carried out at a temperature of from 350.degree. to
450.degree. C., preferably from 400.degree. to 450.degree. C. and in the
absence of air, for example in an inert atmosphere such as nitrogen.
The pore size of the first porous carbon, prior to absorbtion therein of
the liquid fraction, may be increased by any conventional activation
process, for example by heating at 350.degree. to 450.degree. C. in air or
carbon monoxide or by chemical treatment using for example zinc chloride
or phosphoric acid.
The carbonisation of the first porous carbon containing absorbed liquid
fraction to produce the second porous carbon is also suitably carried out
under similar conditions to those employed for carbonisation of the solid
fraction.
The porous body produced with the invention is believed to comprise a
relatively macroporous carbon body (produced by carbonisation of the solid
fraction with or without subsequent activation) the walls of the pores
being coated with relatively microporous carbon produced by carbonisation
of the liquid fraction.
The resultant porous body may be further activated to increase its specific
surface, as described above. In this way the specific surface area of the
body may be increased from a value in the range 150 to 200 m.sup.2 /gm to
a value in the range 300 to 400 m.sup.2 /gm.
The resultant porous carbon may be used as a catalyst support and catalyst
may be introduced into the body by conventional means, for example by
depositing catalyst materials in the porous carbon.
In order that the invention may be well understood, the following Examples
are given by way of illustration only.
EXAMPLE 1
An ethylene cracker pitch having a ring and ball softening point of
105.degree. C. was extracted with toluene to give a mixture of .alpha.-
and .beta.-fractions (33% by weight of starting pitch) as residue.
The mixture of .alpha.- and .beta.-fraction was carbonised at 385.degree.
C. for 1 hour under nitrogen in a muffle furnace, with a reduction of
about 25% of its weight, to give a first porous carbon.
An equal volume of n-heptane was added to the toluene solution to
precipitate a .alpha.-fraction (about 5% by weight of original pitch).
This was filtered off and to the solution was added an equal volume of
methanol.
The solvents were distilled off from the mixture, the pressure being
reduced from atmosphere to 20 mm Hg and temperature being increased from
60.degree. C. to 110.degree. C., to leave a liquid .delta.-fraction (about
10% by weight of original pitch).
The .delta.-fraction was mixed with the first porous carbon (in an amount
of 24.4% by weight based on the weight of first porous carbon) at a
temperature of about 100.degree. C.
The resultant mixture was carbonised for 10 minutes at 400.degree. C. in a
muffle furnace under nitrogen, with a consequent reduction in weight of
about 10%. to produce a second porous carbon having a specific surface
area of 180 m.sup.2 /g (BET).
EXAMPLE 2
A coal tar pitch having a ring and ball softening point of 125.degree. C.
was extracted with Quinoline. The insoluble residue (.alpha.-resin),
amounting to 9% of weight of the pitch, was filtered off and discarded and
to the filtrate was added an equal volume of Toluene to precipitate a
.beta.-fraction. The .beta.-fraction, amounting to 30% by weight of the
starting pitch, was filtered off, dried and carbonised at 385.degree. C.
for one hour under nitrogen in a muffle-furnace, with a loss in weight of
about 20%, to give a first porous carbon.
An equal volume of n-heptane was added to the toluene solution and the
solvents evaporated, leaving a .gamma.-fraction of about 8% by weight of
the original pitch. The liquid Gamma fraction was mixed with the first
porous carbon (in an amount of 12% by weight based on the weight of the
first porous carbon) at a temperature of 100.degree. C.
The resultant mixture was carbonised for 15 minutes, at 425.degree. C., in
a muffle-furnace, under nitrogen, with a consequent reduction in weight of
about 5%, to produce a second porous carbon having a specific surface area
of 250 m.sup.2 /g (BET).
This material was further activated by heating in a muffle-furnace at
400.degree. C. in air for 10 minutes and the porous carbon so produced was
found to have a specific surface area of 340 m.sup.2 /g (BET).
EXAMPLE 3
A mixture was prepared of coal tar pitch having a ring and ball softening
point of 80.degree. C. and powdered coal (N.C.B. Rank No. 305), the coal
content being 30% by weight of the pitch and the mixing being conducted at
a temperature of 140.degree. C.
After extraction with quinoline was described in Example 2, the resin,
amounting to 6% by weight of the pitch/coal mixture, was filtered off and
discarded, and the .alpha.-resin was precipitated from the filtrate with
toluene as described in Example 2. The .beta.-fraction amounted to 25% by
weight of the starting mixture and after filtration and drying was
carbonised at 375.degree. C. for one hour under nitrogen in a
muffle-furnace, with a loss in weight of about 15%, to give a first porous
carbon.
An equal volume of n-heptane was added to the toluene solution and the
solvents evaporated, leaving a .gamma.-fraction of about 15% by weight of
the original pitch/coal mixture. The liquid .gamma.-fraction was mixed
with the first porous carbon (in an amount of 5% by weight based on the
weight of the first porous carbon) at a temperature of 100.degree. C. The
resultant mixture was carbonised for 10 minutes at 400.degree. C. in a
muffle-furnace, under nitrogen, with a consequent reduction in weight of
about 10% to produce a second porous carbon having a specific surface area
of 400 m.sup.2 /g (BET).
* * * * *
|
|
 |
|
 |
Description |
|
