N23
tive. 5. Any products methane
(e.g.
made directly
methanol)
will
more reactive than methane almost
certainly
undesirable
siastes, ‘The race is not always to the swift,
from
nor battle to the strong” -
be much
tend to react further to
end products.
On the Meaning of Surface Area Meas-
First he deals with the most effective way at present
of getting
ducts from methane, ming for ammonia
chemical
ture, which currently direct oxidation
urements for Microporous
BET surface
manufac-
uses about 7% of all
workers,
despite recent claims in the area. Oxidative been
to e.g.
the subject
ethene,
of intense
work in the past few years, suggests
that there
Benson
process,
world-wide
of about
methane
lems: how feasible is it to handle the enormous
quantities
of concentrated
chloric acid generated
during the reaction?
“Despite the enormous
contribution
by chemists in academia but intractable producing viable.
of reacting
meth-
we are a long way from
a process that is commercially
This
chemical
made
to the fascinating
problem
ane selectively,
hydro-
is where
engineer
ancial constraints
the
working
chemist
and
under the fin-
of industry have a major
par-t to play.” Parkyns describes soline process tive coupling
of methane,
as possibly
process nearest to commercial
metal
the
(J.A. Cape and
Kibby, J. Colloid
Interface
Sci., 138
a timely analysis
Nitrogen
adsorption
of
experi-
ments were carried out at 77 K and 0.0050.74 atm on a series of Na-Y zeolite/ &-alumina mixtures ranging from pure zeolite to pure alumina. The results showed that the conventional porous
BET surface area of a micro-
solid,
catalyst,
(mesopores term
such
as zeolite
and macrostructure)
proportional
term was calculated and depended
vol-
factor in the latter
from a simple model,
on the pressures
the BET fit. A consistent areas and micropore
used in
methodology
for obtaining
BET equation
area and a
to the micropore
ume. The proportionality
developed
cracking
is the sum of an external
external volumes
was
surface from the
and t-plots.
Catalytic Conversion
of Propane to
Ethene
realisation,
with complex
photocatalysis
and bio-
catalysis are 21 st century commercial
pro-
jects at best. He concludes:
“I therefore
leave you with the quotation
from Eccle-
Recent US patents
Volume 67 No. 2 -
(Nos. 4929791 and
4929790) to W.W. Keading
and E.W. Va-
lyocsik of Mobil Oil Co. describe a catalytic process for converting
propane
to ethene
over either zeolite ZSM-23 or ZSM-50. Productivity
may be increased
ing the catalyst applied catalysis -
routine
paper with the title above
on dear crude oil
gas. Reactions
hydrides,
is zeolite
the
the Arco gas-to-ga-
(GTG), which uses oxida-
but even this depends and cheap
known
results. A recent
the subject.
to
but there are clearly prob-
have
(1990) 515) contains
30%. The
via chloromethanes,
who
method gives misleading CL.
but Parkyns
converting
high octane gasoline is very attractive
has
may be an inherent
limit of C2 products
are
measure-
with a metre rule. An exception
still looks a difficult goal,
coupling,
area measuremtints
usually taken as unambiguous
ments, almost as ifthey had been obtained
in the UK. The
of methane to oxygenates
such as methanol
Materials
pro-
that of steam refor-
and methanol
the natural gas consumed
methane
but, as the cynic
has added, ‘that’s the way to bet”.”
itself and will
3 January
1991
either by treat-
with SOa (either prior to
N24
cracking
or with catalytic
cracking). 600°C
amounts
Temperatures
with
remarkable
ethene. For example,
during
vary from 500 to selectivities
to
with ZSM-23, having
a SiC2/A1203 ratio of 83:1, and with SOn pretreatment,
the selectivities
wt.-%toethene,
were
46.3
18.3wt.-%topropeneand
29.4 wt.-% to methane
carbons
and toxic pollutants
must equal
20%. Fleets of automobiles
of 10 or more
in the two dozen smoggiest
cities must run
80%
today’s
more
mobiles
cleanly
than
only
auto-
Trucks must be 50% cleaner!
the area of toxic emissions,
at 10% conversion
by 15%. By
the year 2000, the reductions
regulated
seven
In
the existing law
chemicals
(since
with a WHSV of 3.46 h-’ at 600°C. At 600°C
1970); however,
with a WHSV of 0.86 h-‘, they obtained
that, over the next ten years
52% conversion
the polluting plants must use the best tech-
with ca. 30% selectivity
to
ethene and 31 wt.-% to methane,
the new law stipulates
nology available formaldehyde
of U.S. Clean Air Law
of
to reduce their emissions
of 189 chemicals Highlights
a majority
by 90%. Benzene
must be controlled.
spect to acid rain: a total
and
With re-
of 111 of the
dirtiest power plants in 21 states must cut No doubt about
the
changes
many
of you
recent
have
legislation
of, and
heard
emissions
to the
clean air laws in the United States. The Wall Street
dioxide
1990 (pages Al
of Monday,
and A7) provided
useful comparisons the original
October
29, some
of the existing law vs.
proposal
by President
Bush
emissions
by utilities is imposed
oxide emissions
by 2 million tons a year
(about 25%), beginning that this pioneering
gress and signed by the President. While it
impact upon catalysis
would be inappropriate
many new opportunities
here, some of the more significant ards with regard to tailpipe 1994 automobiles of the nitrogen
oxides
hydrocarbons;
tailpipe
acti-
for
Methane Activation
of 30%
standards
now
for 10 years
100,000 miles as opposed
The
or
to the current 5
years or 50,000 miles; warranties
on pollu-
to existing law,
5 years and 50,000 miles.
In the area of alternative
underthe
sponsored
research
recently
project
seven different
the aim being to develop oxidation
products
pre-
have
on methane collabora-
laboratories
new catalysts for
of methane
or formaldehyde
been
Community
This project involves
tion between partial
fuels, white there
are no existing requirements
contracts
signed for a major European activation.
now must last 8 years or
80,000 miles, as opposed which stipulates
and offer
for research
and a 40% cut in
have to be maintained
tion equipment
will have an
research
stand-
emissions
with a reduction
in 1995. It is clear
legislation
vities in this area,
portions
with regard to smog were: tougher
by the
cap on the sulfur
by the year 2000! Utilities must cut nitrogen
and the final act as it was passed by Conto list all the details
power plants
must make cuts in sulfur dioxide year 2000. A nationwide
Journal
by the year 1995
and more than 200 additional
regarding
enhancements
sulfur dioxide
to give and/or
C2
meth-
anol and to examine various other aspects
vious laws, the final bill supports a reformu-
of the processes
lation of the gasoline
beds). The partners (with the names of the
(beginning
sold in the nine smoggiest mulation
cities; this refor-
will cut the emissions
applied catalysis -
in 1995) of hydro-
Volume 67 No. 2 -
senior
(e.g. the use of fluidised
investigators
Ruhr University, 3 January 1991
in brackets)
Bochum,
Germany
are the (Man-