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Catalytic Reactors
Microactivity Reference
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MICROACTIVITY-Reference, 2004 |
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The
MICROACTIVITY-Reference, designed in 2004, patent nº
PCT/ES2005/070079, collects in one unit 16 years of experience and co-operation
with different research groups. This effort succeeded into an equipment that
covers all the necessities that our co-operators have demanded for these
equipments: maximum repetitivity and reproducibility, maximum versatility
(Basic Unit at atmospheric pressure achieves the maximum level of performance
by means of optional packages), maximum programming capacity of experimented
works, friendly use and remote control via the Ethernet, software packages
integration of the analysis systems. |
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The
MICROACTIVITY-Reference is an automatic and computerized
laboratory reactor for catalytic microactivity reactions with reactor bypass,
preheater, evaporator, pressure control valve and other process layouts in hot
box, which avoids possible condensation of volatile products, at the time that
preheats the reactants efficiently. The equipment consists of an ATMOSPHERIC
PRESSURE BASIC UNIT and some series of EXTRA PACKAGES that improve or modify
its efficiency. |
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MICROACTIVITY-Reference, 2004
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The
MICROACTIVITY-Reference contains a single structure with an
electronic unit, control and MFC's system and includes a hot box where the
reactor and process valves are located. The system has a local control and
on-line remote control, based on TCP/IP Ethernet communications with
distributed control structure. A complete and elaborated security system is
integrated in microprocessor, independent of the computer. For reactions at
high pressure that involve separation of gases and liquids, a new system of
level control of the condensed liquid is introduced with almost no dead volume
(0.3 ml). This way the sample of the liquid outlet is the condensed product
mixture, formed during the latest minutes of reaction. |
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A wide variety of reactions have been carried out in our
reactors: Hydrocracking, Hydrotreating, Isomerization, Hydrogenation,
Hydrodesulphurization (HDS), Oxidation, Hydrodenitrogenation (HDN),
Polymerization, Reforming, Steam Reforming, etc. |
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You can obtain a more detailed information clicking on
technical features or data sheet. |
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EXPERIENCE IN CATALYTIC MICROACTIVITY REACTORS |
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Chemical catalysts play a key role in enhancing and
controlling chemical reactions in a variety of processes of the refinery,
petrochemicals, fine chemicals and fats & oils industries. |
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Due to the fact that at the beginning the PID Eng&Tech
staff was in the investigation team of the Institute of Catalysis and
Petrochemistry, most of our activities for years have been mainly, but not
exclusively, focused on the development of highly efficient catalytic systems
for different reactions. |
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Nowadays, PID Eng&Tech is a technological pacesetter
across the entire spectrum of catalytic processes. Our leadership now, as in
the past, is based firmly on innovative technology.
We place a heavy emphasis on conducting joint R&D
projects of high-tech process technology. Strategic alliances with our
customers have induced some of the most important today's technological
solutions for a variety of catalytic processes. |
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Microactivity Reactor, 1994 |
During the latest years the PID Eng&Tech staff has
designed and constructed about 80 reactors to make catalytic microactivity
studies. We have found that current control technology, available in the
market, does not provide such equipments as microreactors with the necessary
quality features requested and sought by the researcher. That is why a great
deal of our efforts in R&D&i since 1989 have been centered on the
development of an appropriate technology, part of PID Eng&Tech's know-how
at present, such as: |
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- a fine pressure control when working with extremely low
flow rates through the reactor, so that it does not alter the flow conditions
through the catalyst bed, patent nº PCT/ES2005/070080.
- a continuous recovery of the condensed liquid at high
pressure which can be operated with a minimum "dead volume" (at present ~ 0.4
ml or less), to ensure that the samples of the outlet products are taken for
analysis almost in "real time", patent nº PCT/ES2005/070081.
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Microactivity-Pro, 1999
As a result of our efforts and commitment to our customers, in
1994 we developed Microactivity Reactor (15 units in
operation) and in 1999 Microactivity-Pro automated reactor (22
units in operation), which enhances the capacity and performance of the former
one. These reactors have always been custom-made, following the specific
features of each user's process.
Four Runs Microactivity Test MAT-ASTM D3907
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Our Four Runs Microactivity Test Unit MAT ASTM D3907 is a
fully automatic and computerized laboratory reactor for the analysis of fluid
cracking catalysts (FCC). This MAT reactor is design to perform up to four FCC
test in automatic mode. The system has been prepared to carry out FCC test
following the norms described by the standard method ASTM D3907.
The MAT unit has been design to perform continuous control
up to four independent and consecutives FCC tests. The operator will be able to
adjust for each independent experiment stream time, catalyst/oil relationship,
reaction temperature, the regeneration times and temperature, gas flow, and
other parameters. Otherwise the operator can decided to run the experiments in
fixed and normalized conditions as described in ASTM D3907 norm.
The MAT unit assures quasi-zero dead volume using a
perfectly engineered reactor size, a precise pipe lengths and distances.
The oil supply is provided by the way of a HPLC pump what
assures maximum control, stability and precision dosage, using a previous
stabilization stage before dosage.
The system is set up with a four ways valve; this valve
assures few seconds of oil purge to guarantee a stable flow to the reactor.
Feeding periods can be configured from 12 to 200 seconds for 1 cc oil. Shorter
times can be reached for less amount of oil feed. Catalyst load of the reactor
is 0.5 to 6 gr. |
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To assure accuracy in reactor temperature, the system is
provided with a furnace based on radiant technology; this allows the best
temperature control under reactions conditions.
For reaction product analysis, the system automatically
separates liquid and gas fractions. Gases are collected by a burette for
automatic analysis at real run time, during regeneration times.
The system is able to reproduce two GC analyses per gas
sample, what assures data reproducibility.
The CO is converted to CO2 means a CuO reactor at
600ºC. During the catalyst regeneration step, the MAT has been set up for
coke quantification by a CO2 analyzer bases on the adsorption of infrared light
that is capable of measuring the concentrations of CO2. |
Multi-OPERANDO robot system
Multi-Operando system |
Currently PID Eng&Tech is working on a multi-OPERANDO
system for combinatorial chemistry (M. Bañares, PhD, I. Wachs, PhD).
This system is provided of either a microreactors battery or a matrix, which
undertakes an "in situ" analysis of catalysts feasible by means of different
spectroscopic techniques (Raman, UV-Vis, etc
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eases an "on-line" analysis of reaction products by means of gaseous
chromatography or mass spectrometry. |
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The system includes as well a XY-robot which makes possible
the movement sequence programming of the microreactors battery or matrix. This
way the detectors of spectroscopy analysis equipments are able to focus and
measure, sequently and automatically, over different zones in the catalyst beds
of each microreactor. |
Robot unit |
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Finally the microreactors battery or matrix movement is
synchronized with the sample injection of the reaction products into the
analysis equipments, in order to obtain the data on the alteration in the
structure and activity of the catalysts. |
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