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PP-<strong>II</strong>I-41PLASMACATALYTIC REACTOR FOR PRODUCING ACTIVECARBON FROM NATURAL GASMakarov A.A. 1 , Makarov M.A. 1 , Makarov A.M. 1 , Trushkov J.J. 21 ZAO ECAT, Perm, Russia, mak_perm@mail.ru2 Perm state technical university, Perm, RussiaA plasma-and-chemical reactor for the treatment of natural combustible gases,flue gases consists of an input channel with a metal mesh filter and an outputchannel between which a power supply unit, a gas discharge assembly made in theform of the plasma generator, a catalyst chamber and a fan with a control unit arelocated.The gas discharge assembly made as the plasma generator consists of anisolation cassette with a set of plates made of high-porous honeycombed material(HPHM), a dielectric and an electroconductive plate. The catalyst chamber includes aheat- and gas-insulated partition; heating elements fixed on HPHM catalytic elementsmade of metal HPHMs of the chamber; catalytic elements made of high-poroushoneycombed materials and fastenings for heating elements.The power supply unit (the impulse high voltage power source) is constructedaccording to the power-bridge transformer circuit. The basic inductive element, i.e.the transformer, operates in the transit mode and does not save any magnetic power.It operates in symmetrical mode at low excitation currents. Due to this, such atransformer has smaller dimensions with the same capacity; its calculations areeasier. Low excitation current means less quantity of power accumulated in theleakage inductance. Hence, its suppression does not require complex dampingcircuits and switching-over processes in the transformer are considerably “quieter”.The high-porous honeycombed material permeable for the medium being purifiedis used as a discharge electrode. It is connected to one pole of the power supply; theother pole is connected to the electroconductive plate on the opposite side of thedielectric. The channel length is restricted by the distance between the HPHM cells.The number of micro-discharges increases proportionally to the voltage growth. Thustheir density increases which results in more effective use of the surface and morepower in the discharge area. The gas flow that passes through the permeable HPHMelectrode is turbilized, interacting with the chaotic porous structure of the electrode516
PP-<strong>II</strong>I-41material. Besides, the molecules of natural gas are destroyed both the discharge lowtemperatureplasma. HPHM electrode also serves as collecting self-regeneration gasfilter. Due to impact intercepting procedure the most fine-dyspersated particles,including the soot ones are deposited and aggregated on the plates. Free radicalreactions of destruction of organic compounds in the gaseous phase which began inthe gas mixture continue after the air passes the partition on the highly-developedHPHM surface with catalytic cover based on aluminum and rare-earth metal oxides.2 1476~3811671245517
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Boreskov Institute of Catalysisof t
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INTERNATIONAL SCIENTIFIC COMMITTEEV
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SILVER SPONSORThe organizers expres
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PL-1HOW TO DESIGN OPTIMAL CATALYTIC
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MULTIFUNCTIONAL DEVICES FOR INTENSI
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PL-3DESIGN OF CATALYTIC PROCESSES F
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PL-3Indeed preparation and testing
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PL-4The second part of the lecture
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PL-5Reactor designs with intensifie
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PL-6MEMBRANE REACTORS: STATE OF THE
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KEY-NOTE PRESENTATIONS
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KN-1description, that can be charac
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KN-2selective catalytic reduction o
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KN-3Fig. 1. Experimental burner of
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KN-4~200°C. This is based on the H
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KN-5for addressing the quality of t
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KN-6reaction with ethanol and the b
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KN-7at temperature lower than 873K,
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REACTION KINETICS AND REACTION ENHA
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OP-I-2RELATION BETWEEN THE ACTIVATI
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COMPARISON OF CHEMICAL AND ENZYMATI
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OP-I-4NONLINEAR PHENOMENA DURING ME
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OP-I-5SPECIFICITY OF THE OSCILLATIO
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OP-I-6TRENDS IN BISTABILITY DOMAINS
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OP-I-7NON-STEADY-STATE CATALYST CHA
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OP-I-8TRANSIENT KINETIC STUDIES OF
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OP-I-9A REDOX KINETICS FOR THE PART
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OP-I-9500Flow of Air = 0.3 m 3 (STP
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OP-I-11ELUCIDATION OF THE REACTIVIT
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KINETIC MODELLING OF THE JOINT TRAN
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OP-I-13n-HEXANE SKELETAL ISOMERIZAT
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OP-I-14the slow branch of kinetic c
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OP-I-15The hydride palladium comple
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Energy Conservation (field j)∂∂
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OP-I-17Selectivity (mol. %)10099989
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OP-I-18According to GLC the main pr
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OP-I-19and slug dimensions, formati
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OP-I-20A RANS volume of fluids [1]
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OP-I-21the physical-chemical charac
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OP-I-22calculated values of pressur
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OP-I-23where L c - capillary length
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OP-I-24and diffuse transmission thr
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OP-I-25effect of bubble break-up wo
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OP-I-26strong influence on the soli
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OP-I-27wHCOOH=1+K2K1(1 + K3⋅ P⋅
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OP-I-28dimensional profiles detecte
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OP-I-29results. The results of the
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OP-I-30Fig. 1. Hydrodynamics and co
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OP-I-31Convection and diffusion wit
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TEMPERATURE RISE DURING REGENERATIO
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OP-II-2[4]. Similar temperature pro
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OP-II-3(Fig, 1 a, b) upon testing i
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OP-II-4In the second step optimizat
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OP-II-5membrane contactors were stu
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OP-II-6reaction over Cu/CeO 2-x cat
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OP-II-7is modelled by means of a tw
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OP-II-8the reactor [6]. However, th
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OP-II-9Figure 1. Computed volume fr
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OP-II-10assumes variables’ distri
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OP-II-11oxide support, it comes tha
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OP-II-12was connected to G.C. via s
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OP-II-13catalyst bed was 6 mm. Thre
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OP-II-14as coolant is an important
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OP-II-15Flow (L/h)7654321Bottoms ra
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OP-II-16(4) The gas recirculation r
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OP-II-17Catalytic reactions were ca
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OP-II-18At steady surface coverage
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OP-II-19gaimpulsegeneratorwateFig.
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OP-II-20examined (see Figure 1). Th
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OP-II-21References[1]. M.P. Dudukov
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OP-II-22of the hydrogen oxidation a
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OP-II-23TemperaturesensorsThe efflu
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OP-II-24of reactant conversions. Pa
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OP-II-25(surface) ‘wall-reaction
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OP-II-26It was found that the 10 wt
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OP-II-27non-flow type. During the M
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OP-III-A-1A NEW SIMPLE MICROCHANNEL
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BUBBLING FLUIDISED BED PYROLYSIS OF
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PINEWOOD PYROLYSIS UNDER VACUUM CON
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OP-III-A-5PYROLYSIS OF HDPE IN A CO
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OP-III-A-6REACTORS FOR THE GREEN TR
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DEHYDRATION OF GLYCEROL TO ACROLEIN
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OP-III-A-8LACTIC ACID BASED ON BIO
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RECOVERY OF ACETIC ACID FROM PYROLY
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OP-III-A-10LIPASE-CATALYZED REACTIO
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OP-III-A-11INVESTIGATION ON THERMOC
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OP-III-A-12SELECTIVE CATALYTIC DEOX
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ETHANOL STEAM REFORMING OVER COBALT
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OP-III-A-14HYDROTREATMENT CATALYSTS
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ORAL PRESENTATIONSSECTION IIIChemic
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OP-III-B-1Reactor parameters:Intern
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OP-III-B-2JOINT STEAM REFORMING OF
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OP-III-B-3LANDFILL BIOGAS PURIFICAT
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OP-III-B-4MODELING AND SIMULATION O
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OP-III-B-5DemonstratorThe medium-te
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OP-III-B-630/19.6 Nl/min (space vel
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OP-III-B-7mixed in the ratios: 94,8
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OP-III-B-8Table 1.Material balance
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OP-III-B-9Based on the results of t
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OP-III-B-10On this basis it can be
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OP-III-B-11Similar trends caused by
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OP-III-B-12(mol/s g cat)x108r4,6-DM
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OP-III-B-13carbon in Wyoming coal i
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OP-III-B-14MODELING PRODUCT DISTRIB
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OP-III-B-15COMBINED TECHNOLOGY OF U
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MATEMATICAL MODEL FOR DOWNDRAFT BIO
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OP-III-B-17CATALYTIC DEHYDRATION OF
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OP-III-B-18SYNGAS AND HYDROGEN PROD
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POSTER PRESENTATIONSSECTION I
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PP-I-1influence of the direction of
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PP-I-2At the agitation of the liqui
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PP-I-3NOLINEAR PHENOMENA IN CATALYT
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PP-I-4A NEW APPROACH TO KINETIC STU
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PP-I-5KINETICS OF PROX REACTION OVE
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PP-I-6PHENOMENA OF SUPERADIABATIC T
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ELECTROMAGNETIC REACTOR OF WATER TR
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PP-I-8DIRECT SYNTHESIS OF HYDROGEN
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PP-I-9DYNAMICS OF FIRST-ORDER PHASE
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PP-I-10ELECTROCHEMICAL OXIDATION OF
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PP-I-11CHEMPAK SOFTWARE PACKAGE: OP
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PP-I-12COMPUTER SIMULATION OF ENDOT
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PP-I-13MODELLING KINETICS OF PROCES
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PP-I-14THE INVESTIGATION OF REACTIO
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PP-I-15The qualitative picture of s
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Thus, knowing the composition of ra
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PP-I-17current density. Preliminary
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PP-I-18Hydrogenation kinetics was d
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PP-I-19the active mixing, amplitude
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PP-I-20where r, h indicate the radi
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PP-I-21model is very anisotropic be
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PP-I-22- Reduction of the number of
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PP-I-23oscillations of intermediate
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PP-I-25SYNTHESIS OF ETHYLENE OXIDE
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PP-I-26OPTIMUM KINETICS FOR POLYSTY
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PP-I-27TableSpecific surface area (
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PP-I-28γ-preirradiated sample), th
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PP-I-29commercial CFD solver FLUENT
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PP-I-30modulus, a considerable decr
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PP-I-31The destruction ways of CF 3
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PP-I-32[7]. Karoor S, Sirkar K. Gas
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PP-I-33above 750°. The catalytic p
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PP-I-35REVERSE FLOW REACTOR WITH FO
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FLOW-RECIRCULATION METHOD FOR INVES
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TO A PROBLEM OF OPTIMIZATION OF FUN
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PP-I-38THE INFLUENCE OF REACTION MI
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PP-I-39METHANOL OXIDATIVE STEAM REF
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PP-I-41CORRECT INVESTIGATION OF THE
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PP-I-42NEW APPROACH OF DEFINITION O
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PP-I-43STREAM HEAT EXCHANGE OF AERO
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PP-I-44HIGH TEMPERATURE OXYGEN TRAN
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PP-I-45KINETICS OF TRANSESTERIFICAT
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MATHEMATICAL MODELING AND OPTIMIZAT
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PP-I-47The basic side reaction is r
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PP-I-49EXPERIMENTAL STUDY OF THE HA
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PP-I-51ON THE KINETICS AND REGULARI
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PP-I-52DIFFERENTIAL THERMAL ANALYSI
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PP-I-53oxidation reaction demonstra
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PP-I-54of reaction. It is establish
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PP-I-55effects, are energetically c
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PP-I-56The experiments and simulati
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PP-I-57In the studied range of temp
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PP-I-58HeadingsAdvances in Chemical
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PP-I-59calculated. During the aroma
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PP-I-60with honeycomb catalyst) act
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Т - temperature, K, D eff - effect
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PP-I-62stirring rate were adopted u
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PP-I-63m 2 = (k 1 y 0 1 +k -1 +k 1
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POSTER PRESENTATIONSSECTION II
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PP-II-1values of operating paramete
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⎡⎛⎢⎜bF⎣⎝=2ab ⎞ 6+ ⎟
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PP-II-4HONEYCOMB MONOLITHIC CATALYS
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MATHEMATICAL MODELING OF THE ALUMIN
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PP-II-6MODELING OF VINYL ACETATE SY
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PP-II-7СENTRIFUGAL DISK REACTORAvv
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PP-II-83) An opportunity of operati
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PP-II-10UV-ACTIVATION OF METHANE CO
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PP-II-11COMBINED APPROACH (FMEA- HA
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PP-II-12Testing the pilot variant o
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PP-II-14NOVEL MICROREACTOR FOR THE
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PP-II-15of 1-2.5 lead to a decreasi
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PP-II-16stages. Kinetic parameters
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PP-II-17whiskers, which assure an a
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PP-II-18с m , с cat - density of
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PP-II-19decrease. So, the potential
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PP-II-20products became a mixture o
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PP-II-21A numerical algorithm and s
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PP-II-22motions at any external con
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PP-II-23One of the main technologic
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PP-II-24100 m x 250 μm x 0.5 μm,
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PP-II-25A model was developed to ca
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PP-II-26The results of calculations
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PP-II-27modes of reaction and two d
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PP-II-29OZONE-DESTRUCTION REACTOR B
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PP-II-30Fig. 1. Axial profile of me
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PP-II-31isobutylene in butene fract
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PP-II-322.5x10 -3 ( i )2.5x10 -3 (
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PP-II-33No olefinreadsorptionWith o
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PP-II-34using titania or Ag-doped t
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PP-II-35accidents, is condition dep
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PP-II-36be seen that at temperature
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PP-II-37the solid phase solute conc
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PP-II-38As shown in Table 1, the ca
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PP-II-39better to the obtained in t
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PP-II-40Hydrodynamic regime in the
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PP-II-41activity, relative unit1,21
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PP-II-42One of the major indicators
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PP-II-43These conditions are confor
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PP-II-44For the hepten, alpha-methy
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PP-II-46PARTIAL OXIDATION OF METHAN
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PP-II-47DEVELOPMENT OF VORTEX APPAR
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MODELING OF CFTALYTIC α-OLEFINS OL
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PP-II-49Hinselwood kinetic equation
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3) iterate concentrations at a cut
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PP-II-51data such flow sheet provid
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PP-II-53ON THE TECNOLOGY OF TECHNIC
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PP-II-54PROPYLENE POLYMERIZATION AN
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REACTOR FOR LIQUID-PHASE PROCESSES
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PP-II-56MODELING OF CATALYTIC MICRO
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PP-II-57MATHEMATICAL MODELING OF BE
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PP-II-58HONEYCOMB CATALYSTS WITH PO
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POSTER PRESENTATIONSSECTION IIISECT
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ReferencesPP-III-1[1]. A.N. Pestrya
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PP-III-2Table1. Percentages of diff
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PP-III-3conversion for the reaction
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PP-III-4900Reformer temperature (K)
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PP-III-5Catalytic performance of th
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PP-III-6optimization permit better
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PP-III-8DE-NO X SYSTEM BASED ON H 2
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PP-III-9SEPARATION BETWEEN CHLORIDE
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CONVERSION OF WASTE COTTON TO BIOET
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PP-III-12THE METHOD OF GLYCERIC ACI
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NOx conversion vs. temperature is p
Page 465 and 466: PP-III-14intermetallic diffusion at
Page 467 and 468: PP-III-15The conversion of O 2 was
Page 469 and 470: PP-III-16H 2consumpition (a.u)(a)39
Page 471 and 472: PP-III-17the characteristic structu
Page 473 and 474: PP-III-18Figure 1. Influence of tem
Page 475 and 476: PP-III-19(a)(b)CH 4conversion, %100
Page 477 and 478: PP-III-20take into account own size
Page 479 and 480: PP-III-2110080CS-18CS-34CHZ30CHZ801
Page 481 and 482: EXPERIMENTALPP-III-22We synthesized
Page 483 and 484: PP-III-23Base composition component
Page 485 and 486: PP-III-25CO REMOVAL AT THE MICROSCA
Page 487 and 488: HYDROGEN PRODUCTION FROM METHANOL U
Page 489 and 490: PP-III-27NON CATALITIC PRODUCTION O
Page 491 and 492: PP-III-28Different reaction conditi
Page 493 and 494: PP-III-29followed by WGS reaction.
Page 495 and 496: PP-III-30As a solvent-coreactants w
Page 497 and 498: PP-III-31It was concluded that on t
Page 499 and 500: PP-III-32Hydrogenolysis of glycerol
Page 501 and 502: PP-III-331,6W 0, μmol Н 2/min1,20
Page 503 and 504: PP-III-34preparation (glass fiber f
Page 505 and 506: PP-III-35In the modification proces
Page 507 and 508: PP-III-36The kinetics of acid hydro
Page 509 and 510: PP-III-37reaction: i) C=O double bo
Page 511 and 512: PP-III-38methane and carbon monoxid
Page 513 and 514: PP-III-39from 25 to 60, which was d
Page 515: PP-III-401% w/w for Pd with respect
Page 519 and 520: PP-III-43METHANOL AND DIMETHYL ETHE
Page 521 and 522: PP-III-44goal is attained by using
Page 523 and 524: OLIGOMERISATION OF TERTIARY AMINE L
Page 525 and 526: PP-III-47meter (Shimazu Co.; TOC-50
Page 527 and 528: PP-III-48the range of 29-87 kJ/mol
Page 529 and 530: PP-III-49determine the optimal type
Page 531 and 532: PP-III-50NEW CONCEPT FOR A SELF CLE
Page 533 and 534: PP-III-51HYDROGEN PRODUCTION BY MET
Page 535 and 536: PP-III-52CATALYTIC UPGRADING OF PRO
Page 537 and 538: PP-III-53CATALYTIC CONVERSION OF FI
Page 539 and 540: PROCESS FOR THE PRODUCTION OF BUTYL
Page 541 and 542: PP-III-55been previously fixed and
Page 543 and 544: PP-III-56The influence of reaction
Page 545 and 546: PP-III-57sample does not contain so
Page 547 and 548: PP-III-58The re-activation of the e
Page 549 and 550: PP-III-59The aim of this work is th
Page 551 and 552: PP-III-61BIODIESEL FROM MICROALGAE
Page 553 and 554: DEVELOPING MICROFLUIDIC DEVICE WITH
Page 555 and 556: THREE-PHASE DIRECT OILS HYDROGENATI
Page 557 and 558: Co-BASED CATALYSTS FOR THE HYDROLYS
Page 559 and 560: PP-III-65KINETIC STUDY OF THE CATAL
Page 561 and 562: PP-III-66PRODUCTION OF HYDROGEN AND
Page 563 and 564: PP-III-67ENHANCED GASIFICATION OF P
Page 565 and 566: PP-III-68INFLUENCE OF SPILLOVER ON
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PP-III-69AEROBIC OXIDATIVE COUPLING
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PP-III-70MECHANISMS FOR CHEMICAL RE
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PP-III-70SBS molecules and increase
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PP-III-71and as a resut, could enha
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PP-III-72conversion). Al 2 O 3 /PSS
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PP-III-73SBA50TiSBA% Transmittance5
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PP-III-74stove heating. Another par
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PP-III-75TG [%]0-10-20-30380°C400
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PP-III-76The elementary version of
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PP-III-77thermodynamically enhanced
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PP-III-78GFC textileStructuringmeta
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PP-III-79All the prepared spinel-ox
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PP-III-80Our new process is polluti
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PP-III-81Fig. 1. Scheme of the biog
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PP-III-82Pic. 1 Pic. 2Pic. 1. Schem
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ARKHIPOV Vladimir AfanasievichResea
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CENTENO Felipe OrlandoNúcleo de Ex
Page 601 and 602:
FLID Mark RafailovichScientific Res
Page 603 and 604:
HOSEN Mohammad AnwarUniversity of M
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KOZLOVA EkaterinaBoreskov Institute
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MAKARSHIN Lev LvovichBoreskov Insti
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ONSAN Zeynep IlsenDepartment of Che
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REBOLLAR MoisesInstituto De Investi
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SHEIKH Munir AhmedTraining and Staf
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SULMAN Esfir MikhailovnaTver Techni
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ZHAPBASBYEV Uzak KairbekovichKazakh
Page 619 and 620:
OP-I-3 Pécar D., Gorsek A.COMPARIS
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OP-II-3Kucherov A.V., Finashina E.D
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OP-III-A-9 Rasrendra C.B., Girisuta
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PP-I-9Bykov V., Tsybenova S.B.DYNAM
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PP-I-43 Pechenegov Y.Y., Kuzmina R.
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PP-II-10 Basov N.L., Oreshkin I., T
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PP-II-45 Stepanek J., Koci P., Kubi
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PP-III-19 Fedorova Z.A., Danilova M
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PP-III-53 Pölczmann G., Valyon J.,
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XIX International Conference on Che
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