EP2135493A1 - Systeme a plasma - Google Patents

Systeme a plasma

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Publication number
EP2135493A1
EP2135493A1 EP08738134A EP08738134A EP2135493A1 EP 2135493 A1 EP2135493 A1 EP 2135493A1 EP 08738134 A EP08738134 A EP 08738134A EP 08738134 A EP08738134 A EP 08738134A EP 2135493 A1 EP2135493 A1 EP 2135493A1
Authority
EP
European Patent Office
Prior art keywords
plasma system
electrodes
path
ions
stage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP08738134A
Other languages
German (de)
English (en)
Inventor
Edward Forde
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Limerick
Original Assignee
University of Limerick
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Limerick filed Critical University of Limerick
Publication of EP2135493A1 publication Critical patent/EP2135493A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32—Gas-filled discharge tubes
    • H01J37/32431—Constructional details of the reactor
    • H01J37/32715—Workpiece holder
    • H01J37/32724—Temperature
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32—Gas-filled discharge tubes
    • H01J37/32009—Arrangements for generation of plasma specially adapted for examination or treatment of objects, e.g. plasma sources
    • H01J37/32018—Glow discharge
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32—Gas-filled discharge tubes
    • H01J37/32431—Constructional details of the reactor
    • H01J37/32532—Electrodes
    • H01J37/32541—Shape
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01J—ELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32—Gas-filled discharge tubes
    • H01J37/32431—Constructional details of the reactor
    • H01J37/32798—Further details of plasma apparatus not provided for in groups H01J37/3244 - H01J37/32788; special provisions for cleaning or maintenance of the apparatus
    • H01J37/32816—Pressure
    • H01J37/32825—Working under atmospheric pressure or higher
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00—Generating plasma; Handling plasma
    • H05H1/24—Generating plasma
    • H05H1/46—Generating plasma using applied electromagnetic fields, e.g. high frequency or microwave energy
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00—Generating plasma; Handling plasma
    • H05H1/24—Generating plasma
    • H05H1/46—Generating plasma using applied electromagnetic fields, e.g. high frequency or microwave energy
    • H05H1/4645—Radiofrequency discharges
    • H05H1/466—Radiofrequency discharges using capacitive coupling means, e.g. electrodes
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05H—PLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H2242/00—Auxiliary systems
    • H05H2242/20—Power circuits
    • H05H2242/22—DC, AC or pulsed generators

Definitions

  • the invention relates to a plasma treatment system.
  • gas discharge at atmospheric pressure requires about 27000 V/cm across the electrode gap.
  • the electrodes are coated with a dielectric material in order to prevent sparking.
  • the coating is tough in order to reduce the pitting associated with the high voltage discharges. Also, they have rounded edges in order to avoid the creation of local high electric fields.
  • the applied voltage frequency is above one kHz and below about thirty kHz depending on the process gas.
  • Helium produces metastable ions that assist glow discharge while air contains O 2 which inhibits glow discharge.
  • dielectric barrier discharge (DBD) a large number of active species is produced. For glow discharge a minimum flow rate of process gas is required.
  • the transfer of electrical energy from inductors or capacitors to a high frequency discharge requires the matching of impedances for maximum power transfer.
  • the driving frequency is of the order of 5 to 30 kHz while the discharge has a current spike equivalent to several MHz for glow discharge and a large number of lesser spikes in the MHz region for DBD.
  • the capacitor impedance must supply this high current pulse.
  • a parallel inductor allows parallel resonance to create a high charge on the capacitor to supply the high current discharge for every half cycle.
  • a high voltage transformer is needed to raise the voltage from a level at which the system is operated. Three phase mains electricity can be used to get a 600VDC bus thus lowering the currents being switched and simplifying the construction of wound components. Doubling the single phase mains of 23 OVAC to create a 650VDC bus also serves to reduce the current.
  • the invention is directed towards achieving more effective plasma generation, with a higher density of ions.
  • a plasma system comprising:
  • a drive circuit for driving the pairs of electrodes so that gas flowing along the path is ionized
  • system further comprises a feedback means for returning some active species back to the start of the path.
  • the drive circuit controls electrode drive using pulse width modulated signals.
  • the drive circuit comprises a series resonant circuit followed by parallel resonant circuit for conversion.
  • the drive circuit comprises a central controller linked with an electrode drive circuit for each pair of electrodes.
  • the electrode drive circuits are isolated from the central controller by opto-couplers.
  • the electrodes comprise a common electrode on one side of the path for a plurality of electrode pairs and an opposing discrete electrode for each pair. In another embodiment, the electrodes have rounded edges on a side facing the path.
  • the edges have a radius in the range of 2mm to 4mm.
  • the electrodes are of aluminium material.
  • the electrodes have a dielectric coating.
  • the dielectric coating is of aluminium oxide.
  • the separation between opposed electrodes is in the range of 1.5mm to 5mm, preferably approximately 2.5mm.
  • the cross-sectional area of the path is in the range of 500mm 2 and 900mm 2 .
  • the distance between successive pairs of electrodes is in the range of 2mm and 6mm, preferably approximately 3mm.
  • the electrodes are in the form of a series of ridges on a base plate.
  • the base plate is integral with heat sink fins.
  • the drive circuit applies sufficient voltage to cause ion multiplication by collision.
  • the drive circuit applies a voltage across the electrodes in the range of 7kV to l5kV.
  • the voltage is approximately 12kV.
  • the circuit applies a drive frequency is in the range of 4kHz to 2OkHz across the electrodes.
  • in the frequency is in the range of 7kHz to 15kHz.
  • system further comprises means for pumping a gas along the path.
  • the gas is pumped at a pressure in the range of 0.5 bar to 1.5 bar.
  • the pairs of electrodes are driven in sequence, and the timing, voltage levels, and frequency of electrode driving causing an increase in ionized active species velocity and/or density.
  • the drive circuit drives each pair of electrodes sequentially in a flow direction along the path.
  • the drive circuit delivers an electrical phase to each pair of electrodes.
  • orientation of the drive is changed periodically to create a swirling motion of ions in the path.
  • system further comprises a catalytic converter for converting waste process gas arising from used ionized gas.
  • the system comprises a treatment chamber fed by the ionized gas outlet, and the catalytic converter is fed by the treatment chamber.
  • a textile treatment system comprising a plasma system as defined above.
  • a sterilizer system comprising a plasma system as defined above.
  • a chemical vapour deposition system comprising a plasma system as defined above.
  • an ozone generating system comprising a plasma system as defined above.
  • a method of treating a surface or item comprising the steps of operating a plasma system as defined above and directing ions from the path towards the surface or item.
  • the ions are directed to ' a person's skin for cosmetic or therapeutic treatment.
  • the ions are directed for sterilising medical equipment.
  • the ions are directed for surface treatment of natural or man- made fibres.
  • the ions are directed for surface treatment of films.
  • the ions are directed for surface treatment of engineering parts.
  • the ions are directed for surface treatment of food containers.
  • the ions are directed for surface treatment of food. In another embodiment, the ions are directed for surface treatment of gaskets to enhance their function.
  • Fig. 1 is a diagram illustrating a plasma treatment system of the invention
  • Fig. 2 shows an AC waveform for driving electrodes as derived from the digital control signals
  • Fig. 3 shows pulse width modulation timing for the system
  • Fig. 4 is a block diagram illustrating how a sine wave is created from an IGBT Bridge output
  • Fig. 5 is a diagram of an alternative electrode configuration
  • Fig. 6 is a diagram illustrating barrier discharge
  • Fig. 7 is a plot showing density reduction with distance from output
  • Fig. 8 shows a plot of the electron and ion density per stage
  • Fig. 9 is a sketch of an electrode cartridge of a system of the invention.
  • Figs. 10 and 11 are plots for an alternative embodiment
  • a plasma treatment system 1 is shown in Fig. 1.
  • a gas enters from the left hand side and passes through four electrode pairs 2, 3, 4, and 5, each pair providing an ionisation stage along a path 6. Also, there is a feedback path 7.
  • the electrodes are of aluminium and have an aluminium oxide coating.
  • the axial (in the direction of the path 6) separation of the pairs of electrodes is about 3mm and is generally in the range of 2mm to 6mm.
  • the transverse spacing between electrodes of a pair is 2mm, and more generally preferably in the range of 1.5mm to 5mm.
  • the voltage across each pair of electrodes is in the range of 7kV to 15kV and is in this embodiment 12kV.
  • the gas is air and the applied pressure at entry to the path is about 1 bar.
  • the electrodes 2, 3, 4, and 5 are shaped to provide a cross-sectional area through the path 6 of about 700mm 2 .
  • a high voltage sine wave causes breakdown of the gas in the gaps between the electrodes.
  • the output of the first stage contains some ions and a large number of excited species including metastables. Recombination occurs to some of the species while in transit to the second stage.
  • the species arriving at the second stage cause seeding of the next discharge at that stage and a larger amount of species is created than produced by the first stage. This is because the collision frequency increases with increase in the number of ions thus accelerating the production of further ions under an electric field.
  • the process continues through each successive stage, yielding a much higher density of active species than would be produced by a single pair of electrodes with an equivalent surface area. A new maximum density is reached after four stages depending on distance between stages, gas, and electrode material.
  • Fig. 2 is shown the sine wave that is derived from a pulse waveform.
  • the pulse is shown as being bipolar in order to represent the forward and reverse flows through the full bridge of insulated gate bipolar transistors (IGBTs).
  • IGBTs insulated gate bipolar transistors
  • the sine wave peaks are centred on the midpoints of the pulse.
  • Fig. 3 shows how the percentage ON time of the pulse can vary from 52% to 98%.
  • a short OFF time of 2% is required to allow for transistor switching delays.
  • the beginning of each pulse is delayed 2% from the start of the timing. This is repeated for the 100 to 200 count time when the voltage output is of the opposite polarity.
  • Fig. 4 shows how timing pulses from the pulse width modulator are used through opto-coupler circuitry to turn on pairs of transistors in the IGBT bridge.
  • the top right and bottom left transistors are ON current flows through a series inductor and capacitor, the parallel combination of C and the transformer primary and returns via a second series inductor.
  • the two inductors in series with the resonant series capacitor are tuned at the resonant frequency to pass the fundamental signal.
  • the capacitor across the primary is used to tune the resonant frequency of the parallel circuit on the transformer output.
  • Fig. 5 shows that the electrodes may be comprised of one common electrode with a number of individual electrodes. Multiple electrodes may be constructed on one block of metal with channels to isolate the electrodes and their discharges. Electrodes on one side of the flow channel may be without a dielectric barrier. Using barriers on both opposing electrodes produces a similar discharge for each polarity of applied voltage.
  • Fig. 6 shows the basic system for which the equations concerning dielectric barrier discharge is derived.
  • E(x,t) is the electric field across the electrodes
  • Uext(t) is the applied voltage
  • iext(t) is the electrode current.
  • Fig. 7 shows that the density of species produced reaches a new maximum after about 5 stages.
  • the number of stages required to reach this maximum depends on the gas, the electrode material, the distance between stages and the flow rate.
  • Fig. 8 shows the logarithmic decay of active species with distance travelled from the plasma system exit. The exiting species are then available to provide stronger surface treatment. With a half bar of input pressure the resultant output reaches a velocity of over 100 metres per second and carries a high density of ions for several tens of centimetres. A species density of 10 15 per cm 3 may be achieved which is several orders of magnitude higher than with existing technology.
  • the electrodes By using an air pressure of 0.5 to 1 bar of air pressure from a compressor there is good air flow through the gap between the electrodes.
  • the electrodes have rounded edges of about 3mm radius and extend over an area of 30 x 100 to 9mm x 340mm. If the electrodes are driven by a high voltage sine wave a discharge will be created when the electric field exceed 27000 volts per cm. A range of frequencies from IkHz to 5OkHz is usable but it is more suitable to work in the region of 10kHz. It can also be helpful if the applied voltage is modulated to form bursts of active and quiet periods. This reduces the tendency to pitting in the electrodes. The forced flow of process gas, usually air, also has this effect.
  • the system uses a full bridge of IGBTs to drive a series resonant circuit to convert the square wave to a sine wave for the transformer primary.
  • the timing required is produced using programmable logic in which the 16 MHz clock signal was divided to produce a pair of 20 kHz square waves for a 10 kHz square wave.
  • the output level is detected by measuring the primary voltage of the high-tension transformer for safety reasons. This provides a good indication of the actual output voltage.
  • the high-tension output drives a parallel resonant circuit in which the capacitor impedance is close to the impedance of the DBD discharge. Frequency Resonance tuning is provided by the high-tension inductance.
  • the primary series and secondary parallel resonant circuits are a well known means of converting a square wave signal to sine wave for a resistive load. Some reactive load exists and the reactive current is returned to the reservoir capacitors through on-chip anti-parallel diodes in the IGBT full bridge.
  • the electrode arrangement is made so that electrodes are readily replaced and the electrode arrangement can be modified without affecting the rest of the system. Two sub-assemblies are bolted together using a spacer layer that determines the electrode gap. When these assemblies are separated it is possible to remove plates containing the electrodes.
  • the electrodes have a ceramic coating designed to withstand the discharge current and the temperature increase.
  • the system has 10 5 times the output species density of DBD systems and 10 3 times the density of plasma jets. It has a homogenous output that is suitable for even treatment over the electrode length.
  • Single stage DBD systems cannot be increased in size to compete with this performance due to physical limitations.
  • the capacitance of wide electrodes demands very high current levels in the primary circuit. Multiple jets do not give the uniform treatment available from this homogenous output.
  • the power electronics system is digital so the power is created by smaller devices than would be necessary for equivalent output from a linear system.
  • the reactive components do not need heat sinking while the semiconductors in the IGBT bridge are easily kept to a safe temperature.
  • the output voltage can be readily modified from 6 to 12kV using pulse width modulation of the bridge drive to allow for different gases and electrode gaps. This change is achieved in software and may be user defined.
  • the electrode configuration is designed for ease of service and design modification to suit a variety of uses.
  • the electrode gap may be varied from 1.5 to 4.0 mm but preferably below 2.5mm to minimise the voltage requirement.
  • the inter-electrode distance may be from 3mm upwards but should be as low as possible in order to minimise losses due to recombination while separating the discharges.
  • Scrubbing through a catalyst, makes the system safe for a factory or laboratory environment.
  • AIl cooling fans are monitored for reliable performance and the system is shut down when defective cooling is detected.
  • the temperature of the heat sink that cools the grounded electrode is monitored to prevent operation when the dielectric barrier deteriorates.
  • the cartridge 20 is a plug-in cartridge for insertion of the electrodes in a replaceable manner.
  • the cartridge 20 comprises a pair of identical opposed electrode blocks 21 and 22, each comprising a series of electrodes 23 in the form of ridges on one side (facing the ionisation path), and on the outside heat sink fins 24.
  • the path between the electrodes 23 outlets into a treatment conduit 26 having openings into catalytic converters 27 and 29 through which waste gas is driven to atmosphere by fans 28 and 30 respectively.
  • process gas in one embodiment air, is drawn in a flow A into the manifold 25, and passes in a flow B along the path where it is ionised. Ionised air outlets into the treatment conduit 26 in a flow C where it impinges against the sample S being treated. Waste air flows (D) through the catalytic converters 27 and 29 where ozone is converted to oxygen for safe discharge E to atmosphere. Flow into the converters is assisted by an inflow G from atmosphere, which inflow also helps to prevent direct discharge of ionized gas to atmosphere.
  • cooling air D pumped in a flow F along the heat sink fins 24 according to a temperature control scheme, hi one embodiment the temperature in the path is maintained above 80° in order to reduce the extent of ozone generated, hi another embodiment, the temperature is maintained below this level so that more ozone is generated, it that is desirable for the application.
  • single-phase mains electricity is fed to a switch mode power supply to create a 24 V DC supply. It also goes to a single phase rectifier and two series reservoir capacitors where it is doubled and powers a 650 volt DC bus. Provision is made to reduce noise emissions and noise susceptibility.
  • the 650 V bus supplies current to a full bridge comprised of Insulated Gate Bipolar Transistors (IGBTs). This are driven by four opto-coupler circuits that are powered by a flyback transformer for floating gate drive voltage creation and also the generation of a 5 volt DC supply for the logic circuitry.
  • the flyback transformer operates from the 24 volt bus.
  • the drive module also contains a transformer to convert the primary voltage of the HT transformer to a safe level for measurement.
  • the output voltage measured is the sine wave that appears across the input to a high-tension transformer after series resonance through an inductor and a capacitor.
  • the current that comes from the base of each IGBT bridge is measured by a Hall effect device. Both of these voltage and current measurements are fed to peak detect circuits. The peak detected current is also fed to a comparator for immediate switch off if a set limit is exceeded.
  • the power circuit is controlled by the logic circuit which has a user interface to an LCD display and some key-switches. It also applies power to cooling fans as appropriate and monitors the fan current to assure reliable operation.
  • a master/slave configuration is created using an RS485 bus that communicates with other plasma units to build a larger system capable of treating wide surfaces.
  • the electrodes are arranged in two vertical columns so that the ion flow produces a strong electric wind downwards from the electrodes.
  • This output is used to indirectly treat material.
  • the treatment area can be closed in so that the ions do not escape to the environment. They are sucked in to a pair of scrubbers either side of the output. Suction is achieved by fans that pull the process gas through appropriate catalysts that cause ozone to recombine as oxygen molecules.
  • the process gas can be normal air, dry air or any other gas mixture.
  • Using long electrodes we get a homogenous jet of high relative strength. This is more suitable for many purposes than a small round jet or a line of such jets.
  • the use can be for surface modification of plastic, metal, textile or other surfaces, destruction of bacteria or viri or prions, chemical vapour deposition, efficient ozone generation or any other application that may arise.
  • the invention finds many applications.
  • the applications call for different mechanical solutions and operating parameters.
  • To raise the surface energy of textiles a wide jet is required.
  • To sterilise Yoghurt containers a deep jet is required.
  • To achieve chemical vapour deposition we must have both so that we can ionize another gas and deposit parts of it on a surface.
  • Other possibilities such as purifying recycled air in an aeroplane require different electrode arrangements.
  • Tests on wetability and on bacteria destruction show major improvements over single stage treatment both direct and indirect.
  • the oxygen content of a polypropylene surface was doubled.
  • Bacteria destruction in 5 seconds using indirect treatment equalled that achieved in 30 seconds with direct treatment and in 5 minutes using single stage electrodes for indirect treatment.
  • n c n ⁇ ( ⁇ v) (collisions I s) (1)
  • v the flow velocity of the incoming gas
  • ⁇ the collisional cross-sectional area
  • n ⁇ the number of particles of type 1 per unit volume.
  • the discharge current is only limited by dielectric barriers; there is no external rreessiissttaannccee.
  • the values b e ,' T e and n i.on are assumed to be functions of the local electric field. They are determined by the electron distribution function, which is obtained from the Boltzmann kinetic equation.
  • the quantity n C* is the collisional frequency. Prior to the application of the first high voltage pulse to the system, this quantity is equal to zero given that ion flow will only commence after the initial stage.
  • Kinetic theory is incorporated into the model by means of atmospheric reactions numbered 1,2,... j.
  • the product of rate coefficient k. with the densities of respective species q and r gives the number of charged particles given by specific reactions in atmospheric air plasma.
  • Equation (16) - (21) describes the homogeneous barrier discharge completely as the profile of external voltage is given. This system is solved numerically. For the four electrode phases, the output of one stage is taken to be the input for the next stage and so on. Collisional frequencies are calculated and these are applied to equations (2) and (3) as shown above.
  • results of the application of multi-stage ion flow to the system are shown in figure 7. These take recycling into account, whereby a small percentage of the output species are fed back to the first electrode stage, essentially forming a feedback loop. Due to the fact that the species densities will continuously be increasing at the output due to feedback, it is conceivable that these values for electron and ion densities respectively will be even greater than those currently being predicted. A feedback efficiency of 1% was assumed for these calculations. The results show a gain of approximately 10 5 as opposed to a single electrode stage DBD reactor and also depict a gain of approximately double what would be expected for a four-stage electrode system without feedback. However, as already stated, it is conceivable that this gain could considerably increase due to varying the feedback portion.
  • the high output density makes the system suitable for applications where direct treatment may be damaging to the treated surface or where other indirect treatment methods are much weaker. This is best demonstrated in the use for treating the skin of living people or animals. It also applies to textile treatment where DBD filaments can damage fibres under direct treatment.
  • the drive circuit could drive the stages in sequence, an electrical phase being delivered to each stage.
  • the phases may be 45° apart.
  • the first four discharges may be of one orientation and the next four discharges of opposite orientation, thus swirling the ions from side to side as they travel from stages one to four.
  • the voltage phases result from pulse width modulated signals.
  • the peak of each phase is centred on the mid-point of each square wave and depends on the width.
  • the conversion is produced by series resonant circuits followed by parallel resonant circuits.
  • Puls5 creates the timeframe for each cycle at lOkHz.
  • PuIs 1 is co-incident with Puls5 but the duration of each high in PuIs 1 varies from 50 to 98% depending on the level of output voltage required.
  • Output 1 shows the square wave of voltage that appears on the IGBT full bridge. It is a pulse width modulated signal that is converted to sine wave by resonant circuits.
  • Pulsel and Outputl are delayed by 2 clock pulses from the start of Puls5. This delay is repeated at 100+2 for the second half of the cycle. For lOkHz this is a 2 microsecond delay to allow the IGBT bridge to settle and it could easily be changed to a value of 3 for slower transistors.
  • the rising edge of PuIs 1 clocks the status of Puls5 into a D flip-flop whose output determines the direction of Outputl. While this flip-flop is not necessary for PuIs 1 it is required for Puls2, 3 & 4. They are delayed by increments of 25 and a rising Puls3, for instance, clocks in the Puls5 status so that the Output3 (not shown) will have the necessary polarity.
  • Puls5 is a divide by 2 stage at the output of a counter that counts from 0 to 100. The count is compared to hardwired numbers 2, 27, 52 & 77 that initiate PuIs 1, 2, 3 & 4. The count is compared to four registers containing the endpoints 2-0, 77-25, 2-50 & 25-75 representing 52-100, 77-125, 102-150 & 125-175 on the timing diagram. Puls2 starts at 27 and ends between 77 and 99 or between 0 and 25 for a width of 50 to 98. Timing for the second and successive phases may be obtained by using the start of both halves of phase 1 to save the status, so as to know whether the first or second half of the waveform should be generated. This status is loaded by the arrival of a later phase and the correct alignment is maintained. This minimises the number of signal wires needed for a multiphase system.

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  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Plasma & Fusion (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Electromagnetism (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Plasma Technology (AREA)

Abstract

Le système à plasma selon l'invention comprend une cartouche enfichable (20) ayant une paire de blocs d'électrodes opposées identiques (21, 22) comprenant chacun une série d'électrodes (23) se présentant sous forme de crêtes sur un côté (en face du chemin d'ionisation) et sous forme d'ailettes de dissipation de chaleur (24) sur l'extérieur. Le système comprend également un collecteur d'admission de gaz de procédé (25). Le chemin entre les électrodes (23) aboutit à un conduit de traitement (26) ayant des ouvertures donnant dans des convertisseurs catalytiques (27, 29) à travers lesquels du gaz résiduaire est évacué dans l'atmosphère par des ventilateurs (28, 30) respectivement. Le gaz de procédé, tel de l'air, est aspiré dans un écoulement A jusque dans le collecteur (25), puis passe dans un écoulement B le long du chemin suivant lequel il est ionisé. L'air ionisé sort dans le conduit de traitement (26) dans un écoulement C, dans lequel il entre en collision avec l'échantillon S en cours de traitement. L'air résiduaire s'écoule (D) à travers les convertisseurs catalytiques (27, 29) dans lesquels l'ozone est converti en oxygène pour être évacué E sans risque dans l'atmosphère. Chaque paire d'électrodes opposées (23) constitue un étage d'ionisation auquel une onde sinusoïdale à tension élevée provoque la dégradation du gaz dans les interstices entre les électrodes. La sortie du premier étage contient certains ions et un grand nombre d'espèces excitées, notamment des métastables. Une recombinaison se produit pour certaines des espèces en cours de transit au second étage. Les espèces arrivant au second étage provoquent l'ensemencement de la décharge suivante à cet étage et il se crée une quantité d'espèces supérieure à celle produite par le premier étage. Cela est dû au fait que la fréquence de collision s'accroît avec l'augmentation du nombre d'ions, ce qui accélère la production d'ions supplémentaires sous un champ électrique. Le processus se poursuit à chaque étage successif, ce qui produit une densité d'espèces actives nettement supérieure à celle qui serait produite par une seule paire d'électrodes ayant une surface équivalente.
EP08738134A 2007-04-11 2008-04-10 Systeme a plasma Withdrawn EP2135493A1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
IE20070259 2007-04-11
IE20070897 2007-12-12
PCT/IE2008/000043 WO2008126068A1 (fr) 2007-04-11 2008-04-10 Système à plasma

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EP2135493A1 true EP2135493A1 (fr) 2009-12-23

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IE (1) IE20080271A1 (fr)
WO (1) WO2008126068A1 (fr)

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