Patent Application
20240216887
The present disclosure relates to a plasma reactor for plasma-based gas conversion comprising a plasma chamber wherein, when in operation, a plasma is formed. The plasma chamber comprises one or more gas inlets for introducing a feed gas into the plasma chamber and at least one gas outlet opening for evacuating converted and unconverted feed gas from the plasma chamber.
Plasma reactors for plasma-based gas conversion are gaining an increased interest for a variety of chemical reaction applications.
A first example of the potential benefit of using plasma reactors is for the conversion of carbon dioxide and methane into value added chemicals or renewable fuels.
A second example of growing interest in using plasma reactors is for the conversion of N2 and O2 from air into reactive NO and NO2, generally named NOx.
A plasma reactor for NOx production is for example disclosed by Jardali et al. in Green Chem, 2021, 23, 1748-1757. Jardali et al. proposes to use the NOx molecules for the production of high yield nitrogen content organic fertilizers. Indeed, by mixing NO2 with livestock manure, a nitrate is formed that stabilizes the ammonium and hence minimizes or eliminates NH3 losses. On the other hand, present fertilizers are mainly produced from non-sustainable fossil fuels via the Haber-Bosch process which leads to serious environmental problems, involving for example, large carbon dioxide production. Hence, production of fertilizers based on the plasma technology can be an environmentally friendly alternative or a complementary solution to the present fertilizers production methods.
Different types of plasma reactors exist for the purpose of plasma-assisted gas conversion. Plasma reactors can differ in design, geometry, and/or mode of operation, depending on the particular application for which the plasma reactor is used.
An example of a plasma reactor for NOx production is a rotating gliding arc (RGA) reactor, as discussed by Jardali et al. The RGA reactor comprises a plasma chamber wherein a plasma is to be formed and one or more gas inlets for supplying the feed gas into the plasma chamber. In this example the feed gas is N2 and O2. The feed gas is introduced in the plasma chamber of the RGA reactor as a swirling flow about a central axis of the reactor. The RGA reactor further has a cathode in the form of a spark plug (with ground electrode removed), an anode having a conical portion, and a cylindrical outlet portion for evacuating the converted gases (NOx) and non-converted gases (N2 and O2). By applying a high-voltage between the first and second electrode, a gliding arc discharge is generated in the plasma chamber.
Although the results of Jardali et al. show to be promising for NOx production, in order for the plasma reactor technology to become commercially attractive for large scale applications, further improvements are still desirable. What is important is to obtain a high production yield of NOx with a low energy consumption. The energy consumption is also named energy cost and is generally expressed in Joules per mol of feed gas.
Similarly, if plasma reactor technology is to be commercially deployed for other plasma-based gas conversion applications, such as CO2 or CH4 conversion, increasing production yield and minimizing the energy cost is vital.
Hence there is room for improving plasma reactors for gas conversion.
It is an object of the present disclosure to provide a plasma reactor for plasma-based gas conversion wherein the production yield is increased and/or energy cost is reduced when compared to prior art arc plasma reactors.
The present invention is defined in the appended independent claims. The dependent claims define advantageous embodiments.
According to a first aspect of the present disclosure, a plasma reactor for plasma-based gas conversion is provided. The plasma reactor comprises a plasma chamber having one or more gas inlets configured for introducing a feed gas into the plasma chamber, a first electrode (31) and a second electrode (32) for generating a gas discharge in the plasma chamber, and at least one gas outlet opening for evacuating converted and unconverted feed gas from the plasma chamber. A central axis of the plasma reactor is passing through the at least one gas outlet opening of the plasma chamber.
The plasma reactor according to the present disclosure is characterized in that it comprises an effusion nozzle coupled to the plasma chamber and wherein the effusion nozzle is made of or at least partly is made of an electrically conducting material.
The effusion nozzle comprises a radial circumferential wall radially delimiting a gas-receiving cavity elongating along the central axis from a first end to a second end, an axial entrance opening at the first end of the gas-receiving cavity for receiving converted and unconverted feed gas exiting the at least one gas outlet opening of the plasma chamber, and an axial wall at the second end of the gas-receiving cavity axially delimiting the gas receiving cavity at the second end of the gas receiving cavity.
The effusion nozzle further comprises one or more effusion openings configured for evacuating converted and unconverted feed gas from the gas-receiving cavity.
The plasma reactor is further characterized in that the effusion nozzle is forming an extension of the second electrode or alternatively, the effusion nozzle or part of the effusion nozzle is forming the second electrode.
Hence, in embodiments wherein the effusion nozzle is an electrode extension, the second electrode comprises the effusion nozzle, i.e., the effusion nozzle is part of the second electrode. In other embodiments wherein the effusion nozzle is forming the second electrode, the effusion nozzle corresponds to or is the second electrode.
Advantageously, by providing an effusion nozzle comprising an axial wall, the axial wall will block the axial flow of converted and unconverted gas flowing out of the reactor chamber and thereby force the gas to recirculate within the gas-receiving cavity. In this way, the overall residence time of the gas in the plasma reactor is increased. An increased residence time is positively influencing gas conversion production yields.
Advantageously, by providing an effusion nozzle comprising an axial wall forcing the gas to recirculate, heat is trapped inside the nozzle which increases temperature of the walls of the effusion nozzle and/or plasma chamber. As a consequence, conversion by thermal chemical reactions is enhanced, which positively influences gas conversion production yields.
In embodiments, the axial wall can be construed as an axial blind flange.
In embodiments, the axial wall can have different shapes, for instance the shape is not limited to a flat-shaped wall or a wall with uniform thickness. In embodiments, the axial wall can have a non-uniform thickness.
In embodiments, the axial wall comprises a protruding element protruding inside the gas-receiving cavity. This protruding element can take a number of different shapes such as any of the following non-limiting list of shapes: a cone, a cylinder, a hemisphere, a cuboid, a frustum, a pyramid, a prism, a cross, a helix shape, or any combination thereof.
In some embodiments, the protruding element is protruding inside the gas-receiving cavity in a direction parallel with the central axis.
In embodiments, the effusion openings are, for example, effusion holes or effusion slits.
In embodiments, the effusion nozzle is removably coupled to the plasma reactor. Indeed, with the plasma reactor according to the present disclosure, a centralized plasma discharge is formed between the first electrode and the blocking wall of the effusion nozzle, acting as the second electrode, hence, any corrosion and/or hot spot in the contact point of the plasma and the surface will occur in the body of the effusion nozzle. By having a removeable effusion nozzle, the effusion nozzle can be replaced, which is a simpler and cheaper device to be manufactured. In this way, the service time of the reactor body is maximized.
In embodiments, the plasma reactor according to the present disclosure is of a type of any of the following plasma reactor types a rotating gliding arc plasma reactor, a dual vortex plasmatron, a gliding arc plasmatron, or an atmospheric pressure glow discharge plasma reactor.
In embodiments, the plasma reactor is a rotating gliding arc plasma reactor operable in a rotating arc mode and operable in a steady arc mode.
In embodiments, the plasma reactor according to the present disclosure is a plasma reactor operable in a pressure range in the plasma chamber between 1 mbar and 5 bar, preferably between 100 mbar and 5 bar, more preferably between 500 mbar and 2 bar.
In embodiments, the effusion nozzle is made of an electrically conducting material and the effusion nozzle is electrically coupled to an electrode of the plasma reactor.
In embodiments, the effusion nozzle is electrically coupled to the second electrode so as to form an extension of the second electrode, preferably, the first electrode is high-voltage cathode electrode and the second electrode is a grounded anode electrode.
According to a second aspect of the present disclosure, the plasma reactor of the present disclosure is used for conversion of N2 and O2 molecules into NO and NO2 molecules, or for conversion of CO2 molecules into value added chemicals or renewable fuels.
These and further aspects of the present disclosure will be explained in greater detail by way of example and with reference to the accompanying drawings in which:
The drawings of the figures are neither drawn to scale nor proportioned. Generally, identical components are denoted by the same reference numerals in the figures.
The present disclosure will be described in terms of specific embodiments, which are illustrative of the disclosure and not to be construed as limiting. It will be appreciated by persons skilled in the art that the present disclosure is not limited by what has been particularly shown and/or described and that alternatives or modified embodiments could be developed in the light of the overall teaching of this disclosure. The drawings described are only schematic and are non-limiting.
Use of the verb “to comprise”, as well as the respective conjugations, does not exclude the presence of elements other than those stated. Use of the article “a”, “an” or “the” preceding an element does not exclude the presence of a plurality of such elements.
Furthermore, the terms first, second and the like in the description and in the claims, are used for distinguishing between similar elements and not necessarily for describing a sequence, either temporally, spatially, in ranking or in any other manner. It is to be understood that the terms so used are interchangeable under appropriate circumstances and that the embodiments of the disclosure described herein are capable of operation in other sequences than described or illustrated herein.
Reference throughout this specification to “one embodiment” or “an embodiment” means that a particular feature, structure or characteristic described in connection with the embodiments is included in one or more embodiment of the present disclosure. Thus, appearances of the phrases “in one embodiment” or “in an embodiment” in various places throughout this specification are not necessarily all referring to the same embodiment, but may. Furthermore, the particular features, structures or characteristics may be combined in any suitable manner, as would be apparent to one ordinary skill in the art from this disclosure, in one or more embodiments.
Plasma Reactor with Effusion Nozzle, General
Various types of plasma reactors for performing plasma-based gas conversion exist in the art and the present disclosure is for instance related to plasma reactors wherein an arc discharge is generated between two electrodes in order to create a gas discharge plasma. Examples of different types of prior art plasma reactors for gas conversion are for example disclosed by Bogaerts and Centi in “Plasma technology for CO2 conversion: A personal perspective on prospects and gaps.” Front. Energy Res., 8, 111 (2020).
The plasma reactors according to the present disclosure are also named atmospheric pressure plasma reactors as they typically operate in a pressure range between a few mbar to one bar and above. In its simplest form, a gas discharge plasma is created by applying an electric potential difference between two electrodes, positioned in a gas, further named feed gas. The potential difference can in principle be direct current (DC), alternating current (AC), ranging from 50 Hz to MHz (radio-frequency; RF), or pulsed. Embodiments of different types of plasma reactors according to the present disclosure are further discussed below in more detail.
What the various types of plasma reactors 1 for gas conversion have in common is that they comprise a plasma chamber 10 wherein, when the plasma reactor 1 is in operation, a plasma 50 is formed, as schematically illustrated on
Typically, the plasma chamber 10 of the plasma reactor 1 comprises one or more gas inlets 11 configured for introducing a feed gas into the plasma chamber 10, and at least one gas outlet opening 12 for evacuating converted and unconverted feed gas from the plasma chamber 10. On
The plasma reactor 1 comprises a central axis Z passing through the gas outlet opening 12 of plasma chamber 10, as illustrated on
In embodiments, the gas outlet opening 12 of the plasma chamber, comprises an outlet surface that is transverse or orthogonal with respect to the central axis Z.
The plasma reactor according to the present disclosure is characterized in that it comprises an effusion nozzle 20 that is coupled to the plasma chamber 10, as schematically illustrated on
The gas-receiving cavity is configured for receiving a gas flow of converted and unconverted feed gas exiting through the at least one gas outlet opening 12 of the plasma chamber. For instance, the gas-receiving cavity 21 comprises an axial entrance opening 26 at the first end that is configured for receiving this gas flow of converted and unconverted feed gas exiting the plasma chamber. An axial entrance opening 26 has to be construed as an opening that is transverse with respect to the central axis Z.
As illustrated for example on
In embodiments, the axial entrance opening of the effusion nozzle comprises an entrance surface that is transverse or orthogonal with respect to the central axis Z.
The gas-receiving cavity 21 further comprises an axial wall 22 at the second end of the gas-receiving cavity. The axial wall 22 will block the gas flow, in a direction essentially parallel with the central axis Z, of converted and unconverted feed gas exiting the plasma chamber 10 as the gas will hit the axial wall and be forced to change direction, and hence recirculate within the gas-receiving cavity 21.
In other words, the axial wall 22 prohibits the gas flow to proceed flowing in its forward direction along the central axis Z and hence the axial wall 22 forces the gas flow to change its flow direction, i.e. rerouting the gas flow.
In embodiments, the axial wall is an axial blind flange that is transverse with respect to the central axis Z.
In embodiments, as schematically illustrated on
Typically, the overall direction of the gas flow exiting the plasma chamber and entering the gas-receiving cavity of the effusion nozzle is in a direction parallel with central axis Z.
In other words, the effusion nozzle assures that the gas flow out of the plasma chamber is blocked in its forward direction as gas molecules bounce against the axial wall 22. In this way, the gas molecules start to recirculate within the gas-receiving cavity 21.
When using the effusion nozzle, for a same gas flow rate of feed gas, the pressure inside the plasma chamber will generally increase and the time the feed gas stays in the reactor before being evacuated is increased, thereby increasing the production yield.
Further, the recirculation of the gas in the receiving-cavity contributes to improve the heat transfer to the walls of the effusion nozzle and an increased temperature can positively influence the production yield as further outlined below.
Indeed, with the effusion nozzle according to the present disclosure, heat escaping from the reactor is reduced and the effusion nozzle retains some of the heat from the plasma. The turbulent mixing allows for a better heat transfer to the walls compared to for example a laminar flow because with turbulent flow a better mixing is obtained. A laminar flow tends to shield the heat more.
The production yield can be further increased due to an effect known as “wall-stabilization” of the plasma, where the temperature gradient of the plasma column becomes less steep as the heat transfer towards the walls increases. This leads to a more stable, less contracted plasma column (or arc), which improves the conversion.
The axial wall 22 can have various shapes and hence the axial wall is not necessarily a flat wall or a wall having a homogenous thickness. Hence, the axial wall has to be construed as any wall that is suitable to prohibit the gas flow to proceed flowing in its forward direction along the central axis Z and hence forcing the gas flow to change its flow direction, i.e., rerouting the gas flow.
In embodiments, the axial wall 22 comprises a protruding element 24 protruding inside the gas-receiving cavity 21 in a direction parallel with the central axis Z. The axially protruding element 24 separates the gas flow, i.e., the gas flow is forced to flow around the protruding element 24 and hence the protruding element could further contribute to forcing the recirculation of the gas inside the gas-receiving cavity. In other words, the axially protruding element 24 disperses the gas inside the gas-receiving cavity.
In embodiments, the central axis Z of the plasma reactor 1 is crossing the protruding element 24. Detailed embodiments of the protruding element will be discussed in the section below where specific examples of effusion nozzles are given.
With reference to
In embodiments, the first electrode is a high-voltage electrode and the second electrode is a grounded electrode, preferably the first electrode is a cathode and the second electrode is an anode.
In other embodiments, the second electrode is a high-voltage electrode, e.g., a cathode, and the first electrode is grounded electrode, e.g., an anode.
In embodiments, as for example illustrated on
Hence, for embodiments wherein the effusion nozzle is forming an electrode extension, as illustrated on
In embodiments, as illustrated on
In other embodiments, wherein the second electrode comprises a first part and a second part, the entire plasma chamber, i.e., the walls delimiting the plasma chamber, forms the first part of the second electrode and the effusion nozzle forms the second part of the second electrode. An example of such an embodiment is for example shown on
In other embodiments, as illustrated for example on
In embodiments, at least the radial circumferential wall 25 and the axial wall 22 of the effusion nozzle are forming part of the second electrode 32.
Hence, as the effusion nozzle is part of the electrode, the effusion nozzle is made of or at least partly made of an electrically conducting material, e.g., stainless steel.
In embodiments, at least the radial circumferential wall 25 and the axial wall 22 are made of an electrically conducting material. In other embodiments, at least the axial wall, or at least the protruding element of the axial wall are made of an electrically conducting material.
With reference to
In embodiments, as shown on
In embodiments, as shown on
Plasma reactors according to the present disclosure comprising an effusion nozzle and wherein the effusion nozzle 20 is forming part of the second electrode 32 or wherein the effusion nozzle is the second electrode, have a major effect on the operation and performances of the plasma reactor. Indeed, when the plasma reactor 1 according to the present disclosure is in operation, the arc discharge is elongated and due to the axial wall 22 of the effusion nozzle, a central steady arc discharge can be created through the gas-receiving cavity of the effusion nozzle.
Indeed, the axial wall or at least a central portion of the axial wall forms an electrode tip for the second electrode, allowing to create a central arc discharge through the gas-receiving cavity of the effusion nozzle. The arc can hereby be sustained at a lower power and gas production yield can be increased at a lower cost.
The effusion nozzle 20 further comprises one or more effusion openings 23, such as for example effusion holes or effusion slits, for evacuating converted and unconverted feed gas from the gas-receiving cavity 21.
The coupling of the effusion nozzle to the plasma chamber can be performed by various coupling means, known to the skilled person, such as but not limited to welding, soldering or screwing. The coupling is made in such a way that no gas or only an insignificant amount of gas could escape through the coupling interface.
In
In embodiments, the effusion nozzle can be manufactured as a single piece, e.g., mechanically manufactured as a single metal piece that is attachable to the plasma chamber.
In other embodiments the effusion nozzle can be composed of multiple pieces or sections that are attached to each other. In embodiments, the effusion nozzle is for example composed of two pieces that are attached to each other. For example, a first separate section of the effusion nozzle can be formed by a circumferential wall 25 radially delimiting the gas-receiving cavity 21 and a second separate section can be formed by an axial flange forming the axial wall 22. The second section can then be attached to the first section by welding, screwing or any other suitable coupling means such that no or only an insignificant amount of gas could escape through the coupling interface.
In embodiments as illustrated on
In embodiments, the gas outlet opening 12 of the plasma chamber is circular and at least a portion of the gas-receiving cavity 21 of the effusion nozzle has a tubular shape having an inner diameter matching with a diameter of the circular gas outlet opening of the plasma chamber.
For example, in embodiments, an inner tubular portion of the gas-receiving cavity 21 can have a length along the central axis in a range between to 40 mm and have an inner diameter in a range between 10 to 20 mm and wherein this inner diameter is matching with a diameter of the gas outlet opening of the plasma chamber. In other embodiments, depending on the dimensions and type of plasma reactor, the dimensions of the gas-receiving cavity can vary and be scaled up or down.
In further embodiments wherein the gas outlet opening 12 of the plasma chamber is circular, at least a portion of the gas-receiving cavity 21 of the effusion nozzle has a shape of a truncated cone wherein a diameter of a side, e.g. a top side, of the truncated cone is matching with a diameter of the gas outlet opening of the plasma chamber.
The shape of the gas-receiving cavity is however not limited to a cylindrical or conical shape. In other embodiments the gas-receiving cavity is radially delimited by a circumferential wall having any compatible shape. For example, the inner shape of the gas-receiving cavity can also have the shape of a cuboid or at least a portion of the gas-receiving cavity can have the shape of a cuboid.
In the embodiments shown on
In embodiments, the protruding element is rotationally symmetric with respect to the central axis Z.
This protruding element can have the shape of any of: a cone, a cylinder, a hemisphere, a cuboid, a frustum, a pyramid, a prism, a cross, a helix shape, or any combination thereof. A protruding element having a shape of a cuboid, a pyramid, a hemisphere and a frustum is respectively illustrated on
The protruding element of the embodiment shown on
In embodiments wherein, the axial wall 22 comprises a protruding element 24, the axial wall 22 is manufactured out of single piece. In other embodiments, the axial wall is made out of two parts: an axial blind flange and the protruding element. The protruding element can be mechanically attached to the axial blind flange by welding, soldering or any suitable attachment means.
As discussed above, the axial wall 22 also plays the role of electrode tip for the second electrode. In embodiments, wherein the axial wall 22 comprises a protruding element 24, the protruding element 24 is forming an electrode tip 32a for the second electrode 32.
The number of effusion openings 23 in the effusion nozzle can vary from embodiment to embodiment. Typically, the effusion nozzle 20 comprises between 1 and 100 effusion openings, but the number of effusion openings can also be larger.
In embodiments wherein the effusion nozzle comprises a plurality of effusion openings, the effusion nozzle comprises 2 or more effusion openings, preferably 4 or more effusion openings or more preferably 6 or more effusion openings. Advantageously by providing multiple effusion openings, the temperature of the walls of the effusion nozzle resulting from the heat transfer of the recirculating gas, as discussed above, is more evenly distributed and hot temperature spots on for example one side or one particular area of the effusion nozzle can be avoided.
In embodiments comprising a plurality of effusion openings, the effusion openings are radially distributed. The cross-sectional view shown on
In further embodiments, the effusion openings of the effusion nozzle are randomly distributed. In other embodiments, the effusion openings are distributed within a band of a radial circumferential wall of the effusion nozzle.
In embodiments, as shown on
However, in other embodiments the angle between the central hole axis of the effusion hole and the central axis Z can be different from 90° and this angle can have a value in a range between 0° and 90°. For example, an effusion hole having a central hole axis at 45° with respect to the central axis Z is shown in
In other embodiments, the effusion holes may be oriented tangentially with respect to the nozzle boundary.
In other embodiments as illustrated in
The number and dimensions of the effusion openings 23 are generally defined in relation to the overall dimensions and parameters of the plasma reactor. Effusion openings can for example have a diameter between 0.1 and 10 mm. The number of openings 23 and their specific dimensions depend on the reactor dimensions, flow rate, power and type of gas used.
The effusion openings are not necessarily holes, and the holes do not necessarily have a circular opening. The opening of the hole can have any suitable shape.
In embodiments, the effusion opening is a slit, i.e., having the shape of a rectangle.
In embodiments, the effusion openings 23 are configured such that when the plasma reactor 1 is in operation an overpressure is generated inside the nozzle.
In embodiments, the effusion openings 23 are configured such that when the plasma reactor 1 is in operation, for a given constant supply rate of the feed gas: 1≤P1/Pref≤5, wherein P1 is the pressure measured inside the plasma chamber and Pref is a reference pressure corresponding to a pressure obtained in the plasma chamber for the same constant supply rate of feed gas but with the effusion nozzle removed from the plasma chamber. In other words, the pressure effect of using an effusion nozzle is either no effect, i.e., the same pressure is maintained or there is an overpressure created in the plasma chamber. Preferably, the pressure ratio is in the range: 1≤P1/Pref≤3. More preferably, 1<P1/Pref≤3. In other words, in the latter case when P1/Pref>1, an overpressure is generated in the plasma chamber.
In embodiments, the effusion openings 23 are configured such that when the plasma reactor is in operation, the pressure inside the plasma chamber is between 1 mbar and 5 bar, preferably between 100 mbar and 5 bar, more preferably between 500 mbar and 2 bar.
In embodiments, the plasma chamber comprises a tubular outlet extension extending the gas outlet opening 12 of the plasma chamber along the central axis Z, and wherein the tubular outlet extension has an outer thread. In these embodiments, a circumferential inner wall portion of the gas-receiving cavity 21 of the effusion nozzle 20 comprises an inner thread 27 matching with the outer thread of the tubular outlet extension of the plasma chamber so as to form a screwed coupling between the effusion nozzle 20 and the plasma chamber 10. This allows to easily remove the effusion nozzle from the plasma chamber and to replace the effusion nozzle with another effusion nozzle.
Embodiments wherein the effusion nozzle is removeable from the plasma reactor, and hence can be replaced, has a major advantage. Indeed, with the effusion nozzle according to the present disclosure, the generated centralized plasma discharge is formed between the cathode knob and the blocking section of the effusion nozzle, hence, any corrosion and/or hot spot in the contact point of the plasma and the surface will occur in the body of the effusion nozzle, which is a simpler and cheaper device to be manufactured, and therefore, maximizes the service time of the reactor body.
Example of embodiments of effusion nozzles wherein a circumferential inner wall portion of the gas-receiving cavity comprises a thread 27 are shown in
In other embodiments, the effusion nozzle is welded to the plasma chamber.
The effusion nozzles are preferably made of a metal, e.g., stainless steel.
In embodiments, the effusion nozzle is made of an electrically conducting material and the effusion nozzle is forming part of an electrode of the plasma reactor. In other embodiments, the effusion nozzle is forming an electrode of the plasma reactor.
In other embodiments, depending on the type of plasma reactor used, the effusion nozzle is electrically insulated from the plasma chamber by an insulator, e.g., a ceramic or otherwise non-conductive insulator.
In embodiments, the effusion nozzle is partly made of an electrically conductive material and partly made of an electrically non-conductive material, i.e., an insulator. For example, in embodiments, the protruding element can be made of an electrically conductive material and the other parts of the effusion nozzle can be made of an electrically non-conductive material such as for example a ceramic. In these embodiments wherein the protruding element is made of an electrically conductive material, the protruding element is electrically connected with the anode.
A number of different types of plasma reactors for gas-conversion that are operable with an effusion nozzle according to the present disclosure will be discussed in more detail.
A first type of plasma reactor comprising an effusion nozzle is a gliding arc, GA, plasma reactor. The GA discharge is a transient type of arc discharge.
What these GA plasma reactors have in common is that they comprise a first electrode, a second electrode electrically insulated of the first electrode, and a power supply configured for maintaining a high-voltage between the first and second electrode. The high-voltage is typically in the kV range.
Examples of a 3D GA discharge plasma reactor are a 3D gliding arc plasmatron, GAP, and a rotating gliding arc, RGA, reactor. Both types of reactors operate between cylindrical electrodes.
With reference to
In embodiments, the second electrode (or anode) of a 3D RGA is at least partly formed by a first wall portion of the plasma chamber. Through this first wall portion, a wall opening is made forming the gas outlet opening 12 of the plasma chamber 10.
In embodiments, the first wall portion of the plasma chamber that at least partly is forming the second electrode is a conical portion having a shape of a truncated hollow cone elongating along the central axis Z.
Generally, the effusion nozzle 20 is made of an electrically conducting material and the effusion nozzle is electrically coupled to the second electrode so as to form an extension of the second electrode 32.
For example, in the embodiments shown on
In the embodiment shown on
As with the 2D GA reactor, also with the 3D GA reactor, by applying a high-voltage between the first 31 and second electrode 32, a gliding arc discharge is generated in the plasma chamber. Typically, when applying a voltage of about 3 kV between the first and second electrode, an arc is created in the shortest gap between cathode and anode. In an RGA plasma reactor, the arc immediately starts gliding along the reactor body due to the swirling gas flow inside the plasma chamber. During gliding, one side of the arc remains attached to the top face of the cathode, while the other side glides around the surface of the reactor body, which results in an arc elongation. While the arc is gliding, it also rotates around the internal surface of the anode. When powered by a current source, the elongation of the arc is represented by a nearly linear increase in the discharge voltage. The discharge current decreases due to the rising arc length, and thus rising arc resistance. During arc elongation, energy is dissipated into heat and radiation. Therefore, if the supplied power is not sufficient to sustain further arc extension, the arc will extinguish, which is presented by a sudden drop of the discharge current, and a reciprocal jump in the electrode voltage. As a result, re-ignition will take place in the shortest gap between both electrodes. This is the common iterative operating mode of the reactor.
In embodiments, the plasma reactor is a rotating gliding arc plasma reactor operable both in a rotating arc mode, as discussed above, and operable in a steady arc mode. A rotating arc mode is a mode wherein the arc rotates along the anode, while in the steady arc mode, the arc is more fixed and has a constant length. These two modes of operation are for example discussed by Jardali et al.
Indeed, with an RGA reactor, if certain conditions are met, the arc can stabilize due to the intense heat transfer to the walls of the plasma chamber. In this so-called steady arc regime, the supplied power is high enough for the arc to elongate through the third section 10c of the plasma chamber and reach the entrance opening of the effusion nozzle 20. At this high power level, the arc does not extinguish, and remains relatively stable in the centre of the plasma chamber with a constant arc length. This steady state arc regime is reflected by the relatively constant values for discharge voltage and current. When in the steady arc regime, the effusion nozzle further allows the plasma to elongate until it reaches the axial wall 22 or more precisely the protruding element 24 of the wall 22.
For an RGA reactor operating in the steady arc regime, for a given gas flow rate of introducing the feed gas into the plasma chamber and for a given power supplied by the power supply, the electrode separation distance SElec measured along the central axis Z between a tip of the first electrode 31 and the axial wall or a central portion of the axial wall that is forming an electrode tip for the second electrode is defined such that, when in operation, the steady arc discharge is anchored between the tip of the first electrode 31 and the tip of the second electrode 32. In this way, the plasma is extending through the effusion nozzle up to the axial wall. Such a plasma extension increases the production yield of the gas conversion.
With reference to
Another example of a 3D gliding arc reactor is a gliding arc plasmatron. An example of an embodiment of a GAP reactor is schematically illustrated in
As is the case with the RGA, also with the GAP reactor, following extinction of the arc, the arc is again initiated at the shortest interelectrode distance, and expands till the upper part of the plasma chamber, rotating around the central axis Z of the reactor until it more or less stabilizes in the center after about 1 ms. In the ideal scenario, the inner gas vortex passes through this stabilized arc, allowing a larger fraction of the gas being converted than in a classical two-dimensional GA discharge.
A further example of a 3D GA plasma reactor is a so-called dual vortex plasmatron, DVP, as schematically illustrated on
Another type of plasma reactors that comprise an effusion nozzle according to the present disclosure are so-called atmospheric pressure glow discharges, APGD, reactors. A basic APGD reactor is schematically illustrated in
In embodiments, the APGD reactor additionally uses a vortex flow generator. Such a vortex flow effectively lowers the cathode temperature due to turbulence, and thus enables operation at higher power with longer interelectrode distance. In addition, the turbulence allows somewhat more gas to pass through the plasma.
In embodiments, to further enhance the gas fraction passing through the plasma, APGD reactors make use of a ceramic tube with a smaller inner radius of 2.5 mm that fits within a few mm around the cathode pin. In these embodiments, a spiral groove is carved on the pin, guiding the gas into the tube, and acting as effective cooling for the cathode pin, preventing it from melting, and thus also enabling the use of higher power. The plasma region is indeed limited to a radius of 2.5 mm or less, as predicted by modelling, so this ceramic tube with small inner radius makes sure that the plasma fills the entire reactor, and all the gas passes through the active plasma, yielding improved gas conversion.
Method for Operating the Plasma Reactor with Effusion Nozzle
According to a further aspect of the present disclosure, a method for operating a plasma reactor that comprises an effusion nozzle as discussed above is provided. The method comprises steps of: supplying a feed gas into the plasma chamber, using a power supply for generating a high-voltage between the first and the second electrode, supplying power with the power supply so as to generate an arc discharge between the first electrode and the second electrode and thereby initiate a gas discharge plasma in the plasma chamber, increasing the supplied power so as to extend the arc discharge through the effusion nozzle until a central steady arc discharge is anchored between the first electrode and the axial wall of the effusion nozzle, extracting converted and unconverted feed gas through the effusion openings.
For embodiments wherein the axial wall 22 of the effusion nozzle comprises a protruding element 24 protruding inside the gas-receiving cavity 21 in a direction parallel with the central axis Z, the central steady arc discharge is preferably anchored between the first electrode and the protruding element.
With the present method of operating the plasma reactor having an effusion nozzle, the performances of plasma-based gas conversion are increased, as will be further outlined below.
Performance of Plasma Reactor with Effusion Nozzle
The present invention is, at least in part, based on the inventor's observation and insight that an effusion nozzle as specified above, can improve the performances of a plasma reactor for plasma-based gas conversion. More precisely, that the effusion nozzle can increase the production yield of gas conversion and/or reduce the energy cost when compared to prior art plasma reactors not comprising an effusion nozzle.
Tests have been performed to demonstrate improved performances of conversion of N2 and O2 molecules into NO and NO2 molecules. The tests were performed with the rotating gliding arc plasma reactor illustrated on
The tests were performed in a wide range of N2/O2 gas feed ratios supplied to the RGA plasma reactor, with and without the effusion nozzle. FIG. shows the measured NOx concentrations expressed as volume percent, as function of the N2 fraction. Curve “a” is for a measurement without effusion nozzle and curve “b” is for a measurement with effusion nozzle. In
According to the results, improved NOx concentrations are obtained, as shown on
Further tests have been performed to measure the temperature of the effusion nozzle during operation of the RGA plasma reactor. Results show that the end portion of the effusion nozzle, i.e., the axial wall, heats up to temperatures of 500° C. and above. These high temperatures improve the thermal conversion and therefore higher production yields can be obtained at lower input power.
The improved results obtained with a plasma reactor comprising an effusion nozzle according to the present disclosure can be explained by what is generally named “fast cooling”. This fast cooling is achieved as follows. Firstly, the plasma reactor generates a stable/steady plasma discharge and the effusion nozzle elongates the formed plasma discharge which further increases the plasma volume and maximizes the thermal effect. Secondly, in addition to forcing the flow to circulate in the gas receiving cavity of the nozzle by using an axial end wall, the axial wall of the effusion nozzle also acts as an efficient heat sink to cool down the gas from high temperatures of ˜4000 K within the bulk plasma to ˜1000 K at the outlet of the nozzle. This results in taking advantage of thermal effects, and simultaneously, benefiting from efficient cooling immediately outside the nozzle, which limits the occurrence of the recombination reactions, and thus increases the overall performance.
In embodiments wherein small effusion openings in the effusion nozzle are used, some overpressure inside the nozzle can be caused, which additionally improves performance.
Hence, a further aspect of the present disclosure provides for using a plasma reactor as described above that comprises an effusion nozzle for conversion of N2 and O2 molecules into NO and NO2 molecules. In embodiments, an RGA plasma reactor is used for this conversion of N2 and O2 molecules.
Further embodiments, provide for using a plasma reactor as described above that comprises an effusion nozzle for conversion of CO2 molecules into value added chemicals, or renewable fuels. In embodiments, an RGA plasma reactor is used for this conversion of CO2 molecules.
| Number | Date | Country | Kind |
|---|---|---|---|
| 21172664.1 | May 2021 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2022/062199 | 5/5/2022 | WO |
