GB2497273A - Apparatus for treating a gas stream - Google Patents

Apparatus for treating a gas stream Download PDF

Info

Publication number
GB2497273A
GB2497273A GB1119990.8A GB201119990A GB2497273A GB 2497273 A GB2497273 A GB 2497273A GB 201119990 A GB201119990 A GB 201119990A GB 2497273 A GB2497273 A GB 2497273A
Authority
GB
United Kingdom
Prior art keywords
text
inlet
gas stream
condition
treatment
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.)
Granted
Application number
GB1119990.8A
Other versions
GB201119990D0 (en
GB2497273B (en
Inventor
Sergey Alexandrovich Voronin
John Leslie Bidder
Andrew Arthur Chambers
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.)
Edwards Ltd
Original Assignee
Edwards Ltd
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 Edwards Ltd filed Critical Edwards Ltd
Priority to GB1119990.8A priority Critical patent/GB2497273B/en
Publication of GB201119990D0 publication Critical patent/GB201119990D0/en
Priority to KR1020147016291A priority patent/KR102007549B1/en
Priority to SG11201402404VA priority patent/SG11201402404VA/en
Priority to EP12775288.9A priority patent/EP2780101B1/en
Priority to US14/358,935 priority patent/US9346005B2/en
Priority to JP2014541745A priority patent/JP6153033B2/en
Priority to PCT/GB2012/052443 priority patent/WO2013072658A1/en
Priority to CN201280056784.9A priority patent/CN103930189B/en
Priority to TW101139551A priority patent/TWI553148B/en
Publication of GB2497273A publication Critical patent/GB2497273A/en
Application granted granted Critical
Publication of GB2497273B publication Critical patent/GB2497273B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/005Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by heat treatment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/32Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J19/087Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
    • B01J19/088Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy giving rise to electric discharges
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J37/00Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
    • H01J37/32Gas-filled discharge tubes
    • H01J37/32009Arrangements for generation of plasma specially adapted for examination or treatment of objects, e.g. plasma sources
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05HPLASMA TECHNIQUE; PRODUCTION OF ACCELERATED ELECTRICALLY-CHARGED PARTICLES OR OF NEUTRONS; PRODUCTION OR ACCELERATION OF NEUTRAL MOLECULAR OR ATOMIC BEAMS
    • H05H1/00Generating plasma; Handling plasma
    • H05H1/24Generating plasma
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0216Other waste gases from CVD treatment or semi-conductor manufacturing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/80Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/818Employing electrical discharges or the generation of a plasma
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J2219/0894Processes carried out in the presence of a plasma

Abstract

An apparatus is provided for treating an exhaust gas stream 22 from an upstream processing apparatus. A plasma abatement device 10 has a reaction chamber 14 and a plasma torch 12 for generating a plasma stream for injection into the chamber for treating the gas stream 22. A first inlet 18 conveys a gas stream into the plasma abatement device for treatment, and a second inlet 20, in a normal condition of the apparatus, is in flow communication with a source of reagent for conveying reagent 24 into the plasma device. This reagent improves the efficiency of the treatment. In a back-up condition of the apparatus, the second inlet 20 is in flow communication with an exhaust gas stream source for conveying a gas stream into the device for treatment. This may be the same source that is in communication with first inlet 18 or a separate source from a separate processing apparatus. This allows continual use of the abatement device when the inlet18 become blocked due to debris and contamination. It also ensures that the upstream processing device does not have to be taken off-line whilst the abatement device is replaced or the blockage removed.

Description

APPARATUS FOR TREATING A GAS STREAM
The present invention relates to apparatus for treating a gas stream. The invention finds particular application in the treatment of a gas stream exhaust from a process chamber used in, for example, the semiconductor, solar or flat panel display industry.
One step in the fabrication of semiconductor devices is the formation of a thin film on a semiconductor substrate by chemical reaction of vapour precursors. One known technique for depositing a thin film on a substrate is chemical vapour deposition (CVD), which is commonly plasma enhanced. In this technique, process gases are supplied to a process chamber, housing the substrate, in which they react to form a thin film over the surface of the substrate. Examples of gases supplied to the process chamber to form a thin film include, but are not restricted to: Silane and ammonia for the formation of a silicon nitride film; Silane, ammonia and nitrous oxide for the formation of a SiON film; TEOS and one of oxygen and ozone for the formation of a silicon oxide film; and Al(CH3)3 and water vapour for the formation of an aluminium oxide film.
Gases exhausted from a process chamber can be treated with high efficiency and at a relatively low cost using a plasma abatement device. In the plasma abatement process, the gas stream to be treated is conveyed to a thermal atmospheric pressure plasma discharge (a plasma flare) which is primarily a source of heat. The plasma is preferably formed from an inert gas such as nitrogen and the process gasses passed to the flare subsequent to its formation as this protects the plasma forming device from damage. The plasma causes dissociation of the gas stream into reactive species, such as radicals, which can combine with oxygen or hydrogen species (also conveyed to the plasma flare) to produce relatively stable by-products.
A reaction chamber is located downstream of the plasma generator. The purpose of the reaction chamber is to provide a reaction space, remote from the plasma forming device, in which the gases exhausted from the process chamber can be treated by the plasma and react with additional reagent gases such as oxygen or hydrogen. The reaction chamber may consist of a pipe of dimensions which may for example be approximately 30 mm to 50 mm in diameter and 90 mm to 150 mm in length.
The noxious gases produced in the process chamber, namely unused precursor gases and the reaction by-products, must be treated as and when they are exhausted from the process chamber. They are not stored and then treated.
Accordingly the plasma abatement device, sometimes referred to as a plasma burner, or torch, must be operational during processing. If for whatever reason the burner stops working or it needs to be taken off line for cleaning or repair the substrate processing also has to stop. This is clearly not desirable since the processing ideally runs continuously 24 hours and day, seven days a week.
Accordingly it has been known to have a back up plasma burner device which can be brought in online should the main plasma burner break down or be taken off-line for any reason. However this is a very expensive solution to the problem since a very expensive plasma burner is kept largely inoperative a lot of the time.
According to the present invention there is provided apparatus for treating a process gas stream, comprising a plasma abatement device having a reaction chamber, a plasma torch for generating a plasma stream for injection into the chamber for treating said process gas stream, a first inlet for conveying said process gas stream into the plasma abatement device for treatment; and a second inlet which, in a normal condition of the apparatus, is in flow communication with a source of reagent for conveying reagent into the plasma device for improving the efficiency of the treatment and which, in a back-up condition of the apparatus, is in flow communication with said process gas stream source for conveying a gas stream into the device for treatment.
The present invention also provides a system comprising an apparatus for treating a process gas stream, said apparatus further comprising at least one processing chamber, a primary gas duct for conveying a process gas stream from the process chamber to the first inlet of the plasma abatement device for treatment and a reagent gas duct connected between a source of reagent and the second inlet of the plasma abatement device for conveying reagent into the device for improving the efficiency of the treatment in the normal condition of the apparatus, a secondary gas duct connected between one of said at least one process chambers and the second inlet for conveying a process gas stream to the device for treatment in a back-up condition of the apparatus, and a control for selectively switching between the normal condition and back-up condition.
Other preferred and/or optional aspects of the invention are defined in the accompanying claims.
In order that the invention may be well understood, some embodiments thereof, which are given by way of example only, will now be described with reference to the accompanying drawings, in which: Figure 1 is a schematic view of a plasma abatement device in a normal condition of a treatment apparatus; Figure 2 is a schematic view of a plasma abatement device in a backup condition of the treatment apparatus; Figure 3 is a schematic view of a processing system comprising the treatment apparatus in a normal condition; Figure 4 is a schematic view of a processing system comprising the treatment apparatus in a back-up condition; Figure 5 is a schematic view of another plasma abatement device in a normal condition of a treatment apparatus; Figure 6 is a schematic view of the other plasma abatement device in a backup condition of the treatment apparatus; Figure 7 is a schematic view of a processing system comprising another treatment apparatus in a normal condition; Figure 8 is a schematic view of a processing system comprising the treatment apparatus in a back-up condition; Figure 9 shows a part view of a plasma abatement device; and Figure 10 shows an inlet arrangement for a plasma abatement device.
Figures 1 and 2 are schematic views of a plasma abatement device 10 forming part of an apparatus for treating a gas stream. The device 10 comprises a plasma generator, or torch, 12 and a reaction chamber 14. The torch provides a plasma flare 16 for treating a gas stream conveyed to the device from a process chamber (see Figures 3, 4, 7 and 8). The plasma device is preferably a DC plasma device comprising aDO plasma torch, such as that described in EP1 71 5937. The chamber 14 is provided with a first inlet 18 and a second inlet 20. In a normal condition of the apparatus shown in Figure 1, the first inlet 18 is in fluid communication with a processing chamber. The stream of process gases 22 emitted from a processing chamber is caused to flow via inlet 18 into reaction chamber 14 and the plasma flare 16. The second inlet 20 is in fluid communication with a source of a reagent 24, typically oxygen, (see Figures 3, 4, 7 and 8). The reagent is caused to flow via inlet 20 into the chamber 14 where it is mixed with the process gases to improve the efficiency of treatment within the plasma flare 16. In a back-up condition of the apparatus shown in Figure 2, a process gas 22 from a process chamber is conveyed to the second inlet 20 in place of the reagent 24. The back-up condition of the apparatus is selected if another plasma abatement device of the apparatus becomes inoperative or if a duct conveying process gas to another plasma device becomes occluded. Therefore in the back-up condition different process gases may be conveyed to the same reaction chamber. Alternatively or additionally, if the duct conveying process gas to the first inlet 18 becomes occluded, for instance by the build-up of solid deposits in the duct, the process gas 22 can be diverted to the second inlet 20 rather than the first inlet.
The present invention recognises that the supply of reagent to the reactor chamber can be dispensed with or at least can be supplied to the abatement process downstream of the reaction chamber. For example, it may be supplied into a spray tower (or wet scrubber) downstream of the reaction chamber to complete the treatment of the process exhaust gases. Accordingly, the gas stream is heated by the plasma 16 inside the reaction chamber 14, and then reacts with the reagent downstream of the reactor chamber. As the reaction takes place outside of the reactor and the gas temperature is colder the system efficiency is lower in this operating regime. Accordingly, in accordance with the present invention, the inlet normally used for the reagent gases can be used instead to inject process gases.
This may be necessary if, for example, another abatement device such as a plasma burner goes offline. Generally a process tool, or system, will comprise a plurality of processing chambers and a respective plurality of plasma burners. Should one burner go offline, the process gas from the associated processing chamber is directed towards the reagent inlet of another plasma burner. That plasma burner therefore can treat process gases from more than one processing chamber but without the use of reagent in the reaction chamber.
One of the requirements of modern plasma abatement systems is to have an available back up inlet. The present invention provides a plasma abatement device with several separate gas inlets.
The present invention involves the understanding that whilst reagent is thought to be required for improving treatment of process gases in the reaction chamber, the requirement of reagent is subsidiary to the need for uninterrupted treatment of process gases. Accordingly, the flow of reagent into a device can be interrupted or injected downstream so that process gases can be diverted to the device through the inlet normally used for the reagent.
A processing system is shown in Figure 3 during a normal condition of an apparatus for treating a gas stream. Two process chambers 26, 28 are arranged for processing products such as semi-conductor wafers or flat panel displays. The processing is enabled by the use of various gases for etching, depositing or cleaning in a vacuum generating by one or more vacuum pumps (not shown, but located between the process chambers 26, 28 and abatement devices). These gases are noxious and cannot be released without treatment. A plurality of plasma abatement devices 10, as described in relation to Figures 1 and 2, are arranged to treat process gases released from the process chambers 26, 28.
Primary gas ducts 30 convey a process gas stream 21, 22 from the process chambers 28, 30, via vacuum pumps, to the first inlet 18 of the plasma abatement device 10 for treatment. Treated gas 38 is exhausted from the plasma abatement devices 10 for disposal or storage. Reagent gas ducts 32 are connected between one, or more, source(s) of reagent 34 and the second inlet 20 of the plasma abatement device for conveying reagent 24 into the device for improving the efficiency of the treatment in the normal operating condition of the apparatus.
As shown in Figure 4 when the apparatus is in the back-up condition, a secondary gas duct 36 is connected between the process chamber 26 and the second inlet 20 of the plasma abatement device 10 shown on the right for conveying a process gas stream 21 to the device for treatment. In this example, the plasma abatement apparatus 10 shown on the left in Figure 4 has become inoperative or primary process gas duct has become partially or fully occluded. In this case, process gas 21 is diverted for treatment by the plasma abatement device 10 shown on the right in the Figure and therefore treatment of all of the gases exhausted from the process chambers is uninterrupted and the process tool 26 can remain operative.
There is a relatively modest reduction in the efficiency of the gases without the reagent but this is considered preferable to interruption of treatment of exhaust gases from one of the process chambers 26 or interruption of the operation of said process chamber 26. The arrangement benefits in that a properly functioning plasma abatement device is not redundant in the apparatus and only when inoperative is gas diverted elsewhere in the apparatus for treatment.
Referring to both Figures 3 and 4, the treatment apparatus comprises a valve arrangement for allowing reagent to be conveyed through the reagent ducts 32 in the normal condition of the device. When treatment is interrupted in one of the abatement devices 10, the second gas stream is conveyed through the second process gas duct 36 in the back-up condition of the device.
The valve arrangement in the example shown in Figures 3 and 4 comprises first valves 40 located to convey process gas in the primary ducts 30 selectively towards either the first inlets 18 or the second inlets 20. Second valves 42 are located to convey selectively either reagent along the reagent ducts or process gas towards the second inlets 20. In this preferred arrangement, valves 40 and 42 are three way valves. The primary, reagent and secondary ducts share portions of the conduits, or pipes, which convey gas in the apparatus. That is, the primary and secondary ducts are co-extensive upstream of the first valves 40 and the secondary ducts and reagent ducts are co-extensive downstream of the second valves 42.
It will be apparent to those skilled in the art that the valves may be arranged differently from the arrangement shown in Figures 3 and 4 whilst still achieving the same desired result.
A control 44 is provided for selectively switching between the normal condition shown in Figure 3 and back-up condition shown in Figure 4. The control 44 is shown in Figure 4 and is connected by control lines 46 (shown schematically in broken lines) to the valves 40, 42. The control selectively operates the valve arrangement for switching between the normal condition and the back-up condition. Switching may be initiated manually by an operative or may be automatic. In this latter case, a sensor 48 may be provided for sensing an operative condition of a plasma abatement device and outputting a signal to the control in the event that one or more of the plasma abatement devices are inoperative. For example, the sensor may monitor current of the DC plasma torch and, if the current falls below a predetermined current -indicative of a reduced gas flow, a system fail signal is outputted to the control 44 which can then activate a back-up condition. Similar sensors may be provided for the other plasma abatement devices of the system.
In the arrangement shown in Figures 3 and 4, there is a plurality of plasma abatement devices 10 having a respective plurality of first inlets 18 arranged to be in flow communication with a plurality of process chambers 26, 28. Whilst two such plasma abatement devices are shown connected to respective processing chambers, more than two may be provided as required. In the normal condition of the apparatus, the said second inlets 20 are arranged to be in flow communication with a source of reagent. In the back-up condition of the apparatus at least one second inlet is arranged to be in flow communication with one of said process chambers for receiving a gas stream from said process chamber for treatment.
Therefore, in this arrangement, one plasma abatement device acts as a back-up for another plasma abatement device and is arranged in the back-up condition to receive a gas stream from a different one of said process chambers to the process chambers that it receives a gas stream from in the normal condition.
In an alternative arrangement shown in Figures 5 and 6, in the normal condition of the apparatus the first inlet 18 is arranged to be in flow communication with a the process chamber 26 via a primary duct 30 to convey a gas stream 21 from the process chamber for treatment. The second inlet 20 is arranged to receive a reagent 24 from the source of reagent 34 along a reagent duct 32 for improving the efficiency of the treatment. This arrangement is similar to the arrangement shown in Figures 3 and 4. In the back-up condition, shown in Fig. 6, however the second inlet is arranged to be in flow communication with the same process chamber 26 such that if flow is restricted to the first inlet along the primary duct 30 i.e. along a portion 48 of the primary duct, the gas stream 21 from said process chamber can be conveyed through the second inlet 20 via the secondary duct 50 for treatment.
Valves 52 and 54 are operable by a control (not shown) in a similar way to that shown in Figures 3 and 4.
In a modification of the arrangements previously described in Figures 3 and 4 or Figures 5 and 6, at least one of the plasma abatement devices comprises at least three inlets and one of said inlets only conveys a gas stream or reagent into the plasma abatement device in the back-up condition of the apparatus. A plasma abatement device 60 arranged in this way is shown in Figures 7 and 8 and comprises three additional inlets 62, 64, 66. In the normal condition of the apparatus in which there are multiple similar plasma abatement devices 60, the first inlet 18 receives a gas stream from a first chamber, the second inlet receives a reagent from
S
the source of reagent 34 and the further inlets 62, 64, 66 are not used. In a back-up condition, the further inlets may receive a second gas stream 68, a third gas stream or a fourth gas stream 72 from respective process chambers. In this way, three further gas streams can be treated if their respective plasma abatement devices become inoperative, whilst still maintaining a flow of reagent into the device to improve the efficiency of treatment. Optionally the second inlet 20 could also be used to treat a gas stream from a further process chamber; although in this case reagent would not be supplied to the device 60.
In a preferred arrangement, at least one, and more preferably all, of the plasma abatement devices comprises the same number of inlets as there are process chambers, such that in the back-up condition of the apparatus, the gas streams from all of the process chambers can be conveyed to the device through respective said inlets for treatment in said device.
The first inlet and the second inlet of a said plasma abatement device are configured to direct fluid into reaction chamber 14 so that fluid conveyed through the first inlet or the second inlet is directed away from the second inlet or the first inlet respectively to reduce mixing of the fluids in either of the inlets. Figure 9 shows a view of the reactor chamber 14, a plasma flare 16 and first and second inlets 18, 20.
The first inlet 18 introduces gas flow in a direction which is generally perpendicular from the direction of gas flow introduced to the reactor through second inlet 20. It will be seen therefore that gas from one inlet is directed away from the other inlet so that reaction of the two gases does not generally take place in either of the inlets.
Instead, reaction between the two gases occurs in the plasma flare 16 resulting in more efficient treatment of the gas stream or streams.
Also shown in Figure 9 are two double-headed arrows 74, 76. Arrow 74 shows the range of positions in which the first inlet is preferably located whilst still achieving the same effect, namely that gases passing through the two inlets are directed away the other inlets. On the other hand, the arrow 76 shows the range of undesirable positions in which the first inlet 18 may be located which would result in gas from one inlet being directed towards the other inlet.
The preferred arrangement directing gas from one inlet away from another inlet, particularly where there are a multiplicity of inlets are shown in Figures 1 and 7 in which the inlets are configured to convey fluid into the device in directions which are generally parallel one direction with another direction. As will be seen from these Figures, the inlets are arranged with one inlet vertically above an adjacent inlet and with each inlet mechanically separated from the other inlets to space the inlets apart.
The configuration of the inlets into the reaction chamber 14 is more important if both inlets are to be used to inject process gases. It is important that the different process gases do not react with each other prior to being injected into the plasma flare. As both inlets may be used to inject process gas in the back-up operational condition the inlets therefore should not be located opposite each other as shown by the range of positions 76 in Figure 9. It is possible to have the inlets located such that the gases are injected at an angle to each other. However better results are io available when the inlets are configured with the flow of gases all being directed in the same direction into the reactor chamber.
Figure 3 is a schematic view of a plasma abatement device in accordance with the present invention.
A multiple inlet arrangement is shown in Figure 10 which can be adopted in any of the previously discussed embodiments. The inlet arrangement has a "slice-type" structure having four inlets 78, 80, 82, 84 separated from each other mechanically by spacers 86. The "slice-type" structure allows introduction of different process gases into one plasma reactor chamber without their mixing at the inlets.
The treatment apparatus as described with reference to the Figures constitutes an improvement as part of a processing system comprising at least one processing chamber. The apparatus comprises a primary gas duct, i.e. conduit, for conveying a process gas stream from the process chamber to the first inlet of the plasma abatement device for treatment and a reagent gas duct connected between a source of reagent and the second inlet of the plasma abatement device for conveying reagent into the device for improving the efficiency of the treatment in the normal condition of the apparatus. A secondary gas duct connected between one of said at least one process chambers and the second inlet conveys a process gas stream to the device for treatment in a back-up condition of the apparatus. A control means selectively switches between the normal condition and back-up condition.
Typically, the system comprises a plurality of process chambers, wherein in the normal condition of the apparatus a plurality of process gas streams are conveyed from the process chambers to the first inlets of respective plasma abatement devices, and in the back-up condition the gas stream a process gases is conveyed to the second inlet of one of said plasma abatement devices.
If there is only one process chamber, in the normal condition of the apparatus a process gas stream is conveyed from the process chamber to the first inlet of a single plasma abatement device, and in the back-up condition the gas stream is diverted to the second inlet of device for treatment in place of the reagent.
The invention has been described above with respect to a preferred embodiment. It will be understood by those skilled in the art that changes and modifications may be made thereto without departing from the scope of the invention as set out in the appended claims.

Claims (1)

  1. <claim-text>Claims 1. Apparatus for treating a process exhaust gas stream from a process device, comprising a plasma abatement device having a reaction chamber, a plasma torch for generating a plasma stream for injection into the chamber for treating a process exhaust gas stream, a first inlet for conveying the process exhaust gas stream into the plasma abatement device for treatment; and a second inlet which, in a normal condition of the apparatus, is in flow communication with a source of reagent for conveying reagent into the plasma device for improving the efficiency of the treatment and which, in a back-up condition of the apparatus, is in flow communication with a process exhaust gas stream source for conveying a process exhaust gas stream into the device for treatment.</claim-text> <claim-text>2. Apparatus according to claim 1, wherein in the normal condition, the first inlet is in flow communication with a first process chamber for conveying into the device a first process ehxaust gas stream for treatment and in the back-up condition the second inlet is in flow communication with a second process chamber for conveying into the device a second process exhaust gas stream for treatment.</claim-text> <claim-text>3. Apparatus according to claim 2, comprising a first duct arranged to convey reagent from the reagent source to the second inlet, a second duct arranged to convey the second process exhaust gas stream from the second process chamber to the second inlet, and a valve arrangement for allowing reagent to be conveyed through the first duct in the normal condition of the device and allowing the second process exhaust gas stream to be conveyed through the second duct in the back-up condition of the device.</claim-text> <claim-text>4. Apparatus according to claim 3, wherein the valve arrangement comprises first and second valves located in respective first and second ducts, the first valve being operable to allow flow communication through the first duct and the second valve being operable to allow flow communication in the second duct.</claim-text> <claim-text>5. Apparatus according to any of the preceding claims, comprising a plurality of said plasma abatement devices having a respective plurality of said first inlets arranged to be in flow communication with a plurality of process chambers, and in the normal condition of the apparatus, the plasma abatement devices having a respective plurality of said second inlets arranged to be in flow communication with a source of reagent in the normal condition of the apparatus, wherein in the back-up condition of the apparatus at least one second inlet is arranged to be in flow communication with one of said process chambers for receiving a process exhaust gas stream from said process chamber for treatment.</claim-text> <claim-text>6. Apparatus according to claim 5, wherein in the back-up condition of the apparatus the first inlet is arranged to be in flow communication with a said process chamber and the second inlet is arranged to be in flow communication with a different one of said process chambers.</claim-text> <claim-text>7. Apparatus according to claim 5, wherein in the normal condition of the apparatus the first inlet is arranged to be in flow communication with a said process chamber and in the back-up condition the second inlet is arranged to be in flow communication with the same said process chamber such that if flow is restricted to the first inlet the process exhaust gas stream from said process chamber can be conveyed through the second inlet for treatment.</claim-text> <claim-text>8. Apparatus according to claim 5, wherein at least one of the plasma devices comprises at least three inlets and one of said inlets only conveys a process exhaust gas stream or reagent into the plasma abatement device in the back-up condition of the apparatus.</claim-text> <claim-text>9. Apparatus according to claim 8, wherein in the back-up condition of the apparatus, at least one of the plasma abatement devices comprises a said first inlet which is arranged to be in flow communication with a first process chamber for conveying a first process exhaust gas stream into the device for treatment, a said second inlet which is arranged to be in flow communication with a second process chamber for conveying a second process exhaust gas stream into the device for treatment, and a third inlet which is arranged to be in flow communication with a third process chamber for conveying a third process exhaust gas stream into the device for treatment.</claim-text> <claim-text>10. Apparatus according to claim 9, wherein at least one of the plasma abatement devices comprises the same number of inlets as there are process chambers, such that in the back-up condition of the apparatus, the process exhaust gas streams from all of the process chambers can be conveyed to said at least one device through respective said inlets for treatment in said device.</claim-text> <claim-text>11. Apparatus according to claim 10, wherein each of the plasma abatement devices comprise the same number of inlets as there are process chambers, such that in the back-up condition of the apparatus, the process exhaust gas streams from all of the process chambers can be conveyed to any one of the devices through respective said inlets for treatment in said any one device.</claim-text> <claim-text>12. Apparatus according to any of the preceding claims, wherein the first inlet and the second inlet of a said plasma abatement device are configured to convey fluid into plasma abatement device in respective directions selected so that fluid from conveyed through the first inlet or the second inlet is directed away from the second inlet or the first inlet respectively to reduce mixing of the fluids in either of the inlets.</claim-text> <claim-text>13. Apparatus according to claim 12, wherein the inlets of a said plasma abatement device are configured to convey fluid into the device in directions which are generally parallel one direction with another direction.</claim-text> <claim-text>14. Apparatus according to claim 13, wherein the inlets are arranged with one inlet vertically above an adjacent inlet.</claim-text> <claim-text>15. Apparatus according to claim 13 or 14, wherein each inlet is mechanically separated from the other inlets.</claim-text> <claim-text>16. Apparatus according to any of the preceding claims, comprising a control configured for selective switching between the normal condition and the back-up condition.</claim-text> <claim-text>17. Apparatus according to claim 16, wherein the control which is manually operable for switching between the normal condition and the back-up condition.</claim-text> <claim-text>18. Apparatus according to claim 16, comprising a plurality of said plasma abatement devices and a sensor for sensing a reduction in treatment of a gas stream by any one of the plasma abatement devices and outputting a signal to the control which in response conveys the gas stream to a second or further inlet of another of said plasma abatement devices.</claim-text> <claim-text>19. A system comprising an apparatus according to any of the preceding claims, further comprising at least one processing chamber, a primary gas duct for conveying a process exhaust gas stream from the process chamber to the first inlet of the plasma abatement device for treatment and a reagent gas duct connected between a source of reagent and the second inlet of the plasma abatement device for conveying reagent into the device for improving the efficiency of the treatment in the normal condition of the apparatus, a secondary gas duct connected between one of said at least one process chambers and the second inlet for conveying a process exhaust gas stream to the device for treatment in a back-up condition of the apparatus, and a control for selectively switching between the normal condition and back-up condition.</claim-text> <claim-text>20. A system according to claim 19, comprising a plurality of process chambers, wherein in the normal condition of the apparatus a plurality of process exhaust gas streams are conveyed from the process chambers to the first inlets of respective plasma abatement devices, and in the back-up condition the process exhaust gas stream from a said process chamber is conveyed to the second inlet of one of said plasma abatement devices.</claim-text> <claim-text>21. A system according to claim 20, wherein in the normal condition of the apparatus a process exhaust gas stream is conveyed from the process chamber to the first inlet of a said plasma abatement device, and in the back-up condition the process exhaust gas stream is diverted to the second inlet of device for treatment.</claim-text>
GB1119990.8A 2011-11-19 2011-11-19 Apparatus for treating a gas stream Active GB2497273B (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
GB1119990.8A GB2497273B (en) 2011-11-19 2011-11-19 Apparatus for treating a gas stream
PCT/GB2012/052443 WO2013072658A1 (en) 2011-11-19 2012-10-03 Apparatus for treating a gas stream
SG11201402404VA SG11201402404VA (en) 2011-11-19 2012-10-03 Apparatus for treating a gas stream
EP12775288.9A EP2780101B1 (en) 2011-11-19 2012-10-03 Apparatus for treating a gas stream
US14/358,935 US9346005B2 (en) 2011-11-19 2012-10-03 Apparatus for treating a gas stream
JP2014541745A JP6153033B2 (en) 2011-11-19 2012-10-03 Gas flow treatment equipment
KR1020147016291A KR102007549B1 (en) 2011-11-19 2012-10-03 Apparatus for treating a gas stream
CN201280056784.9A CN103930189B (en) 2011-11-19 2012-10-03 For processing the equipment of air-flow
TW101139551A TWI553148B (en) 2011-11-19 2012-10-25 Apparatus for treating a gas stream

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1119990.8A GB2497273B (en) 2011-11-19 2011-11-19 Apparatus for treating a gas stream

Publications (3)

Publication Number Publication Date
GB201119990D0 GB201119990D0 (en) 2012-01-04
GB2497273A true GB2497273A (en) 2013-06-12
GB2497273B GB2497273B (en) 2017-09-13

Family

ID=45475418

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1119990.8A Active GB2497273B (en) 2011-11-19 2011-11-19 Apparatus for treating a gas stream

Country Status (9)

Country Link
US (1) US9346005B2 (en)
EP (1) EP2780101B1 (en)
JP (1) JP6153033B2 (en)
KR (1) KR102007549B1 (en)
CN (1) CN103930189B (en)
GB (1) GB2497273B (en)
SG (1) SG11201402404VA (en)
TW (1) TWI553148B (en)
WO (1) WO2013072658A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017068609A1 (en) * 2015-10-19 2017-04-27 カンケンテクノ株式会社 Exhaust gas treatment device

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2535528A (en) 2015-02-23 2016-08-24 Edwards Ltd Apparatus for treating gas
GB2540992A (en) * 2015-08-04 2017-02-08 Edwards Ltd Control of gas flow and power supplied to a plasma torch in a multiple process chamber gas treatment system
JP2020507219A (en) * 2017-02-03 2020-03-05 アプライド マテリアルズ インコーポレイテッドApplied Materials,Incorporated Plasma mitigation of nitrous oxide from semiconductor process wastewater
KR102282582B1 (en) * 2019-10-14 2021-07-29 영진아이엔디(주) Energy saving type scrubber system for treating waste gas and method for the same
TWI786954B (en) * 2021-11-22 2022-12-11 財團法人工業技術研究院 Device and method of simultaneously removing flammable gas and nitrous oxide

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5779991A (en) * 1996-11-12 1998-07-14 Eastern Digital Inc. Apparatus for destroying hazardous compounds in a gas stream
JP2003183832A (en) * 2001-12-20 2003-07-03 Sekisui Chem Co Ltd Discharge plasma treatment method
WO2005079958A1 (en) * 2004-02-20 2005-09-01 The Boc Group Plc Method and apparatus for treating a fluorocompound-containing gas stream
US20070284242A1 (en) * 2004-01-06 2007-12-13 Michel Moisan Method For Treating Gases By High Frequency Discharges
US20110135552A1 (en) * 2009-12-03 2011-06-09 Applied Materials, Inc. Methods and apparatus for treating exhaust gas in a processing system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000133494A (en) * 1998-10-23 2000-05-12 Mitsubishi Heavy Ind Ltd Microwave plasma generation device and method
RU2286837C2 (en) 2002-05-08 2006-11-10 ЛАУ Эдмунд Кин Он Method and device for treating harmful waste
FR2873045B1 (en) * 2004-07-13 2007-01-19 Air Liquide TREATMENT OF GASEOUS EFFLUENTS BY ATMOSPHERIC PRESSURE PLASMA
JPWO2008068917A1 (en) * 2006-12-01 2010-03-18 カンケンテクノ株式会社 Semiconductor manufacturing exhaust gas abatement system
JP5153218B2 (en) * 2007-06-12 2013-02-27 キヤノン株式会社 Digital data broadcast receiving apparatus and control method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5779991A (en) * 1996-11-12 1998-07-14 Eastern Digital Inc. Apparatus for destroying hazardous compounds in a gas stream
JP2003183832A (en) * 2001-12-20 2003-07-03 Sekisui Chem Co Ltd Discharge plasma treatment method
US20070284242A1 (en) * 2004-01-06 2007-12-13 Michel Moisan Method For Treating Gases By High Frequency Discharges
WO2005079958A1 (en) * 2004-02-20 2005-09-01 The Boc Group Plc Method and apparatus for treating a fluorocompound-containing gas stream
US20110135552A1 (en) * 2009-12-03 2011-06-09 Applied Materials, Inc. Methods and apparatus for treating exhaust gas in a processing system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017068609A1 (en) * 2015-10-19 2017-04-27 カンケンテクノ株式会社 Exhaust gas treatment device

Also Published As

Publication number Publication date
US20140334982A1 (en) 2014-11-13
KR20140101801A (en) 2014-08-20
JP2015502249A (en) 2015-01-22
US9346005B2 (en) 2016-05-24
TWI553148B (en) 2016-10-11
TW201326450A (en) 2013-07-01
SG11201402404VA (en) 2014-09-26
GB201119990D0 (en) 2012-01-04
EP2780101B1 (en) 2021-02-17
GB2497273B (en) 2017-09-13
KR102007549B1 (en) 2019-10-21
WO2013072658A1 (en) 2013-05-23
CN103930189B (en) 2016-08-24
EP2780101A1 (en) 2014-09-24
JP6153033B2 (en) 2017-06-28
CN103930189A (en) 2014-07-16

Similar Documents

Publication Publication Date Title
EP2780101B1 (en) Apparatus for treating a gas stream
US20230317437A1 (en) Vacuum pump protection against deposition byproduct buildup
CN101429651B (en) Multi-port pumping system for substrate processing chambers
KR101283264B1 (en) Gas combustion apparatus
US9133836B2 (en) Vacuum pumping system
US20170350395A1 (en) Improvements in or relating to vacuum pumping arrangement
KR20220106941A (en) Systems and methods for reducing effluent build-up in a pumping exhaust system
CN103972010A (en) Gas supply system for substrate processing chamber and method therefor
TWI453788B (en) High efficiency trap for deposition process
US20190282948A1 (en) Semiconductor processing system
EP2032235B1 (en) Method and apparatus for treating a gas stream
WO2020068338A1 (en) Atomic oxygen and ozone device for cleaning and surface treatment
EP2311065B1 (en) Remote plasma cleaning method and apparatus for applying said method
KR101006384B1 (en) Waste Gas Purification Apparatus
JP2009297709A (en) Plasma processing system for fluid or fluid mixture
CN102776487A (en) Semiconductor processing equipment and semiconductor processing method
US20240055278A1 (en) Gas supply apparatus, vacuum processing apparatus, and gas supply method
CN113384979A (en) Method and system for selective exhaust gas treatment
KR20220093303A (en) A Plasma Scrubber Apparatus With a Structure of Distributing a Supplying Amount
KR20010009000A (en) Pumping System of a Low Pressure Chemical Vapour Deposition Apparatus
JP2008266710A (en) Vacuum film deposition equipment