Abatement method and apparatus
12447438 ยท 2025-10-21
Assignee
Inventors
Cpc classification
F23G5/50
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23G2208/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23G2900/50001
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23G2207/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23G2209/142
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
B01D53/34
PERFORMING OPERATIONS; TRANSPORTING
F23G5/50
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
An abatement apparatus and method are disclosed. The abatement apparatus is for treating an effluent stream from a semiconductor processing tool and comprises: a first abatement device configured to receive the effluent stream and operable to run in an active mode to treat the effluent stream; a second abatement device operable to run in an idle mode; and control logic operable, on receipt of an indication of an alarm condition associated with the first abatement device, to run the second abatement device in the active mode. In this way, a first or primary abatement device is provided which treats the effluent stream and a second or back-up abatement device is provided, should the first abatement device malfunction. However, by only causing the second abatement device to operate in the active mode when the first abatement device malfunctions, significant energy savings can be made.
Claims
1. An abatement apparatus for treating an effluent stream from a semiconductor processing tool, comprising: a first abatement device configured to receive said effluent stream and operable to run in an active mode to treat said effluent stream wherein the active mode of the first abatement device comprises supplying fuel gas to a foraminous burner in the first abatement device to affect flameless combustion along an exit surface of the foraminous burner; a second abatement device operable to run in an idle mode and an active mode wherein the idle mode comprises maintaining a pilot light but not supplying fuel gas to a second foraminous burner in the second abatement device and the active mode of the second abatement device comprises supplying fuel gas to the second foraminous burner in the second abatement device to affect flameless combustion along an exit surface of the second foraminous burner; a divert valve operable to supply said effluent stream to one of said first abatement device and said second abatement device; a bypass valve upstream of said divert valve; and control logic operable, on receipt of an indication of an alarm condition associated with said first abatement device, to switch said second abatement device from running in the idle mode to running in the active mode of the second abatement device; wherein said alarm condition has a divert time associated therewith and said control logic is operable to activate said bypass valve to prevent supply of said effluent stream to said divert valve should said second abatement device fail to switch from said idle mode to said active mode of the second abatement device within said divert time.
2. The abatement apparatus of claim 1, wherein said alarm condition indicates that an operational characteristic of said first abatement device has varied more than a threshold amount.
3. The abatement apparatus of claim 2, wherein said operational characteristic comprises at least one of a pressure, a flow rate, a sensor error and a valve error.
4. The abatement apparatus of claim 1, wherein said control logic is operable to control said divert valve to supply said effluent stream to said second abatement device following receipt of said indication of said alarm condition associated with said first abatement device.
5. The abatement apparatus of claim 1, wherein said control logic is operable to receive an indication of a mode status of said second abatement device and to control said divert valve to supply said effluent stream to said second abatement device when said indication of a mode status indicates that said second abatement device is running in said active mode of the second abatement device.
6. The abatement apparatus of claim 5, wherein said indication of said mode status of said second abatement device is determined from an indication of a temperature of said second abatement device.
7. The abatement apparatus of claim 1, wherein said control logic is operable to shutdown said first abatement device following operation of said divert valve to supply said effluent stream to said second abatement device.
8. The abatement apparatus of claim 1, wherein said control logic is operable to deactivate said bypass valve to supply said effluent stream to said divert valve upon receipt of an indication that said second abatement device is running in said active mode of the second abatement device.
9. The abatement apparatus of claim 1, comprising a first isolation valve between said divert valve and said first abatement device.
10. The abatement apparatus of claim 9, wherein said control logic is operable to activate said first isolation valve to prevent supply of said effluent stream to said first abatement device following activation of said divert valve to supply said effluent stream to said second abatement device.
11. A method for treating an effluent stream from a semiconductor processing tool, the method composing: providing a first abatement device configured to receive said effluent stream and operable to run in an active mode to treat said effluent stream wherein the active mode of the first abatement device comprises supplying fuel gas to a foraminous burner in the first abatement device to affect flameless combustion along an exit surface of the foraminous burner; providing a second abatement device operable to run in an idle mode and an active mode wherein the idle mode comprises maintaining a pilot light but not supplying fuel gas to a second foraminous burner in the second abatement device and the active mode of the second abatement device comprises supplying fuel gas to the second foraminous burner in the second abatement device to affect flameless combustion along an exit surface of the second foraminous burner; providing a divert valve operable to supply said effluent stream to one of said first abatement device and said second abatement device; providing a bypass valve upstream of said divert valve; and on receipt of an indication of an alarm condition associated with said first abatement device, switching said second abatement device from running in the idle mode to running in the active mode of the second abatement device; wherein said alarm condition has a divert time associated therewith and said bypass valve is activated to prevent supply of said effluent stream to said divert valve should said second abatement device fail to switch from said idle mode to said active mode of the second abatement device within said divert time.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) Embodiments of the present invention will now be described further, with reference to the accompanying drawings, in which:
(2)
(3)
DETAILED DESCRIPTION
(4) Before discussing the embodiments in any more detail, first an overview will be provided. Embodiments provide an arrangement whereby two or more abatement devices (such as combustion chambers) are provided downstream from a processing chamber of a processing tool generating an effluent stream. Typically, one of the abatement devices is operated as a primary abatement device and is activated by having the abatement chamber raised to a suitable operating temperature for abatement to occur. Meanwhile, a second abatement device remains inactive, typically in an idle mode, ready to be activated and is activated when a problem is detected with the operation of the primary abatement device. Once the secondary abatement device is operating correctly, the effluent stream supplied from the process tool ceases to be supplied to the primary abatement device and instead is supplied to the secondary abatement device. This provides for the seamless operation of the processing tool without interruption, even when operating issues arise with the abatement system.
(5) Abatement Apparatus
(6)
(7) Control logic 90 couples with sensors within the first abatement device 80A and the second abatement device 80B. The sensors typically provide parametric data regarding the operation of the abatement devices 80A, 80B, that data is processed by the control logic 90. Alternatively, it will be appreciated that the sensors may be configured to only report values out of range to the control logic. The control logic 90 is coupled to provide signals to control the bypass valves 50A, 50B, the divert valve 60, the isolation valves 70A, 70B, the first abatement device 80A and the second abatement device 80B.
(8) The operation of the abatement apparatus 10 will now be described with reference to
(9) Abatement of the effluent stream continues until the processing occurring within the processing tool 30 completes or an alarm condition is detected within the first abatement device 80A. In particular, at step S20, the control logic 90 operates to detect any of the alarm conditions described in Table 1.
(10) TABLE-US-00001 TABLE 1 Drain water high alarm Abatement alarm 10 sec Water low pressure alarm Abatement alarm 10 sec Quench high water flow Abatement alarm 10 sec Quench low water flow Abatement alarm 10 sec Quench water flow transducer error Abatement alarm 10 sec Packed tower high water flow Abatement alarm 10 sec Packed tower water flow transducer error Abatement alarm 10 sec Weir high water flow Abatement alarm 10 sec Weir water flow transducer error Abatement alarm 10 sec Fuel/air low differential pressure Abatement alarm 10 sec Fuel gas high pressure alarm Abatement alarm 10 sec Regulated fuel gas low pressure alarm Abatement alarm 10 sec Bypass valve position fault: inlets 1 to 6 Bypass alarm 10 sec LS609/610 drain tank water level-sensor Abatement alarm 30 sec error LS601/610 drain tank water level-sensor Abatement alarm 30 sec error Packed tower low water flow Abatement alarm 5 sec Weir low water flow Abatement alarm 5 sec Excess air high flow alarm **** Abatement alarm 5 sec Excess air low flow alarm **** Abatement alarm 5 sec Excess air flow error **** Abatement alarm 5 sec
(11) On the occurrence of any of those alarm conditions, at step S30, the control logic 90 sends a signal to the second abatement device 80B to cause it to switch to an operational or active mode. In particular, the control logic 90 causes the temperature within the second abatement device 80B to increase. Although various techniques can be envisaged for determining whether the second abatement device 80B is in its operational or active mode and has achieved the operating temperature, in this embodiment a temperature sensor monitors whether the temperature within the second abatement device 80B has increased in response to the activation signal by more than 50 C.
(12) Each alarm condition has a timeframe associated therewith. The timeframe defines the amount of time between an alarm condition being detected and a possible failure occurring in the first abatement device 80A. Accordingly, at step S40, a determination is made of whether that timer has expired. If the timer has not expired, then the control logic determines, at step S50, whether the second abatement device 80B is active. Should the second abatement device 80B not be active and ready to receive a diverted effluent stream then there is a risk that the first abatement device 80A will have failed and the effluent stream will be insufficiently abated.
(13) Accordingly, should the control logic 90 determine that the second abatement device 80B is not yet in the active mode when the timeframe expires, then, at step S60, the control logic 90 will activate the bypass valves 50A, 50B which prevents the effluent stream from being provided to the abatement apparatus 10 and instead supplies the effluent stream to other infrastructure for capture and/or processing. The control logic 90 will typically also cause additional nitrogen to be provided to the pumps 40A, 40B and to be mixed with the effluent stream being provided by the bypass valves 50A, 50B to ensure that any components within the effluent stream remain below their lower flammable limit. The control logic 90 will also typically activate a warning.
(14) Should the second abatement device 80B achieve its active or operational mode then, at step S70, the control logic 90 deactivates any active bypass valves 50A, 50B. The control logic 90 ensures that the isolation valve 70B is set to couple the second abatement device 80B with the divert valve 60. The control logic 90 then operates the divert valve 60 to divert the effluent stream from the first abatement device 80A to the second abatement device 80B. The control logic 90 then activates the isolation valve 70A to isolate the first abatement device 80A from the divert valve 60. The control logic 90 then sends a signal to shut down the first abatement device 80A. Maintenance on the first abatement device 80A can then occur.
(15) Hence, it can be seen that in one embodiment, when an alarm condition occurs on first abatement device 80A the switch over process to second abatement device 80B should occur without interruption to the production tool. However, second abatement device 80B is not available instantaneously as proof of burner should be sensed by reading a 50 C. increase in burner temperature. The system or individual inlet will typically go to bypass mode whilst second abatement device 80B is started.
(16) In one embodiment, abatement alarms have a timeout, e.g. water flow alarm of 10s. This timeout can be used to trigger the second abatement device 80B to start up from idle mode. If second abatement device 80B is then ready before the alarm timeout expires switchover to second abatement device 80B is seamless.
(17) One embodiment envisages a twin abatement concept which refers to two abatement systems coupled to one process tool with a single or multiple vacuum pumps; typically 6 pumps max. There is a primary and backup abatement whereby the primary has 100% of the process chamber gas loading. The backup abatement remains in an idle mode until required to take over all of the process gas load.
(18) Typically, additional 3-way process ball valves are required to provide a divert switching function 60 from device 80A to device 80B (per pump exhaust line) whenever device 80A enters alarm condition.
(19) The switchover procedure controls the bypass valves 50A, 50B, the divert valve 60, the abatement device 80A isolation valve and the abatement device 80B isolation valve.
(20) During the first abatement device 80A alarm timeout period, second abatement device 80B burner is established. Once an appropriate temperature increase is reached the divert valve 60 switches towards abatement device 80B. Isolation valves 70B will be open once the second abatement device 80B is started and there are no alarms present. Idle is not an alarm condition.
(21) This approach pre-empts the failure of a critical system and enables a backup system to finish the wafer batch. Knowing the alarm timeout means a seamless switch of process gas can occur without causing a warning or alarm condition at the process tool or chamber. If the alarm timeout period is insufficient to seamlessly switch the backup, there are two other interlocked devices. A nitrogen dilution module (not shown) can deliver 50-500 slm purge into the vacuum pump exhaust to dilute process gases to < lower flammable limit. A nitrogen flow switch (not shown) ensures the vacuum pump has sufficient nitrogen flow. These devices are interlocked to the tool or chamber. Providing both devices are healthy, the tool will receive a warning indication (soft shutdown). Once the backup abatement become available the warning signal is removed. If the backup abatement does not become available or either of the additional interlocked devices fails, the tool will receive an alarm indication (hard shutdown).
(22) Although illustrative embodiments of the invention have been disclosed in detail herein, with reference to the accompanying drawings, it is understood that the invention is not limited to the precise embodiment and that various changes and modifications can be effected therein by one skilled in the art without departing from the scope of the invention as defined by the appended claims and their equivalents.
(23) Although elements have been shown or described as separate embodiments above, portions of each embodiment may be combined with all or part of other embodiments described above.
(24) Although the subject matter has been described in language specific to structural features and/or methodological acts, it is to be understood that the subject matter defined in the appended claims is not necessarily limited to the specific features or acts described above. Rather, the specific features and acts described above are described as example forms of implementing the claims.