Embodiment
The present invention is about the device for monitoring, control and clean semiconductor processing system and/or its parts and method, and is about the composition for this kind of cleaning.
In an aspect, the present invention is about remove deposition from the parts of this semiconductor processing system or semiconductor processing system, wherein this system or system unit is contacted with a cleaning combination that comprises a gas phase reactive material.
As used herein, term " gas phase reactive material " is intended to broadly be construed as denoting following material, comprise: one or more halide and/or misfit thing (with the form of gaseous state or steam), the ion of this one or more compound and/or misfit thing and electric slurry form, and from this one or more compound, one or more misfit thing and ion and derivative element and the ion of electric slurry form.As the gas phase reactive material being used in wide in range operation of the present invention can also differently refer to any combination of (but being not limited to) " gas phase reactive composition ", one " cleaning agent ", one " purge gas ", one " etching gas ", one " gaseous halide ", one " gaseous cleaning agent ", " reactive halide ", one " cleaning compound ", one " cleaning combination ", " cleaning steam ", one " etchant vapor " or this type of term.
As used herein, with regard to an Ion Implantation Equipment, " ion source region " includes, but are not limited to vacuum chamber, source arc chamber, source insulator, extractor electrode, inhibition electrode, High-Voltage Insulation, source sleeve pipe, filament, negative electrode and repellel electrode.As those who familiarize themselves with the technology will understand, term " ion source region " uses with its widest meaning, for example, Claude Bernard (Bernas) or freeman (Freemen) ion source assembly comprise a filament and repellel electrode, and IHC source assembly comprises negative electrode and anticathode.
The present invention has considered the cleaning of semiconductor processing system and parts thereof, together with other substrate and device, and the deposition impact that these substrates and device are subject to form on it in its normal process operation.This operation includes, but are not limited to the cleaning of vacuum fore line and roughing pump.In view of description herein, as those who familiarize themselves with the technology will understand, the selected mouth that purge gas may be flowed through in a plurality of mouthfuls is to walk around some district and/or the target given zone of implanter.For example, XeF
2or other purge gas can be through sending the mouth that needs the district of cleaning by approaching.Clenaing effect also can strengthen, as long as most of purge gass will be introduced into target area and do not exhausted (for example, as occurred) by reacting of carrying out with residue in the situation that () purge gas is only introduced by source housing along circulation path.Selected mouth can be pre-existing in or form/produce for this object.This technology can be used for cleaning ion source region, magnetic/analyzer region, vacuum system, process chamber of (but unrestricted) implanter etc.Cleaning can by by purge gas continuous flow by and/or go through predetermined time through implanter Suo Yao district or region and measure to realize.Alternatively, or combination with it, purge gas can be gone through predetermined time and measures to allow purge gas diffusion and react with unwanted residue and/or deposition in being closed in system.
The present invention provides an implanted ions system in different aspects, and this system has following ability: the filament by being suitably controlled at temperature in arc chamber and in the ion source of the arc chamber of growing/be etched in is to realize the growth of desirable filament or the etching of alternative filament.
Extra aspect of the present invention system about use reactive gas for example WFx, AsFx, PFx and TaFx (wherein x has the suitable value in a stoichiometry ground or the scope of value) in position or the cleaning arrangement of offing normal under electricity slurry or hot conditions, clean the region of Ion Implantation Equipment or the parts of Ion Implantation Equipment.
Of the present invention another is to be about BrF about aspect
3for in position or the cleaning arrangement of the offing normal purposes of cleaning implanted ions system or its one or more parts under the condition of ambient temperature, high temperature or electricity slurry.
The operation of one implanted ions system causes the Shen that produces the material relevant with ionization in this system or its parts to be amassed.The present invention has considered monitoring, control and/or has cleaned this implanted ions system and/or its one or more parts, to remove at least in part this type of deposition relevant with ionization from this system and/or its parts.This cleaning method is about this system and/or its parts are contacted to realize their at least part of removing under the condition that can make this gas phase reactive material react with this deposition with a cleaning combination that comprises a gas phase reactive material.
Except the deposition relevant with ionization being caused by unstrpped gas itself, also have been found that the deposition that forms or residue may be due to unstrpped gas and the reactivity of material that forms this system unit in an implanted ions system.For example, the vacuum chamber of an implanted ions system can form with stainless steel or aluminium.System unit in this vacuum chamber can use graphite (for example, standard or vitreous), insulating material (for example, boron nitride) and/or encapsulant (for example Teflon
kel-FTM, PEEKTM, DelrinTM, VespelTM, VitonTM, Buna-N, silicon etc.) construct.Other material of chemical reaction susceptible that can exist in this implanted ions system and that deposition is wherein produced includes but not limited to pottery, epoxy composite, aluminium nitride, aluminium oxide, silicon dioxide and boron nitride containing lead oxide.
This ion source itself can be by tungsten, graphite, molybdenum or tantalum, sometimes have a small amount of copper and silver to form.This ion source arc is made up of or a graphite body tungsten or molybdenum conventionally, and this graphite body is lined with tungsten or molybdenum.In this case, a kind of feed material of fluoride source (for example BF
3, GeF
4, SiF
4, AsF
5, AsF
3, PF
5, and/or PF
3) under operating temperature, for example, react with the material of arc chamber tungsten or the molybdenum of the lining of arc chamber or this chamber (from), to form an intermediate by-products, this accessory substance and then can move and decompose with Shen long-pending tungsten or molybdenum in this system and discharge fluorine.
For example, such as GeF of a unstrpped gas
4the free fluoride that can dissociate in this source housing and produce can etching corrode the material in this arc chamber, for example tungsten.Will there is this kind of reaction in tungsten on a colder surface, so if at electricity slurry through clashing into and therefore this filament system heat, this fluoride can react with tungsten on these walls of arc chamber, these walls of etching also form WF
6gas.WF
6then can on this hot filament, amass tungsten in Shen, cause the growth of its size.
Work as GeF
4while producing a large amount of free fluorine, unstrpped gas is BF such as
3or SiF
4produce the free fluorine of less amount and correspondingly still less the tungsten Shen of degree is long-pending on filament, although it is few, but still very important.
Not fluorine-containing unstrpped gas (for example PH
3and AsH
3) be problematic, because may cause that the metal Shen on filament amasss on the wall of arc chamber, and result filament attenuates.
Therefore the present invention has considered to clean an implanted ions system or its one or more parts, for removing at least in part identical with the material of this arc chamber deposition relevant with ionization.
Can in an implanted ions system, carry out according to cleaning of the present invention, wherein plurality of raw materials gas is introduced in this system simultaneously.Unstrpped gas can also be used with one or more gas phase reactive material simultaneously, or can be input in this system with one or more gas phase reactive material ALT pulse.
The deposition relevant with ionization of cleaning method indication of the present invention comprises multiple material, and these materials can be for example by the normal running that forms and accumulate interfering ion implant system in the equipment of ion source or other ionization process.The long-pending material in institute Shen can differently comprise, by forming below or substantially by forming below: silicon, boron, phosphorus, germanium, arsenic, tungsten, molybdenum, selenium, antimony, indium, carbon, aluminium and/or tantalum.
The deposition relevant with ionization in ion source arc and on extractor electrode can form thin slice and form little particle.Once these particles form, can be with an ion beam transmission, be for example implanted to the bundle of the doping of one in wafer ion.If this type of transmission particle arrives this wafer, the particle contamination producing on this wafer may seriously reduce the productive rate of the useful device that can manufacture on this wafer.Cleaning method of the present invention was removed before this type of deposition relevant with ionization can form thin slice and particle, and realized thus the minimizing of particle on product wafer and the productive rate of raising semiconductor device.
Can comprise the effective any material of the deposition relevant with ionization to removing at least in part this implanted ions system according to the present invention for the gas phase reactive material or the purge gas that clean.
The present invention has also considered to use gas phase reactive material to remove the deposition relevant with ionization from undesirable position by suitably controlling reaction, and/or at the long-pending material in the Shen, position of hope.In special execution mode of the present invention, tungsten has formed the material through removing as undesirable deposition, and in other execution mode, and amass on the surface of benefiting from its existence in tungsten Shen, ground that is supposed to.One gas (for example XeF of the tungsten fluoride intermediate product therefore, forming reactively
2, GeF
4, SiF
4, BF
3, AsF
5, AsF
3, PF
5, and/or PF
3) can be used in control of the present invention and cleaning method.In addition, such as WF of multiple tungsten fluoride gas
6, WF
5, and/or WF
4can be directly used in control of the present invention and cleaning method.Thereby gas phase reactive material of the present invention includes, but are not limited to XeF
2, GeF
4, SiF
4, BF
3, AsF
5, AsF
3, PF
5, PF
3, F
2, TaF
3, TaF
5, WF
6, WF
5, and/or WF
4.
In different special execution modes, this gas phase reactive material can be used jointly with volatile one " the cleaning reinforcing agent " or " coreagent " that increase this gas phase reactive material, causes removing than the more deposition of gas phase reactive material of use nothing cleaning reinforcing agent or coreagent.For example, use XeF
2removing iridium deposition can be by Lewis's (Lewis) alkali and using of electronics feedback key class and strengthen jointly.In specific application, can use carbon monoxide, trifluoro phosphine, and trialkyl phosphine class.
As an other example, in an implanted ions system, wherein feed gas is ionized to continuous electricity slurry in an arc chamber with tungsten wall, on these walls, on one side a filament is installed and another side is provided with a repellel and they separate by ceramic insulator and these walls, the parts of this arc chamber may be fed the catabolite of gas, element and the carbon contamination of arc chamber.
In this case, be useful on a cleaning agent (for example XeF that removes the metal pollutant (for example tungsten) that forms volatile fluoride
2) can combine with an oxygenated additive, this oxygenated additive is by pollutant carbon is transformed into CO, CO
2, and/or COF
2and effectively removed.The oxygenated additive component that is useful on this object includes but not limited to NO, N in special execution mode of the present invention
2o, NO
2, CO
2and/or O
2.
Therefore the present invention has considered to comprise a cleaning agent that effectively removes a metal pollutant (forming the fluoride compound of a volatility (gaseous state) of this metal by reaction) and both cleaning combinations of a cleaning agent that effectively remove carbon contamination thing (by formed volatile oxide or an oxyfluoride by it).These cleaning reagents can side by side or sequentially flow in this arc chamber.
In one embodiment, these reagent flow in this arc chamber under the condition of ionization simultaneously, and these cleaning agents have all carried out ionization to the pollutant of metal and carbon is transformed into from this chamber by the volatile compound that its machinery suction is easily removed like this.
The condition that can make this gas phase reactive material react with deposition can comprise the conditions such as any suitable temperature, pressure, flow velocity, composition, under these conditions, this gas phase reactive material contacts with pollutant and chemically interacts and for example, removes this type of material to (be subject to the surface of the implanter equipment of the long-pending material contamination in institute Shen) from this substrate.
The example of operable different condition includes but not limited to ambient temperature, exceedes the temperature of ambient temperature, exists electricity slurry, there is no electricity slurry, lower than atmospheric pressure, atmospheric pressure and superatmospheric pressure.
The exact temperature that removes deposition for the contact of gas phase reactive material can be from the scope of about 0 DEG C to about 2000 DEG C at different execution modes.Contact can comprise this gas phase reactive material in a carrier gas or with a pure form or with the mixture of other cleaning agent, a dopant etc. in send.This gas phase reactive material can heat to carry out chemical reaction with deposition at ambient temperature, to improve kinetics.
Reacting between this gas phase reactive material and pollutant deposition can monitor and/or regulate by the response characteristic based on changing between cleaning agent and pollutant.This type of response characteristic can comprise the existence of pressure, time, temperature, concentration, a concrete material, the speed of pressure change, the speed that (a concrete kind) concentration changes, change of electric current etc.Therefore, stop to introducing the realization that this gas phase reactive material can be based on a predetermined response characteristic in system, for example the predetermined voltage in vacuum chamber, tided over one predetermined time an amount or predetermined temperature, existence, product in this system or other material or the realization of a predetermined current condition in this monitoring operates of concentration, a concrete accessory substance of a concrete element in this system.
Tungsten deposition can be caused with the reacting of arc chamber of an implanter system by feed gas.Can depend on the temperature gradient of this system and/or flow to and via the electric current of filament and/or any other characteristic of effectively determining and can monitor for the method for cleaning this type of deposition.
For example, can at one first temperature, react with this arc chamber from the fluorine of feed material, form WF by following reaction (1) or (2)
6:
3F
2(g)+W(s)→WF
6(g) (1)
6F(g)+W(s)→WF
6(g) (2)
Can also there is reacting between the tungsten material of purge gas and this arc chamber, for example:
3XeF
2+W→3Xe+WF
6 (3)
Alternatively, WF
6(or WF
5or WF
4) can directly offer this system.
Then the tungsten fluoride once forming in this system or otherwise exist can move to the another location of this system.Depend on the temperature of other position, this tungsten fluoride can be at the long-pending tungsten of this position etching or Shen.On this filament, temperature is by the actual current flux depending primarily on by it.Temperature in other position of this arc chamber can change, and this depends on the design, heater current of concrete position and arc chamber, together with other non-heater current.
If the second place ties up to high temperature, tungsten fluoride decomposes, and tungsten is amassed by Shen and fluorine is released, as long as tungsten fluoride exists, the size of tungsten deposition will be grown.The long-pending reaction in Shen can comprise following reaction (4), (5) and/or (6):
WF
6→W+3F
2 (4)
2WF
5→2W+5F
2 (5)
WF
4→W+2F
2 (6)
On the contrary, if the second place ties up to moderate temperature, tungsten fluoride can this position of etching, removes tungsten and in product, retains fluorine, and etched like this position dwindles along with etched carrying out.This etching reaction can comprise following reaction (7), (8) and/or (9):
WF
6(g)+2W(s)→3WF
2(g) (7)
2WF
6(g)+W(s)→3WF
4(g) (8)
5WF
6(g)+W(s)→6WF
5(g) (9)
Therefore,, for removing of tungsten deposition, can select with the temperature of the parts of deposition so that the speed removing and scope maximize.
In other execution mode of the present invention, in arc chamber, boron and/or molybdenum deposition remove in a corresponding mode.
Cleaning agent can be undertaken by the variation of monitoring pressure in contact process with contacting of processing equipment in the method for the invention, and in the time that pressure is changed to zero, contact stops.
Alternatively, this contact can be by this gas phase reactive material of monitoring or the reactant that obtains thus, or the dividing potential drop of the product producing in this contact and carrying out, and when this dividing potential drop reaches a predetermined value, that is, when a terminal, this contact stops.For example, this kind of endpoint monitoring can use a suitable endpoint monitoring device to carry out, for example, at U.S. Patent number 6,534,007 and Application No.: 10/273,036,10/784,606,10/784, the endpoint monitoring device of a type of describing more comprehensively in 750 and 10/758,825, or a thermoelectric pile infrared (TPIR) or other Infrared Detectors.
In another embodiment, this contact can be used the parts of this processing change system to be undertaken by check the flowing of gas phase reactive material, and these parts allow regulate the dividing potential drop of gas phase reactive material and therefore control reaction rate.
In another execution mode, carry out this cleaning operation by the Continuous Flow of the gas reaction material of a predetermined flow velocity.
As discussed about reaction (1)-(9) hereinbefore, the deposition of the tungsten relevant with ionization can carry out Shen and amasss and to moderate temperature, carry out etching at low temperature at very high temperature.In this regard, the deposition relevant with ionization means owing to electricity slurry but the deposition that may not form owing to the operation of ion.Therefore,, as long as still there is enough surfaces of heat, the Shen of tungsten is long-pending also can for example, be occurred in the situation that there is no electricity slurry (, not having ion).In Shen, long-pending or etched position is the filament of implanter system, and temperature and current flux system are directly related each other.When this filament is during through etching, filament can attenuate and the resistance of electric current can be increased along with the reducing of cross section of this filament, can reduce like this by the current flow of this filament.If the condition of this filament has promoted the Shen on it long-pending, can be along with Shen is constantly long-pending and reduce to the resistance of electric current, because the cross section of this filament increases and filament chap, the current flow of correspondingly wherein passing through has also had increase.
In another aspect, the present invention system about monitoring the Shen on the filament of source long-pending and due to the method for filament growth, be by the current flow of this filament about monitoring.Because long-pending due to Shen, the cross section of filament has increased, so can reduce and electric current can increase to keep the electricity of this filament in being supported in arc chamber to starch needed temperature the resistance of electric current.Therefore one of the electric current increase monitoring can be used for representing the needs to filament cleaning.
In an other aspect, the present invention system is about being monitored the etching of this filament or cleaned etching method by the current flow of filament by monitoring.Because due to etching, sputter or evaporation, filament cross section reduces, can increase and electric current can reduce to keep the electricity of this filament in being supported in arc chamber to starch needed temperature the resistance of electric current.Therefore one of this electric current monitor reduce can be used for representing additional material Shen to amass needs that are subject on etched filament, or stop cleaning or the needs of ionization process.
Another embodiment of the present invention comprises that the electric current based on crossing this filament as the above monitoring stream describing in detail controls the method for the state of this filament.
In one embodiment, an instruction that reduces to provide the approaching fracture of filament of the heater current of being monitored, as response, one gas phase reactive material flow in this system (for example, when in the time clashing into electricity slurry, or alternately, make electricity slurry close but filament remain heat (for example,~2000 DEG C)), produce the Shen long-pending reaction of metal on this filament to bring out, for example, from the tungsten of this arc chamber walls.This reaction can allow to proceed to until this electric current in a preset range of this implanted ions system of valid function, indicate this filament " regrowth " to a gratifying degree.
In another embodiment, the increase of the heater current of monitoring provides an instruction, that is: because the long-pending filament in Shen of material is grown.As response, allow after cooling one period of predetermined time of this filament, or to a predetermined temperature (it can be for example from room temperature in the scope up to approximately 2000 DEG C) afterwards, this gas phase reactive material flows into this system, like this, filament is cooled to is enough to allow this filament of etching.After this, can be allowed thereafter to proceed to until electric current in a preset range of this implanted ions system of valid function, indicates this filament to taper to a suitable degree as the etching reaction subsequently of media by this gas phase reactive material.
Therefore method of the present invention can be enough at least in part to remove from this substrate the time of deposition and removes a deposition from this substrate by a substrate is contacted with a gas phase reactive material, this deposition comprise boron, silicon, arsenic, phosphorus, germanium, tungsten, molybdenum, selenium, antimony, indium, tantalum and carbon one of at least.Gas phase reactive material for this object can comprise one or more following material: XeF
2, XeF
4, XeF
6, GeF
4, SiF
4, BF
3, AsF
5, AsF
3, PF
5, PF
3, F
2, TaF
3, TaF
5, WF
6, WF
5, WF
4, NF
3, IF
5, IF
7, KrF
2, SF
6, C
2f
6, CF
4, Cl
2, HCl, ClF
3, ClO
2, N
2f
4, N
2f
2, N
3f, NFH
2, NH
2f, HOBr, Br
2, BrF
3, C
3f
8, C
4f
8, C
5f
8, CHF
3, CH
2f
2, CH
3f, COF
2, HF, C
2hF
5, C
2h
2f
4, C
2h
3f
3, C
2h
4f
2, C
2h
5f, C
3f
6, COCl
2, CCl
4, CHCl
3, CH
2cl
2, and CH
3cl.
In the operation of the present invention, the xenon compound of fluoridizing can be used as cleaning agent and electric slurry source reagent, and can comprise the fluorine atom of any suitable number.With respect to lower F/Xe compound, the ratio that F is higher with one of Xe enables relatively to clean sooner and more effectively.Higher steam pressure has improved the delivery rate of cleaning agent and has enabled to send more material.
In one embodiment of the present invention, xenon hexafluoride is used as a cleaning agent or electric slurry source reagent.Although XeF
6steam pressure at room temperature than XeF
2steam pressure approximately high seven times, XeF
6, and XeF
4, be very easily to react with water.Xe F
6the most advantageously not being to use in about the existence of water, hydro carbons, hydrogen or reducing agent or the cleaning environment of generation.But, in the time that use has the cleaning compound of low vapor pressure more, may need to adjust circulation circuit to avoid in circulation path unsuitable pressure drop and keep the suitable high delivery rate of cleaning agent.
The device of implementing method of the present invention can form in any suitable manner and arrange, to provide gas phase reactive material to this cleaning.
In one embodiment, the invention provides an implanted ions and clean assembly, comprise: (i) implanted ions system, this system comprises one or more parts, in the process of the implanted ions processing of this system, on these parts, accumulation has the deposition relevant with ionization, (ii) one clean assembly, comprise the cleaning combination source containing a cleaning combination, this cleaning combination comprises a gas phase reactive material, for example a kind of halide compound, this halide compound and deposition are reactive and under cleaning condition, at least in part remove deposition from one or more parts to realize, this cleaning condition comprises contacting of this cleaning combination and deposition, (iii) circulation circuit, it is suitable for cleaning combination to be sent to from cleaning combination source one or more and is used for the parts that contact with it under cleaning condition, and (iv) flow component, the Cleaning Process composition that it is suitable for being controlled at cleaning state flows by this circulation circuit, from one or more parts, remove at least in part deposition to realize.
Flow component in above-mentioned assembly can be any suitable type, for example comprise valve, valve actuator, flow restricter, adjuster, pump, mass flow controller, pressure gauge, residual gas analyser, CPU, barrier film, etc.This type of flow component system adaptive to work under used concrete cleaning condition.
One or more parts (in the implanted ions processing procedure of these parts in this system, accumulation has the deposition relevant with ionization thereon) in implanter device can be any suitable types, for example, vacuum chamber, arc chamber, electrode, filament, bushing, electromagnetic waveguide, wafer-process parts, clamp ring, wheel, dish, etc.In one embodiment, these parts are a vacuum chamber or parts with which.
Cleaning combination source can comprise a material storage that contains this cleaning combination and distribute external member.This material storage and distribution external member comprise a container, and this container can be for example, to define the columniform container of being as general as of its inner volume.In a special execution mode, this cleaning combination can be that solid and this cleaning combination can be supported on the surf zone strengthening in this container under the condition of ambient temperature.The surf zone of this enhancing can comprise structure wherein, for example pallet, as at U.S. Patent number 6,921, described in 062, or porous inertia foams, for example be subject to anodized aluminium, stainless steel, nickel, bronze etc., consistent evaporation rate of this cleaning material to be provided and and then to provide and be enough to carry out the distribution of relevant cleaning process and the steam pressure of ionization steps.In the situation that utilizing pallet, in batch operation, cleaning combination can be subject to the support of some tray surfaces, and these pallets have relative flow channel pipe, upwards flow into its distribution openings for steam at this container.
Circulation circuit in above-mentioned equipment arrangement adapts to this cleaning combination is sent to arc chamber from this cleaning combination source under cleaning condition.This adaptation can be the different qualities based on cleaning combination.For example, in the time that this cleaning combination has a low steam pressure, can avoid the unnecessary pressure drop in circulation path with high conduction.Maximizing conductance and minimizing the method for compressing that circulates is well-known in this area.
In all cleaning methods of the present invention, thereby can optionally clean with other method and device the life-span that extends implanted ions system (particularly ion source).The method of this type of life-saving can comprise that change one implanted ions system is to adapt to concrete substrate, long-pending material and/or the gas phase reactive material in Shen.The change of system and device can include but not limited to provide the following: the extractor electrode with active thermal control system; Reduce the extractor electrode (actively heated extraction electrode) of the active heating of the frequency/generation of electric discharge; The extractor electrode that comprises the preferred aluminium of metal, molybdenum or aluminium oxide (Al2O3); Long-range electric slurry source; Extractor electrode is associated with heater; Extractor electrode is associated with cooling device; Smooth undistinguishable (featureless) extractor electrode; Electricity slurry chamber, these electricity slurry chambers receive many source gas through being arranged to, and these source gases can be decomposed to produce by a fluid stream of the outlet of this chamber and the reactant gas of conduit, to this reactive gas is delivered to ionization chamber by electricity slurry; Hygrosensor, these hygrosensors are through being designed to the substantial end of the gas of detection reaction and the exothermic reaction in the lip-deep pollution for the treatment of system; The protection (for example, providing the gear that resists this type of material to protect thing around to the parts of gas phase reactive material susceptible) of the parts of the infringement that is subject to gas phase reactive material in this processing equipment; And/or the use of the system unit that comprises aluminium or aluminium oxide.
The method that extends the life-span of processing equipment can include but not limited to: extractor electrode is carried out to initiatively heating to reduce frequency and the generation of electric discharge; Heating extractor electrode higher than being delivered on the condensing temperature of ionogenic source material; Control on one's own initiative the temperature (for example carrying out combined heated or cooling this electrode with a heating or cooling ion source) of the ionogenic extractor electrode that is suitable for used particular type; And/or in extraction process, keep this extractor electrode under high temperature.The change of this type of additional device and method U.S. Patent Application Publication No. 2006/0272776 and 2006/0272775 and International Patent Publication No. W WO 05/059942 in carried out more fully describing, it is incorporated to herein in full by reference.
In a special execution mode, this implanted ions system comprises an arc chamber and a dopant source, and wherein this dopant source can comprise for example BF
3, XeF
2, AsH
3, PH
3, GeF
4, SiF
4, H
2se, AsF
5, AsF
3, PF
5, PF
3or other boron, silicon, arsenic, phosphorus or germanic dopant source.
In another embodiment, the present invention system is about the method for an implanted ions, the method is included in the arc chamber of an implanted ions system by a dopant source γ-ray emission one electricity slurry, this dopant source gas flow is the dopant source ion to be formed for implanting by this arc chamber, wherein pass through in the process of at least a portion time in the process of this arc chamber in this dopant source gas flow, gas phase reactive material and dopant source gas flow through this arc chamber concurrently, to realize the cleaning in this implanted ions system.
Generally, although what dopant source gas and gas phase reactive material can walk abreast flows to realize situ cleaning, but preferably carry out cleaning operation in a mode in succession typically, for example, when this ion source produces one first electricity slurry from one first dopant source, and when this ion source produces one second electricity slurry from one second dopant source subsequently, use a cleaning step of getting involved, wherein gas phase reactive material flows through this ion source, is with or without electricity slurry and generates.
In one embodiment, the invention provides the method for the silicon substrate that forms a doping, the method comprises in Xe+ implanted ions one silicon substrate, and in this silicon substrate, implants dopant ion after this.In this process, implant the crystal structure of Xe+ ion for this substrate of amorphization (amorphize).
For example, at the xenon of the fluoridizing electricity slurry (XeF for cleaning
2electricity slurry) generation in, Xe+ ion can carry out the low energy sputter cleaning in some sources itself.After extraction, Xe+ ion can carry out ion source components downstream, some high energy sputters of for example vacuum wall, ion optics, wafer disks and wafer support.
Similarly, using tungsten fluoride kind, for example WF
6, WF
5, and/or WF
4situation under, free fluoride can ion source component sputter cleaning, different and/or tungsten can amass on ionogenic different parts in Shen.Depend on the temperature of all parts in system in the behavior of cleaning and Shen occurs between long-pending.
The present invention is method and the device about the ion source region of the cleaning one implanted ions system using in the manufacture of a microelectronic device in different aspect systems.This ion source region can comprise the negative electrode source of a for example indirect, a freeman (Freeman) source or a Claude Bernard (Bernas) source.
The present invention be in one embodiment about from Ion Implantation Equipment and wherein contained parts by this vacuum chamber and/or parts are contacted under time enough and enough conditions with a gas phase reactive halide compositions original position removal of residue so that removal of residue from this vacuum chamber and/or parts at least in part, and be about completing by such mode, , in the time that residue is different from the material that forms vacuum chamber and/or parts, this gas phase reactive material optionally reacts with residue and reacts and (for example substantially do not react with the formation vacuum chamber of Ion Implantation Equipment and/or the material minimally of parts, and preferably do not react completely), and in the time that residue is identical with the material that forms vacuum chamber and/or parts, gas phase reactive material can be to be all reactive with residue and vacuum chamber and/or parts.
As used herein, being applied to this gas phase reactive halide and reactive term " optionally " of a residue is for being described in preferential the reacting between this gas phase reactive halide and a residue.Although keep not reacting in fact with the formation vacuum chamber of Ion Implantation Equipment and/or the material of parts, if this vacuum chamber and/or parts comprise and the same or analogous element of those residues itself, gas phase reactive halide can react with the formation vacuum chamber of Ion Implantation Equipment and/or some material of parts.For example, in the time optionally reacting and removed with the tungsten deposition from parts, this gas phase reactive material may also react with the tungsten in parts itself.For the generation of this coreaction, residue and parts needn't be accurately identical materials, but can comprise some common materials.
In another embodiment, Ion Implantation Equipment parts clean in an independent special chamber (parts move into wherein from an Ion Implantation Equipment) with offing normal.
Consider in further detail situ cleaning, this kind of cleaning depends primarily on following three factors: clean reactive character of precursor, the volatility of cleaning reaction accessory substance, and the reaction condition using in chemical cleaning.This cleaning combination must remove the wearing and tearing of the material of unnecessary residue simultaneous minimization formation Ion Implantation Equipment.The accessory substance producing by cleaning reaction must be enough volatile to facilitate removing of they by vacuum system or other the aspirator of Ion Implantation Equipment.
The cleaning of the residue forming for the material identical with one or more parts of Ion Implantation Equipment can cause some wearing and tearing of parts itself.Exactly, use XeF
2utilize and the system of tungsten arc chamber, remove tungsten deposition and can cause removing from some tungsten of the inside of arc chamber from one as a cleaning agent.But for system effectiveness is maximized, the loss of some internal material of angle (if this system is not cleaned and allow tungsten deposition to be accumulated in this system) arc chamber reducing from systematic function is not very critical.
This gas phase reactive material can comprise for example a kind of xenon compound steam of fluoridizing, for example XeF
2steam.XeF
2be a preferred reactive halide gas, and at room temperature can distil, but can use a heater to heat to increase rate of sublimation.Known XeF
2be an effective silicon etchant and microelectromechanical systems (MEMS) device process in be used as a silicon selective etch agent.Exactly, XeF
2react below with silicon basis.
2XeF
2(g)+Si(s)→2Xe(g)+SiF
4(g)(10)
This silicon/XeF
2reaction can activate and occur, that is, and not electricity consumption slurry or thermic heating.XeF
2with the reaction rate of Si far above XeF
2with SiO
2reaction rate, make XeF
2optionally react with Si.
XeF
2or other xenon compound of fluoridizing as the etchant for metal boron usefully for operation of the present invention.Although be not wishing to be bound by theory, think that boron is etched according to following reaction (11):
3XeF
2(g)+2B(s)→3Xe(g)+2BF
3(g)(11)
The present invention considers to use XeF2 as the etchant for arsenic, phosphorus and germanium, and can be about following reaction:
5XeF
2(g)+2As(s)→5Xe(g)+2AsF
5(g)(12)
5XeF
2(g)+2P(s)→5Xe(g)+2PF
5(g) (13)
2XeF
2(g)+Ge(s)→2Xe(g)+GeF
4(g) (14)
This type of reaction can be used or do not use high energy activation and carry out.
In the time that residual material is different from those materials, method of the present invention and device are used for the parts removal of residue from Ion Implantation Equipment at least in part, for example, remove at least 25%, more preferably at least 50% and most preferably at least 75% this kind of residue, and complete by such mode: with regard to forming the material of Ion Implantation Equipment parts, such as aluminium, tungsten, molybdenum, graphite, insulating material, sealant material etc., optionally remove residue.
In the time that residue and the material of component parts are identical material, wish the residue removing of similarity degree, keep material removing in low degree from parts, for example, in the scope of micron or tens of microns, to affect indistinctively the performance of parts simultaneously.In addition, because generally not having uniform thickness or Shen, amasss deposition, they can have more reactivity than the material of parts itself in cleaning process, and this gas phase reactive material compositions is than reacting with this residue with reacting more optionally of parts part like this.
Can adopt several forms gas phase reactive material compositions to be delivered to the ion source region that may carry out situ cleaning, comprise an immobilising mode, a continuous mode and a mode of directly introducing.This type of cleaning way is more fully described in international publication WO 07/127865, together with the device and the methodology that effectively use in the operation of the present invention.The disclosure content of international publication WO 07/127865 is combined in this as a whole by quoting.Although described use XeF in conjunction with different execution modes of the present invention at this
2as a cleaning combination, but it should be understood that and can use other compound of fluoridizing, for example WF
6, WF
5, and/or WF
4, substitute or in conjunction with XeF
2, maybe can use other and the extra compound of fluoridizing.For example can use BrF
3carry out etch tungsten and do not need electricity slurry.In another aspect, the present invention system is about the performance of an implanted ions system of improvement use solid dopant material and the method that extends its life-span, and the method comprises use XeF
2or N
2f
4as a carrier gas of described solid dopant material.This solid dopant material includes, but are not limited to element arsenic, phosphorus, selenium, antimony, SbF
3, InCl, SeO
2, Sb
2o
3and InCl
3.As considered in the present invention, use XeF
2or N
2f
4as Sb
2o
3, InCl
3or a carrier gas of other solid dopant material removed this chamber, source with and parts on long-pending Sb, In and other dopant in institute Shen.Even if switching to boron after Sb implants, this instantaneous method also there is effectiveness.At least double by the advantage of this method gained: first, it provides real-time source to clean to prevent or reduced dopant and has been accumulated on this source housing and parts thereof, has therefore improved Ion source characteristics and has extended the ionogenic life-span simultaneously; The second, it strengthens and/or has stablized electric slurry and/or beam electronic current.
In another aspect, the present invention system is about the performance of an implanted ions system of improvement use gaseous state dopant material and the method that extends its life-span, and the method comprises uses XeF
2or N
2f
4as with the body of gas in the lump of described gas doping material.This gaseous state dopant material includes, but are not limited to GeH
4and BF
3.As considered in the present invention, use XeF
2or N
2f
4as with GeH
4or the body of gas in the lump of other gaseous state dopant material removed Ji Yuan chamber, Shen with and parts on Ge or other dopant.The advantage obtaining by this operation of the present invention is at least double: first, it provides real-time source to clean to stop or reduced dopant and has been accumulated on this source housing and parts thereof, has therefore improved Ion source characteristics and has extended ion source life; The second, it strengthens and/or has stablized electric slurry and/or beam electronic current.
In another aspect, the present invention system about a fore line of the implanted ions system of cleaning to remove the method for relevant with ionization deposition herein, comprise the fore line of an implanted ions system is contacted under following reaction condition with a purge gas, wherein said purge gas and this deposition have chemical reactivity and wherein remove at least in part to realize.Deposition includes, but are not limited to comprise B, Ge, Si, P and As, or those materials of their mixture.This purge gas includes but not limited to XeF
2, N
2f
4, F
2and be reactive material that other is fluoridized with a deposition of aforementioned formation.As have the knack of this operator and understand, the amount of needed purge gas depends on the amount of the deposition of existence.The hot amount discharging in the process of reacting with deposition at purge gas similarly, depends on the flow velocity of purge gas.The identification of the accessory substance kind producing from cleaning process and concentration depend on that the flow velocity of purge gas, the associativity of deposition form and pump purging flow velocity.Only for the object of non-limitative illustration, below to using XeF
2an example that cleans phosphorus from a fore line describes:
Be used for determining at the needed XeF of cleaning process
2the chemical reaction system of amount: 5XeF
2(g)+2P (s) → 5Xe (g)+2PF
5(g).Forming enthalpy (with kJ/mol) takes from Lange ' s Handbook of Chemistry (14th ed) and lists the heat being discharged in course of reaction for determining: XeF at this
2(164); Xe (0); P (0); And PF
5(1594.4).XeF
2flow velocity determined the required time of cleaning process length together with discharged heat.Heating XeF is not provided
2the means of gas cylinder, maximum lasting flow velocity is about 50sccm, supposes and has enough pipeline conductivities of sending.If by using a heating jacket to keep this gas cylinder at room temperature, flow velocity can be increased to 100sccm or larger.Clean the required XeF of phosphorus deposition
2amount shown in table 1, and the hot amount discharging in this cleaning reaction process is shown in table 2.
Table 1
The quality (g) of phosphorus deposition |
Required XeF
2Amount (g)
|
10 |
137 |
Table 2
XeF
2Flow velocity (sccm)
|
Produce hot speed (watt) |
50 |
17.6 |
100 |
35 |
200 |
70 |
Produce speed shown in table 3 from the maximum of the different accessory substances in above-mentioned cleaning reaction.
As have the knack of this operator and understand, because the composition of residue may be different, be therefore based on following hypothesis in the data shown in table 3: the composition that it is that element that the amount system of accessory substance is defined as for every kind of element supposition 100% forms.In addition, the Cmax of these materials depends on the dilution flow rate in gas extraction system.For example,, if roughing pump has the nitrogen purge of a 10slpm, just at the downstream of this pump, PF
3maximum stable state concentration be 3330ppm.If XeF
2flow velocity be greater than 50sccm, this value can increase.
In an execution mode of said method, this purge gas flows into this implant source chamber, and turbine pump cuts out and roughing pump is opened.This operation has strengthened the flow velocity through the purge gas of the deposition top of fore line, and therefore a cleaning process is faster provided.The speed of cleaned gas stream can be further by making therein this purge gas be stored in room temperature or this more than room temperature gas cylinder heats.Preferably in this operation, the delivery line from gas cylinder to Ion Implantation Equipment is heated similarly.
In another execution mode of said method, this purge gas flows in this implant source chamber in a stream of pulses mode, wherein this implant source chamber, this pump and fore line is charged to a certain pressure and is then extracted into lower pressure.Repeat this process until remove the deposition on the fore line of implanted ions system.This operation is preferably used the isolating valve in the import of this roughing pump.
In a preferred operation, above-mentioned execution mode further comprises making therein this purge gas be stored in room temperature or this more than room temperature gas cylinder heats.
For all execution modes, the method is preferably further included in a Drechsel system in the outlet of this roughing pump to remove produced volatile byproducts from cleaning process.
Each execution mode preferably further comprises as from Air Products and Chemicals, Inc. (the U.S., Pennsylvania) a commercially available Xe recovery system, and be described in http://www.fabtech.org/product_briefings/_a/new_product_air_pro ducts_offers_on_site_xenon_recovery., in, it is incorporated herein.
Another execution mode that cleans the method for a fore line of an implanted ions system is included in the fore line that a turbine pump downstream provides this purge gas and described purge gas flow through continuously to this implanted ions system.The continuous flow of described purge gas can directly enter the region between pressure vessel, pressure vessel and source turbine pump, or the downstream of source turbine pump.The deposition (even in the time that this implantation process carries out) on fore line is preferably cleaned in this operation, reduces thus the interruption of implanted ions operation.
In the above-described embodiment, this purgative gas is preferably stored in a gas cylinder; The method preferably further comprises making therein this purge gas be stored in room temperature or this more than room temperature gas cylinder heats.
Above-mentioned execution mode is preferably further included in this low vacuum delivery side of pump and provides a Drechsel system to remove produced volatile byproducts from this cleaning process.
Above-mentioned execution mode further comprises to be provided just like from Air Products and Chemicals, Inc. (the U.S., continent, Pennsylvania) commercially available Xe recovery system, and be described in http://www.fabtech.org/product_briefings/_a/new_product_air_pro ducts_offers_on_site_xenon_recovery., in, it is incorporated herein.
In another aspect, the present invention system has the performance of an implanted ions system of a negative electrode and the method that extends its life-span about improvement, the method comprises this negative electrode is contacted with the admixture of gas being made up of the long-pending gas at least one purge gas and at least one Shen, wherein said admixture of gas balance this material of the Shen Jiyu of material on this negative electrode or other material peeling off from this negative electrode.The purge gas of admixture of gas has removed Shen and has amassed dopant material on this negative electrode and the material of negative electrode, and the long-pending gas in the Shen of admixture of gas causes that dopant material Shen amasss on this negative electrode directly or indirectly.This admixture of gas has kept the balance between peeling off of the accumulation of dopant material on this negative electrode and it or other material, and has therefore extended the ionogenic life-span.To understand not only dopant material can amass or etching through Shen, and the material of arc chamber walls (for example, W or Mo) can amass or etching through Shen.Purge gas directly (via sputter or chemical etching) or indirectly (via the chemical deaeration of tungsten fluoride/molybdenum fluoride) prevent that Shen is long-pending or reduce rate of deposition.The long-pending gas in Shen is via halogen cycle (W or Mo from the fluorine etching of gas from cooling wall, and then W or Mo are decomposed on very hot negative electrode), or by negative electrode practically Shen amass dopant molecule/atom (for example,, from BF
3b) and cause Shen on negative electrode long-pending, and a similar mechanism is applied to the ionogenic filament of Claude Bernard.For the long-pending situation in dopant Shen in other sensitive compressible members of insulator or arc chamber, purge gas tends to the dopant deposition of chemical etching through forming, or first purge gas can amass to stop or to minimize Shen with the long-pending gas reaction in Shen before dopant Shen is long-pending.Can how to stop Shen long-pending with example explanation purge gas in the first situation: gas GeH is amassed in Shen
4can make Ge deposition be formed on negative electrode, insulator or other parts.If purge gas is XeF
2, its can with GeH
4reaction is to form the GeF that has more volatile at least one tittle than Ge
2and/or GeF
4, and therefore can remove from source region via suction.In addition, any one or both of the long-pending gas in Shen and purge gas can be also dopant gas.The storage of this admixture of gas in ion source implanter and distribute can be by completing with the following: an absorption-desorption device (being called as SDS-safe delivery source), it is described in U.S. Patent number 5, in 518,528, and its content is incorporated to herein by quoting; One fluid storage and the distribution system (being called as the vacuum actuated gas cylinder of VAC) comprising for keeping the container of a fluid under a desirable pressure is described in U.S. Patent number 6,101, and in 816, and its content is incorporated to herein by quoting; Or fluid-mixing storage and the distribution system (being called as VAC-Sorb) of SDS and a VAC, it is described in U.S. Patent number 6,089, in 027 and its content be incorporated to herein by quoting.These fluid storage and distribution system provide gas lower than sending under atmospheric pressure, and more safer and more effective than high-pressure fluid storage and distribution system thus.In addition, some gases in this admixture of gas can be stored together and distribute in SDS, VAC or VAC-Sorb system, and the coexistence system of these gases in high-pressure fluid storage and distribution system is incompatible.
In an execution mode of above method, the multiple gases of admixture of gas side by side flows to contact this negative electrode or be subject to long-pending other sensitive compressible members affecting in Shen.
In another execution mode of above method, the multiple gases of admixture of gas sequentially flows to contact this negative electrode or be subject to long-pending other sensitive compressible members affecting in Shen.
In another execution mode of above method, the combination that admixture of gas comprises at least one hydrogen-containing gas and at least one fluoro-gas, wherein this hydrogen-containing gas as purge gas and this fluoro-gas as the long-pending gas in Shen.
In another execution mode of above method, the combination that this admixture of gas comprises at least one non-impurity gas (not containing the gas of As, P, Ge, B, Si or C) and at least one impurity gas, wherein this non-impurity gas as purge gas and this impurity gas as the long-pending gas in Shen.
The example of purge gas is but is not limited to Xe/H
2, Ar/H
2, Ne/H
2, Xe/NH
3, Ar/NH
3, Ne/NH
3, Ar/Xe and Ar/Xe/H
2.
(but being not limited to): the F of example system of the long-pending gas in Shen
2, N
2f
4, ClF
3, WF
6, MoF
6, GeF
4and NF
3.
(but being not limited to): the AsH of example system of admixture of gas
3/ AsF
3, AsH
3/ AsF
5, PH
3/ PF
3, PH
3/ PF
5, SiH
4/ SiF
4, H
2/ Xe/SiF
4, GeH
4/ GeF
4, H
2/ Xe/GeF
4, H
2/ GeF
4, B
2h
6/ BF
3, H
2/ BF
3, F
2/ BF
3, CO
2/ F
2, CO
2/ CF
4, CO/F
2, CO/CF
4, COF
2/ F
2, COF
2/ CH
4, COF
2/ H
2.
Feature of the present invention and advantage more fully illustrate by following nonrestrictive example.
Example 1
This example shows improvement on ion source life and the utilization of implanter, and this can realize by removing deposition with a chemical.Preferably, remove deposition with regular interval so that the pollutant thin slice in prevention implanter and the accumulation of conductive membranes.
Situ cleaning system is by the XeF that is certainly arranged in the gas cabinet of Ion Implantation Equipment with regular interval
2supply container introduce XeF
2carry out, wherein XeF
2clean steam to introduce in this ion source each 10-15 minute of twice of every day.Test to assess the flowing dynamics of this cleaning reagent with a high electric current implanter.Determine XeF
2cleaning characteristics and confirmed that this cleaning agent does not have adverse influence to the beam current tube parts of implanter.So, use XeF
2the cleaning process of reagent is for using and be associated lattice in the moderate electric current implanter device.
Fig. 1 system is by this class moderate electric current implanter in position before the enforcement of cleaning process and a chart of the ion source life data that collected afterwards.These data systems develop for a doped compositions that comprises arsenic hydride and hydrogen phosphide.Before cleaning, be subject to the restriction of two kinds of common fault modes, this ion source has the average operation life-span of about 250 ± 90 hours.
Main fault mode system is from the excessive leakage of an inhibitor voltage source.In order successfully to extract a stabilizing ion bundle, inhibitor voltage is applied on an electrode that is positioned this arc chamber outside.This electrode carries out electricity isolation by multiple little insulators, and the accumulation of a conductive membranes on one or more in these insulators may cause that excessive inhibitor reveals.
One second pattern system of fault is attributable to the short circuit of parts in the arc chamber of thin slice of the long-pending material in institute Shen.
Find, these fault modes can minimize by the Process of Chemical Cleaning of original position.Regularly twice cleaning every day increased the life-span in source in production.
XeF
2the impact of the Leakage Current on inhibitor further illustrates in Fig. 2, and Fig. 2 system is for a chart of moderate electric current instrument Leakage Current before introducing situ cleaning operation and afterwards.Each data point is illustrated in the average inhibitor electric current in the process of the time that need to implant a wafer batch, and these points are along with several ionogenic life-spans mark and draw.The size of revealing depends on the elapsed time starting from the replacing of the insulator of last preventive maintenance.These data illustrate that regular situ cleaning greatly reduces Leakage Current, and it never reaches the upper control limit of 1.5mA like this, need a source without scheduling to safeguard at this point.
Also use and comprise BF
3and PH
3one implant doping and mix and assessed the effect of situ cleaning.This source under these conditions, operated 497 hours and under an electric arc restrictive condition (being about the tungsten on filament or boron deposition) there is fault, this is attributable to BF
3chemical property.Operation system is favourable about single source life-span and the history average long-term in same systems of 497 hours in pilot system compared with 299 hours.This is a single data point, but it is applicable to the model of setting up.In this case, the improvement of source service life looks it is owing to using XeF in this source arc chamber
2etching tungsten deposition.
The photo of Fig. 3 A and 3B provides the other evidence of cleaning agent effect.In two photos, after showing and approximately producing 98 days in each case, remove the outward appearance of ion pressure vessel after the ion source assembly of periodically preventive maintenance.For the photo in Fig. 3 A, carry out situ cleaning every day twice, and for the photo in Fig. 3 B, do not clean.
In the time not cleaning, there is the long-pending material in Shen of real mass, wherein some has started leafing and slabbing.In periodic maintenance activity, with manually cleaning and remove the long-pending material in Shen from the inner surface of shell.Look cleaner with this shell of situ cleaning, without spending the less time or not taking time and carry out Manual-cleaning.Deposition is by unreacted XeF
2flow out this arc chamber and pass on the wall of vacuum chamber and remove, and dopant and other deposition remove by chemical reaction.
Among this ion source and around deposition produce so-called " implanter memory effect ".In the time becoming another kind of from a dopant source gas and changing, after flowing into termination, this first impurity gas for a long time, continues extraction from this ion source electricity slurry from the ion of this first dopant element.This effect is causing in some cases the severe contamination of desirable ion beam current and is causing the deterioration of implantation process.
One example of this implanter memory effect ties up to a BF
2p in implantation pollutes.This pollution is so serious to the consequence system of process yields, so that numerous semiconductor production facilities is all being avoided the implantation scheduling of phosphorus and boron on same tool.Substantive obstacle when this ties up to scheduling implant procedure.P/BF
2pollution results from and uses PH
3the source of implantation in phosphorus deposition.When for BF
2 +implantation is replaced with BF
3when gas, some fluorine reactions have formed
31p
19f
+.
31p
19f
+quality be 50.This be enough to very much approach for
11b
19f
2desirable 49 quality, like this PF
+with BF
2 +ion is implanted altogether.Result system, BF
2 +implantation has been subject to having in extra fine quality-energy range the restriction of some high current system of MIN quality analytic ability.
Use from PH
3the P+ ion beam of impurity gas uses a high electric current implanter to operate about 200 hours to XeF in simulation is produced
2cleaning is assessed, to determine its impact on this implanter memory effect.This system switches to BF
3the BF2+ of gas and use one high dose (5 × 1015ions/cm2) directly implants an exposed silicon monitor wafer.At BF
2 +in the process of implanting, the parsing boring ratio of the analysis magnet of system opens to guarantee that polluting effect is enough large to using the routine of secondary ion mass spectroscopy (SIMS) analysis to measure conventionally largelyr.
BF
3, argon and XeF
2cleaning performance system by these 3 kinds of gases of operation each and then by using BF
2 +the amount that implantation monitor wafer is monitored residual contamination thing periodically compares.With BF
2the amount of the P implanting altogether measures by SIMS.In a typical SIMS spectrum of the phosphorus of implanting shown in Fig. 4 A, wherein the peak in phosphorus spectrum is corresponding to the PF from this ion source extraction
+the implantation depth of ion, and this dosage is corresponding at BF
2in an about pollution level of 3%PF.
Fig. 4 B system is used BF
3or XeF
2pollution level is as the figure of a function of scavenging period, and wherein this figure is from PH
3be transformed into BF
3normalization immediately afterwards (normalize) is to pollution level.As operation BF
3even PF is polluted also almost without impact after 2 hours when electricity slurry.In the time using argon electricity slurry, obtain similar result (not shown).By comparing, PF pollutes and is using XeF
2situ cleaning has only reduced twice after 15 minutes, and is using XeF
2situ cleaning reduced almost 5 times after 30 minutes.
Use before situ cleaning, this medium current implanter unit monthly every instrument is that average 3.3 sources are changed, and wherein average source Renewal process and conformity test subsequently need about 5 hours, is equivalent to the annual production time of every instrument lose nearly 200 hours.Source service life has doubled effectively by situ cleaning, has produced the extra production time of approximately 100 hours for each medium current instrument.The saving that test wafer produces, together with the saving (carrying out every year up to 40 conformity tests for each medium current implanter) of the required metrology tool of the reprocessing of production time and qualified wafer, has proved the validity of situ cleaning.
Example 2
This examples prove the control of filament growth in the ion source of an illustrative Ion Implantation Equipment system.
Fig. 5 A system shows XeF with regard to the heater current of increase and weight
2one chart of the effect that stream and arc power change.The figure shows the figure of filament weight (using gram) as the function of the operation elapsed time of implanter system (in hour).Line higher in this figure represents the XeF with 2.2 standard cubic centimeters per minute (sccm)
2the arc power operation of flow and 100 volts/0.05 ampere to this, has been determined the filament weight increases of one 319 milli Grams Per Hours after operation in 3 hours.In this figure, lower line has reflected the XeF of 0.5sccm
2flow and 40 volts/0.05 ampere arc power, this filament weight that has produced 63 milli Grams Per Hours in the lasting time of implementation of 3 hours increases.
Fig. 5 B shows XeF with regard to heater current
2one chart of the effect that flow and arc power change.The figure shows the figure of heater current (using ampere meter) as the function of the time of implementation of implanter system.Line higher in this figure represents the XeF with 2.2 standard cubic centimeters per minute (sccm)
2the arc power operation of flow and 100 volts/0.05 ampere, to this, increases at the heater current of having determined 16 amperes/hour.In figure, lower line has reflected the XeF of 0.5sccm
2the arc power of flow and 40 volts/0.05 ampere, this heater current that has produced 2.3 amperes/hour in the lasting time of implementation of 3 hours increases.
Fig. 6 is the chart of filament changes in weight (per hour using milligram) as a function of average heater current (with ampere meter).This figure uses for the heated filament utmost point condition of low discharge and high flow capacity and for the data under the electricity slurry condition of low discharge and high flow capacity and shows the effect that heat flow (without electricity slurry) and electric slurry condition transmit for tungsten.These data illustrate, the transmission of tungsten in system can be by selecting suitable treatment conditions optionally adjust to realize the long-pending or alternative etching in the Shen of material on filament.
Example 3
This example demonstrates the improvement in ion source life and implanter utilization that can realize by the supply of monitoring cathode bias power.
Fig. 7 be shown cathode bias power variation as the chart of a function of time and gas type.Exactly, work as GeF
4while flowing, halogen cycle is amassed on negative electrode W Shen, and it causes that substrate bias power increases (to keeping setting ion beam current).Work as PH
3while flowing, phosphonium ion sputtering cathode, causes the decline of cathode bias power.In this example, PH
3with GeF
4ratio system make substrate bias power finally about 76 hours after, arrive its maximum output.Monitor in this way this substrate bias power, and take suitable action can improve ion source life.
Fig. 8 has shown the chart of negative electrode W changes in weight as a function of substrate bias power.Exactly, use XeF
2as source gas, tungsten (W) can by simple change cathode bias power and from negative electrode etched or Shen amass in negative electrode.High substrate bias power is increased to the temperature of negative electrode a degree that is conducive to the long-pending reaction in W Shen, and low substrate bias power is reduced to temperature to moderate bias power the condition that is conducive to W etching reaction.Depend on the state of negative electrode, can select substrate bias power with from the unwanted deposition of cathodic etching, be maybe back on negative electrode long-pending the W Shen of needs, and therefore can improve ion source life.
Although invention has been described with reference to different special execution modes, be understood that the present invention is not thereby restricted, and extend to and contain different other change and the execution mode understood as haveing the knack of this operator.Therefore, the present invention is intended to broadly explain and annotate according to appended claim.