throbber
2016
`
`J. Electrochem. Soc.: SOLID-STATE SCIENCE AND TECHNOLOGY
`
`August 1988
`
`110, 215 (1983).
`3. H. Nakane, M. Nakayama, T. Ayabe, T. Nishimura, and
`T. Kimura, in “Proceedings of Semiconductors and
`Integrated Circuits Technology,” Vol. 1, p. 571 (1978).
`4. M. K. Lee, C. Y. Lu, and C. T. Shih, This Journal, 130,
`2249 (1983).
`5. D. E. Clark, C. G. Pantano, Jr., and L. L. Hench, “Corro-
`
`sion of Glass,” Magazines for Industry, New York
`(1979).
`6. W. A. Pliskin and H. S. Lehman, This Journal, 112, 1013
`(1965).
`7. W. A. Pliskin, J. Vac. Sci. Technol., 14, 1064 (1977).
`8. R. J. H. Lin, J. C. Lee, and P. B. Zimmer, ALO-5300-T2,
`U.S. Department of Energy, Washington, DC (1979).
`
`Etching of Tungsten and TungstenSilicide Films by
`Chlorine Atoms
`
`D. S. Fischl,*:' G. W. Rodrigues,” and D. W. Hess**
`
`Department of Chemical Engineering, University of California, Berkeley, California 94720
`
`ABSTRACT
`
`Thin films of tungsten and tungsten silicide were etched both within and downstream from a Cl, plasma discharge at
`200 mtorr pressure and temperatures below 150°C. When samples were positioned downstream from the discharge, etch-
`ing proceededsolely by chemical reaction of the film with chlorine atoms. Without a discharge, molecular chlorine did not
`etch tungsten or tungstensilicide. Downstream and in-plasma tungsten etch rates were approximately equalat 110°C, but
`the chlorine atom etch rate dropped morerapidly than the in-plasmaetch rate as temperature decreased. The chemical re-
`action between chlorine atoms and the tungsten film was proportional to the gas phase Cl atom mole fraction. A pretreat-
`mentconsisting of either a dilute hydrofluoric acid dip or a short plasma etch cycle was necessary for atom etching of
`tungstensilicide films. The etch rates of tungstensilicide in Cl, plasmas were approximately an order of magnitude higher
`andless temperature sensitive than those in the downstream (atom) configuration.
`
`The patterning of tungsten and tungstensilicide for mi-
`croelectronic circuits has been accomplished by a variety
`of halogen-based dry processing etching techniques(1-8).
`Publications on the patterning of these materials using
`chlorine have only summarized theeffects that the process
`parameters have on the anisotropy,etch rate, and selectiv-
`ity (5). The limited results suggest that the etch rate of
`tungsten is related to the concentration of chlorine atoms,
`Cl, produced by either laser irradiation (8) or gas-phase
`electron impact dissociation (5) of molecular chlorine, Cly.
`However, the etching process was controlled empirically
`and thus is not based on a fundamental understanding of
`the etching mechanism.
`Control of thin film etching processes during microelec-
`tronic device manufactureis often difficult. In large part,
`the difficulties arise from the complexity of RF glow dis-
`charges, coupled with plasma-film interactions. One
`method of simplifying the etch chemistry of these pro-
`cesses is to utilize an upstream discharge to generate reac-
`tive atoms for etching. Since ion, electron, and photon
`bombardment are absent in this configuration, the pure
`atom etch chemistry can be studied. Comparison of down-
`stream etching with in-plasma or discharge etching then
`generates insight into the role of the plasma. Furthermore,
`such investigations yield fundamental information con-
`cerning atom reactions with materials. In this paper we
`present results on the chlorine atom etching (downstream
`or flowing afterglow reactor configuration) and Cl» dis-
`charge etching of tungsten and tungstensilicide thin films.
`
`Corporation 300W RF generator and matching network to
`the upstream discharge via two 1.0 cm wide copper bands
`that were placed aroundthe 3.8 cm diam quartz discharge
`tube. Spacing between the bands was 1.0 cm. A metal box
`enclosed the discharge area to ensure RF shielding and to
`facilitate forced air cooling of the tube. The 3.8 em diam
`Pyrex flow tube contained two 90° bends to prevent light
`from the upstream discharge from reaching the reactor
`and thus the photomultiplier tube. The flow tube was
`coated with Halocarbon Corporation 1200 wax to minimize
`recombination of Cl atoms. The tubes and reactor were
`connected using MDC Corporation glass to metal Kwik-
`Flange adapters.
`Samples were placed inside the 2.6 liter Pyrex reactor
`chamber on a temperature controlled 2.5 cm diam
`anodized aluminum rod that served as thelower electrode
`for plasma etching experiments. Rod temperature was var-
`ied from 25° to 150°C using heating tape and an Omega En-
`gineering Incorporated Model 650/660 controller. In order
`to reduce the surface area for atom recombination and
`thus increase the atom concentration at the sample sur-
`face, the upper electrode was removed during tungsten
`atom etching experiments.
`Molecular and atomic chlorine traveled approximately
`60 cm from the discharge section to the sample location.
`The chlorine flow rate was controlled by a needle valve
`and measured with a rotameter. Vacuum was provided by
`a liquid nitrogen cold trap and a Busch Corporation Lotos
`corrosion resistant mechanical pump. The pressure in the
`reactor (200 mtorr) was established bya throttling valve at
`the exit from the reactor and was monitored by a capaci-
`tance manometer.
`The gas phase chlorine atom concentration at the posi-
`tion of the sample was measuredbytitration with nitrosyl
`chloride (10-13). The NOC]titrant (Matheson) entered the
`reactor approximately 7 cm upstream from the samplelo-
`cation through a manifold to disperse gas evenly through-
`out the flow cross section. Flow rate was regulated by a
`needle valve and measured with a Tylan FM 360 mass flow-
`meter. Monel and Teflon were the materials used for the
`NOCI delivery system. A Hamamatsu R1928 photomul-
`tiplier tube with a Melles Griot 03FTV008 filter was used to
`monitor the 550 nm emission (chemiluminescence) result-
`*Electrochemical Society Student Member.
`**Electrochemical Society Active Member.
`ing from the recombination reaction of chlorine atoms (9,
`‘Present address: Air Products and Chemicals, Inc., Applied Re-
`13, 14) at the position of the sample.
`search and Development, Allentown, PA 18195.
`Tungsten films were prepared by sputter deposition and
`2Present address: Department of Chemical Engineering, Univer-
`had a thickness of 100 nm and resistivity of 500 »p0-cm.
`sity of Wisconsin, Madison, Wisconsin 53706.
`Pageads Abot-o7-25 to IP 10.220.39.221 address. Redistribution subject to ECS te rms of use (see ecsdl.org/site/terms_use) uRATBSUDReExdbibital.Obl
`
`
`Experimental
`The reactor used for plasma etching (in the discharge)
`has been described in an earlier publication (5). The flow
`reactor was modified for atom etching by connectinga dis-
`charge and flowtube upstream from the etching reactor. A
`schematic of the system can be found in Ref.(9).
`An upstream RF discharge was used to dissociate Cl,
`molecules into Cl atoms, which then passed through a
`flow tube into the reactor where they reacted chemically
`with tungsten or tungsten silicide samples without the in-
`fluence of the discharge. Power was supplied by a Tegal
`
`Page 1 of 4
`
`Samsung Exhibit 1011
`
`

`

`Fraction 0.0
`ChlorineAtomMole
`
`
`0
`
`100
`Molecular Chlorine Flow Rate (sccm)
`Fig. 1. Effect of Cl, flow rate on the atom yield in the reactor at 200
`mtorr total pressure and for two different powers to the upstream dis-
`charge.
`
`200
`
`Chemical vapor deposition was used to form the 250 nm
`thick tungstensilicide films which had a resistivity of 1000
`wO-cm, and an approximate Si/W ratio of 2.5. Both film
`types were deposited onto oxidized silicon wafers, which
`were then broken into samples of approximately 1 em? [de-
`tails of film preparation can be foundin Ref. (5)]. Etch rates
`were determined from the film thickness and the time re-
`quired for the film to visually clear from the oxide surface.
`Results
`Chlorine atoms.—Molecularchlorine gas, Cl., is partially
`dissociated into Cl atoms by the upstream plasma. These
`atoms thentravel through the flow tubeto the reactor with
`some of them recombining by third body(e.g., Cl. or wall)
`collisions. The concentration of gas-phase chlorine atoms
`in the reactor at the location of the sample is varied by
`changing the Cl, flow rate and the upstream discharge
`power. Titration results yield a linear relationship between
`the Cl atom concentration and the square root of the chem-
`iluminescence intensity (13-15). The Cl atom concentration
`is then easily determined by measurementoftheintensity.
`Sinceall experiments are performed at a constant pressure
`of 200 mtorr, results are presented in terms of the chlorine
`atom molefraction.
`The effect of chlorine flow rate on the atom yield in the
`reactor is shown in Fig. 1. At constant RF power,a fixed
`amount of Cl, is dissociated in the upstream discharge.
`The number of atoms that recombine while traveling to
`the reactor depends on the flow rate, pressure, and recom-
`bination kinetics. These data show that the chlorine atom
`mole fraction increases with an increasein flow rate at con-
`stant pressure. This behavior is consistent with a decrease
`in gas residencetimeat higherflow rates since shorterresi-
`dence times mean that more of the atoms produced in the
`discharge arrive at the reactor before recombining (16).
`However, the atom mole fraction levels off at higher flow
`
`200 mTorr
`
`100 secm
`
`0.6
`
`0.5
`
`0.4
`
`0.3
`
`0.2
`
`Fraction
`ChlorineAtomMole
`
`0
`
`50
`
`100
`
`150
`
`Vol. 135, No. 8
`
`TUNGSTEN AND TUNGSTEN SILICIDE FILMS
`
`2017
`
`Residence Time in Flow Tube (sec)
`0.17
`0.08
`0.06
`
`200 mTorr
`
`125 Watis
`
`75 Watts
`
`0.4
`
`0.3
`
`0.2
`
`0.1
`
`rates because, at constant power, the numberof atomspro-
`duced decreases when the residence time in the upstream
`discharge becomestoo short. Figure 1 also showsthat an
`increase in power to the upstream dischargeincreases the
`chlorine atom molefraction. This effect is due to increased
`electron impact dissociation of chlorine molecules.
`Figure 2 showstheeffect of increasing the RF powerto
`the upstream discharge at a constant flow rate of 100 secm
`Cl, and a pressure of 200 mtorr. As expected, an increase in
`power produces an increase in the Cl atom fraction. At
`100W, one-third of the molecular chlorine molecules that
`enter the system remain dissociated when theyarrive at
`the sample location. The data shown in Fig. 2 emphasize
`the fact that molecular dissociation is not linearly related
`to the applied discharge power.
`Tungsten etching.—The effect of temperature on the
`tungstenetch rate at a pressure of 200 mtorr and a total gas
`flow rate of 100 sccm is showninFig. 3. Solid symbols rep-
`resent data from plasma etching experiments (5), where
`the sample is positioned within the discharge and subjec-
`ted to ion bombardment. The open squares are results
`from the current study, where etching of the tungsten film
`is solely due to chemical reaction with chlorine atoms. For
`these data points, the gas-phase mole fraction of chlorine
`atoms, Cl, is 0.5. Without an upstream or in situ discharge,
`no reaction of tungsten occurs with chlorine molecules,
`Cls, at temperatures up to 150°C. However, it should be
`mentioned that thermal dissociation of chlorine molecules
`and subsequent reaction with tungsten occurs at surface
`temperatures above 600°C (8, 17). As the temperatureis re-
`duced, etch rates fall and the rate enhancement by ion
`bombardmentis greater than at higher temperatures. The
`atom and plasma etch rates are approximately equal at
`110°C. Obviously, in plasma etching, the etch rate is not
`critically dependent on thermal heating whichis a control-
`ling factor in atom etching. In the case of plasmaetching,
`ion bombardment from the discharge supplies energy to
`break bonds as well as heat the surface. However, experi-
`ments using thermally bonded samples have shown that
`plasma heating does not significantly affect the tungsten
`etch rate (5). If an Arrhenius temperature dependenceis
`assumed, the apparentactivation energies of the reactions
`are 0.1 and 0.3 eV/molecule for plasma etching and atom
`etching, respectively.
`It was shownin Fig. 2 that the atom concentration in the
`reactor can be varied by changing the upstream discharge
`power. This fact is used to quantitatively determinethe ef-
`fect of the gas-phase chlorine atom concentration on the
`tungsten etch rate. The data in Fig. 4 are from experiments
`at three different temperatures with the flow rate and the
`pressure constant at 100 sccm and 200 mtorr, respectively.
`At these temperatures, the etch rate varies linearly with
`the gas-phase chlorine atom mole fraction. The solid lines
`depict the bestfit for all data and are described by
`
`Temperature (C)
`84
`60
`
`112
`
`40
`
`100 seem
`
`plasma etching
`
`2 mTorr
`
`atom etching
`
`2.4
`
`2.6
`
`28
`
`3.0
`
`3.2
`
`3.4
`
`
`
`EtchRate(nm/min)
`
`Power (Watts)
`Fig. 2. Effect of the upstream poweron the atom yield in the reactor
`mtorr pressure and 100 sccm Cl, flow.
`
`1Ragen A otb-07-25 to IP 10.220.39.221 address. Redistribution subject to ECS terms of use (see ecsdl.org/site/terms_use) unless CC Licensein place (see abstract).
`
`1/Temp X 1000 (1/K)
`Fig. 3. Effect of temperature on the atom and in-discharge etch rate
`of tungsten at 200 mtorr pressure and 100 sccm Cl, flow. The chlorine
`atom mole fraction is 0.5 for the atom etching.
`
`Page 2 of 4
`
`

`

`J. Electrochem. Soc.: SOLID-STATE SCIENCE AND TECHNOLOGY
`
`August 1988
`
`40
`
`30
`
`20
`
`2018
`
`
`
`EtchRate(nm/min)
`
`10 0
`
`0.0
`
`0.6
`0.4
`0.2
`Chlorine Atom Mole Fraction
`
`0.8
`
`Fig. 4. Effect of chlorine atom mole fraction on the tungsten etch
`rate at 200 mtorr pressure, 100 sccm Cl, flow, and three different rod
`temperatures.
`
`Etch rate [nm/min] = 2.3 x 10° Xq exp (—3900/T)
`
`where Xc is the chlorine atom mole fraction in the gas-
`phase andT is the anodized aluminum rod temperature in
`Kelvin. The pre-exponential constant in the equation does
`not change with flow rate over the range of 20-150 sccm.
`This observation indicates that the reaction is not limited
`by a mass-transport boundary layer. At 200 mtorr pressure
`and Xq = 0.5, kinetic theory predicts that approximately
`10'° chiorine atomsstrike a square centimeter of surface
`per second. An etch rate of 40 nm/min requires that ap-
`proximately 10" tungsten atoms leave a square centimeter
`of surface per second. If the etch product is assumed to be
`WCL,, the reaction probability of Cl atomsis approximately
`10-*. This is the predominate product detected by ultra-
`high vacuum experiments with molecular and atomic
`chlorine beamsandis also the product predicted by evalu-
`ation of equilibrium vapor pressures of the possible
`tungsten chloride products at these temperatures(17).
`Tungsten silicide etching—Unlike tungsten, tungsten
`silicide that is exposed to air for longer than a few days
`does not etch spontaneously with chlorine atoms. How-
`ever, if the samples are first dipped in a 5% HFsolution or
`subjected to a Cl, plasma discharge they can be etched
`downstream by chlorine atoms. Apparently, ion bombard-
`ment is necessary to removethesilicon dioxide layer that
`forms on the surface of the samples during exposure to air
`at room temperature. Therefore, tungsten silicide is etched
`by chlorine atomsbyfirst subjecting the samples to a Cl,
`discharge for 30s (200 mtorr, 150 sccm total gas flow, 10W),
`which is the shortest time found to ensure complete re-
`moval of the native oxide layers. The amount of material
`removed during the 30s is calculated based on plasma
`etching experiments at the same temperature and there-
`
`Temperature (C)
`84
`
`112
`
`60
`
`plasma etching
`
`
`
`EtchRate(nm/min)
`
`
`
`EtchRate(nm/min)
`
`200 mTorr
`
`atom etching
`
`maining film thickness is used in the atom etch rate calcu-
`lation. Althouugh this procedure is not ideal, the error is
`small. Furthermore,the etch rates calculated in this man-
`ner are in agreement with the rates obtained by using an
`HF dip prior to the etch run. Because exposure to air re-
`sults in the growthof an oxidefilm on the WSi, surface, the
`upperelectrode used for the plasma etch remains in place
`during the atom experiments. This electrode offers addi-
`tional surface area for Cl atom recombination compared to
`the electrode configuration for the tungsten etching exper-
`iments. Chlorine atom concentrations are thus lower than
`observed for identical upstream discharge studies when
`etching tungsten (compare Fig. 4 and 6). The plasma pre-
`treatment is preferred over the HF dip because thefilm
`clears more uniformly and the endpoint is easier to ob-
`serve. Without a discharge, tungsten silicide did not etch
`in molecular chlorine under the conditions investigated.
`The effect of temperature on theetch rate of tungstensil-
`icide films in the discharge and by Cl atoms is shown in
`Fig. 5, where the data are obtained at 200 mtorr and 150
`sccm Cl, flow rate. The solid symbols are the plasma etch-
`ing results and the open symbols are the Cl atom etching
`results with a Cl mole fraction of 0.2. Clearly, tungsten sili-
`cide is etched by Cl atoms, but at a much slowerrate than
`that obtained in the discharge when ion bombardmentoc-
`curs. However,
`the relatively low atom concentrations
`could also be a major cause of the reduced etch rates in the
`downstream configuration.
`Similar to the tungsten etching results shownin Fig. 3,
`plasmaetch rates of tungsten silicide are less temperature
`dependent than atom etch rates. The apparent activation
`energies calculated from the data in Fig. 5 are 0.06 and 0.16
`eV/molecule for plasma etching and atom etching, respec-
`tively.
`The etch rate ofsilicon is known to be greatly enhanced
`by ion bombardment in Cl, discharges (18, 19). Further-
`more, preliminary investigations in our laboratory indicate
`that heavily doped (approximately 10° cm~*) n* polysili-
`con films are etched by Cl atoms (downstream configura-
`tion) at comparable rates to those observed for W and
`WSi,. Therefore, the large etch rate enhancement due to
`the discharge and the magnitudeof the atom etch rate sug-
`gest that the overall etching process of tungstensilicideis
`limited by the presenceof silicon in the film. Whether this
`observation is duc to volatility considerations, a reduction
`in electron concentration in the solid (resulting in lowered
`etchant adsorption), or the fact that the strong (1.8 eV)
`Si—Sibondis essentially eliminatedin the silicide filmsis
`not clear at this time.
`Thevariation of WSi, etch rate with the limited range of
`chlorine atom mole fractions achieved is shownin Fig. 6
`for 100°C, 200 mtorr, and 150 sccm. Again, the etch rate in-
`creases with an increase in the Cl-atom mole fraction. Un-
`fortunately, because of the limited range of chlorine atom
`concentrations that could be obtained with our apparatus,
`a general kinetic expression describing atom etching of
`the tungstensilicide films was not formulated.
`
`100 C
`
`0.0
`
`0.3
`
`200 mTorr
`150 seem
`
`150 scem
`
`24
`
`2.6
`
`30
`
`3.2
`
`0.2
`0.1
`2.8
`Chlorine Atom Mole Fraction
`1/Temp. X 1000 (1/K)
`Fig. 5. Effect of temperature on the atom and in-discharge etch rate
`Fig. 6. Effect of chlorine atom mole fraction on the tungsten silicide
`of tungstensilicide at 200 mtorr pressure and 150 sccm Cl, flow, The
`etch rate at 100°C temperature, 150 sccm Cl, flow, and 200 mtorr total
`pressure.
`chlorine atom mole fraction is 0.2 for the atom etching.
`PagecdobA07-25 to IP 10.220.39.221 address. Redistribution subject to ECS terms of use (see ecsdl.org/site/terms_use) unless CC Licensein place (see abstract).
`
`Page 3 of 4
`
`

`

`Vol. 135, No. 8
`
`TUNGSTEN AND TUNGSTENSILICIDE FILMS
`
`2019
`
`Conclusions
`Tungsten and tungsten silicide thin films have been
`etched both by Cl, plasma discharges and by Cl] atoms
`without the influence of the plasma. Molecular chlorine
`did not etch the films at the temperatures investigated.
`Both films could be etched by atomic chlorine, however, a
`native oxide layer present on tungsten silicide had to be re-
`moved before the atoms could attack the film. The results
`showthat plasma interactions greatly enhance the Cl atom
`etch rate of tungsten silicide. However for tungsten, the
`etching process proceeds mainly by chemical reaction of
`the film with Cl atoms and is less affected by the plasma.
`
`Acknowledgments
`The authors thank P. Marmillion at IBM Essex Junction,
`Vermontfor supplying the tungsten and tungstensilicide
`samples used in this investigation. The corrosion resistant
`pump was supplied by Busch Incorporated, Virginia
`Beach, Virginia and maintained by Semivac Corporation
`in Milpitas, California. This work was funded by Intel Cor-
`poration and the California State MICRO program.
`
`Manuscript submitted Oct. 9, 1987; revised manuscript
`received Jan. 18, 1988.
`
`REFERENCES
`1. S. P. Murarka, Solid State Technol., 181 (Sept. 1985);
`S.P. Murarka, “Silicides for VLSI Applications,”
`Academic Press, Inc., Orlando, FL (1983),
`2. Y. Pauleau, Solid State Technol., 61 (Feb., 1987); R. 5S.
`Blewer, ibid., 117 (Nov. 1986).
`
`ocfc0a
`
`3. T. P. Chow and A. J. Steckl, This Journal, 131, 2325
`(1984).
`4. Workshop on Tungsten and Other Refractory Metals
`for VLSI Applications, Continuing Education in En-
`gineering, University Extension, University of Cali-
`fornia, Berkeley, Palo Alto, CA, Nov. 12-14, 1986.
`. D. S. Fisch! and D. W. Hess, This Journal, 134, 2265
`(1987).
`. G. Koren, Appl. Phys. Lett., 47, 1012 (1985).
`. M. Rothschild, J. H. C. Sedlacek, and D. J. Ehrlich,
`ibid., 49, 1554 (1986).
`. M. Rothschild, J. H. C. Sedlacek, J. G. Black, and D. J.
`Ehrlich, J. Vac. Sci. Technol. B; 5, 414 (1987).
`. D. A. Danner and D. W. Hess, J. Appl. Phys., 59, 940
`(1986).
`10. M. A. A. Clyne and W. S$. Nip, in “Reactive Interme-
`diates in the Gas Phase,” by D. W. Setser, Editor,
`Chap. 1, Academic Press, Inc. (1979).
`11. M. A. A. Clyne, H. W. Cruse, and R. T. Watson, J. Chem.
`Soc., Faraday Trans. I, 68, 153 (1972).
`12. M. A. A. Clyne and H.W. Cruse, ibid., 68, 1281 (1972).
`13. M. A. A. Clyne and D. H. Stedman, Trans. Faraday
`Soc., 64, 1816 (1968).
`14. M. A. A. Clyne and D. H. Stedman,
`(1968).
`15. M. A. A. Clyne and D. J. Smith, J. Chem. Soc., Faraday
`Trans. 2,75, 704 (1979).
`16. C. G. Hill, “An Introduction to Chemical Engineering
`Kinetics and Reactor Design,” p. 262, John Wiley
`and Sons, Inc., New York (1977).
`17. M. Balooch, D. S. Fischl, D. R. Olander, and W. J. Siek-
`haus, This Journal, 135, 0000 (1988).
`18. S. C. McNevin and G. E. Berker, J. Vac. Sci. Technol. B,
`3, 485 (1985).
`19. R.H. Bruce, Solid State Technol.,, 64 (Oct. 1981).
`
`ibid., 64, 2698
`
`Phosphorous Vacancy Nearest Neighbor Hopping Induced
`Instabilities in InP Capacitors
`|. Experimental
`
`DepartmentofElectrical and Computer Engineering, Centerfor Advanced Materials Research, Oregon State University,
`Corvallis, Oregon 97331
`
`M. T. Juang, J. F. Wager, and J. A. Van Vechten”
`
`Variable temperature bias-stress measurements were performed on n-type InP MIS capacitors. Two distinct activa-
`tion energies at 40-50 meV and1.1-1.2 eV were obtained over a temperature range of 100-350 K. These energies are consist-
`ent with the instability mechanisms of thermionic tunneling into native oxide traps and phosphorous vacancy nearest
`neighbor hopping (PVNNBH). Theestimated fraction of shift in these particular samples due to PVNNHvaries both with
`stress time and with temperature from about 20%for short times at 300 K to about 80%for long times at 350 K.
`
`ABSTRACT
`
`The drain current of an InP metal insulator semicon-
`ductorfield effect transistor (MISFET)is often observed to
`decrease as a function of time after the application of a
`positive gate bias which induces an accumulation of elec-
`trons in the channel. Various models have been proposed
`for this drain current drift (DCD) phenomena[see Ref.(1)
`for a critical review of proposed DCD models}.
`In this study, we have employed variable temperature
`bias-stress measurements (see the section on Experimen-
`tal Procedure for a description of this technique) of InP
`MIS capacitors in order to determine the dominant DCD
`mechanisms from an analysis of the activation energy of
`the flatband shift. There are two advantages inherent in
`bias-stress measurements of MIS capacitors compared to
`DCD measurements of InP MISFET’s.First, fabrication of
`the MIS capacitor requires fewer processing steps so that
`the interface chemistry can be precisely controlled and the
`electrical instabilities may be correlated to the interface
`chemistry. A second advantage is that the flatband shift
`depends only on the carrier density in the channel while
`*Electrochemical Society Active Member.
`Inin + Vp* + 4e° = Vin” Inp™?
`{1]
`Rage dot04-07-25 to IP 10.220.39.221 address. Redistribution subject to ECS terms of use (see ecsdl.org/site/terms_use) unless CC Licensein place (see abstract).
`
`
`drain currentinstabilities depend on both the carrier den-
`sity and carrier mobility. Thus, interpretation of bias-
`stress measurements is more direct than that of DCD.
`Twodistinct activation energies at 40-50 meV and 1.1-1.2
`eV were obtained from variable temperature bias-stress
`measurements over a temperature range of 100-350 K. The
`40-50 meV activation energy dominates the flatband shift
`at low temperatures and is consistent with thermally acti-
`vated tunneling of electrons from the InP conduction
`band into a discrete trap in the native oxide. An activation
`energy of 1.2 eV was predicted (2) for phosphorous va-
`cancy nearest neighbor hopping (PVNNH) in which the
`channel electrons are captured by shallow acceptors that
`are created by the hopping of an In atom into a phos-
`phorous vacancy.
`PVNNH leads to DCD in the following manner. Con-
`sider an InP MISFETwhich has processing-induced P va-
`cancies in the channel region underits gate. Nearest neigh-
`bor hopping of an In atom into the P vacancy is described
`by the following defect reaction
`
`Page 4 of 4
`
`

This document is available on Docket Alarm but you must sign up to view it.


Or .

Accessing this document will incur an additional charge of $.

After purchase, you can access this document again without charge.

Accept $ Charge
throbber

Still Working On It

This document is taking longer than usual to download. This can happen if we need to contact the court directly to obtain the document and their servers are running slowly.

Give it another minute or two to complete, and then try the refresh button.

throbber

A few More Minutes ... Still Working

It can take up to 5 minutes for us to download a document if the court servers are running slowly.

Thank you for your continued patience.

This document could not be displayed.

We could not find this document within its docket. Please go back to the docket page and check the link. If that does not work, go back to the docket and refresh it to pull the newest information.

Your account does not support viewing this document.

You need a Paid Account to view this document. Click here to change your account type.

Your account does not support viewing this document.

Set your membership status to view this document.

With a Docket Alarm membership, you'll get a whole lot more, including:

  • Up-to-date information for this case.
  • Email alerts whenever there is an update.
  • Full text search for other cases.
  • Get email alerts whenever a new case matches your search.

Become a Member

One Moment Please

The filing “” is large (MB) and is being downloaded.

Please refresh this page in a few minutes to see if the filing has been downloaded. The filing will also be emailed to you when the download completes.

Your document is on its way!

If you do not receive the document in five minutes, contact support at support@docketalarm.com.

Sealed Document

We are unable to display this document, it may be under a court ordered seal.

If you have proper credentials to access the file, you may proceed directly to the court's system using your government issued username and password.


Access Government Site

We are redirecting you
to a mobile optimized page.





Document Unreadable or Corrupt

Refresh this Document
Go to the Docket

We are unable to display this document.

Refresh this Document
Go to the Docket