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Claims  |
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We claim:
1. A process for the production of a solid thin film containing silicon and
nitrogen on a substrate, said film having a aggregate low concentration of
carbon and oxygen of less than about 51 atom percent, which process
comprises:
(A) contacting the substrate with a gaseous mixture substantially in the
absence of silane itself comprising:
(i) a volatile cyclic organic silicon nitrogen source, and
(ii) hydrogen, under plasma enchanced chemical vapor deposition conditions
including a pressure lower than 10 Torr and a temperature greater than
ambient temperature for a time sufficient to produce a silicon nitride
thin film having ceramic-like properties.
2. The process of claim 1 wherein the organic silicon nitrogen source is
selected from compounds consisting of silicon and nitrogen, and optionally
carbon and hydrogen.
3. The process of claim 2 wherein the organic silicon nitrogen source is
selected from 1,1,3,3,5,5-hexamethylcyclotrisilazane,
1,2,3,4,5,6-hexmethylcyclotrisilazane,
1,1,3,3,5,5,7,7-octamethylcyclotetrasilazane,
1,2,3,4,5,6,7,8-octamethylcyclotetrasilazane, or mixtures thereof.
4. The process of claim 1 wherein the aggregate of the carbon and oxygen
present in the deposited thin film is less than about 45 atom percent.
5. The process of claim 1 wherein the plasma enhanced chemical vapor
deposition conditions are temperatures of between about 200.degree. and
400.degree. C. and pressures of between about 0.1 and 0.7 Torr.
6. The process of claim 1 wherein the ratio of the organic silicon nitrogen
source tohydrogen is between about 0.1/19.9 to 0.7/19.3 by volume.
7. The process of claim 6 wherein the ratio of the volatile cyclic organic
silicon nitrogen source (i) to hydrogen (ii) is between about 0.2/19.8 and
0.6/19.4 by volume.
8. The process of claim 7 wherein the ratio is about 0.3/19.7 by volume.
9. A method for depositing a thin surface film comprising silicon nitride
on a substrate, which method comprises:
(a) contacting said substrate with a gaseous mixture substantially in the
absence of silane itself comprising:
(i) a volatile cyclic organic silicon-nitrogen source, and
(ii) a hydrogen-nitrogen source;
(b) producing an enhanced plasma discharge in the gaseous mixture under
reaction conditions including a pressure lower than 10 Torr and a
temperature greater than ambient temperature to produce chemical vapor
desposition, and ceramic-like properties on said substrate having an
aggregate low concentration of carbon and oxygen of less than about 20
atom percent.
10. The process of claim 9 wherein the hydrogen-nitrogen source is selected
from compounds consisting of hydrogen and nitrogen, or of silicon,
nitrogen and hydrogen.
11. The process of claim 10 wherein the hydrogen-nitrogen source is
selected from hydrogen, nitrogen, ammonia, or mixtures thereof.
12. The method of claim 9, wherein:
in step (a)(i) the organic silicon nitrogen source is selected from
1,1,3,3,5,5-hexamethylcylotrisilazane,
1,2,3,4,5,6-hexamethylcylotrisilazane,
1,1,3,3,5,5,7,7-octamethylcyclotetrasilazane,
1,2,3,4,5,6,7,8-octamethylcyclotetrasilazane, or mixtures thereof;
and the ratio of organic silicon nitrogen source to hydrogen nitrogen
source is between about 0.1/19.9 and 0.4/19.6 by volume.
13. The process of claim 12 wherein the plasma enhanced chemical vapor
deposition conditions are temperatures of between about and 400.degree. C.
and pressures of between about 0.1 and 0.7 Torr.
14. The process of claim 13 wherein the temperature is about 300.degree. C.
and the pressure is between about 0.2 and 0.4 Torr.
15. The process of claim 13 wherein the ratio of the volatile cyclic
organic silicon nitrogen source (i) to the hydrogen nitrogen source (ii)
is between about 0.2/19.8 and 0.6/19.4 by volume.
16. The process of claim 15 wherein the ratio is about 0.3/19.7 by volume.
17. The process of claim 1 wherein the plasma enhanced chemical vapor
deposition conditions comprise a power between 20 and 80 watts and, a
power density of between about 0.37 and 1.5 watts per cm.sup.2.
18. The process of claim 1 wherein the plasma is produced using
capacitively coupled parallel plate electrodes.
19. The process of claim 1 wherein the plasma is produced using an
inductively coupled electrodeless reactor.
20. A substrate having a surface thin film comprising silicon nitride
produced by the process of claim 1.
21. A substrate having a surface thin film comprising silicon nitride
wherein the silicon nitride thin film is produced by the process of claim
9.
22. A process for the production of a solid thin film containing silicon
and nitrogen on a substrate said film having an aggregate low
concentration of carbon or oxygen of less than about 51 atom percent,
which process comprises:
(a) contacting the substrate with a gaseous mixture itself consisting
essentially of:
(i) 1,1,3,3,5,5-hexamethylcyclotrisilazane,
1,2,3,4,5,6-hexamethylcyclotrisilazane, or mixtures thereof, and
(ii) hydrogen, wherein (i) and (ii) are in a ratio of between about
0.1/19.9 and 0.4/19.6 by volume,
(b) reacting the gaseous mixture in step (a) in an enchaned plasma
discharge in the gaseous mixture under reaction conditions to produce
chemical vapor deposition on said substrate of a thin film of ceramic-like
silicon nitride having an aggregate low concentration of carbon and oxygen
of less than 51 atom percent, wherein said conditions comprise
temperatures of between about 200.degree. and 400.degree. C., pressures of
between about 0.2 and 0.7 Torr and a power of between about 20 and 40
watts, and a power density of between about 0.4 and 1.75 watts per
cm.sup.2 ; and
(c) recovering the silicon-nitrogen thin film coated substrate having
ceramic like character.
23. The process of claim 22 wherein in step (a), the gaseous mixture
component (ii) is hydrogen, the ratio of (i) and (ii) is about 0.4/19.6
percent by volume, and;
in step (b) the temperature is about 200.degree. C., the pressure is about
0.3 Torr and the thin film deposited is between about 0.01 and 1
micrometers in thickness.
24. On a substrate, the thin film comprising silicon nitride deposited by
the process of claim 9.
25. On a substrate the thin film comprising silicon nitride deposited by
the process of claim 22.
26. The process of claim 22 wherein the film has an aggregate low
concentration of carbon and oxygen of less than about 40 atom percent. |
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Claims  |
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Description  |
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BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to a method for producing thin films of
silicon nitride. More specifically, the present invention relates to a
method of producing a thin film of silicon ceramic-like nitride on an
object by subjecting a vapor of a cyclic silicon-nitrogen precursor, such
as 1,1,3,3,5,5-hexamethylcyclotrisilazane, with hydrogen alone or a source
of hydrogen and nitrogen, such as ammonia. These thin films do not require
the usual post-deposition pyrolysis at 800.degree. C. or higher, and are
useful as passivation coatings on objects, such as semiconductor inter
metal dielectric layers.
2. Description of the Related Art
Plasma enhanced chemical vapor deposition (PECVD) of silicon nitride
(SiNxHy, where x is between about 0.8 and 1.5 and y is between about 0.4
and 1.2) are used as final passivation layers in microelectronic circuits.
Silicon nitride is preferred due to its impermeability to water and to
sodium ion diffusion as well as mechanical toughness and high dielectric
constant.
In the past, typical methods for film production involve the plasma
enhanced reaction of silane (SiH.sub.4) with either nitrogen (N.sub.2) or
ammonia (NH.sub.3). The difficulties encountered in the control of SiNxHy
stoichiometry along with the pyrophoric nature of silane has lead to the
investigation of organosilicon monomers as sources of silicon for SiNxHy
thin film formation.
In U.S. Pat. No. 4,158,717, N. H. Nelson discloses a preparation of a
silicon nitride film by the plasma discharge of a vapor of
azidotrimethylsilane. Temperatures between 100.degree.-400.degree. C. and
a pressure of 0.15 to 0.20 Torr were used.
M. R. Gulett et al., in U.S. Pat. No. 4,330,569 disclose a method of
conditioning a nitride surface.
J. Janca et al., in Acta Phys. Slov., Vol. 33 (#3), pp. 187-193, published
in 1983 disclose the preparation of thin silicon nitride films which are
deposited in the RF discharge plasma of 1.5 MHz of vaporizable linear
hexamethyldisilazane [(CH.sub.3).sub.3 Si].sub.2 NH, or
azidotrimethylsilane (CH.sub.3).sub.3 SiN.sub.3 in the presence of
nitrogen.
V. I. Belyi et al., in Mikroelectronica (Akad.Nauk SSSR), Vol. 15, p.
146-149 (1986) [see Soviet Microelectronics, Vol. 15, No. 2, p. 91-94
(1986)], disclose the plasma polymerization of hexamethylcyclotrisilazane
at 0.1 W/cm.sup.2 (RF) in ammonia. The film produced showed large Si-H and
N-H peaks by infrared spectral analysis, as well as substantial Si-C and
C-H absorptions.
D. V. Tsu et al., in Physical Review B:, Vol. 33 (#10), pp. 7069 to 7076,
published in 1986, disclose the preparation of silicon nitride thin films
by remote plasma-enhanced chemical vapor deposition using gas mixtures of
silane and either nitrogen or ammonia.
B. Arkles in the Journal of the Electrochemical Society, pp. 233-234,
published in January, 1986, discloses that silicon nitride is formed from
cyclic and linear organosilazane prepolymers as single components. The
materials are pyrolyzed at temperatures of 350.degree. C. or greater.
Complete conversion to ceramic occurs at temperatures exceeding
700.degree. C.
A. M. Wrobel in the Journal of Macromolecular Science-Chemistry, Vol. A15
(#2), pp. 197-213, published in 1981, disclose the polymerization of
hexamethyltrisilazane as a single component in a microwave plasma at 2.45
gigahertz (GHz). The polymerizations to provide thin polysilazane films
were conducted at substrate temperatures of 25.degree., 200.degree.,
400.degree., 600.degree. and 800.degree. C.
A. M. Wrobel et al., disclose in Polymer, Vol. 17, pp. 673-677 and 678-684,
published in 1986, the prepartion of thin polysilazane films by the glow
discharge polymerization of hexamethylcyclotrisilazane as a single
component at 20 kHz.
A. M. Wrobel et al., in Plasma Polymerization (M. Shen and A. T. Bell,
eds.) American Chemical Society Symposium Services, No. 108, ACS,
Washington, D.C., pp. 237-249, published in 1979, disclose the plasma
polymerization of hexamethylcyclotrisilazane in a glow discharge at 20
kilohertz (kHz). A combination of the monomer and ammonia at 0.3 Torr were
used in one example. Considerable organic character is present. Pyrolysis
of the layer at 600.degree. and 800.degree. C. showed a loss of Si-C
bonds, formation of methane, and increasing inorganic ceramic character.
M. Kryszewski et al., in Plasma Polymerization (M. Shen and A. T. Bell,
eds.) American Chemical Society Symposium Series, No. 108, ACS,
Washington, D.C., Chapter 13, pp. 219-235, published in 1979, disclose the
plasma polymerization of hexamethylcyclotrisilazane vapor under glow
discharge conditions of 20 kilohertz (kHz). Upon pyrolysis of the thin
films at a RF value of 13.5 MHz in a glow discharge, cyclic SiN compounds
were evolved.
J. Tyczkowski et al., in Thin Solid Films, Vol. 55, pp 253-259, published
in 1978, disclose the production of polysilazane films by the
hexamethylcyclotrisilazane as a single component in a glow discharge at 20
kHz.
M. Gazicki et al., in Plasma Chemistry and Plasma Processing, Vol. 3, (No.
3), pp. 279-327, published in 1983, disclose the glow discharge plasma
polymerization of hexamethylcyclotrisilazane under glow discharge
conditions.
M. Gazicki et al., in the Journal of Applied Polymer Science, Vol. 21, pp.
2031-2019, published in 1977, disclose the glow discharge polymerization
at 20 kHz of hexamethylcyclotrisilazane as a single component to produce
polysilazane as a thin film.
N. Voke et al. Materials Research Society Symposia Proceedings (Symposium
held in Palo Alto, Calif., U.S.A., Apr. 15-18, 1986), Vol. 68, pp.
175-181, published in Pittsburgh, Pa. in 1986, disclose the plasma
enhanced chemical vapor deposition of silicon-nitride thin films under
different experimental conditions using silane and ammonia.
W. Verbeek in U.S. Pat. No. 3,853,567 and G. W. Winter, et al., in U.S.
Pat. No. 3,892,583 disclose a method of making a shaped article of silicon
carbide and nitride of silicon carbide and nitride by decomposing a
silazane at about 200.degree. to 800.degree. C.
T. H. Hirai et al., in the Journal of Materials Science, Vol. 16, pg. 17-29
and also on pp. 2877-2882, published in 1981 disclose the deposition of
CVD-S.sub.3 N.sub.4 layers including carbon.
J. J. Nicki et al., in the Journal of Less-Common Metals, Vol. 37, pg.
317-329, published in 1974, disclose the CVD of layers of Si-C and Si-C-N.
C. L. Beaty in "Silicon Nitride and Silicon Carbide from Organometallic and
Vapor Precursors", Chapter 3 in Ultrastructure Processing of Ceramics,
Glasses and Composites, edited by L. L. Hench, John Wiley and Sons, New
York, N.Y., published in 1984 disclose a number of methods of preparation
of silicon nitride.
E. J. Charlson et al., in "Electrical Properties of Glow Discharge
Polymerized Films", in Organic Coatings and Applied Polymer Science
Proceedings, Vol. 47, pg. 146-150, American Chemical Society, Washington,
D.C., published in 1982 disclose some methods of preparing polymerized
Si-N films. S. K. Varshney at al., "Surface Structure and Properties of
R.F. Plasma Polymerized Hexamethyldisilazane", in the same volume pg.
151-153 disclose the properties of glow discharge produced polymer films
from hexamethyldisilazane.
S. K. Varshney et al., "Plasma Polymerization of Silanes", in Organic
Coatings and Applied Polymer Sciences Proceedings, Vol. 46, pg. 127-133,
American Chemical Society, Washington, D.C. 20036 disclose the results of
plasma polymerization of silanes.
K. S. Mazdiyasni et al., in The Journal of the American Ceramic Society,
Vol. 61, Nos. 11-12, pg. 504-508, published in 1978 disclose the
characterization of organosilicon-infiltrated porous reaction sintered
Si.sub.3 N.sub.4.
A. M. Wrobel et al., Journal of Macromolecular Science-Chemistry, Vol. A12,
No. 7, pg. 1041-1054, published in 1978 disclose the effect of glow
discharge conditions or structure and thermal properties of polysilazane
thin films. The films were produced by glow discharge polymerization of
hexamethylcyclotrisilazane with various gases: argon, nitrogen, hydrogen
and ammonia. The polymer films produced with hydrogen and ammonia under
these conditions had considerable organic carbon, (C-H stretches) content.
A post deposition pyrolysis of the film is described to obtain specific
physical properties.
If the cyclic intermediate is polymerized normally, as in a normal plasma,
a porous silicon nitride thin film having --CH.sub.3 groups is obtained.
The film is porous to alkali ions and is not dense because the polymeric
molecules are not closely packed. The film is not a good chemical barrier
because of the porosity. To obtain the desired porosity, it is necessary
to pyrolyze the film to 1000.degree. C. or higher to form silicon and
carbon radicals which crosslink and produce a film having the desired high
density (d=1.8 to 2.1) and low porosity. These temperatures normally
damage or destroy other films or substrates present in microelectronic
devices, and are to be avoided if at all possible.
A major problem encountered in most of the methods of the above cited art
is the use of SiH.sub.4 as a silicon precursor. SiH.sub.4 is a dangerous,
pyrophoric material to use under laboratory or industrial conditions. None
of the above articles or patents individually or collectively in any
fashion teach, disclose or suggest the present invention. It is therefore
very useful to have a PECVD process to deposit a thin layer of silicon
nitride having a minimum of carbon, oxygen, and/or hydrogen on a substrate
under mild reaction and substrate conditions, and without the need for
post-deposition pyrolysis to reduce the organic nature of the films to
form a stable ceramic film.
SUMMARY OF THE INVENTION
The present invention relates to a process for the production of a solid
thin film containing silicon and nitrogen on a substrate, said film having
a aggregate low concentration of carbon and oxygen of less than 51 atom
percent, which process comprises:
(A) contacting the substrate with a gaseous mixture itself comprising:
(i) a volatile cyclic organic silicon/nitrogen source, and
(ii) a reactant independently selected from hydrogen alone or from a
hydrogen/nitrogen source,
under plasma enhanced chemical vapor deposition conditions of pressure
lower than 10 Torr and temperature greater than ambient temperature for a
time sufficient to produce a silicon nitride thin film.
When ammonia only is used in subpart (ii), the carbon and oxygen content is
less than 20 atom percent, in a preferred embodiment.
A prefered embodiment is the process wherein the ratio of the volatile
cyclic organic silicon/nitrogen source (i) to the hydrogen source (ii) is
betweeen about 0.1/19.9 and 0.6/19.4 percent by volume.
In a separate aspect, the present invention relates to the process wherein
in step (a), subpart (ii), the reactant is selected from hydrogen gas or
ammonia.
In another additional aspect, the present invention relates to a process
for the production of a solid thin film containing silicon and nitrogen on
a substrate said film having an aggregate low concentration of carbon or
oxygen of less than 10 atom percent, which process comprises:
(a) contacting the substrate with a gaseous mixture itself comprising:
(i) 1,1,3,3,5,5-hexamethylcyclotrisilazane,
1,2,3,4,5,6-hexamethylcyclotrisilazane, 1,1,3,3,5,5,7,7-octamethyl
cyclotetrasilazane, 1,2,3,4,5,6,7,8-octamethylcyclotetrasilazane, or
mixtures thereof, and
(ii) hydrogen, nitrogen, ammonia, hydrazine or mixtures thereof, wherein
(i) and (ii) are in a ratio of between about 0.1/19.9 and 0.4/19.6 by
volume,
(b) producing an enhanced plasma discharge in the gaseous mixture under
conditions to produce chemical vapor deposition on said substrate of a
thin film of silicon nitride having an aggregate low concentration of
carbon and oxygen of less than 10 atom percent, wherein said conditions
comprise temperatures of between about 200.degree. and 400.degree. C.,
pressures of between about 0.2 and 0.7 Torr and a power density of between
about 0.4 and 1.2 watts per cm.sup.2 ; and
(c) recovering the silicon-nitrogen thin film coated substrate.
In another aspect, the present invention relates to an article or substrate
having a silicon-nitrogen thin layer which is produced by the process
described herein.
BRIEF DESCRIPTION OF THE FIGURES
FIGS. 1-9 relate to cyclic monomer and hydrogen.
FIG. 1 describes a schematic diagram of the electrical components and
deposition configuration of the materials for the plasma enhanced chemical
vapor deposition of the present invention.
FIG. 2 shows a graph of the refractive index of the silazane layer produced
using cyclic monomer and hydrogen as a function of the plasma power.
FIG. 3 shows a graph of the deposition rate of the polysilazane film as a
function of the power for the monomer and hydrogen reaction.
FIG. 4 shows a graph of the refractive index of the coating as a function
of the cyclic monomer flow rate at 20 W and 40 W of power in the presence
of hydrogen.
FIG. 5 is a FTIR spectrum of the silazane polymer coating produced by the
reaction of the cyclic monomer and hydrogen at 40 watts.
FIG. 6 is an FTIR spectrum of the silicon nitride film produced using
cyclic monomer and hydrogen at 20 watts. This is not an optimum film.
FIG. 7 is a comparison of the deposition rate of the silicon nitride
polymer film versus the cyclic monomer flow rate in the hydrogen system at
20 watts of power (.cndot.) and 40 watts of power (0).
FIG. 8 is a graph of the deposition rate (.cndot.) versus the pressure
within the reaction system for the cyclic monomer and hydrogen. The
refractive index (0) of the film remains fairly stable.
FIG. 9 is a graph of the deposition rate versus the temperature of the
substrate for the cyclic monomer and hydrogen system.
FIGS. 10-14 relate to the cyclic monomer and ammonia system.
FIG. 10 shows the deposition rate ( ) and refractive index (.cndot.) vs.
flowrate for cyclic monomer and ammonia, where the total flowrate is 20.0
sccm (cubic centimeters per minute at standard temperature and pressure).
FIG. 11 shows FTIR spectra of as-deposited and aged films produced at 0.7
sccm 1,1,3,3,5,5-hexamethylcyclotrisilazane (HMCTSZN), 19.3 sccm NH.sub.3,
300.degree. C., 0.3 Torr, 40 W. The film thickness is 128 nm.
FIG. 12 shows FTIR spectra of about 100 nm SiN film deposited at
200.degree. C. and 400.degree. C., 0.2 sccm HMCTSZN, 19.8 sccm NH.sub.3,
0.3 Torr, 40 W.
FIG. 13 shows the deposition rate ( ) of SiN and refractive index (.cndot.)
vs. RF power.
FIG. 14 shows typical CV plots for about 100 nm films of SiN deposited at
25 W and 35 W, on p-type silicon. The solid traces represent as-deposited
films, and the dashed trace represents the result of annealing the 35 W
film. Other deposition conditions are: 0.2 sccm HMCTSZN, 19.8 sccm
NH.sub.3, 300.degree. C., 0.3 Torr.
DETAILED DESCRIPTION OF THE INVENTION AND PREFERRED EMBODIMENTS
Definitions
As used herein:
"HMCTSZN" refers to the cyclic monomer
1,1,3,3,5,5-hexamethylcyclotrisilazane (cyclic monomer).
"Hydrogen" or "hydrogen source" refers to hydrogen as a gas.
"Hydrogen-nitrogen source" refers to ammonia, hydrogen, nitrogen, ammonia,
hydrazine or mixtures thereof.
"sccm" refers to cubic centimeters per minute at standard temperature
(0.degree. C.) and standard pressure (760 mm of Hg).
"Silicon-nitrogen source" refers to organic cyclic silicon nitrogen having
6, 8 or 10 atom cyclic rings. The organic groups, methyl, ethyl, vinyl,
phenyl are attached to the ring structure to produce a stable volatile
molecule.
EXPERIMENTAL DETAILS
(Cyclic Monomer and Hydrogen Gas)
The plasma polymerized SiNxHy films in the present study were deposited on
p-type silicon substrates in a quartz, axial flow, capacitively coupled
reactor as described in FIG. 1. The current reactor consists of a quartz
tube 11 that is 15 cm in diameter and 60 cm long. Two stainless steel
parallel plate electrodes 12A and 12B are suspended by macor insulating
supports 13A and 13B from the upstream stainless steel reactor end plate
14. Electrodes 12A and 12B are circular with an 8.3 cm diameter, and have
a 2.3 cm electrode gap. The upper electrode 12A is powered by an ENI
(Model HF-300) 13.56 MHz rf generator 15 using a Heathkit (model 5A-2060A)
matching network 16. The lower electrode 12B, upon which the substrates
were placed, is grounded 16, and is heated by resistance (cartridge)
heaters 17. A thermocouple 18 imbedded in this electrode is used to
monitor temperature. Pressure is measured with a capacitance manometer 19,
while the system is evacuated through a liquid nitrogen cold trap 20, by a
50 cfm corrosion-resistant mechanical pump 21. Prior to venting, exhaust
gasses are scrubbed by a series of bubblers 22 filled with bleach and
water. Electronic grade hydrogen 23 (and optionally nitrogen 24) and
1,1,3,3,5,5-HMCTSZN monomer 25 are introduced axially via line 26 into the
reactor and flow is directed to the center of the electrode gap. H.sub.2
is regulated by a rotameter 27 and needle valve 28. HMCTSZN 25 is
contained in a PYREX flask 27 placed in a constant temperature mineral oil
bath 30 is maintained at about 39.degree. C., to increase monomer vapor
pressure (BP=186.0.degree. C..perspectiveto.1 atm). This reactant flows
into the reactor through a stainless steel delivery line 26 and calibrated
metering valve 31, which are heated to 50.degree. C. to prevent vapor
condensation.
Prior to deposition, a ten minute preclean of the reactor 11 is performed
using a hydrogen 23 charge to ensure minimal oxygen or water vapor
contamination on the walls. The discharge is then extinguished, and the
monomer is added. The system in reactor 11 is equilibrated at 0.3 Torr for
twenty minutes prior to the actual SiN deposition to assure constant and
steady flow rates. In all experiments performed, the reactor pressure is
between about 0.1 and 1 Torr, preferably about 0.3 Torr. Substrate
temperatures vary from between about 200.degree. C.-400.degree. C.,
preferably between about 300.degree. and 400.degree. C., while total
reactant gas flow rates are maintained at 20 sccm. The average HMCTSZN
flow rate is about 0.2 sccm unless otherwise stated, with the remainder of
the total flow being hydrogen source. Upon completion of the deposition,
all films are cooled to 100.degree. C. under nitrogen, at 1 Torr, prior to
exposure to the atmosphere. The power is between about 30 and 50 watts,
preferably about 40 watts. The power density is usually between about 0.4
and 1.2 watts per cm.sup.2 (preferably between about 0.6 and 0.9,
especially about 0.75.)
Thickness and refractive indices of the films on silicon substrates are
determined ellipsometrically with a Gaertner L116A ellipsometer.
The relative composition and bonding structure of the films is studied by
use of a Mattson Instruments, Inc., Cygnus 25 Fourier Transform Infrared
Spectrometer (FTIR). Chemical composition information is obtained by Auger
Electron Spectroscopy (AES) using a KRATOS XSAM 800 surface analysis
system.
Dielectric properties of the films are determined by capacitance-voltage
(CV) analysis of metal-insulator-semiconductor (MIS) structures. The
aluminum electrodes are 1100 microns in diameter, and CV measurements are
performed with the use of a Hewlett Packard automatic CV station at a
frequency of 1 MHz.
Hydrogen gas with the cyclic monomer greatly reduces N-H, Si-H and C-H in
the deposited film. Hydrogen does abstract --CH.sub.3, probably as
methane, but it also leaves the film as H.sub.2 gas. The resulting film
has between about 40-52% of the carbon, probably present as Si-C, and
--C-C--. The films obtained are more ceramic-like than organic-like
because of these bonds.
In FIG. 2 is shown the grph of the refractive index versus plasma power for
the reaction of cyclic monomer 1,1,3,3,5,5-HMCTSZN (0.2 sccm), with
hydrogen (19.8 sccm) at a pressure of 0.3 Torr and temperature of
300.degree. C. The higher refractive index of this film is achieved at
higher plasma power. This is interpreted to mean the film is more
inorganic (ceramic-like). Higher refractive index films show lower C-H,
N-H, and Si-H stretching bands in the infrared spectrum. The film density
at 40 W power is about 1.8 g/cm.sup.3 indicative of a ceramic-like film
structure.
FIG. 3 shows the deposition rate (Angstroms/minute) for the polysilazane
film as a function of the RF power. The other conditions are cyclic
monomer 0.20 sccm, hydrogen 19.8 sccm, pressure 0.3 Torr and a temperature
of 300.degree. C. As the power increases above 30 watts, the deposition
rate remains about 30 Angstroms/minutes.
FIG. 4 shows the refractive index of the polysilazane film versus monomer
flow rate. T=300.degree. C., P=0.3 Torr, total flow rate of hydrogen and
cyclic monomer is 20.0 sccm. To achieve a higher refractive index
indicative of an inorganic ceramic-like Si-C and SiN film, a combination
of low monomer flow rates and higher RF power is used. A plateau is
observed in flow rate (up to 0.40 for 40 W). Better polysilazane films are
produced under these conditions.
FIG. 5 is an FTIR spectrum for the polysilazane film produced with cyclic
monomer and hydrogen [0.2/19.8 sccm 0.3 Torr 300.degree. C., 40 Watts].
The film is primarily inorganic (or ceramic like). The same spectrum is
obtained after the film is exposed to 85.degree. C. saturated water vapor
atmosphere for seven days, or periods of about 1 year at 25.degree. C. and
about 50% humidity. The polysilazane film shows no signs of oxidation.
This behavior is also observed when the film is immmersed in 85.degree. C.
water (liquid) for seven days. The polysilazane films are very oxidation
resistant. The carbon present is bound in a very stable manner.
FIG. 6 is the FTIR spectrum of the polysilazane film produced at 20 Watts
of power (see FIG. 10 for the other experimental conditions). This film
has more organic-like character (more C-H, bonds), and is more easily
oxidized.
FIG. 7 shows a graph of the deposition rate for the polysilazane film
formation as a function of monomer flow rate [monomer, 0.2 sccm, hydrogen,
19.8 sccm, T=300.degree. C., P=0.3 Torr.] Clearly, at 40 W the deposition
rate is still continuing to increase whereas at 20 W, a plateau in the
rate is observed.
FIG. 8 shows a graph of the deposition rate of the polysilazane films (at
its usual) experimental conditions as a function of pressure. The
refractive index of the film appears to be independent of deposition
pressure.
FIG. 9 shows a graph of the deposition rate of the polysilazane film formed
from cyclic monomer and hydrogen (usual experimental conditions, power
constant 40 W). The deposition rate drops off as the temperature is
increased. The refractive index of the film is generally independent of
the deposition temperature.
For the hydrogen gas embodiments, the power is between about 20 and 80
Watts, density 0.37 and 1.5 Watts/cm.sup.2 (preferably 30 and 50 watts,
about 0.5 to 1.2 watts/cm.sup.2).
Films Deposited Using Cyclic Monomer with a Nitrogen Hydrogen Source
(HMCTSZN and Ammonia)
In an additional embodiment a silicon nitrogen source, such as
1,1,3,3,5,5-HMCTSZN, is polymerized in ammonia gas, usually without
nitrogen or hydrogen being present. Referring to FIG. 1, hydrogen at 23 is
replaced with electronic grade ammonia which is introduced in the same
manner as is described above for the hydrogen system. It is also possible
to use mixtures of ammonia and hydrogen, and ammonia and nitrogen.
Optionally, nitrogen at 24 may be added. The other reaction parameters and
procedures described above for the hydrogen system are essentially the
same for this ammonia system.
The dependence of film deposition rate on monomer flow rate (FIG. 10) shows
that even at very low flow rates of HMCTSZN, appre. ciable deposition
rates can still be obtained. The linear dependence observed has been noted
in the PECVD of other organosilicon monomers. In addition, FIG. 10
indicates that a decrease in HMCTSZN flow rate corresponds to a linear
increase in refractive index.
An FTIR of an as.deposited HMCTSZN/NH.sub.3 film is shown in FIG. 11 (top).
Infrared vibrational assignments are as follows: Si-CH.sub.3 (2960 and
1258 cm.sup.-1), N-H (3350 and 1165 cm.sup.-1), Si-NH.sub.2 (1540
cm.sup.-1), Si-H (2180 cm.sup.-1), and Si-N (890 cm.sup.-1). FTIR spectra
of films deposited at decreasing HMCTSZN flow rate (0.7-0.4 sccm) indicate
a decrease in the intensity of Si-CH.sub.3 vibrations. Such results are
consistent with refractive index observations shown in FIG. 10. An
Si-CH.sub.3 shoulder at 1258 cm.sup.-1 on the 1165 cm.sup.-1 N-H peak
still exists at 0.4 sccm HMCTSZN, indicating that some carbon is still
present in the films, less than about 20 atom percent, preferably less
than 10 atom percent, although the concentration is lower than in films
produced at 0.7 sccm HMCTSZN. Elimination of visible Si-CH.sub.3 stretches
occurs when HMCTSZN flow rates reach 0.2 sccm.
After exposure to air for one week (at 27.degree. C., 50 percent relative
humidity) the films produced at 0.7 sccm HMCTSZN undergo extensive
oxidation and the refractive indices (RI) drop from 1.64 to 1.54. Indeed,
aging of plasma polymerized organosilicon films having carbon present is
known to occur. In addition, FTIR spectra show a disappearance of the Si-H
peak as well as a substantial reduction in both the N-H stretch at 3350
cm.sup.-1 and the Si-N stretch (FIG. 3). The appearance of a strong peak
at 1040 cm.sup.-1 corresponding to Si-O, and a weak absorption at 1650
cm.sup.-1, that of a C.dbd.O functionality, occur as well. These results
demonstrate that as the film ages, nitrogen and hydrogen are liberated,
possibly in the form of NH.sub.3, as the film essentially converts to
silicon dioxide. This observation is also confirmed by AES studies which
indicate that little nitrogen remains after air oxidation. Films of SiN
produced at 0.4 and 0.2 sccm did not oxidize or age, at least as
determined by FTIR spectra recorded up to three months after film
deposition.
It appears that the rate at which the film is deposited plays a key role in
the ultimate concentration of carbon incorporated in the film. Carbon
seems to be primarily present in the form of CH.sub.3 substituents
attached to silicon atoms in the parent monomer structure. Although
previous studies indicate the presence of methylene (--CH.sub.2 --) groups
at 1030 cm.sup.-1, this absorption (--CH.sub.2 --) is not observed. Not
wishing to be bound by theory, it appears that the linkage of monomer ring
structures in the film is believed to be primarily formed by Si-NH-Si
bonds. Films deposited at higher deposition rates may not have adequate
time for abstraction of methyl (--CH.sub.3) substituents from the parent
monomer because new film is deposited too quickly over trapped Si-CH.sub.3
moieties. Indeed, abstraction of methyl groups by hydrogen radicals
generated in the gas phase is believed to occur in the present process.
Since the films deposited at higher deposition rates are less dense, due
in part to increased hydrogen content and to possible steric effects
associated with incorporation of Si-CH.sub.3 and Si-NH.sub.2 structures,
it theoretically should be easier for water vapor or oxygen to penetrate
the film structure and oxidize silicon and carbon atoms.
Films which are deposited at 0.2 sccm HMCTSZN and 40 W exhibit a weak
dependence of deposition rate on substrate temperature between 150.degree.
C. and 400.degree. C. Deposition rates decrease linearly from 5.5 nm/min
at 150.degree. C. to 4.1 nm/min at 400.degree. C., while refractive
indices vary from 1.69 to 1.81 over the same range of temperatures. Since
the films apparently densify with increasing substrate temperature (see
FTIR data below), the deposition rate is believed to be independent of
temperature, which is in agreement with experimental results observed for
SiN.sub.x H.sub.y deposited from SiH.sub.4 and NH.sub.3. These results can
be contrasted to the more standard organosilicon plasma polymerization
processes in which far greater temperature effects have been reported.
FTIR analyses of films deposited over this temperature range show a
substantial decrease in N-H, SiNH.sub.2, and Si-H absorption as
temperature increases as shown in FIG. 12. Lowered hydrogen content with
increased substrate temperature is consistent with the trend toward higher
refractive index as well, since films should densify at elevated
temperatures. The spectra of films deposited at 400.degree. C. (FIG. 4
top) closely resemble those of conventional PEGVD SiNxHy produced with
SiH.sub.4 and NH.sub.3. Films deposited at 150.degree. C. oxidize
substantially after three weeks of air aging, as noted by the
disappearance of the Si-H stretch and the appearance of an intense Si-O
absorption. Noticeable decreases in the N-H stretch at 3350 cm.sup.-1 and
the Si-N stretch are also observed. This behavior is similar to that of
oxidized films formed at higher monomer flowrates and again suggests the
possible liberation of NH.sub.3. Although no Si-CH.sub.3 stretches are
detected in the as-deposited film, a carbonyl stretch appears as aging
occurs; thus, some carbon is still present. According to FTIR analyses,
films of the present invention deposited at temperatures of 200.degree. C.
or greater, preferably between about 300.degree. and 400.degree. C., do
not change or age. We believe the lack of aging is because the films are
initially more dense and contain lower hydrogen and carbon content,
preferably less than 20 atom percent, and are therefore not easily
penetrated by or reactive to water vapor and oxygen.
RF power has an even greater effect on the chemical composition and
structure of bot the ammonia and hydrogen films than does substrate
temperature. A pronounced effect of power on the refractive index as seen
in FIG. 13 is observed. Films deposited over the range of 20.80 W
(preferably 5-35 W) show a nearly linear increase in refractive index with
power, but no further change occurs above 35 W. FTIR spectra indicate an
increasingly "inorganic" film structure as rf power increases. At power
levels below 35 W, a distinct absorption at 1258 cm.sup.-1 is visible
indicating the presence of Si-CH.sub.3 groups. However, at 35-50 W, this
peak for organic carbon is no longer discernable. A decrease in Si-H, N-H
(1165 and 3350 cm.sup.-1), and SiNH.sub.2 peak intensities with increasing
power is also observed. Films produced at rf powers below 35 W show aging
effects similar to those produced at low temperature (150.degree. C.).
Thus, increases in power and temperature have similar effects on film
composition and structure. Films contain low carbon and hydrogen
concentrations, preferably less than 20 atom percent, especially less than
10 atom percent, are more stable and undergo little, if any, oxidation
upon exposure to air. Increased substrate temperature is believed to cause
enhanced desorption of organic substituents during film formation as well
as increased surface mobility of reactive species, which lead to more
thermodynamically stable inorganic structures. In addition to causing more
fragmentation of gas phase reactant monomer, elevated rf power may produce
similar effects to those of elevated substrate temperature via particle
bombardment of the substrate surface. Clearly, temperature increases
caused by enhanced surface bombardment of energetic ions is known.
FIG. 13 also illustrates the dependence of deposition rate on plasma power.
As the power is increased to 20 W, an increase in deposition rate takes
place, while above this value, a nearly constant rate of about 5.2 nm/min
is maintained. The increase at the lower values is likely due to the
enhanced production of active radicals in both the gas phase and on the
surface as more extensive fragmentation of the HMCTSZN molecule takes
place due to an increase in the free electron density and electron energy
in the plasma. This trend is consistent with previous observations of
plasma polymerization.
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