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| United States Patent | 5252518 |
| Link to this page | http://www.wikipatents.com/5252518.html |
| Inventor(s) | Sandhu; Gurtej S. (Boise, ID);
Doan; Trung T. (Boise, ID) |
| Abstract | A LPCVD method for depositing a film of TiN on a semiconductor structure
includes reacting an organometallic titanium source gas such as TMAT and
organic silane as a reactive gas. The deposited film is a mixed phase of
TiN and TiSi.sub.2 and is characterized by a low contact resistance, good
step coverage and good barrier properties. The reaction is preferably
carried out in a cold wall CVD reactor at relatively low temperatures
(i.e. 200.degree. C.) and at pressures of from about 0.05 to 30 Torr. |
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Title Information  |
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| Publication Date |
October 12, 1993 |
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| Filing Date |
March 3, 1992 |
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Title Information  |
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| Market Size |
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Market Review  |
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Technical Review  |
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Claims  |
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We claim:
1. A method of forming a mixed phase TiN/TiSi.sub.x layer in the
fabrication of a semiconductor device, comprising the steps of:
a. providing a semiconductor device under fabrication;
b. placing the device in a vacuum chamber;
c. applying a stream of a titanium source gas formed of an organometallic
precursor within the vacuum chamber; and
d. applying a stream of an organic silane reactive gas within the vacuum
chamber;
such that the titanium source gas and the silane reactive gas combine and
deposit a film of mixed phase TiN+TiSi.sub.x on the semiconductor device.
2. The method as recited in claim 1 and wherein:
the organometallic precursor is tetrakisdimethyl-amino titanium (TMAT).
3. The method as recited in claim 2 and wherein:
the organic silane reactive gas is Tris(Dimethylamino)Silane (SIN).
4. The method as recited in claim 1 and further comprising:
applying a carrier inert gas at a flow rate to control a gas distribution
above the semiconductor device to control a uniformity of the deposited
film.
5. The method as recited in claim 1 and wherein:
the pressure in the vacuum chamber is between about 0.1 to 10 Torr.
6. The method as recited in claim 1 and wherein:
a temperature in the vacuum chamber is between 40.degree. C. to 500.degree.
C.
7. In semiconductor manufacture, an LPCVD method for depositing a mixed
phase TiN/TiSi.sub.2 film on a substrate comprising the steps of:
a. placing the substrate in a vacuum chamber;
b. combining an organometallic titanium source gas, a carrier gas and an
organic silane reactive gas for a time period between about 20 seconds to
about 5 minutes in the vacuum chamber to form and deposit a film of a
TiN/TiSi.sub.2 mixture on the substrate.
8. The method as recited in claim 7 and wherein:
the organometallic titanium source gas is tetrakis-dimethyl-amino titanium
(TMAT); and
the organic silane reactive gas is Tris(Dimethylamino)Silane (SIN).
9. The method as recited in claim 8 and wherein: the carrier gas is
selected from the group consisting of Hydrogen, Argon or Nitrogen.
10. The method as recited in claim 8 and wherein:
a flow rate of the TMAT is about 3 to 200 sccm;
a flow rate of the SIN is about 3 to 200 sccm; and
a flow rate of the inert carrier gas is about 10 to 5000 sccm.
11. The method as recited in claim 10 and wherein:
a pressure in the vacuum chamber is about 0.05 to 30 Torr.
12. The method as recited in claim 11 and wherein:
a temperature in the vacuum chamber is from about 40.degree. to 500.degree.
C.
13. In a semiconductor manufacturing process a LPCVD method of depositing a
mixed phase TiN/TiSi.sub.2 film on a substrate comprising the steps of:
a. placing the substrate in a vacuum chamber at a pressure of from about
0.05 to 30 Torr;
b. adjusting the temperature of the substrate to about 40.degree. C. to
350.degree. C.;
c. applying a stream of an organometallic source gas of
tetrakis-dimethyl-amino titanium (TMAT) within the vacuum chamber;
d. applying a stream of an organic silane reactive gas of
Tris(Dimethylamino)Silane (SIN) within the vacuum chamber;
e. combining the source gas and reactive gas to form a mixed phase
TiN/TiSi.sub.2 film on the substrate; and
f. controlling a uniformity of the film with a flow of carrier gas within
the vacuum chamber.
14. The method as recited in claim 13 and wherein:
the method is carried out in a cold wall CVD reactor.
15. The method as recited in claim 14 and wherein:
the stream of TMAT is about 10 sccm;
the stream of SIN is about 20 sccm; and
the stream of inert gas is about 50 sccm.
16. The method as recited in claim 15 and wherein:
the deposited film is formed mostly of TiN and a small quantity of
TiSi.sub.2.
17. The method as recited in claim 16 and wherein:
the TiN/TiSi.sub.2 film is deposited on a silicon substrate.
18. The method as recited in claim 17 and wherein:
the TiN/TiSi.sub.2 film is deposited on a SiO.sub.2 substrate. |
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Claims  |
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Description  |
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TECHNICAL FIELD
This invention relates to the formation of TiN films in semiconductor
manufacture and more particularly to a novel LPCVD process for depositing
TiN films by reacting organometallic precursors with organic silane.
BACKGROUND OF THE INVENTION
Titanium nitride (TiN) films are widely used in semiconductor manufacture.
Titanium nitride has become an integral part of advanced metallization
schemes for many ultra large scale integrated circuit (ULSI) applications.
It is used for example, as a diffusion barrier against junction spiking
for aluminum contacts to silicon. In addition, TiN serves as a glue layer
between tungsten and inter-metal dielectrics and to preserve the junction
integrity from worm hole effects during the chemical vapor deposition
(CVD) of tungsten.
Almost all of the applications utilizing TiN use physical deposition
methods such as reactive ion sputtering or nitridation of sputter
deposited titanium in nitrogen-containing gases at high temperatures. All
of these processes suffer from poor step coverage of the deposited films.
In general, TiN does not have sufficient step coverage which in some
applications can lead to unreliable, high leakage and high resistivity
contacts. This problem is magnified for ULSI applications where sub-micron
high aspect ratio contact/via holes are required.
In order to overcome this step coverage problem, CVD deposition of TiN has
also been proposed. CVD of TiN is expected to give conformal step coverage
because reactants or reactive intermediates diffuse rapidly along the
substrate surface before reacting. TiN films deposited using titanium
tetrachloride as a source gas and ammonia, hydrogen or nitrogen gas
mixtures as reactive gases have been studied and evaluated for ULSI
metallization in the past.
U.S. Pat. No. 4,977,106 to Smith discloses such a CVD process for the
deposition of TiN using titanium tetrachloride as a source gas and either
silane or SiH.sub.4 and ammonia as a reactive gas. In general, however,
the reaction temperatures with these processes have been high. It is known
that high temperature processes may have an adverse effect on the
completed semiconductor devices. In addition, the deposited films
contained small amounts of chlorine impurity which can potentially cause
corrosion related failure.
In addition to these problems deposition of TiN using a process such as
that disclosed in the Smith patent produces a single phase TiN film. Such
a film has a high contact resistance when deposited on a silicon
substrate. A separate conductive layer such as Ti must therefore be
initially deposited on the silicon substrate in the formation of
semiconductor contacts.
To solve the problems associated with high temperatures and impurities,
metal organic chemical vapor deposition (MOCVD) of TiN films using
tetrakis-dimethylamino titanium [Ti(N(CH.sub.3).sub.2).sub.4 ] (TMAT) have
been proposed recently (K. Sugijama et al, SOC, Sic. 122,1545 (1975); R.
M. Fix et al, MRS Smp. Proc. 168, 357 (1990). Such
dialkylamino-derivatives of titanium have been known since the experiments
of Bradley (Bradley et al, J. Chem. Soc., 1960, 3857) and when used as
metal organic precursors permit the deposition of high purity TiN films at
relatively low temperatures (i.e. 200.degree. C). In general with such CVD
processes for the deposition of TiN films, TMAT is used as a titanium
source gas and ammonia is utilized as a reactive gas. A problem with such
processes is that step coverage of the deposited film is poor. In
addition, as with the process previously described the contact resistance
at the TiN/Si interface is very high and a previously deposited layer of
TiSi.sub.2 is required at the contact.
There is then a need in the art for a process for conformally depositing
high purity mixed phase TiN and TiSi.sub.x films having a low contact
resistance at relatively low temperatures. Accordingly it is an object of
the present invention to provide a process for depositing high quality and
conformal mixed phase TiN/TiSi.sub.x films at low temperatures. It is a
further object of the present invention to provide such a process that is
suitable for large scale semiconductor manufacture. It is a further object
of the present invention to provide a process for depositing mixed phase
TiN/TiSi.sub.x films with metal organic chemical vapor deposition (MOCVD)
or (LPCVD) using tetrakis-dimethyl-amino titanium (TMAT) as a metal source
and organic silane as a source of Si and N. It is yet another object of
the present invention to provide a process for depositing mixed phase
TiN/TiSi.sub.x films with the deposited films characterized by a low
contact resistance, good step coverage and good barrier properties.
SUMMARY OF THE INVENTION
In accordance with the present invention a low pressure LPCVD process for
depositing mixed phase TiN/TiSi.sub.x films is provided. Briefly stated,
the process of the invention uses a metal organic precursor such as
tetrakisdimethyl-amino titanium (TMAT) as a metal source and organic
silane in the form of Tris(Dimethylamino)Silane (SIN) as a reactive gas
and as a source of Silicon and Nitrogen to deposit a mixed phase film of
TiN+TiSi.sub.2 on a substrate. The substrate, which can be in the form of
a silicon wafer, is held in a reaction chamber under a vacuum for a period
determined by the deposition rate and the film thickness desired.
The chemical reaction can be summarized as:
Ti-source+SIN .fwdarw.TiN+TiSi.sub.x +organic byproducts
The process is preferably carried out in a cold-wall reactor at
temperatures as low as 200.degree. C. and at pressures between 0.1 to 2
Torr. The deposited film will be a mixed phase of TiN and TiSi.sub.2. Only
a small fraction of the film however, will be in the form of TiSi.sub.2.
Such a film is characterized by low contact resistance, good step coverage
and good barrier properties.
Other objects, advantages, and capabilities of the present invention will
become more apparent as the description proceeds.
DESCRIPTION OF PREFERRED EMBODIMENTS
LPCVD depositions of TiN on a substrate are preferably carried out in
accordance with the invention in a cold-wall CVD reactor. The titanium
source gas is preferably a metal organic source such as
tetrakis-dimethyl-amino titanium [Ti(N(CH.sub.3).sub.2).sub.4 ] (TMAT)
Such a metal organic precursor is from a class of synthesized compounds
known in the art as dialkylamino-derivatives. TMAT is liquid at room
temperature and has a vapor pressure of 1 Torr at 60.degree. C. SIN is
liquid at room temperature and has a vapor pressure of 30 Torr at
60.degree. C.
The source gas (TMAT) and an organic silane reactive gas, such as
tris(dimethylamino) silane (SIN), are reacted to form a deposited film
that is a mixture of TiN and TiSi.sub.2. Such a mixed phase film deposited
on a silicon or SiO.sub.2 substrate can be used to form contacts having
low contact resistance and good barrier properties. Since all the
reactants are organic, deposition at low temperatures can be accomplished.
A large flow of a carrier gas controls the gas distribution above the
substrate surface and is used to control the uniformity of the films
across the wafer.
As an example, a silicon wafer is placed in the vacuum chamber of a cold
wall CVD reactor. The separate gases can then be fed into the CVD reactor
through separate inlets. Helium or other gases can be used as a carrier
gas and to regulate the uniformity of the film on the wafer surface. Mixed
phase TiN/TiSi.sub.2 films can be deposited on Si and SiO.sub.2 substrates
over a wide range of temperatures (40.degree. C.-500.degree. C.) and
pressures (0.05 to 30 Torr). In general, a deposition rate of about 40 to
1000 per minute can be obtained.
For a MOCVD precursor such as TMAT, Ti supplied by the TMAT will bond with
nitrogen supplied by the SIN to form TiN on the surface of the substrate.
At the same time a small fraction of the Ti supplied by the TMAT will bond
with silicon supplied by the SIN to form TiSi.sub.x preferably in the form
of TiSi.sub.2. The deposited film will thus be a mixture of TiN and
TiSi.sub.2. The TiSi.sub.2 component of the deposited film will provide an
electrical path between the contacts and the surface of the substrate.
With this arrangement there is no need to deposit a separate film of
TiSi.sub.2 to provide a low contact resistance as the mixed phase
TiSi.sub.2 provides this function.
In addition to TMAT as an organic source of titanium, other organometallic
precursors such as TIAZ at a flow rate of 3 to 200 sccm can also be
utilized. Other sources of organic silane at a flow rate of 3 to 200 sccm
may also be utilized in this application. Additionally other carrier gases
such as Ar and N.sub.2 may be utilized in the LPCVD deposition process of
the invention at a flow rate of 10 to 5000 sccm. Representative process
conditions are as follows:
Temperature 40.degree. C.-500.degree. C.
Pressure 0.1 to 2 Torr
Flow rate of organometallic source 10 sccm
Flow rate of organic silane 20 sccm
Flow rate of inert carrier gas 50 sccm
Deposition rate 40 to 1000 .ANG./minute
Time of deposition 20 sec to 5 minutes.
Although the invention has been described with respect to preferred
embodiments thereof, many variations and modifications will become
apparent to those skilled in the art. It is therefore the intention that
the appended claims be interpreted as broadly as possible in view of the
prior art to include all such variations and modifications.
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Description  |
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