Abstract: A microwave plasma reactor for manufacturing synthetic diamond material via chemical vapour deposition the microwave plasma reactor comprising: a microwave generator configured to generate microwaves at a frequency f; a plasma chamber comprising a base a top plate and a side wall extending from said base to said top plate defining a resonance cavity for supporting a microwave resonance mode wherein the resonance cavity has a central rotational axis of symmetry extending from the base to the top plate and wherein the top plate is mounted across said central rotational axis of symmetry; a microwave coupling configuration for feeding microwaves from the microwave generator into the plasma chamber; a gas flow system for feeding process gases into the plasma chamber and removing them therefrom; and a substrate holder disposed in the plasma chamber and comprising a supporting surface for supporting a substrate on which the synthetic diamond material is to be deposited in use; wherein the resonance cavity is configured to have a height as measured from the base to the top plate of the plasma chamber which supports a TM resonant mode between the base and the top plate at said frequency f and wherein the resonance cavity is further configured to have a diameter as measured at a height less than 50% of the height of the resonance cavity as measured from the base which satisfies the condition that a ratio of the resonance cavity height / the resonance cavity diameter is in the range 0.3 to 1.0.
A MICROWAVE PLASMA REACTOR FOR MANUFACTURING
SYNTHETIC DIAMOND MATERIAL
Field of Invention
The present invention relates to a microwave plasma reactor for manufacturing
synthetic diamond material using chemical vapour deposition techniques.
Background of Invention
Chemical vapour deposition (CVD) processes for synthesis of diamond material are
now well known in the art. Useful background information relating to the chemical
vapour deposition of diamond materials may be found in a special issue of the Journal
of Physics: Condensed Matter, Vol. 21, No. 36 (2009) which is dedicated to diamond
related technology. For example, the review article by R.S Balmer et al. gives a
comprehensive overview of CVD diamond materials, technology and applications
(see "Chemical vapour deposition synthetic diamond: materials, technology and
applications" J . Phys.: Condensed Matter, Vol. 21, No. 36 (2009) 364221).
Being in the region where diamond is metastable compared to graphite, synthesis of
diamond under CVD conditions is driven by surface kinetics and not bulk
thermodynamics. Diamond synthesis by CVD is normally performed using a small
fraction of carbon (typically <5%), typically in the form of methane although other
carbon containing gases may be utilized, in an excess of molecular hydrogen. If
molecular hydrogen is heated to temperatures in excess of 2000 K, there is a
significant dissociation to atomic hydrogen. In the presence of a suitable substrate
material, synthetic diamond material can be deposited.
Atomic hydrogen is essential to the process because it selectively etches off nondiamond
carbon from the substrate such that diamond growth can occur. Various
methods are available for heating carbon containing gas species and molecular
hydrogen in order to generate the reactive carbon containing radicals and atomic
hydrogen required for CVD diamond growth including arc-jet, hot filament, DC arc,
oxy-acetylene flame, and microwave plasma.
Methods that involve electrodes, such as DC arc plasmas, can have disadvantages due
to electrode erosion and incorporation of material into the diamond. Combustion
methods avoid the electrode erosion problem but are reliant on relatively expensive
feed gases that must be purified to levels consistent with high quality diamond
growth. Also the temperature of the flame, even when combusting oxy-acetylene
mixes, is insufficient to achieve a substantial fraction of atomic hydrogen in the gas
stream and the methods rely on concentrating the flux of gas in a localized area to
achieve reasonable growth rates. Perhaps the principal reason why combustion is not
widely used for bulk diamond growth is the cost in terms of kWh of energy that can
be extracted. Compared to electricity, high purity acetylene and oxygen are an
expensive way to generate heat. Hot filament reactors while appearing superficially
simple have the disadvantage of being restricted to use at lower gas pressures which
are required to ensure relatively effective transport of their limited quantities of
atomic hydrogen to a growth surface.
In light of the above, it has been found that microwave plasma is the most effective
method for driving CVD diamond deposition in terms of the combination of power
efficiency, growth rate, growth area, and purity of product which is obtainable.
A microwave plasma activated CVD diamond synthesis system typically comprises a
plasma reactor vessel coupled both to a supply of source gases and to a microwave
power source. The plasma reactor vessel is configured to form a resonance cavity
supporting a standing microwave. Source gases including a carbon source and
molecular hydrogen are fed into the plasma reactor vessel and can be activated by the
standing microwave to form a plasma in high field regions. If a suitable substrate is
provided in close proximity to the plasma, reactive carbon containing radicals can
diffuse from the plasma to the substrate and be deposited thereon. Atomic hydrogen
can also diffuse from the plasma to the substrate and selectively etch off non-diamond
carbon from the substrate such that diamond growth can occur.
A range of possible microwave plasma reactors for synthetic diamond film growth
using a CVD process are known in the art. Such reactors have a variety of different
designs. Common features include: a plasma chamber; a substrate holder disposed in
the plasma chamber; a microwave generator for forming the plasma; a coupling
configuration for feeding microwaves from the microwave generator into the plasma
chamber; a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and a temperature control system for controlling the
temperature of a substrate on the substrate holder.
A useful overview article by Silva et al. summarizing various possible reactor designs
is given in the previous mentioned Journal of Physics (see "Microwave engineering of
plasma-assisted CVD reactors for diamond deposition" J . Phys.: Condens. Matter,
Vol. 21, No. 36 (2009) 364202). This article identifies that from a purely
electromagnetic standpoint, there are three main design criteria: (i) the choice of the
resonant mode; (ii) the choice of the coupling structure (electric or magnetic); and (iii)
the choice of dielectric window (shape and location).
Having regard to point (i), Silva et al. identify that circular transverse magnetic (TM)
modes, and particularly TM0mn modes, are most suitable. In this notation, the first
index number (here 0) indicates that the electric field structure is axisymmetric, which
will yield a circular plasma. The indices m and n represent the number of nodes in the
electric field in the radial and axial directions, respectively. Silva et al indicate that a
number of different modes have been used in prior art reactors including: TM0n ;
TM012; TM013; TM020; TM022; TM023 ; and TM03 1.
Having regard to point (ii), Silva et al. identify that electric field (capacitive) coupling
using an antenna is the most widely used and that magnetic (inductive) coupling is
rarely used because of the limited power than can be coupled. That said, a
commercially available IPLAS reactor is disclosed as using magnetic coupling to
support a TM012 mode.
Having regard to point (iii), Silva et al. describe that an essential element associated
with both electric and magnetic coupling schemes is a dielectric window which is
generally made of quartz and delimits a reduced pressure zone inside the cavity in
which reactant gases are fed to form a plasma when excited by the electromagnetic
field. It is described that the use of a quartz window allows a user to select a single
electric field anti-node region (of maximum electric field) such that the plasma can be
ignited only in this region and the formation of parasitic plasma at other electric field
maxima within the chamber can be avoided. The quartz window is conventionally in
the form of a bell-jar placed over the substrate on which deposition is to occur and
around an electric field anti-node located adjacent the substrate. Other dielectric
window configurations are also disclosed. For example, an ASTEX reactor is
described which includes a dielectric window in the form of a plate located across the
reactor chamber approximately at the cavity mid-plane while a second-generation
ASTEX reactor is described as having a dielectric window in the form of a quartz
tube which is not directly exposed to the plasma so as to give the reactor better power
handling capabilities.
In addition, the article discloses various geometries of prior art reactor chambers
including: a cylindrical chamber such as the MSU reactor which is designed to
support a TM012 mode, the ASTEX reactor which is designed to support a TM013
mode, or LIMHP reactor designs supporting a TM023 mode or a TM022 mode; an
ellipsoidal chamber such as the AIXTRON reactor; and other non-cylindrical
chambers such as the second generation ASTEX reactor which has a central
cylindrical component purported to support a TM0n mode between the substrate
holder and a top portion of the chamber and laterally extending side lobes supporting
a TM021 mode so that the chamber as a whole supports multiple modes. The second
generation ASTEX reactor has only one Ez-field maximum in the upper part of the
central section of the chamber which is the case for a TM0n mode, but two Ez maxima
in its lower half, as expected for a TM021 mode.
Having regard to the patent literature, US6645343 (Fraunhofer) discloses an example
of a microwave plasma reactor configured for diamond film growth via a chemical
vapour deposition process. The reactor described therein comprises a cylindrical
plasma chamber with a substrate holder mounted on a base thereof. A cooling device
is provided below the substrate holder for controlling the temperature of a substrate
on the substrate holder. Furthermore, a gas inlet and a gas outlet are provided in the
base of the plasma chamber for supplying and removing process gases. A microwave
generator is coupled to the plasma chamber via a high-frequency coaxial line which is
subdivided at its delivery end above the plasma chamber and directed at the periphery
of the plasma chamber to an essentially ring-shaped microwave window in the form
of a quartz ring. The invention as described in US6645343 focuses on the ringshaped
microwave window and discloses that the coupling of microwaves in the
reactor chamber is distributed in circularly symmetric fashion over the entire ring
surface of the microwave window. It is taught that because the coupling is distributed
over a large surface, high microwave power levels can be coupled without high
electric field intensities developing at the microwave window thus reducing the
danger of window discharge.
As such, US6645343 addresses two of the three design criteria described by Silva et
al. in their Journal of Physics article discussed previously, i.e., the choice of the
coupling structure (magnetic) and the choice of dielectric window (ring-shaped
dielectric widow located around the side wall of a cylindrical reactor chamber).
US6645343 is silent as to what resonant mode the chamber should be design to
support and what design criteria should be applied to the chamber in order to best
support the desired resonance mode to achieve a uniform, stable, large area plasma
across the surface of a large area substrate/holder for achieving uniform CVD
diamond growth over large areas.
It light of the above discussion and the prior art mentioned therein, it will be evident
that it is a well known aim in the field of CVD diamond synthesis to form a uniform,
stable, large area plasma across the surface of a large area substrate/holder for
achieving uniform CVD diamond growth over large areas and that many different
plasma chamber designs and power coupling configurations have been proposed in
the art for trying to achieve this goal. However, there is an on going need to improve
upon the prior art arrangements in order to provide larger CVD growth areas, better
uniformity, higher growth rates, better reproducibility, better power efficiency and/or
lower production costs. It is an aim of certain embodiments of the present invention
to address this on going need.
Summary of Invention
According to a first embodiment of the present invention there is provided a
microwave plasma reactor for manufacturing synthetic diamond material via chemical
vapour deposition, the microwave plasma reactor comprising:
a microwave generator configured to generate microwaves at a frequency f;
a plasma chamber comprising a base, a top plate, and a side wall extending
from said base to said top plate defining a resonance cavity for supporting a
microwave resonance mode, wherein the resonance cavity has a central rotational axis
of symmetry extending from the base to the top plate, and wherein the top plate is
mounted across said central rotational axis of symmetry;
a microwave coupling configuration for feeding microwaves from the
microwave generator into the plasma chamber;
a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and
a substrate holder disposed in the plasma chamber and comprising a
supporting surface for supporting a substrate on which the synthetic diamond material
is to be deposited in use;
wherein the resonance cavity is configured to have a height, as measured from
the base to the top plate of the plasma chamber, which supports a TM0n resonant
mode between the base and the top plate at said frequency f , and
wherein the resonance cavity is further configured to have a diameter, as
measured at a height less than 50% of the height of the resonance cavity as measured
from the base, which satisfies the condition that a ratio of the resonance cavity height
/ the resonance cavity diameter is in the range 0.3 to 1.0.
According to a second embodiment of the present invention there is provided a
microwave plasma reactor for manufacturing synthetic diamond material via chemical
vapour deposition, the microwave plasma reactor comprising:
a plasma chamber comprising a base, a top plate, and a side wall extending
from said base to said top plate defining a resonance cavity for supporting a
microwave resonance mode, wherein the resonance cavity has a central rotational axis
of symmetry extending from the base to the top plate, and wherein the top plate is
mounted across said central rotational axis of symmetry;
a microwave coupling configuration for feeding microwaves from a
microwave generator into the plasma chamber;
a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and
a substrate holder disposed in the plasma chamber and comprising a
supporting surface for supporting a substrate on which the synthetic diamond material
is to be deposited in use;
wherein the resonance cavity is configured to have a height, as measured from
the base to the top plate of the plasma chamber, which supports a TM0n resonant
mode between the base and the top plate at a frequency in the range 400 to 500 MHz,
800 to 1000 MHz, or 2300 to 2600Mz, and
wherein the resonance cavity is further configured to have a diameter, as
measured at a height less than 50% of the height of the resonance cavity as measured
from the base, which satisfies the condition that a ratio of the resonance cavity height
/ the resonance cavity diameter is in the range 0.3 to 1.0.
According to a third embodiment of the present invention there is provided a method
of manufacturing synthetic diamond material using a chemical vapour deposition
process, the method comprising:
providing a microwave plasma reactor as described above;
locating a substrate over the substrate holder;
feeding microwaves into the plasma chamber;
feeding process gases into the plasma chamber; and
forming synthetic diamond material on the substrate.
Brief Description of the Drawings
For a better understanding of the present invention and to show how the same may be
carried into effect, embodiments of the present invention will now be described by
way of example only with reference to the accompanying drawings, in which:
Figure 1 shows a cross-sectional view of a microwave plasma reactor configured to
deposit synthetic diamond material using a chemical vapour deposition technique in
accordance with an embodiment of the present invention;
Figure 2 shows a cross-sectional view of another microwave plasma reactor
configured to deposit synthetic diamond material using a chemical vapour deposition
technique in accordance with an embodiment of the present invention; and
Figure 3 shows a cross-sectional view of yet another microwave plasma reactor
configured to deposit synthetic diamond material using a chemical vapour deposition
technique in accordance with an embodiment of the present invention.
Detailed Description of Certain Embodiments
The present inventors have considered a number of reactor design criteria in order to
try and achieve one or more of the following advantageous technical effects: larger
area CVD diamond growth; better CVD diamond uniformity across the growth area;
higher growth rates; better reproducibility; better power efficiency; and/or lower
production costs. The design criteria include: (1) resonance mode and chamber
geometry; (2) microwave coupling structure, dielectric window shape and location;
and (3) configurations for stabilizing the plasma formed within the reactor chamber.
These design criteria are discussed in turn below.
Resonance Mode and Chamber Geometry
Certain embodiments of the present invention are based on the seemingly counter
intuitive finding that it is advantageous to use a plasma reactor chamber having a
relatively small diameter to form a uniform, stable, large area plasma for achieving
uniform CVD diamond growth over large areas.
The present inventors have noted that large diameter chambers can support several, or
indeed many, resonance modes. It has been further noted that these modes can
interact. The present inventors consider that even a weak interaction is a problem. If a
parasitic mode exists at even a few percent of the main resonant mode it can be
sufficient to disrupt the plasma uniformity. The present inventors have found that if
the diameter of the plasma chamber is too large this can lead to poorer plasma
stability with a tendency for the plasma to 'jump'. The alternative, however, is that
the chamber diameter becomes too small and the plasma becomes compressed and
non-uniform across the substrate.
Furthermore, the present inventors consider that a cavity formed within a specific,
relatively small, diameter range allows the formation of localized higher order
axisymmetric modes at the substrate making the E-field across the substrate more
uniform without forming very intense radial E-fields at the top corners of the
substrate. It should be noted that these localized higher order axisymmetric modes
are distinct from the disruptive parasitic modes discussed previously which are
supported across the chamber as a whole and which undesirably disrupt the primary
microwave mode of the resonance cavity.
Further still, the present inventors also consider that it is advantageous to provide a
resonance cavity having a relatively low Q factor. The Q factor of a resonance cavity
is the ratio of energy stored/energy dissipated per cycle. The present inventors
consider that for CVD diamond synthesis the Q factor of the plasma chamber in use
(i.e. with plasma present in the plasma chamber) should be relatively low (e.g. less
than 1000, 500, 200, 100, 80, 50, 30, or 20). That is, the resonance cavity is weakly
resonant and is highly damped, with a high rate of energy loss. Such cavities have a
larger range of frequencies at which they will resonate and thus operate at larger
bandwidths. The Q factor may be modified by modifying the volume of the chamber
and the volume and conductivity of the plasma. A small, weakly conductive plasma
in a large cavity might be expected to have a higher Q factor than a large volume
plasma in a small cavity. Accordingly, a small cavity with a large plasma volume is
considered preferable for this additional reason. This condition can most readily be
achieved by providing a plasma chamber with a relatively small diameter (as the
height of the cavity must be selected to support a standing microwave).
The Q factor of the microwave cavity may be important for several reasons. First, the
microwave source will produce power over a spectrum of frequencies and will vary
from source to source. For the reactor to be able to operate across that range of
frequencies without any other adjustments to the matching network it is apparent that
a low Q factor can be advantageous. Secondly, the plasma itself affects the resonant
frequency and matching of the chamber from its unloaded condition as the complex
permittivity of even a weakly ionized plasma is different from that of an un-ionized
gas. Optimally, a compromise must be reached whereby the plasma can be excited in
the cavity without having to make adjustments to the matching network as it is set
during normal operation. Thirdly, a high Q cavity (and matching network) will show
a large change in phase and magnitude of reflection with frequency. This means that
the source frequency becomes critical in determining how much power is coupled into
the plasma. Changes in the frequency of the source can occur for a variety of reasons
and high Q cavities will be less tolerant of any small differences in manufacturing
tolerances.
With the above in mind, the present inventors consider that it is advantageous to use a
relatively small diameter cavity in order to provide the following beneficial technical
effects:
(i) Improve resonance mode purity within the chamber and avoid complex
interactions between numerous modes during operation over the long timescales
required for CVD diamond synthesis. For example, a small diameter
chamber can reduce the problem of slight temperature instabilities in the
CVD diamond growth surface stimulating an unwelcome higher order
mode.
(ii) A cavity formed within a specific, relatively small, diameter range is
considered to allow the formation of localized higher order axis-symmetric
modes at the substrate making the E-field across the substrate more
uniform without forming very intense radial E-fields at the top corners of
the substrate.
(iii) A small diameter cavity which has a relatively low Q factor is more easy
to start and tune, and is less sensitive to variations in microwave source
frequency.
Such a relatively small diameter cavity also helps to alleviate the problem of complex
and interacting gas convection currents forming within the chamber leading to plasma
instability. That is, the present inventors consider that a small diameter cavity
provides a more simple and easier to control system in terms of both gas flow and
microwave power within the plasma chamber such that a more uniform, stable, large
area plasma can be formed and maintained to achieve uniform CVD diamond growth
over large areas. At the same time, the diameter of the cavity should not be so small
that the plasma becomes compressed and non-uniform across the substrate.
So, the question remains as to what shape and dimensions the chamber should
actually have to fulfil the aforementioned requirements.
Having regard to the aforementioned discussion, the shape and dimensions of the
chamber will be dependent on: (i) the frequency of the microwaves; (ii) the desired
standing wave mode; and (iii) the desired Q factor for the chamber.
Having regard to microwave frequency, there are two standard frequencies of
generator used in the UK: 2450 MHz and 896 MHz (in mainland Europe, the
Americas and Asia, the lower frequency standard is 915 MHz, in Australia it is 922
MHz). Decreasing the frequency by a factor of 2.7 from 2450 MHz to 896 MHz will
allow a scale up in CVD deposition diameter of the order 2.7 for a given mode
structure. Accordingly, the lower standard frequency is preferred for larger area
deposition. The choice of other permitted bands, e.g. 433 MHz, is also possible. In
some respects, a lower frequency of, for example, 433 MHz is advantageous for
achieving even larger area CVD diamond deposition. Thus, decreasing the frequency
by a factor of 2.07 from 896 MHz to 433 MHz will allow a scale up in CVD
deposition diameter of the order of 2.07.
Having regard to the desired mode, as it is desired to create a concentration in the Ez
component of the electric field (an anti-node point) at or immediately above the
substrate to activate a plasma in this region, it is considered preferable to use a
transverse magnetic rather than a transverse electric mode as the latter cannot generate
a high electric field axisymmetrically at a conductive surface oriented transverse to
the direction of propagation.
It has been found that using a TM0n mode is advantageous as it has been found to be
the most compact (small) mode which can be practicably used in a diamond CVD
plasma reactor. A TM0n standing wave may be formed to be a half wavelength with
a node in the centre of the chamber and an anti-node at the base of the chamber over
the substrate and an anti-node at the top of the chamber. This low order mode has the
additional advantage of a large frequency separation to other modes, when compared
with the frequency separation of higher order modes, thus reducing the likelihood of
hopping between different modes. As such, the TM0n has also been found to be
advantageous in terms of mode purity and stability for this reason.
For the TM0n mode, and taking into account the previous discussion, a microwave
plasma reactor for manufacturing synthetic diamond material may comprise:
a microwave generator configured to generate microwaves at a frequency f;
a plasma chamber comprising a base, a top plate, and a side wall extending
from said base to said top plate defining a resonance cavity for supporting a
microwave resonance mode, wherein the resonance cavity has a central rotational axis
of symmetry extending from the base to the top plate, and wherein the top plate is
mounted across said central rotational axis of symmetry;
a microwave coupling configuration for feeding microwaves from the
microwave generator into the plasma chamber;
a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and
a substrate holder disposed in the plasma chamber and comprising a
supporting surface for supporting a substrate on which the synthetic diamond material
is to be deposited in use;
wherein the resonance cavity is configured to have a height, as measured from
the base to the top plate of the plasma chamber, which supports a TM0n resonant
mode between the base and the top plate at said frequency f , and
wherein the resonance cavity is further configured to have a diameter, as
measured at a height less than 50%, 40%, 30%, 20%, or 10% of the height of the
resonance cavity as measured from the base, which satisfies the condition that a ratio
of the resonance cavity height / the resonance cavity diameter is in the range 0.3 to
1.0.
Such a design has been found to be useful in creating a larger, more uniform plasma
than other configurations for CVD diamond synthesis. It has been found that using a
reactor as defined above allows a substrate of the order of 150 mm in diameter to be
covered with a uniform plasma to form very high quality, uniform CVD diamond
material over the entire area at a fast growth rate. Surprisingly, when compared to
many different, and in most cases more complex, reactor designs, the seemingly more
compact and simple design described herein has been found to be advantageous for
CVD diamond synthesis. Furthermore, the present invention is completely contrary
to the general direction taken by practitioners in this field who have moved towards
the use of larger plasma chambers, having more complex geometries in an attempt to
meet the aim of achieving high quality, uniform CVD diamond growth over larger
areas. For example, only one prior art reactor described by Silva et al. discloses the
use of a TMo mode, the second-generation ASTEX reactor. The present reactor
design is distinguished over the second-generation ASTEX reactor by two key
features: (i) the T mode is defined as being supported between the base and top
plate of the resonance cavity (rather than between a substrate table and a top plate as
in the second-generation ASTEX design); and (ii) the diameter of the resonance
cavity in at least a lower portion of the resonance cavity satisfies the condition that a
ratio of the resonance cavity height / the resonance cavity diameter is in the range 0.3
to 1.0 (this requires the diameter of the cavity to be relatively narrow in contrast to the
ASTEX design which has a very broad chamber having laterally extending portions
designed to support a TM02 i mode). As such, the ASTEX design goes completely
against the inventive concept of embodiments of the present invention which is to
form a narrow, compact resonance cavity with a TMon mode supported between a
base and top plate of the plasma chamber.
Certain embodiments of the present invention have been found to have the following
advantageous features: (i) improved resonance mode purity within the plasma
chamber thereby limiting complex, uncontrollable interactions between numerous
modes during operation over the long time-scales required for CVD diamond
synthesis; (ii) improved control of localized higher order axis-symmetric modes at the
substrate making the E-field across the substrate more uniform without forming very
intense radial E-fields at the top corners of the substrate; (iii) improved gas flow
control (e.g. the small, simple chamber design can reduce adverse convection currents
within the chamber leading to non-uniform CVD diamond growth); and (iv) improved
start-up and tuning capabilities (e.g. by providing a low Q-factor resonance cavity).
The first three points are believed to be important for achieving high quality, uniform
CVD diamond growth over large areas whereas the final point is important for
providing a robust industrial process.
Optionally, the ratio of the resonance cavity height / the resonance cavity diameter is
in the range 0.4 to 0.9 or 0.5 to 0.8. For example, the resonance cavity height as
measured from the base to the top plate of the plasma chamber may be in the range
150 mm to 300 mm, 150 mm to 250 mm, or 200 mm to 250 mm. Furthermore,
optionally the resonance cavity diameter may be in the range 200 mm to 500 mm, 250
mm to 450 mm, or 300 mm to 400 mm. These dimensions are particularly preferred
for operation at a microwave frequency in the range 800 MHz to 1000 MHz.
However, the previously discussed requirement for the resonance cavity height to
resonance cavity diameter ratio to be within the stated limitations holds for alternative
operating frequencies such as those in the range 400 MHz to 500 MHz or 2300 MHz
to 2600 MHz. Accordingly, the resonance cavity may be configured to have a height,
as measured from the base to the top plate of the plasma chamber, which supports an
approximately cylindrical TM0n resonant mode between the base and the top plate at
a frequency within ±50 MHz of the frequency f of the microwave generator. For an
operational frequency in the range 2300 MHz to 2600 MHz, the resonance cavity
height as measured from the base to the top plate of the plasma chamber may be in the
range 50 mm to 110 mm, 50 mm to 90 mm, or 70 mm to 90 mm. The resonance
cavity diameter at this operational frequency may be in the range 70 mm to 180 mm,
90 mm to 160 mm, or 110 mm to 150 mm. For an operational frequency in the range
400 MHz to 500 MHz, the resonance cavity height as measured from the base to the
top plate of the plasma chamber may be in the range 300 mm to 600 mm, 300 mm to
500 mm, or 400 mm to 500 mm. The resonance cavity diameter at this operational
frequency may be in the range 400 mm to 1000 mm, 500 mm to 900 mm, or 600 mm
to 800 mm.
According to one configuration, the resonance cavity is cylindrical. That is, the side
wall of the resonance cavity has a substantially uniform diameter over a majority (e.g.
greater than 50%, 60%, 70%, 80%, 90%, or 95%) of its height from base to top plate.
This differs considerably from the ASTEX configuration which has a widely varying
diameter leading to the possibility of complex multi-mode interactions in a lower
portion of the chamber where the substrate holder is disposed.
Alternatively, the side wall of the plasma chamber may be tapered outwardly towards
the top plate of the resonance cavity in at least an upper portion of the resonance
cavity at a height greater than 50% of the height of the resonance cavity to reduce the
strength of a high electric-field anti-node in an upper portion of the resonance cavity
in use. Again, this differs considerably from the ASTEX configuration which has a
larger diameter in a lower portion of the plasma chamber and a narrower diameter in
an upper portion of the chamber. In the present alternative arrangement, a ratio of a
lower diameter / an upper diameter of the resonance cavity may be greater than 0.4
and less than 1, wherein the lower diameter is measured at a height less than 50% of
the height of the resonance cavity and the upper diameter is measured at a height
greater than 50% of the height of the resonance cavity as measured from the base.
Optionally, the ratio may be in a range 0.5 to 0.9, 0.6 to 0.9, or 0.7 to 0.8. For
example, the lower diameter may lie in a range 200 mm to 450 mm, 250 mm to 450
mm, 300 mm to 400 mm, or 330 mm to 400 mm, and the upper diameter may lie in a
range 300 mm to 500 mm, 350 mm to 500 mm, 350 mm to 450 mm, or 400 mm to
450mm. These dimensions are particularly preferred for operation at a microwave
frequency in the range 800 MHz to 1000 MHz. For an operating frequency of 400 to
500 MHz, the lower diameter may lie in a range 400 mm to 900 mm, 500 mm to 900
mm, 600 mm to 800 mm, or 650 mm to 800 mm, and the upper diameter may lie in a
range 600 mm to 1000 mm, 700 mm to 1000 mm, 700 mm to 900 mm, or 800 mm to
900 mm. For an operating frequency of 2300 to 2600 MHz, the lower diameter may
lie in a range 70 mm to 160 mm, 90 mm to 160 mm, 100 mm to 150 mm, or 120 mm
to 150 mm, and the upper diameter may lie in a range 100 mm to 200 mm, 120 mm to
200 mm, 130 mm to 170 mm, or 150 mm to 170 mm.
The low diameter resonant cavities described above will result in a relatively large
ratio of plasma volume to chamber volume in use. The volume of the resonance
cavity may be in a range 0.002 m3 to 0.060 m3, 0.007 m3 to 0.040 m3, 0.010 m3 to
0.030 m3, or 0.015 m3 to 0.025 m3. As such, these chambers can form a low Q-factor
resonance cavity, e.g. not more than 1000, 500, 200, 100, 80, or 50 in use. These
dimensions are particularly preferred for operation at a microwave frequency in the
range 800 MHz to 1000 MHz. For an operating frequency of 400 to 500 MHz, the
volume of the resonance cavity may be in a range 0.018 m3 to 0.530 m3, 0.062 m3 to
0.350 m3, 0.089 m3 to 0.270 m3, or 0.133 m3 to 0.221 m3. For an operating frequency
of 2300 to 2600 MHz, the volume of the resonance cavity may be in a range 9.8 x 10 5
m3 to 2.9 x 10 3 m3, 3.4 x 10 4 m3 to 1.96 x 10 3 m3, 4.9 x 10 4 m3 to 1.47 x 10 3 m3, or
7.35 x l 0 4 m3 to 1.23 x l O m3.
It should be noted that while terms such as "top", "base", "upper" and lower" are used
in this specification when describing the plasma reactor, it is possible to invert the
reactor. As such, these terms refer to the location of the reactor components relative
to each other and not necessarily their location relative to the earth. For example, in
standard usage, the substrate will be supported by the base of the chamber which will
form the lower wall of the chamber relative to the earth. However, it is possible to
invert the reactor such that the base of the chamber supporting the substrate will form
the upper wall of the chamber relative to the earth. In the inverted orientation gas
flow towards the substrate may be parallel to principle thermally driven convection
currents (which are in an upwards direction due to the large amount of heat generated
in the plasma which is below the substrate in an inverted arrangement). This inverted
arrangement may have some benefits for certain applications.
In addition to the basic chamber dimensions discussed above, it has been found that
the geometry of the substrate and/or substrate holder within the resonance cavity can
affect the uniformity of the plasma formed in use. In particular, it has been found that
the uniformity of the plasma can be further improved by ensuring that the substrate
and/or substrate holder and the resonance cavity are configured to satisfy the
condition that a ratio of a resonance cavity diameter / substrate (and/or substrate
holder) diameter is in the range 1.5 to 5, 2.0 to 4.5, or 2.5 to 4.0, wherein the
resonance cavity diameter is measured at a height less than 50%, 40%, 30%, or 20%
of a height of the resonance cavity, e.g., as measured at a height of the supporting
surface of the substrate holder or as measured at the growth surface of the substrate.
For example, the substrate (or substrate holder) diameter may be in a range: 165 mm
to 415 mm, 185 mm to 375 mm, 205 mm to 375 mm, 205 mm to 330 mm, or 240 mm
to 330 mm for a microwave frequency f in the range 400 to 500 MHz; 80 mm to 200
mm, 90 mm to 180 mm, 100 mm to 180 mm, 100 mm to 160, or 115 mm to 160 mm
for a microwave frequency f in the range 800 to 1000 MHz; or 30 mm to 75 mm, 33
mm to 65 mm, 37 mm to 65 mm, 37 mm to 58 mm, or 42 mm to 58 mm for a
microwave frequency f in the range 2300 to 2600 MHz.
The aforementioned conditions assume that the substrate holder will be of a
comparable size to the substrate in use. In practice, the substrate holder can be made
with a larger diameter than the substrate to be used in a CVD diamond process. In
that case, the uniformity of the plasma over the growth surface of the substrate will be
primarily affected by the geometry of the substrate and thus the aforementioned
diameter ranges may apply to the substrate only and not the substrate holder.
It should also be noted that the substrate holder may be formed by the base of the
plasma chamber. The use of the term "substrate holder" is intended to cover such
variations. Furthermore, the substrate holder may comprise a flat supporting surface
which is the same diameter (as illustrated) or larger than the substrate. For example,
the substrate holder may form a large flat surface, formed by the chamber base or a
separate component disposed over the chamber base, and the substrate may be
carefully positioned on a central region of the flat supporting surface. In one
arrangement, the supporting surface of the substrate holder may have further
elements, for example projections or grooves, to align, and optionally hold, the
substrate. Alternatively, no such additional elements may be provided such that the
substrate holder merely provides a flat supporting surface over which the substrate is
disposed.
One potentially problem the inventors have found when using a small cavity
arrangement as described above, is that of over heating in wall components of the
chamber. As will be discussed in more detail below, it has been found to be
advantageous to provide an arrangement in which the walls of the resonance cavity
are exposed to the plasma in use, i.e. the plasma is not contained within a bell jar.
Vacuum engineers have advised that plasma reactor vessels should be manufactured
from welded stainless steel as this is the accepted material of choice for ultra-high
vacuum (UHV) chambers. However, it has been found that this creates problems with
arcing at interfaces, soot formation on hot surfaces, and generally poor heat transfer.
Furthermore, these chambers cost a large amount of money to build. Aluminium has
been found to be a better material thermally and is also easy to machine. Thus, while
stainless steel is a good material for vacuum chambers, its very poor thermal
performance makes it not well suited to use in areas where high power densities are
experienced. Materials such as aluminium, while not traditionally regarded as
suitable for high vacuum, are actually quite good for reasonably high vacuum usage
where conventional elastomer seals can be used. As such, the resonance cavity is
preferably made of aluminium or an alloy thereof which comprises at least 80%, 90%,
9 5%, or 98%o by weight of aluminium.
Microwave coupling structure, dielectric window shape and location
Instabilities in the plasma can cause the plasma to "jump" and ignite process gases at
other regions of high electric field away from the desired location immediately above
the substrate. One solution to this problem is to use a bell jar to confine the process
gases near the substrate. Because the process gases are at a significantly reduced
pressure compared to the gases outside the bell jar the breakdown voltage is reduced
such that the plasma can exist only within the bell-jar. The composition of the gas in
the bell jar can also be chosen to assist breakdown at a lower electric field. However,
using a bell jar presents its own problems. For example, silicon impurities from a
quartz bell jar can become incorporated into the CVD diamond grown using such an
arrangement leading to a degradation in product purity. Further still, bell jars tend to
over-heat at high powers leading to reduced overall service life or in extreme cases
catastrophic damage. This is at least partially due to the proximity of the plasma. A
larger bell jar which is more removed from the plasma may partially solve this
problem but such an arrangement is more prone to the effects of convection and
therefore loss of plasma stability. Indeed, the present inventors consider that the
problem of convection within the chamber (at least relatively complex and
uncontrolled convection within the chamber) leading to loss of plasma stability is also
apparent in large volume chambers which do not use a bell jar. This problem is
solved by using a small, narrow diameter TM0n cavity arrangement as previously
described.
Feeding high power microwaves into such a small, narrow diameter TM0n cavity
without a bell-jar can in itself create several problems. However, these problems can
be overcome where necessary through further modification of the chamber in terms of
how microwave power is coupled into the chamber and how the electric and magnetic
fields are manipulated within the chamber. These further modifications are discussed
below.
One problem is how to avoid plasma formation and electrical breakdown at an antinode
in the electromagnetic field away from the desired location immediately above
the substrate. This problem is partially solved by providing a relatively small, narrow
diameter TM0n cavity as previously described such that relatively few
electromagnetic anti-nodes will be present within the chamber. However, even using
this TMon cavity design, there is still a second anti-node present in an upper portion
of the chamber that is in effect a mirror image of the electric field that exists at the
substrate end of the cavity.
There are several possible ways of alleviating the problem of plasma formation and
electrical breakdown at the upper anti-node. For example, it has been found that there
is less risk of plasma formation at the upper anti-node if the microwave power is
inductively coupled, rather than capacitively coupled, into the chamber.
That said, Silva et al. identify that electric field (capacitive) coupling using an antenna
is the most widely used and that magnetic (inductive) coupling is rarely used because
of the limited power than can be coupled. The present inventors are interested in
operating at high power to achieve high CVD diamond growth rates for a
commercially useful industrial process. Accordingly, following the disclosure of
Silva et al. a skilled person would be taught to use capacitive coupling. Contrary to
this teaching, the present inventors have realized that if a relatively small, narrow
chamber design is utilized, high power densities can be achieved even when using
inductive coupling. Furthermore, by using inductive coupling the previously
described problems associated with capacitive coupling can be alleviated. As such,
the combination of inductive coupling and a small, narrow plasma chamber has been
found to be advantageous in achieving high power densities, and thus high CVD
diamond growth rates, while alleviating the problem of plasma formation at an upper
anti-node in a resonant cavity.
The question remains as to how the microwaves should be inductively coupled into
the chamber. One option is to inductively couple high power microwaves via a plate
shaped dielectric window in an upper portion of the chamber in a similar manner to
the ASTEX and LIMHP reactors discussed in the background section. However, it
has been found that such a dielectric plate is damaged by high electric field regions in
the upper central portion of the chamber in use and can lead to dielectric material
contaminating CVD diamond grown using such an arrangement. This problem can
be alleviated by feeding in microwave power through an annular dielectric window
disposed at or near an end of the cavity. Several options are possible for the
positioning of the annular window. The annular window can be positioned on an end
wall of the chamber or on a side wall. In both cases similar regions of high magnetic
field are being excited inductively. However, in contrast to the annular dielectric
window disclosed in US6645343, the present inventors have found it preferable to
position the annular window on an end wall of the chamber such that microwaves are
coupled into the chamber in a direction parallel to the central rotational axis of the
chamber.
It is considered to be advantageous to limit the area of dielectric material exposed to
the plasma in use. For example, the resonance cavity may comprise internal walls
configured to be exposed to a plasma formed within the resonance cavity in use, the
internal walls comprising metallic surfaces forming at least 75%, 80%>, 85%>, 90% or
9 5% of a total surface area of the internal walls within the resonance cavity. As
previously stated, the metallic surfaces are preferably made of aluminium. In a
particularly advantageous arrangement, the resonance cavity has a small volume and a
large proportion of the internal walls which are exposed to the plasma in use are
formed by metallic surfaces. The volume of the resonance cavity may be in a range
0.002 m3 to 0.06 m3, 0.007 m3 to 0.04 m3, 0.01 m3 to 0.03 m3, or 0.015 m3 to 0.025
m3. These dimensions are particularly preferred for operation at a microwave
frequency in the range 800 MHz to 1000 MHz. Again, these dimensions may be
scaled according to the operating frequency. For example, for operation at a
microwave frequency in the range 400 MHz to 500 MHz the values may be scaled by
a factor of 2.073 and for operation at a microwave frequency in the range 2300 MHz
to 2600 MHz the values may be scaled by a factor of 0.3 663. As such, at a microwave
frequency f in the range 400 to 500 MHz the resonance cavity may have a volume in a
range 0.018 m3 to 0.530 m3, 0.062 m3 to 0.350 m3, 0.089 m3 to 0.270 m3, or 0.133 m3
to 0.221 m3. At a microwave frequency f in the range 2300 to 2600 MHz the
resonance cavity may have a volume in a range 9.8 x 10 5 m3 to 2.9 x 10 3 m3, 3.4 x
10 4 m3 to 1.96 x 10 3 m3, 4.9 x 10 4 m3 to 1.47 x 10 3 m3, or 7.35 x 10 4 m3 to 1.23 x
I ) 3 m3.
A relatively small portion of the internal walls may be formed by dielectric material
for inductively coupling microwaves into the resonance cavity. A particularly
advantageous arrangement comprises an annular dielectric window, formed in one or
several sections, the annular dielectric window forming no more than 25%, 20%,
15% , 10% , or 5% of the total surface area of the internal walls within the resonance
cavity.
Configurations for stabilizing the plasma formed within the reactor chamber
Even when inductive coupling is used, there is still a risk of plasma formation in the
upper part of the chamber. One way to further alleviate this problem is to provide an
arrangement which at least partially eliminates the high electric field anti-node in the
upper portion of the chamber without unduly affecting the high electric field region in
the lower portion of the chamber. One way to achieve this is to provide an
electrically conductive surface which extends into the chamber and over the upper
anti-node. The electrically conductive surface may form a bowl of uniform curvature,
a pointed cone, or any intermediate conical structure. A conical surface having a
rounded tip is preferred. In one preferred arrangement, the conical surface is
configured to be approximately orthogonal to the electric field vector of the resonance
mode of the cavity thereby minimizing perturbations in the electric field as a result of
the introduction of the conical surface into the resonance cavity. That is, it is possible
to eliminate the anti-node without affecting the basic TM0n electric field profile in the
lower part of the chamber by placing a conductive metal surface approximately
orthogonal to the electric field in the region of the upper high electric field anti-node
to effectively eliminate the upper high electric field region. While the resonant
frequency of the chamber should not be unduly altered, the Q factor will reduce due to
a reduction in the stored energy in the cavity while the energy dissipated per cycle
remains the same.
The electrically conductive surface can extend up to one quarter guided wavelength
and may extend from the driven or non-driven end of the plasma chamber. By
"driven-end", we mean the end where the microwaves are coupled into the chamber.
An alternative possibility is to place the electrically conductive surface at the nondriven
end resulting in an arrangement where the microwave window is positioned
around the substrate although this arrangement could lead to damage of the dielectric
window.
In light of the above, one configuration comprises a cone-shaped electrically
conductive member extending into the resonance cavity to at least partially eliminate
a high electric field anti-node in the resonance cavity in use as compared with an
equivalent resonance cavity without the cone-shaped electrically conductive member
present. The cone-shaped electrically conductive member may be supported by the
base or the top plate of the plasma chamber and is oriented such that a tip of the coneshaped
electrically conductive member lies on the central rotational axis of symmetry
of the resonance cavity. For example, the substrate holder may be supported by the
base of the plasma chamber and the cone-shaped electrically conductive member can
be supported by the top plate of the plasma chamber. In one particularly useful
arrangement, the cone-shaped electrically conductive member forms an annular recess
within the resonance cavity and the previously described annular dielectric window
may be disposed within the annular recess. This arrangement is useful to prevent
damage of the dielectric window in use.
The electrically conductive surface as described above is useful in providing a plasma
chamber which effectively only has one primary electric field anti-node. That is, an
electrically conductive surface can be provided which extends into the chamber to
mask off all other primary electric field anti-nodes except the one located adjacent the
growth surface of the substrate in use to improve mode purity and alleviate the
problem of plasma formation away from the area of interest at the growth surface of
the substrate. Such a single anti-node chamber is considered to be advantageous for
manufacturing high quality synthetic diamond material over large areas. In this
regard, it should be noted that the chamber may still comprise localized modes as a
result of the presence of the substrate within the chamber. However, the resonance
cavity can be designed so that only one primary electric field anti-node is supported
by the walls of the chamber.
An alternative to the use of a cone-shaped electrically conductive surface to eliminate
the high electric field region in the upper portion of the chamber is to provide a
plasma chamber in which an upper portion of the resonance cavity has a larger
diameter than a lower portion of the resonance cavity, the upper portion of the
resonance cavity being configured to reduce a high electric-field anti-node in the
upper portion of the resonance cavity in use. For example, the side wall of the
chamber may be outwardly tapered in an upper portion of the chamber so as to reduce
the upper anti-node of a TM0n mode. The reduction in the Ez component of the Efield
is sufficient to prevent breakdown occurring in this region. Such a taper may run
from the base of the chamber or may initiate part way up the chamber wall with a
lower portion of the chamber remaining cylindrical. Alternatively still, a step may be
provided in the side wall of the chamber to provide a broader upper portion. These
arrangements also have the benefit of decreasing the power density in the upper
portion of the chamber which alleviates the problem of plasma formation in the upper
portion of the chamber. Accordingly, providing a broader upper portion to the plasma
chamber has the effect of reducing the electric field in the upper portion of the
chamber.
As an alternative, or in addition to the above, use of a gas inlet which is oriented to
inject process gas from the top plate towards the growth surface of the substrate can
aid in pushing the plasma down towards the substrate and prevent plasma jumping
into an upper region of the chamber.
In light of the above, it is considered that the desired chamber design may fulfil the
following design parameters:
(i) A small, narrow chamber designed to support a TM0n resonance mode between a
base and a top plate of the chamber is advantageous.
(ii) The microwave power may be inductively coupled into the chamber via a ring
shaped dielectric window. Preferably the ring-shaped dielectric window is positioned
on an end wall of the plasma chamber such that microwaves are coupled into the
plasma chamber in a direction substantially parallel to the axis of the plasma chamber.
(iii) The chamber may be configured to at least partially cancel a large electric field
anti-node in an upper portion of the chamber. This may be achieved using an
electrically conductive cone-shaped surface or alternatively by broadening the
diameter of the upper portion of the chamber to support a cancelling mode in an upper
portion of the chamber. An axially disposed gas inlet can also aid in preventing
plasma jumping to the upper anti-node. As such, the cone or taper may not be
essential if axially oriented gas flow is utilized.
One useful arrangement is to combine the features of a ring-shaped microwave
window and a centrally disposed cone. Another useful combination is a ring-shaped
microwave window and an axially disposed gas inlet. Yet a further useful
combination is the provision of all three of the aforementioned features, i.e. a ringshaped
microwave window, a centrally disposed cone, and an axially disposed gas
inlet.
Embodiments of the present invention provide a plasma reactor chamber which is
capable of forming a uniform, stable, large area plasma for achieving uniform CVD
diamond growth over large areas.
Examples
Figures 1 shows an example of a microwave plasma reactor as described herein. As
can be seen by reference to Figures 1, the microwave plasma reactors comprise the
following basic components: a plasma chamber 2; a substrate holder 4 disposed in the
plasma chamber for holding a substrate 5; a microwave generator 6, for forming a
plasma 8 within the plasma chamber 2; a microwave coupling configuration 10 for
feeding microwaves from the microwave generator 6 into the plasma chamber 2; and
a gas flow system comprising a gas inlet 12 and a gas outlet 14 for feeding process
gases into the plasma chamber 2 and removing them therefrom.
The microwave coupling configuration 10 comprises a coaxial line comprising an
inner conductor 16 and outer conductor 18. The coaxial line is configured to transmit
microwaves from the microwave generator 6 to an annular dielectric window 20. The
dielectric window 20 is made of a microwave permeable material such as quartz. It
forms a vacuum-tight annular window in a top portion of the plasma chamber 2 . The
microwave generator 6 and the microwave coupling configuration 10 are configured
to generate a suitable wavelength of microwaves and inductively couple the
microwaves into the plasma chamber 2 to form a standing wave within the plasma
chamber 2 having a high energy node located just above the substrate 5 in use. A top
plate 22 comprises one or more waveguides to transmit microwaves from the coaxial
line through the dielectric window 20.
The dimensions of the plasma chamber 2, the microwave wavelength, and the position
of the top plate 24 are selected to generate a TM0n standing wave within the plasma
chamber between the base of the chamber 24 and the top plate 22. The height h
between the base 24 and the top plate 22 and the diameter d of the chamber are
selected to have a ratio as previously defined.
The plasma chamber forms a tight microwave cavity with solid metal walls,
preferably aluminium, which are exposed to the plasma in use. The walls of the
plasma chamber may be fluid or gas cooled (e.g. water cooled) to enable higher power
operation. This aids in removing the requirement for a bell jar to constrain the
reactive species, allowing higher powers while also improving material purity.
Figure 2 shows a modified version of the plasma reactor illustrated in Figure 1. In
this modified arrangement an electrically conductive cone-shaped member 34 is
mounted to the top plate 22 and extends into the plasma chamber. The electrically
conductive cone-shaped member 34 is configured to effectively mask the high electric
field anti-node of the TM0n mode in an upper portion of the plasma chamber without
unduly affecting the high electric field anti-node of the TM0n mode in a lower portion
of the plasma chamber.
Figure 3 shows yet another alternative. In the illustrated arrangement the upper
portion of the plasma chamber has a larger diameter d2 than that of the lower portion
of the plasma chamber d} . The ratio of d} / d2 is selected to meet the design criteria
as previously described. The upper diameter d2 can be selected to support a
secondary microwave mode which at least partially cancels the high electric field antinode
of the TMon mode in an upper portion of the plasma chamber.
Embodiments of the present invention improve uniformity in a CVD diamond growth
process. Improvement in uniformity can be measured by one or more of the
following parameters: thickness uniformity or a CVD diamond film (across the
deposition area); uniformity of one or more quality parameters of the diamond
material (e.g. colour, optical properties, electronic properties, nitrogen uptake, boron
uptake, and/or boron activation level); in polycrystalline diamond material, uniformity
of texture, surface morphology, grain size, etc . ; or in single crystal diamond
material where growth takes place on an array of single crystal diamond substrates on
a substrate carrier, uniformity of thickness, morphology, edge twinning, lateral
growth, etc ., between each single crystal. The key parameters chosen for assessing
uniformity depend on the synthesis process, the economics of fabricating the final
product from the synthesis product, and the requirements of the final product itself.
While this invention has been particularly shown and described with reference to
preferred embodiments, it will be understood to those skilled in the art that various
changes in form and detail may be made without departing from the scope of the
invention as defined by the appendant claims.
Claims
1. A microwave plasma reactor for manufacturing synthetic diamond material
via chemical vapour deposition, the microwave plasma reactor comprising:
a microwave generator configured to generate microwaves at a frequency f ;
a plasma chamber comprising a base, a top plate, and a side wall extending
from said base to said top plate defining a resonance cavity for supporting a
microwave resonance mode, wherein the resonance cavity has a central rotational axis
of symmetry extending from the base to the top plate, and wherein the top plate is
mounted across said central rotational axis of symmetry;
a microwave coupling configuration for feeding microwaves from the
microwave generator into the plasma chamber;
a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and
a substrate holder disposed in the plasma chamber and comprising a
supporting surface for supporting a substrate on which the synthetic diamond material
is to be deposited in use;
wherein the resonance cavity is configured to have a height, as measured from
the base to the top plate of the plasma chamber, which supports a TM0n resonant
mode between the base and the top plate at said frequency f, and
wherein the resonance cavity is further configured to have a diameter, as
measured at a height less than 50% of the height of the resonance cavity as measured
from the base, which satisfies the condition that a ratio of the resonance cavity height
/ the resonance cavity diameter is in the range 0.3 to 1.0.
2 . A microwave plasma reactor according to any preceding claim, wherein the
height of the resonance cavity as measured from the base is selected to support a
TMon resonant mode at a microwave frequency f in the range 400 MHz to 500 MHz,
800 MHz to 1000 MHz, or 2300 MHz to 2600 MHz.
3 . A microwave plasma reactor according to claim 1 or 2, wherein the ratio of
the resonance cavity height / the resonance cavity diameter is in the range 0.4 to 0.9 or
0.5 to 0.8.
4 . A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity height, as measured from the base to the top plate of the plasma
chamber, is in a range:
300 mm to 600 mm, 300 mm to 500 mm, or 400 mm to 500 mm at a
microwave frequency f in the range 400 MHz to 500 MHz;
150 mm to 300 mm, 150 mm to 250 mm, or 200 mm to 250 mm at a
microwave frequency f in the range 800 MHz to 1000 MHz; or
50 mm to 110 mm, 50 mm to 90 mm, or 70 mm to 90 mm at a microwave
frequency fin the range 2300 MHz to 2600 MHz.
5 . A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity diameter is in the range:
400 mm to 1000 mm, 500 mm to 900 mm, or 600 mm to 800 mm at a
microwave frequency f in the range 400 MHz to 500 MHz;
200 mm to 500 mm, 250 mm to 450 mm, or 300 mm to 400 mm at a
microwave frequency f in the range 800 MHz to 1000 MHz; or
70 mm to 180 mm, 90 mm to 160 mm, or 110 mm to 150 mm at a microwave
frequency fin the range 2300 MHz to 2600 MHz.
6 . A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity has a volume in a range:
0.018 m3 to 0.530 m3, 0.062 m3 to 0.350 m3, 0.089 m3 to 0.270 m3, or 0.133
m3 to 0.221 m3 at a microwave frequency f in the range 400 to 500 MHz;
0.002 m3 to 0.06 m3, 0.007 m3 to 0.04 m3, 0.01 m3 to 0.03 m3, or 0.015 m3 to
0.025 m3 at a microwave frequency f in the range 800 MHz to 1000 MHz; or
9.8 x 10 5 m3 to 2.9 x 10 3 m3, 3.4 x 10 4 m3 to 1.96 x 10 3 m3, 4.9 x 10 4 m3 to
1.47 x 10 3 m3, or 7 .35 x 10 4 m3 to 1.23 x 10 3 m3 at a microwave frequency f in the
range 2300 to 2600 MHz.
7 . A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity is cylindrical.
8 . A microwave plasma reactor according to any one of claims 1 to 6, wherein an
upper portion of the resonance cavity has a larger diameter than a lower portion of the
resonance cavity, the upper portion of the resonance cavity being configured to
support at least one secondary microwave mode which at least partially eliminates a
high electric-field anti-node in the upper portion of the resonance cavity in use.
9 . A microwave plasma reactor according to claim 8, wherein a ratio of a lower
diameter / an upper diameter of the resonance cavity is greater than 0.4 and less than
1, wherein the lower diameter is measured at a height less than 50% of the height of
the resonance cavity as measured from the base and the upper diameter is measured at
a height greater than 50% of the height of the resonance cavity as measured from the
base.
10. A microwave plasma reactor according to claim 9, wherein said ratio is in a
range 0.5 to 0.9, 0.6 to 0.9, or 0.7 to 0.8.
11. A microwave plasma reactor according to claim 9 or 10, wherein:
at a microwave frequency f in the range 400 to 500 MHz the lower diameter
lies in a range 400 mm to 900 mm, 500 mm to 900 mm, 600 mm to 800 mm, or 650
mm to 800 mm, and the upper diameter may lie in a range 600 mm to 1000 mm, 700
mm to 1000 mm, 700 mm to 900 mm, or 800 mm to 900 mm;
at a microwave frequency f in the range 800 MHz to 1000 MHz the lower
diameter lies in a range 200 mm to 450 mm, 250 mm to 450 mm, 300 mm to 400 mm,
or 330 mm to 400 mm, and the upper diameter lies in a range 300 mm to 500 mm,
350 mm to 500 mm, 350 mm to 450 mm, or 400 mm to 450mm; or
at a microwave frequency f in the range 2300 to 2600 MHz the lower diameter
lies in a range 70 mm to 160 mm, 90 mm to 160 mm, 100 mm to 150 mm, or 120 mm
to 150 mm, and the upper diameter may lie in a range 100 mm to 200 mm, 120 mm to
200 mm, 130 mm to 170 mm, or 150 mm to 170 mm.
12. A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity comprises internal walls configured to be exposed to a plasma
formed within the resonance cavity in use, said internal walls comprising metallic
surfaces forming at least 75%, 80%>, 85%>, 90% or 95% of a total surface area of said
internal walls within the resonance cavity.
13. A microwave plasma reactor according to claim 12, wherein said metallic
surfaces are made of aluminium or an alloy thereof comprising at least 80%, 90%,
9 5%, or 9 8% by weight of aluminium.
14. A microwave plasma reactor according to claim 12 or 13, wherein a portion of
said internal walls is formed by an annular dielectric window, formed in one or
several sections, said annular dielectric window forming no more than 25%, 20%,
15% , 10% , or 5% of the total surface area of the internal walls within the resonance
cavity.
15. A microwave plasma reactor according to any preceding claim, wherein the
microwave plasma reactor further comprises an electrically conductive surface
located within the plasma chamber over a high electric field anti-node region which
would exist in a corresponding plasma chamber which did not comprise the
conductive surface.
16. A microwave plasma reactor according to claim 15, wherein the conductive
surface is cone-shaped.
17. A microwave plasma reactor according to claim 16, wherein the cone-shaped
conductive surface comprises a rounded tip.
18. A microwave plasma reactor according to claim 16 or 17, wherein the coneshaped
conductive surface forms an annular recess in the plasma chamber and an
annular dielectric window is disposed in said recess.
19. A microwave plasma reactor according to any preceding claim, wherein the
resonance cavity is configured to have a Q factor not more than 1000, 500, 200, 100,
80, 50, 30, or 20 in use.
20. A microwave plasma reactor according to any preceding claim, wherein the
microwave coupling configuration is arranged to inductively couple microwaves into
the plasma chamber.
21. A microwave plasma reactor according to any preceding claim, wherein the
gas flow system comprises one or more inlet nozzles disposed opposite the substrate
holder for injecting process gas towards the substrate in use.
22. A microwave plasma reactor for manufacturing synthetic diamond material
via chemical vapour deposition, the microwave plasma reactor comprising:
a plasma chamber comprising a base, a top plate, and a side wall extending
from said base to said top plate defining a resonance cavity for supporting a
microwave resonance mode, wherein the resonance cavity has a central rotational axis
of symmetry extending from the base to the top plate, and wherein the top plate is
mounted across said central rotational axis of symmetry;
a microwave coupling configuration for feeding microwaves from a
microwave generator into the plasma chamber;
a gas flow system for feeding process gases into the plasma chamber and
removing them therefrom; and
a substrate holder disposed in the plasma chamber and comprising a
supporting surface for supporting a substrate on which the synthetic diamond material
is to be deposited in use;
wherein the resonance cavity is configured to have a height, as measured from
the base to the top plate of the plasma chamber, which supports a TM0n resonant
mode between the base and the top plate at a frequency in the range 400 to 500 MHz,
800 to 1000 MHz, or 2300 MHz to 2600Mz, and
wherein the resonance cavity is further configured to have a diameter, as
measured at a height less than 50% of the height of the resonance cavity as measured
from the base, which satisfies the condition that a ratio of the resonance cavity height
/ the resonance cavity diameter is in the range 0.3 to 1.0.
23. A method of manufacturing synthetic diamond material using a chemical
vapour deposition process, the method comprising:
providing a microwave plasma reactor according to any preceding claim;
locating a substrate over the substrate holder;
feeding microwaves into the plasma chamber;
feeding process gases into the plasma chamber; and
forming synthetic diamond material on the substrate.
24. A method according to claim 23, wherein a ratio of a resonance cavity
diameter / substrate diameter is in the range 1.5 to 5, 2.0 to 4.5, or 2.5 to 4.0, wherein
the resonance cavity diameter is measured at a height less than 50%, 40%, 30%, or
2 0% of a height of the resonance cavity.
25. A method according to claim 24, wherein the substrate diameter is in the
range:
165 mm to 415 mm, 185 mm to 375 mm, 205 mm to 375 mm, 205 mm to 330
mm, or 240 mm to 330 mm for a microwave frequency f in the range 400 to 500
MHz;
80 mm to 200 mm, 90 mm to 180 mm, 100 mm to 180 mm, 100 mm to 160, or
115 mm to 160 mm for a microwave frequency f in the range 800 to 1000 MHz; or
30 mm to 75 mm, 33 mm to 65 mm, 37 mm to 65 mm, 37 mm to 58 mm, or
42 mm to 58 mm for a microwave frequency f in the range 2300 to 2600 MHz.
26. A method according to any one of claims 23 to 25, wherein the microwave
plasma reactor is inverted whereby a base of the plasma chamber supporting the
substrate forms an upper wall of the plasma chamber relative to earth.
| # | Name | Date |
|---|---|---|
| 1 | 5424-DELNP-2013-RELEVANT DOCUMENTS [07-08-2023(online)].pdf | 2023-08-07 |
| 1 | IB304.pdf | 2013-07-05 |
| 2 | 5424-DELNP-2013-RELEVANT DOCUMENTS [13-10-2022(online)].pdf | 2022-10-13 |
| 2 | FORM-3.pdf | 2013-07-05 |
| 3 | 5424-DELNP-2013-RELEVANT DOCUMENTS [17-05-2021(online)].pdf | 2021-05-17 |
| 3 | 5424-delnp-2013-Form-13-(18-09-2013).pdf | 2013-09-18 |
| 4 | 5424-DELNP-2013-RELEVANT DOCUMENTS [26-03-2020(online)].pdf | 2020-03-26 |
| 4 | 5424-delnp-2013-Correspondence Others-(18-09-2013).pdf | 2013-09-18 |
| 5 | 5424-DELNP-2013-RELEVANT DOCUMENTS [28-02-2019(online)].pdf | 2019-02-28 |
| 5 | 5424-delnp-2013-Claims-(18-09-2013).pdf | 2013-09-18 |
| 6 | 5424-DELNP-2013-IntimationOfGrant21-03-2018.pdf | 2018-03-21 |
| 6 | 5424-delnp-2013-1-GPA-(18-09-2013).pdf | 2013-09-18 |
| 7 | 5424-DELNP-2013-PatentCertificate21-03-2018.pdf | 2018-03-21 |
| 7 | 5424-delnp-2013-1-Correspondence Others-(18-09-2013).pdf | 2013-09-18 |
| 8 | 5424-DELNP-2013.pdf | 2013-09-30 |
| 8 | 5424-DELNP-2013-ABSTRACT [05-03-2018(online)].pdf | 2018-03-05 |
| 9 | 5424-DELNP-2013-CLAIMS [05-03-2018(online)].pdf | 2018-03-05 |
| 9 | 5424-delnp-2013-Form-3-(10-12-2013).pdf | 2013-12-10 |
| 10 | 5424-DELNP-2013-COMPLETE SPECIFICATION [05-03-2018(online)].pdf | 2018-03-05 |
| 10 | 5424-delnp-2013-Correspondence Others-(10-12-2013).pdf | 2013-12-10 |
| 11 | 5424-delnp-2013-Correspondence Others-(18-12-2013).pdf | 2013-12-18 |
| 11 | 5424-DELNP-2013-FER_SER_REPLY [05-03-2018(online)].pdf | 2018-03-05 |
| 12 | 5424-delnp-2013-Assignment-(18-12-2013).pdf | 2013-12-18 |
| 12 | 5424-DELNP-2013-OTHERS [05-03-2018(online)].pdf | 2018-03-05 |
| 13 | 5424-DELNP-2013-FER.pdf | 2017-09-06 |
| 13 | 5424-DELNP-2013-FORM 3 [01-03-2018(online)].pdf | 2018-03-01 |
| 14 | 5424-DELNP-2013-Information under section 8(2) (MANDATORY) [01-03-2018(online)].pdf | 2018-03-01 |
| 15 | 5424-DELNP-2013-FER.pdf | 2017-09-06 |
| 15 | 5424-DELNP-2013-FORM 3 [01-03-2018(online)].pdf | 2018-03-01 |
| 16 | 5424-delnp-2013-Assignment-(18-12-2013).pdf | 2013-12-18 |
| 16 | 5424-DELNP-2013-OTHERS [05-03-2018(online)].pdf | 2018-03-05 |
| 17 | 5424-DELNP-2013-FER_SER_REPLY [05-03-2018(online)].pdf | 2018-03-05 |
| 17 | 5424-delnp-2013-Correspondence Others-(18-12-2013).pdf | 2013-12-18 |
| 18 | 5424-delnp-2013-Correspondence Others-(10-12-2013).pdf | 2013-12-10 |
| 18 | 5424-DELNP-2013-COMPLETE SPECIFICATION [05-03-2018(online)].pdf | 2018-03-05 |
| 19 | 5424-DELNP-2013-CLAIMS [05-03-2018(online)].pdf | 2018-03-05 |
| 19 | 5424-delnp-2013-Form-3-(10-12-2013).pdf | 2013-12-10 |
| 20 | 5424-DELNP-2013-ABSTRACT [05-03-2018(online)].pdf | 2018-03-05 |
| 20 | 5424-DELNP-2013.pdf | 2013-09-30 |
| 21 | 5424-delnp-2013-1-Correspondence Others-(18-09-2013).pdf | 2013-09-18 |
| 21 | 5424-DELNP-2013-PatentCertificate21-03-2018.pdf | 2018-03-21 |
| 22 | 5424-delnp-2013-1-GPA-(18-09-2013).pdf | 2013-09-18 |
| 22 | 5424-DELNP-2013-IntimationOfGrant21-03-2018.pdf | 2018-03-21 |
| 23 | 5424-delnp-2013-Claims-(18-09-2013).pdf | 2013-09-18 |
| 23 | 5424-DELNP-2013-RELEVANT DOCUMENTS [28-02-2019(online)].pdf | 2019-02-28 |
| 24 | 5424-delnp-2013-Correspondence Others-(18-09-2013).pdf | 2013-09-18 |
| 24 | 5424-DELNP-2013-RELEVANT DOCUMENTS [26-03-2020(online)].pdf | 2020-03-26 |
| 25 | 5424-DELNP-2013-RELEVANT DOCUMENTS [17-05-2021(online)].pdf | 2021-05-17 |
| 25 | 5424-delnp-2013-Form-13-(18-09-2013).pdf | 2013-09-18 |
| 26 | FORM-3.pdf | 2013-07-05 |
| 26 | 5424-DELNP-2013-RELEVANT DOCUMENTS [13-10-2022(online)].pdf | 2022-10-13 |
| 27 | IB304.pdf | 2013-07-05 |
| 27 | 5424-DELNP-2013-RELEVANT DOCUMENTS [07-08-2023(online)].pdf | 2023-08-07 |
| 1 | 5424_05-09-2017.pdf |