The present invention relates to an atomic layer deposition reaction chamber and more particularly to a reaction chamber according to preamble of claim 1. The present invention further relates to an atomic layer deposition reactor and more particularly to a reactor according to preamble of claim 12.
The atomic layer deposition (ALD) process and one ALD cycle consist of four gas exchanges to produce one monolayer. Therefore, ALD cycle time is a limiting factor for the growth rate. Further the cycle time is depending on how fast pulse chemistry can be distributed on a substrate surface and how fast the residual gases are purged from the surface. For good gas exchange and good quality, a uniform gas flow across the substrate surface should be achieved. If gas flow across the substrate is ununiform, it means that the gas flow is different at different parts of the substrate surface. Due to ununiform gas flow the gas doses during one ALD cycle need to be increased and the cycle time and residence time of the gas in the reaction chamber need to be increased. This causes slow process times and decrease in efficiency and also poor material efficiency.
In the prior art reaction chamber and ALD rectors, a uniform gas flow, short cycle time and good material efficiency are compromised. This is especially the case when round shape substrates, such as silicon wafers, are processed. When round shaped substrates processed, gases are exchanged more easily near the edges of the round substrate surface than in the middle of the round substrate
In the prior art reaction chamber 20, as in
The bypass effect of the prior art reaction chambers 20 causes poor precursor gas economy as large proportion of the precursor molecules bypass the substrate surface to be coated and flow directly into the gas outlet 40. Thus, an under dose of precursor gases occurs in the middle parts of the reaction chamber 20 due to the fact that only a small proportion of precursor molecules follow the flow path B. The under dose causes further uniformity issues on the substrate surface and in the coating provided on the substrate surface. When the under dose in the middle parts of the reaction chamber 20 is compensated with high overdose of supplied precursors to the reaction chamber 20, purging the reaction chamber 20 takes longer time as there are precursor molecules to be purged. Thus, the ALD cycle time is prolonged and efficiency of the process is compromised as well as material efficiency.
An object of the present invention is to provide an atomic layer deposition reaction chamber and an atomic layer deposition reactor so as to solve or at least alleviate the prior art disadvantages.
The objects of the invention are achieved by an atomic layer deposition reaction chamber which is characterized by what is stated in the independent claim 1. The objects of the invention are further achieved by an atomic layer deposition reactor which is characterized by what is stated in the independent claim 12.
The preferred embodiments of the invention are disclosed in the dependent claims.
The invention is based on the idea of providing an atomic layer deposition reaction chamber comprising a first end, a second end opposite the first end, and a longitudinal central axis extending between the first end and the second end and a length between the first end and the second end in the direction of the longitudinal central axis. The reaction chamber further comprises a first side wall extending between the first end and the second end, and a second side wall opposite the first side wall and extending between the first end and the second end, the first side wall and the second side wall defining width of the reaction chamber between the first end and the second end, and the reaction chamber having a width central axis extending between the first side wall and the second side wall and perpendicularly to the longitudinal central axis. The reaction chamber also comprises a gas inlet for supplying gases into the reaction chamber and a gas outlet for discharging gases from the reaction chamber. The gas inlet and the gas outlet are provided spaced apart along the longitudinal central axis of the reaction chamber.
According to the present invention, the reaction chamber has an increasing width along the longitudinal central axis in the direction from the first end towards the width central axis. The reaction chamber also has a decreasing width along the longitudinal central axis in the direction from the width central axis towards the second end. The length of the reaction chamber is greater than the width of the reaction chamber along the width central axis.
The reaction chamber having increasing width and decreasing width in the direction between the first end and the second end enables arranging the side walls at a very short distance from the substrate. Further, the increasing and decreasing width is enables arranging the side walls of the reaction chamber partly follow the outer edges of round substrates. Furthermore, the oval or oval-like shape provided by the greater length than the width enables forming sufficient distance between the gas inlet from the substrates in the direction of the first and second end such that precursor gas molecules have adequate time and space to spread before meeting the substrates. Thus, the bypass effect is minimized.
In one embodiment, the reaction chamber has the increasing width along the longitudinal central axis from the first end to the width central axis and the decreasing width along the longitudinal central axis from the width central axis to the second end.
Therefore, the width of the reaction chamber increases from the first end to the width central axis and the decreases from the width central axis to the second end. This provides efficient gas flow and minimal bypass effect.
In another embodiment, the reaction chamber comprises an increasing width area between the first end and the width central axis, the increasing width area extending from the first end to the width central axis and having the increasing width along the longitudinal central axis from the first end to the width central axis. The reaction chamber further comprises a decreasing width area between the width central axis and the second end, the decreasing width area extending from the width central axis to the second end and having the decreasing width along the longitudinal central axis from the width central axis to the second end.
The increasing width area and the decreasing width area is provided as an oval or oval-like reaction chamber enabling good precursor flow uniformity and fast flow between the first end and the second, or between the gas inlet and the gas outlet.
In one embodiment, the first and second side walls comprise an increasing width wall part extending from the first end to the width central axis. The increasing width wall parts are planar wall parts or curved wall parts. The first and second side walls comprise a decreasing width wall part extending from the width central axis to the second end. The decreasing width wall parts are planar wall parts or curved wall parts.
Straight increasing and decreasing wall parts provide simple reaction chamber structure.
Curved increasing and decreasing wall parts provide reaction chamber shape conforming more closely the shape of a round substrate.
In another embodiment, the first and second side walls comprise an increasing width wall part in the increasing width area. The increasing width wall parts are planar wall parts or curved wall parts. The first and second side walls comprise a decreasing width wall part in the decreasing width area. The decreasing width wall parts are planar wall parts or curved wall parts.
Straight increasing and decreasing width areas provide simple reaction chamber structure.
Curved increasing and decreasing width areas provide reaction chamber shape conforming more closely the shape of a round substrate.
In one embodiment, the reaction chamber has the increasing width along the longitudinal central axis in the direction from the first end towards the width central axis and the decreasing width along the longitudinal central axis in the direction from the width central axis towards the second end. The reaction chamber further has a constant width along the longitudinal central axis in the direction from the width central axis towards the first end and from the width central axis towards the second end.
The constant width between the increasing width and the decreasing width may enhance providing more uniform and stable gas flow. Further, a substrate holder may be more easily arranged into the reaction chamber.
In another embodiment, the reaction chamber comprises an increasing width area provided between the first end and the width central axis. The increasing width area comprises the increasing width along the longitudinal central axis in the direction from the first end towards the width central axis. The reaction chamber comprises a decreasing width area provided between the width central axis and the second end. The decreasing width area comprises the decreasing width along the longitudinal central axis in the direction from the width central axis towards the second end. The reaction chamber further comprises a constant width area provided between the increasing width area and the decreasing width area.
The constant width area between the increasing width area and the decreasing width area may enhance providing more uniform and stable gas flow. Further, the constant width area provides structurally good location for a substrate holder.
In one embodiment, the reaction chamber comprises a substrate holder arranged inside the reaction chamber between the first end and the second end and between the gas inlet and the gas outlet.
In another embodiment, the reaction chamber comprises a substrate holder arranged inside the reaction chamber between the first end and the second end and between the gas inlet and the gas outlet. The substrate holder is arranged symmetrically inside the reaction chamber to the intersection of the longitudinal central axis and the width central axis.
Accordingly, the substrate holder takes the advantageous of the increasing and decreasing width areas with fast and uniform gas flow through the substrate holder.
In one embodiment, the substrate holder is arranged to extend in the direction of the longitudinal central axis in the increasing width area and in the decreasing width area.
In another embodiment, the substrate holder is arranged to extend in the direction of the longitudinal central axis from the increasing width area to the decreasing width area.
Therefore, the substrates may be also arranged to extend to the increasing width area and to the decreasing width area such that the side walls of the reaction chamber are provided close to the edges of the substrate.
In a further embodiment, the substrate holder is arranged to extend in the direction of the longitudinal central axis in the increasing width area, in the decreasing width area and in the constant width area.
In a further alternative embodiment, the substrate holder is arranged to extend in the direction of the longitudinal central axis from the increasing width area to the decreasing width area via the constant width area.
Therefore, the substrates may be also arranged to extend from the constant width area to the increasing width area and to the decreasing width area such that the side walls of the reaction chamber are provided close to the edges of the substrate also in a direction towards the gas inlet and the gas outlet.
In one embodiment, the substrate holder comprises in the direction of the longitudinal central axis a front end opposite the first end and a back end opposite the second end. The substrate holder defines a substrate zone inside the reaction chamber between the front end and the back end in the direction longitudinal central axis. The reaction chamber also comprises a supply zone extending in the direction of the longitudinal central axis between the first end of the reaction chamber and the front end of the substrate holder. The gas inlet is provided to the supply zone. The reaction chamber further comprises a discharge zone extending in the direction of the longitudinal central axis between the second end of the reaction chamber and the back end of the substrate holder. The gas outlet is provided to the discharge zone. The increasing width area extends in the direction of the longitudinal central axis from the supply zone to the substrate zone, and the decreasing width area extends in the direction of the longitudinal central axis from the discharge zone to the substrate zone.
Accordingly, the substrate area overlaps the increasing width area and the decreasing width area in the direction of the longitudinal central axis. Thus, the side walls of the reaction chamber are close edges of the substrate in the substrate area.
In one embodiment, the constant width area is provided within the substrate zone in the direction of the longitudinal central axis.
In another embodiment, the constant width area is provided within the substrate zone in the direction of the longitudinal central axis, and the substrate zone has greater length than constant width area in the direction of the longitudinal central axis.
Thus, a uniform gas flow is achieved in the substrate area.
In one embodiment, a first distance between the substrate holder and the first or second side wall along the width central axis is smaller than a second distance between substrate holder and the first or second end along the longitudinal central axis.
Therefore, the substrates are close to the side walls of the reaction chamber and greater space and distance between the gas inlet/gas outlet and the substrate holder may be provided.
In one embodiment, the substrate holder is arranged to support one or more circular substrates or circular semiconductor wafers.
The reaction chamber of the present invention is especially suitable for round substrates as the increasing and decreasing width enables minimizing distance between the round substrate and the side walls of the reaction chamber.
In some embodiments, the reaction chamber comprises a bottom wall, a top wall, the first and second side walls and the first and second ends. The first and second side walls and the first and second ends extend between the bottom wall and the top wall.
In one embodiment, the gas inlet and the gas outlet are provided to the bottom wall. This enables simple reaction chamber construction.
In another embodiment, the gas inlet is provided to the bottom wall in vicinity of the first end and the gas outlet is provided to the bottom wall in vicinity of the second end. This provides great distance between the gas inlet/gas outlet and the substrate holder or substrate together with simple reaction chamber construction.
In a further embodiment, the gas inlet is provided to the first end and the gas outlet are provided to the second end. This provides great distance between the gas inlet/gas outlet and the substrate holder or the substrate.
The present invention further relates to an atomic layer deposition reactor comprising a vacuum chamber and a reaction chamber arranged inside the vacuum chamber. The reaction chamber comprises a first end, a second end opposite the first end, a longitudinal central axis extending between the first end and the second end, and a length between the first end and the second end along the longitudinal central axis. The reaction chamber also comprises a first side wall and the second side wall extending between the first end and the second end, a width central axis extending perpendicularly to the longitudinal central axis between the first and second side walls, and a width between the first and second side wall in the direction of the width central axis. The reaction chamber further comprises a gas inlet for supplying gases into the reaction chamber, and a gas outlet for discharging gases from the reaction chamber. The gas inlet and the gas outlet are provided spaced apart on opposite sides of the width central axis in the direction of the longitudinal central axis.
According to the present invention, the first and second side wall of the reaction chamber are arranged to define an increasing width along of the longitudinal central axis in the direction from the gas inlet towards the width central axis and a decreasing width along the longitudinal central axis in the direction from the width central axis towards the gas outlet, and the length of the reaction chamber is greater than the width of the reaction chamber along the width central axis.
The increasing width and the decreasing width in the direction between the gas inlet and the gas outlet enable arranging the side walls at a very short distance from the substrate, especially outer edges of round substrates. Furthermore, the oval or oval-like shape provided by the greater length than the width enables forming sufficient distance between the gas inlet from the substrates in the direction of the longitudinal central axis such that precursor gas molecules have adequate time and space to spread before meeting the substrates. Thus, the bypass effect is minimized.
In one embodiment, the reactor comprises at least one gas inlet connection extending from outside the vacuum chamber to the reaction chamber and being connected to the gas inlet for supplying gas into the reaction chamber from outside the vacuum chamber, and at least one gas outlet connection extending from outside the vacuum chamber to the reaction chamber and being connected to the gas outlet for discharging gas from the reaction chamber to outside the vacuum chamber.
Thus, the gases supplied to and discharged from the reaction chamber outside vacuum chamber. Controlled and secure processing environment inside the reaction chamber is generated.
In one embodiment, the reaction chamber has the increasing width along the longitudinal central axis in the direction from the gas inlet towards the width central axis. The reaction chamber has the decreasing width along the longitudinal central axis in the direction from the width central axis towards the gas outlet. The reaction chamber further has a constant width along the longitudinal central axis in the direction from the width central axis towards the gas inlet and from the width central axis towards the gas outlet.
The reaction chamber of the reactor may be a reaction chamber as disclosed above.
An advantage of the invention is that the increasing width and the decreasing width in the direction between the gas inlet and the gas outlet, and in the direction of the longitudinal central axis, enable arranging the side walls at a very short distance from the substrate, especially outer edges of round substrates. Furthermore, the oval or oval-like shape provided by the greater length than the width enables forming sufficient distance between the gas inlet from the substrates in the direction of the longitudinal central axis such that precursor gas molecules have adequate time and space to spread before meeting the substrates. Thus, the bypass effect is minimized. At the same time good flow dynamics without gas pockets in the reaction chamber is achieved such that considerable overdose does not need to be utilized and purging the reaction may be carried in short time.
The invention is described in detail by means of specific embodiments with reference to the enclosed drawings, in which
The reactor 10 comprises a vacuum chamber 90. The vacuum chamber 90 is constructed to withstand considerable under pressure. A vacuum device 92 is connected vacuum chamber 90 and arranged to provide vacuum or under pressure inside the vacuum chamber 90. The vacuum device 92 is connected to the vacuum chamber 90 with a vacuum connection 94.
The vacuum device 92 is a vacuum pump or the like device capable of providing vacuum or under pressure inside the vacuum chamber 90. The vacuum device 92 is arranged outside the vacuum chamber 90.
The reactor 10 further comprises a reaction chamber 20 arranged inside the vacuum chamber 90. Substrates are processed inside the reaction chamber 20.
The reaction chamber 20 comprise a first end 24, a second end 26 opposite the first end 24, a first side wall 27 and the second side wall 28 extending between the first end 24 and the second end 26. The reaction chamber 20 has a length between the first end 24 and the second end 26, and a width between the first side wall 27 and the second side wall 28.
The reaction chamber 20 further comprises a bottom wall 23 and a top wall 25. The first end 24, the second end, 26, the first side wall 27 and the second side wall 28 extend between the bottom wall 23 and the top wall 25.
The reaction chamber 20 has a reaction space 21 defined by the walls 23, 25, 24, 26, 27, 28.
The reaction chamber 20 is provided with a gas inlet 30 via which precursor gases, purge gases or the like are supplied inside the reaction chamber 20. In some embodiments, there are one or more gas inlets 30.
The gas inlet 30 is connected to one or more gas sources 100, such as precursor gas source and purge gas source. The gas sources 100 are arranged outside the reaction chamber 20 and outside the vacuum chamber 90. The gas sources 100 are connected to the gas inlet 30 for supplying gases into the reaction chamber 20. Thus, the gases are supplied into the reaction chamber 20 from outside of the vacuum chamber 90. The gas sources 100 are connected to the gas inlet 30 with a gas supply connection 110. The gas supply connection 110 extends from the gas sources 100 and from outside the vacuum chamber 90 to the reaction chamber 20 and to the gas inlet 30. The gas source 100 may be gas bottle or the like.
The reaction chamber 20 is also provided with a gas outlet 40 via which precursor gases, purge gases or the like are discharged from inside of the reaction chamber 20. In some embodiments, there are one or more gas outlets 40.
The gas outlet 40 is connected to a discharge device 200. The discharge device 200 is arranged outside the reaction chamber 20 and outside the vacuum chamber 90. The discharge device 200 is connected to the gas outlet 40 for discharging gases into the reaction chamber 20. Thus, the gases are discharged from the reaction chamber 20 to outside of the vacuum chamber 90. The discharge device 200 is connected to the gas outlet 40 with a gas discharge connection 210. The gas discharge connection 210 extends from the discharge device 200 and from outside the vacuum chamber 90 to the reaction chamber 20 and to the gas outlet 40.
Accordingly, gases, such as precursor gases and purge gases, flow inside the reaction chamber 20 from the gas inlet 30 to the gas outlet 40. The substrates to be processed are arranged in the reaction chamber 20 between the gas inlet 30 and the gas outlet 40.
The reaction chamber 20 is further provided with a substrate holder to which one or more substrates are placed and supported for processing. The substrate holder is arranged between the gas inlet 30 and the gas outlet 40 such that gases flow through the substrate holder between the gas inlet 30 and the gas outlet 40 and subject surfaces of the substrate(s) to the gases.
The gas inlet 30 and the gas outlet 40 are provided to the bottom wall 23 in the vicinity of the first end 24 and the second end 26, respectively.
Alternatively, the gas inlet 30 and the gas outlet 40 are provided to the top wall 25 in the vicinity of the first end 24 and the second end 26, respectively. In an alternative embodiment, the gas inlet 30 and the gas outlet 40 are provided to the first and 24 and second end 26, respectively.
Accordingly, the gas inlet 30 and the gas outlet 40 are provided spaced apart from each other inside the reaction chamber 20, in the direction between the first end 24 and the second end 26. Thus, the substrates may be placed between the gas inlet 30 and the gas outlet 40.
In the present invention, the reaction chamber 20 has generally oval or oval-like shape. This means, that the length of the reaction chamber 20 between the first end 24 and the second end 26 is greater than the width, or greatest width, of the reaction chamber 20. Furthermore, the oval-like shape means that the width of the reaction chamber 20 increases at least along part of the length of the reaction chamber in the direction from the first end 24 towards the second end 26, and the width of the reaction chamber 20 increases at least along part of the length of the reaction chamber in the direction from the second end 26 towards the first end 24. Thus, the width of the reaction chamber 20 increases in the direction from the first end 24 and from the second 26 towards the centre of the reaction chamber 20. The width of the reaction chamber 20 is defined by the side walls of the reaction chamber 20.
The oval or oval-like shape of the reaction chamber 20 is formed between the first end 24 and the second end 26. Alternatively, the oval or oval-like shape is formed at least between the gas inlet 30 and the gas outlet 40.
In the embodiments of
In alternative embodiments of the present invention, the gas inlet 30 and the gas outlet 40 are provided to the top wall 25 of the reaction chamber 20 or to the first end 24 and the second end 26, respectively. The present invention is not restricted to exact location of the gas inlet 30 and the gas outlet 40.
Further, generally the reaction chamber 20 has a length L between the first end 24 and the second end 26. The reaction chamber 20 also comprises a longitudinal central axis X extending in the length direction of the reaction chamber 20, and in the direction between the first end 24 and the second end 26.
The first and second side walls 27, 28 define width W of the reaction chamber 20. In the reaction chamber 20 according to the present invention, the width W of the reaction chamber 20 changes along the longitudinal central axis X. The reaction chamber 20 also comprises a width central axis Y extending in a direction between the first side wall 27 and the second side wall 28, and perpendicularly to the longitudinal central axis X.
The longitudinal central axis X extends in the length direction and the width central axis Y in the width direction of the reaction chamber.
The longitudinal central axis X divides the reaction chamber 20 in the length direction to two halves. The width central axis y divides the reaction chamber 20 in the width direction to two halves.
The reaction chamber of
In this embodiment, the gas inlet 30 and the gas outlet are provided to the bottom wall 23.
There is a substrate holder 50 in the reaction chamber 20 arranged between the first end 24 and the second end 26, or more specifically between the gas inlet 30 and the gas outlet 40. The substrate holder 50 is arranged to hold one or more substrates, especially circular substrates during processing.
The arrows A and B in
As shown in
Therefore, the reaction chamber 20 comprises an increasing width area G between the first end 24 and the width central axis Y along the longitudinal central axis X from the first end 24 to the width central axis Y. Similarly, the reaction chamber 20 comprises a decreasing width area H between the width central axis Y and the second end 26 along the longitudinal central axis X, as shown in
As shown in
Preferably, the substrate holder 50 is arranged in the centre of the reaction chamber 20, in the cross section of the longitudinal central axis X and the width central axis Y.
The substrate holder 50 comprises in the direction of the longitudinal central axis X a front end 54 opposite the first end 24 and a back end 56 opposite the second end 26. The substrate holder 50 defines a substrate zone Z2 inside the reaction chamber 20 between the front end 54 and the back end 56 in the direction longitudinal central axis X.
The reaction chamber 20 further comprises a supply zone Z1 extending in the direction of the longitudinal central axis X between the first end 24 of the reaction chamber 20 and the front end 54 of the substrate holder 50. The gas inlet 30 is provided to the supply zone Z1. The reaction chamber 20 also comprises a discharge zone Z3 extending in the direction of the longitudinal central axis X between the second end 26 of the reaction chamber 20 and the back end 56 of the substrate holder 50. The gas outlet 40 is provided to the discharge zone Z3.
The gas inlet 30 is arranged in vicinity of the first end 24 and the gas outlet 40 is arranged in vicinity of the second end 26.
Accordingly, the reaction chamber 20 comprises three zones along the longitudinal central axis X, the supply zone Z1, The substrate zone Z2 and the discharge zone Z3. Gases are supplied from the gas inlet 30 in the supply zone Z1, and discharged from the discharge zone Z3 with the gas outlet 40, and the gases flow through the substrate zone Z2.
As shown in
In the embodiment of
The diverging wall portions 31 and the converging wall portions 41 are straight or planar.
The diverging wall portions 31 define the increasing width W along the longitudinal central axis X from the first end 24 to the width central axis Y. Further, the converging wall portions 41 define the decreasing width W along the longitudinal central axis X from the width central axis Y to the second end 26. Accordingly, the reaction chamber 20 has the greatest width at the width central axis Y along the longitudinal central axis X.
Therefore, the reaction chamber 20 comprises the increasing width area G between the first end 24 and the width central axis Y along the longitudinal central axis X from the first end 24 to the width central axis Y defined by the diverging wall portions 31. Similarly, the reaction chamber 20 comprises the decreasing width area H between the width central axis Y and the second end 26 along the longitudinal central axis X defined by the converging wall portion 41, as shown in
The diverging wall portions 31 and the converging wall portions 41 provide the oval or oval-like shape of the reaction chamber 20.
As shown in
Preferably, the substrate holder 50 is arranged in the centre of the reaction chamber 20, in the cross section of the longitudinal central axis X and the width central axis Y.
The reaction chamber 20 further comprises the supply zone Z1 extending in the direction of the longitudinal central axis X between the first end 24 of the reaction chamber 20 and the front end 54 of the substrate holder 50. The gas inlet 30 is provided to the supply zone Z1. The reaction chamber 20 also comprises the discharge zone Z3 extending in the direction of the longitudinal central axis X between the second end 26 of the reaction chamber 20 and the back end 56 of the substrate holder 50. The gas outlet 40 is provided to the discharge zone Z3. The substrate zone Z2 is provided between the front end 54 and the back end 56 of the substrate holder 50.
The gas inlet 30 is arranged in vicinity of the first end 24 and the gas outlet 40 is arranged in vicinity of the second end 26.
Accordingly, the reaction chamber 20 comprises three zones along the longitudinal central axis X, the supply zone Z1, the substrate zone Z2 and the discharge zone Z3. Gases are supplied from the gas inlet 30 in the supply zone Z1, and discharged from the discharge zone Z3 with the gas outlet 40, and the gases flow through the substrate zone Z2.
As shown in
The reaction chamber of
In this embodiment, the gas inlet 30 and the gas outlet are provided to the bottom wall 23.
There is a substrate holder 50 in the reaction chamber 20 arranged between the first end 24 and the second end 26, or more specifically between the gas inlet 30 and the gas outlet 40. The substrate holder 50 is arranged to hold one or more substrates, especially circular substrates during processing.
In the embodiment of
The first and second side walls 27, 28 further comprises parallel wall portions 35 extending parallel to each other. The parallel wall portions 35 define constant width W along the longitudinal central axis X.
The parallel wall portions 35 extend in the direction of the longitudinal central axis X. The parallel wall portions 35 are straight or planar.
The parallel wall portions 35 extend from the diverging wall portions 31 towards the second end 26. The parallel wall portions 35 extend from the width central axis Y towards the first end 24 and the second end 26.
The first and second side walls 27, 28 comprise converging wall portions 41 extending from the parallel wall portions 35 to the second end 26. The converging wall portions 41 define the decreasing width W of the reaction chamber 20.
The diverging wall portions 31 and the converging wall portions 41 are curved wall portions. The diverging wall portions 31 and the converging wall portions 41 are curved and outwardly convex.
The reaction chamber 20 comprises the increasing width area G between the first end 24 and the parallel wall portions 35 along the longitudinal central axis X. The increasing width area G is defined by the diverging wall portions 31. The reaction chamber 20 further comprises a constant width area F extending from the increasing width area G towards the second end 26 along the longitudinal central axis X. The constant width area F is defined by the parallel wall portions 35. Further, the reaction chamber 20 comprises the decreasing width area H between the constant width area F and the second end 26 along the longitudinal central axis X, as shown in
The constant width area F is arranged between the increasing widths area G and the decreasing width area H.
Also, in this embodiment, the substrate holder 50 is at the first distance D1 from the first and second side walls 27, 28 and at the second distance D2 from the first and second end 24, 26. The oval or oval-like shape of the reaction chamber 20 is arranged such that the second distance D2 is greater than the first distance D1.
As shown in
The substrate holder 50 is arranged between the first and second ends 24, 26, and between the gas inlet 30 and the gas outlet 40.
Preferably, the substrate holder 50 is arranged in the centre of the reaction chamber 20, in the cross section of the longitudinal central axis X and the width central axis Y.
The reaction chamber 20 comprises the supply zone Z1, the substrate zone Z2 and the discharge zone Z3.
As shown in
Furthermore, the constant width area F is provided within the substrate zone Z2 in the direction of the longitudinal central axis X.
Accordingly, the constant width area F is provided within the substrate zone Z2 in the direction of the longitudinal central axis X, and the substrate zone Z2 has greater length than constant width area F in the direction of the longitudinal central axis X.
The embodiment of
The first end parallel side wall portions 32 extend parallel to the longitudinal centre axis X.
As shown in
The first end constant width area J is provided to the supply zone Z1 of the reaction chamber 20.
The substrate zone Z2 and the increasing width area G are partly overlapped in the direction of the longitudinal centre axis X. Thus, the substrate zone Z2 extends to the increasing width area G.
The embodiment of
The second end parallel side wall portions 42 extend parallel to the longitudinal centre axis X.
As shown in
The second end constant width area K is provided to the discharge zone Z3 of the reaction chamber 20.
The substrate zone Z2 and the decreasing width area H are partly overlapped in the direction of the longitudinal centre axis X. Thus, the substrate zone Z2 extends to the decreasing width area H.
The constant width area F in arranged within the substrate zone Z2 and between the increasing width area G and the decreasing width area H.
The supply flow guides 60 are arranged to the increasing width area G.
The supply flow guides 60 are arranged to substantially parallel to the diverging wall portions 31. There is at least one supply flow guide 60 on opposite sides of the longitudinal central axis X.
The reaction chamber 20 is further provided with discharge flow guides 62 arranged to the discharge zone Z3. The discharge flow guides 62 are arranged to guide the gas flow from the flow path A and flow path B to the gas outlet 40.
The discharge flow guides 62 are arranged to the decreasing width area H.
The discharge flow guides 62 are arranged to substantially parallel to the converging verging wall portions 41. There is at least one discharge flow guide 62 on opposite sides of the longitudinal central axis X.
The supply flow guides 60 are arranged to the increasing width area G.
The supply flow guides 60 are arranged to substantially parallel to the diverging wall portions 31. There is at least one supply flow guide 60 on opposite sides of the longitudinal central axis X.
The reaction chamber 20 is further provided with discharge flow guides 62 arranged to extend from the discharge zone Z3 to the substrate zone Z2. The discharge flow guides 62 are arranged to guide the gas flow from the flow path A and flow path B to the gas outlet 40.
The discharge flow guides 62 are arranged to the decreasing width area H.
The discharge flow guides 62 are arranged to substantially parallel to the converging verging wall portions 41. There is at least one discharge flow guide 62 on opposite sides of the longitudinal central axis X.
In some embodiments the discharge flow guides 62 may be omitted and there are only supply flow guides 60.
The supply flow guides 60 and the discharge flow guides 62 are plates or vanes.
There is a longitudinal substrate holder 50 in the reaction chamber 20 arranged between the first end 24 and the second end 26, or more specifically between the gas inlet 30 and the gas outlet 40. The substrate holder 50 is arranged to hold one or more substrates, especially circular substrates during processing.
The longitudinal substrate holder 50 is arranged to hold or support two or more substrates, such as circular substrates, successively or in a row between the gas inlet 30 and the gas outlet 40. The successive substrates are arranged at same level or height from the bottom 23 of the reaction chamber 20. The longitudinal substrate holder 50 may also arranged to hold or support two or more substrate on top of each other, as shown on
The longitudinal substrate holder 50 is arranged between the first and second ends 24, 26, and between the gas inlet 30 and the gas outlet 40.
Preferably, the longitudinal substrate holder 50 is arranged in the centre of the reaction chamber 20, in the cross section of the longitudinal central axis X and the width central axis Y.
The longitudinal substrate holder 50 extends from the increasing width area G to the decreasing width area H via the constant width area F.
In an alternative embodiment, the constant width area F may be omitted and the longitudinal substrate holder 50 extends from the increasing width area G to the decreasing width area H.
The invention has been described above with reference to the examples shown in the figures. However, the invention is in no way restricted to the above examples but may vary within the scope of the claims.
Number | Date | Country | Kind |
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20215853 | Aug 2021 | FI | national |
Filing Document | Filing Date | Country | Kind |
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PCT/FI2022/050522 | 8/12/2022 | WO |