APPARATUS AND METHOD FOR DEPOSITING ORGANIC MATTER
OF VAPOR PHASE
TECHNICAL FIELD
The present invention relates to a vapor organic material
deposition method and a vapor organic material deposition apparatus in a
fabrication apparatus of a semiconductor apparatus and a fabrication
method of the same, and in particular to a vapor organic material
deposition method and a vapor organic material deposition apparatus
using the same which are capable of fast growing a thin film uniformly on a
wider substrate by spraying a vapor organic material in a gravity direction
using a spraying unit installed in an upper side of the same and accurately
and stably adjusting a thickness of a wider substrate of an organic thin film
by using a diluting gas as a deposition material and continuously carrying
a small size heat source to a scan head.
BACKGROUND ART
Recently, a thin film formation technology by a functional high
molecular compound as an organic compound and an organic metallic
compound is concentrated on a conductive material, photoelectron
material, electro-luminescence device material, etc. including an insulation
layer material of a semiconductor memory.
A vacuum deposition method used one of a representative
technology among the so far developed organic thin film formation
methods is implemented in such a manner that a heat evaporation source
is installed in a lower portion of a vacuum chamber, and a film growing
substrate is installed thereon for thereby forming a thin film. The schematic
construction of an organic thin film formation apparatus using a vacuum
deposition method will be described. There is provided a vacuum
ventilation unit connected with a vacuum chamber. Therefore, a certain
vacuum state is maintained in the vacuum chamber using the vacuum
ventilation unit. An organic material which is an organic thin film material is
evaporated from a heat evaporation source of more than at least one
organic thin film material disposed in a lower portion of a vacuum chamber.
A heat evaporation source of an organic thin film material is a cylindrical or
rectangular parallelepiped container. A film grown organic material is
provided in the container. There are quartz, ceramic, etc. as a container
material. A heating heater is wound on a surrounding surface of a
container unit in a certain pattern. When a certain power is applied, the
temperature of a surrounding portion of a container is increased and at the
same time the container is heated. When a certain temperature is reached,
an organic is evaporated. At this time, the temperature is measured by a
temperature adjusting heat conducting unit installed in a lower portion or in
an upper portion of the container. Therefore, it is possible to maintain an
organic evaporation material to have a constant temperature for thereby
obtaining a desired evaporation rate. The evaporated organic material is
carried to a substrate formed of a glass or wafer material disposed far
from an upper side of a container by a certain distance. The thusly carried
organic material is hardened on the substrate through an absorption,
deposition, re-evaporation processes for thereby forming a thin film.
Here, in the organic compound of an organic thin film material,
since a vapor pressure is high, and a pyrolysis temperature by a heat is
close to an evaporation temperature, it is difficult to control an organic
evaporation rate stably for a long time, so that it is impossible to
implement a high rate thin film deposition. An organic thin film material
evaporated from a heat evaporation source in the vacuum chamber has a
certain orientation corresponding to a shape of a crucible hole of an upper
portion of a heat evaporation source container and is limited to a limited
range and reaches at a substrate, so that it is impossible to obtain a
uniform organic thin film formed on a wide area substrate. In addition, a
film is grown while a substrate is rotated at a certain rate using a
correction unit of a certain orientation for implementing a uniform thin film
formation of an organic thin film, so that a rotation radius is increased, and
a deposition apparatus is made larger. In addition, since an organic thin
film is formed in an unnecessary effective area of a vacuum apparatus, an
efficiency of use of an expensive organic material is decreased for thereby
decreasing a productivity.
As described above, when a product is fabricated in application
with an electro-luminescence device and functional thin film using an
organic thin film in a vacuum deposition method, there are problems such
as a lower film growing rate, a lower organic material use efficiency, a non-
uniformity of an organic thin film, a difficulty for finely adjusting a mixing
amount of a host material and a dopant material, and a difficulty for
forming a uniform organic thin film based on a larger substrate. As an
example of the above problems, the conventional vacuum deposition
apparatus will be described with reference to Figure 1.
Figure 1 is a view illustrating an example of a conventional
vacuum deposition apparatus.
As shown therein, in a conventional vacuum deposition apparatus,
a certain material deposited on a molybdenum boat 6 is prepared by a
certain amount, and an inner pressure of a vacuum chamber 1 is
decreased to 10-6torr. In the case that a deposition material is metal, the
metal is increased near a melting point using a temperature adjusting
apparatus, and the temperature is finely adjusted and is increased until the
material is evaporated. At this time, the material on the molybdenum boat
6 starts to evaporate, a previously engaged shutter 5 is opened, and an
evaporated material molecular is deposited on the substrate. At this time,
a shutter 5 is adapted to prevent an impurity remaining before the material
on the molybdenum boat 6 is evaporated from being deposited on the
substrate.
In the thusly constituted vacuum deposition apparatus, it is not
easy to predict an accurate amount of the depositing material. Therefore,
a large amount of the material must be prepared on the molybdenum boat
6. In addition, since it is impossible to induce vapor in a desired direction,
in the case that the above deposition processes are repeatedly performed,
the interior of the chamber may be polluted. Therefore, in this case, the
interior of the same should be cleaned for thereby causing an
inconvenience. Furthermore, the amount of the material prepared on the
molybdenum boat 6, the opening and closing time of the shutter 4, and the
evaporating time by the temperature adjustment are variables of the
thickness adjustment. It is impossible to finely adjust the above variables.
In addition, in the organic semiconductor fabrication method, there
are a method for using a unit deposition source, and an OVPD(Organic
Vapor Phase Deposition) method proposed by Max Shtein, et. al. in
Princeton university.
In the organic semiconductor fabrication method which uses a unit
deposition source tank, it takes a long time for depositing each layer used
in the organic semiconductor. The amount of the use of the material used
for the deposition of each layer is larger. In addition, there is a problem
that a density of a deposited film and an adhesive force with respect the
substrate are bad. A fabrication yield for a mass production of an organic
semiconductor is decreased. There is a limit in a fabrication process of a
wider area substrate for a mass production. Namely, the limit size of the
area of the substrate is 370x470mm.
The OVPD method is directed to a method for fabricating each
layer used for an organic semiconductor using a carry gas for a vapor
organic material in an Axitron method proposed by Max Shtein, et. al. This
method is capable of more increasing an efficiency in use of an organic
material compared to a method adapted to use a unit deposition source. In
addition, it is possible to theoretically fabricate an organic semiconductor
of a wider area substrate. However, the method of Axitron which uses the
OVPD method uses a scan head of a conventional CVD method. In
addition, the substrate of 200x200mm is tested. In this case, a problem of
an organic thin film which is weak to heat may occur.
In addition, in order to fabricate for a wider area substrate, a
shower head of over 370x470mm must be prepared. However, in this case,
there is a problem in constructing the same. In the deposition method of
Axitron method, the high temperature heat sources of the deposition
source tank 714 and the scan head are fixed. In addition, in a doping in a
fabrication of an organic semiconductor, a separate temperature
adjustment is implemented by providing more than st least two scan heads
in the interior of the system. However, in the OVPD method, since one
scan head is used, if the doping is performed using more than at least two
doping materials which have different thermal properties, the material may
be changed to a material having a bad thermal property. Namely, in the
conventional two methods, the organic semiconductor material is not well
deposited on a substrate of a wider area.
DISCLOSURE OF INVENTION
Accordingly, it is an object of the present invention to provide a
vapor organic material deposition method and a vapor organic material
deposition apparatus using the same which are capable of overcoming the
problems encountered in the conventional art.
It is an object of the present invention to provide a vapor organic
material deposition method of a wider area substrate and a vapor organic
material deposition apparatus using the same which are capable of
increasing an adhesive force with respect to a substrate of an organic thin
film and accurately and stable adjusting a thickness by diluting an organic
material particle in the interior of a deposition source tank in order for an
organic semiconductor material to be deposited on a substrate and
preventing a temperature increase on a wider area substrate by a heat
source of a scan head and in the interior of a deposition chamber using a
gate valve of a buffer chamber and a deposition chamber.
To achieve the above objects, there is provided a vapor organic
material deposition apparatus which includes a deposition chamber which
has an inner space separated from the outside, a mother material
mounting portion formed in a bottom surface of the inner space for
mounting a mother material therein on which a vapor organic material is
deposited, a spraying unit which is positioned in an upper portion of the
mother material mounting portion and is adapted to spray a vapor organic
material in a direction of the mother material mounting portion, and more
than at least one warm keeping heater which radiates a heat to an upper
wall surface and side wall surface, more than at least one organic material
chamber which more than at least one carry gas inlet hole formed in a
hole shape through which a carry gas carrying a vapor organic material is
flown in, more than at least one vapor organic material outlet hole formed
in a hole shape through which an organic material vapor and carry gas are
discharged, a furnace which is formed of a heat-resisting material and has
an inner space for storing an organic material, and an organic material
heating heater which surrounds an outer surrounding portion of the
furnace and heats an inner portion of the furnace to a temperature at
which an organic material is evaporated, a flow amount controller which is
connected with the carry gas inlet hole and controls the amount and
flowing rate of the carry gas flown into the interior of the organic material
chamber, a vapor organic material carry pipe which is formed to pass
through the deposition chamber and the organic material chamber and are
formed in a pipe shape, so that a vapor organic material in the organic
material chamber is carried to a spraying unit, and a vacuum pump which
is adapted to decrease an inner pressure of the deposition chamber.
To achieve the above objects, there is provided a vapor organic
mateπal deposition method which includes a first step in which a heating
heater contacting with an outer surface of an organic material chamber
including an organic material therein radiates heat and heats the organic
material to a temperature above an evaporation temperature, a second
step in which a vapor organic material evaporated by the heating heater is
moved to a spraying unit of the deposition chamber in which a mother
material on which a vapor organic material is deposited is positioned,
through a vapor organic material carry pipe surrounded by a fixed
temperature heater which radiates heat, and a third step in which a vapor
organic material carried to the spraying unit is sprayed in a gravity
direction from an upper portion of the mother material placed in an upper
portion of a mother material mounting portion, and is deposited on an
upper surface of the mother material.
To achieve the above objects, in a vapor organic material
deposition apparatus, there is provided a vapor organic material
deposition apparatus of a wider area substrate which includes a gas
heater which is adapted to heat an inert gas by adjusting a gas reservoir
having an inert gas therein and a MFC(Mass Flow Controller), a heater
pipe wound on an outer portion of a connection pipe for maintaining a
temperature, at least one deposition source tank which stores a gas to be
deposited and an organic material and heats a high temperature gas and
organic material particle by a gas heater in a state that the same are
diluted for thereby generating a diluted organic material in a gaseous state,
a scan head and buffer chamber which have a deposition rate adjusting
unit adapted to check and adjust a movement of the diluted organic
material particle, a gate valve which is adapted to implement a gating
operation for thereby opening and closing a flow of the diluted organic
material particle, and a deposition chamber which is adapted to deposit
the diluted particle flown in from the deposition source tank on a wider
area substrate, wherein the gas heater heats a gas in order for the
deposition source tank adjusts the amount of gas and flows a heat source
into the same, and the gate valve is installed between the buffer chamber
and the deposition chamber for thereby preventing a temperature increase
in a wider area substrate by a heat source of the scan head and in the
interior of the deposition chamber.
To achieve the above objects, in a vapor organic material
deposition method there is provided a vapor organic material deposition
method of a wider area substrate which includes a first step in which an
inert gas which flows from a deposition source tank based on an
adjustment of a gas reservoir which stores an inert gas therein and a
MFC(Mass Flow Controller) is heated using a gas heater based on an
adjustment of a gas mount, and heat source is inputted into the interior, a
step in which a temperature is maintained by a heater pipe wound on an
outer portion of a connection pipe, a step in which at least one deposition
source tank in which a gas to be deposited and an organic material are
stored is heated by a gas heater in a state that a high temperature gas
and an organic material particle are diluted, and a diluted organic material
is obtained in a gaseous state, a step in which a flow of the diluted organic
material particle is checked and adjusted, and a gating operation is
performed with respect to a scan head and buffer chamber attached with a
deposition rate adjusting unit and for opening and closing a flow of a
diluted organic material particle, a step in which a diluted particle flown in
from the gate valve and the deposition source tank is deposited on a wider
area substrate in the deposition chamber, a step in which the gate valve is
installed between the buffer chamber and the deposition chamber and a
temperature increase is prevented in a wider area substrate by a head
source of the scan head and in the interior of a deposition chamber, and a
step in which an organic material which is separated when the scan head
is moved in the buffer chamber is collected by an assistant furnace
installed for a re-circulation of the organic material.
To achieve the above objects, in a fabrication method of an
organic semiconductor apparatus, there is provided a vapor organic
material deposition method of a wider area substrate which includes a
step(S710) in which a substrate is loaded into a deposition chamber in a
deposition apparatus, a step(S712) in which a deposition source tank is
pre-heated and a high temperature gas is flown in at a temperature of
200°C - 600°C, a step(S714) in which a high temperature gas and an
organic material particle are mixed in the interior of the deposition source
tank for thereby forming a mixture, and is heated for thereby generating a
SGHP(Solid-Gas Heterogeneous Phase) material, a step(S716) in which a
large amount of vapor organic material SGHP are carried from the
deposition source tank to the buffer chamber through the connection pipe,
a step(S718) in which the flowing amount of the vapor organic material is
measured using a vapor organic material sensor in the buffer chamber,
and when the flowing amount of the vapor organic material reaches at a
certain set amount, the buffer gate valve is opened, a step(S720) in which
a vapor organic material is deposited based on a scan head operation, a
step(S722) in which after a set deposition time is passes, the scan head is
moved, and a step(S724) in which the buffer gate valve is closed, and the
substrate is unloaded.
BRIEF DESCRIPTION OF THE DRAWINGS
For a more complete understanding of the present invention and
the advantages thereof, reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which like reference numerals denote like parts, and in which:
Figure 1 is a view illustrating an example of a conventional vacuum
deposition apparatus;
Figure 2A is a plan view illustrating a vapor organic material
deposition apparatus according to the present invention;
Figure 2B is a cross sectional view taken along line A-A of Figure
2A;
Figure 2C is a plan view taken along line B-B of Figure 2A;
Figure 2D is a view illustrating an organic material chamber of a
portion C of Figure 2B;
Figure 3A is a cross sectional view illustrating a state that a
spraying unit is moved and sprays a vapor organic material according to
the present invention;
Figure 3B is a cross sectional view illustrating a state that a mother
material mounting unit having a mother material thereon is moved in a
horizontal direction based on a carrying method using an electric magnet
when a spraying unit sprays a vapor organic material according to the
present invention;
Figure 3C is a cross sectional view illustrating a state that a mother
material is deposited on a mother material using a spraying tube according
to the present invention;
Figure 3D is a cross sectional view illustrating a state that a vapor
organic material is deposited on a mother material as a spraying tube is
rotated and moved upwardly and downwardly according to the present
invention;
Figure 4A is a cross sectional view illustrating a state that a vapor
organic material and a carry gas are mixed in the interior of a furnace
according to the present invention;
Figure 4B is a cross sectional view illustrating a state that a vapor
organic material and a carry gas are mixed in the outside of a furnace
according to the present invention;
Figure 5A is a cross sectional view illustrating a rectangular
parallelepiped furnace which has a vapor organic material discharging
hole in an upper end portion according to the present invention;
Figure 5B is a cross sectional view illustrating a rectangular
parallelepiped furnace which has a plurality of vapor organic material
discharging holes in an upper end portion according to the present
invention;
Figure 5C is a cross sectional view illustrating a cylindrical furnace
which has a vapor organic material discharging hole in an upper end
portion according to the present invention;
Figure 5D is a cross sectional view illustrating a cylindrical furnace
which has a plurality of vapor organic material discharging holes in an
upper end portion according to the present invention;
Figure 6 is a cross sectional view illustrating a fixed temperature
heater in an outer portion of a vapor organic material carry pipe according
to the present invention;
Figure 7 is a cross sectional view illustrating a vapor organic
material deposition apparatus of a wider area substrate according to the
present invention;
Figure 8 is a cross sectional view illustrating a plurality of deposition
source tanks and scan heads according to the present invention;
Figure 9 is a view for explaining an operation method of a scan
head in the interior of a deposition chamber, which is capable of carrying a
SGHP organic material according to the present invention;
Figure 10 is a view for explaining a moving method of a scan head
capable of carrying a SGHP organic material in the interior of a system of
Figure 8 according to the present invention;
Figure 11 is a view for explaining a vapor organic material
generation method of an organic semiconductor apparatus according to
the present invention;
Figure 12 is a view for explaining a deposition method in the interior
of a deposition chamber based on a vapor organic material generated
based on the method of Figure 11 according to the present invention;
Figure 13 is a floe chart of an operation of a deposition apparatus
according to the present invention;
Figure 14 is a relative relationship graph of a temperature of a gas
diluted and a deposition amount according to the present invention;
Figure 15 is a graph of a vapor organic material with respect to the
amount of a diluting gas according to the present invention; and
Figure 16 is a graph of a relationship of a deposition source tank
temperature and a deposition amount in the case that only a deposition
source tank is heated without a diluting gas according to the present
invention.
Description of reference numerals of major elements of the drawings
10: mother material 20: organic material
100: deposition chamber 110: spraying unit
112: guide plate 120: guide rail
122: guide rail support plate 130: warm keeping heater
140: mother material mounting. unit 150: vacuum pump
200: organic material chamber 210: vapor organic material carry pipe
220: furnace 230: organic material heater
240: carry gas inlet pipe 300: assistant chamber
310: moving shaft 312: moving block
314: carry unit 320: sealing flange
322: bellows 700: deposition chamber
701 : gas reservoir 702: MFC(Mass Flow Controller)
703: gas heater 706:heater pipe
707: connection pipe 709: scan head
710: buffer chamber 711 : gate valve
712: substrate 713: deposition chamber
714: deposition source tank 715: deposition rate adjusting unit
BEST MODE FOR CARRYING OUT THE INVENTION
<First embodiment
Figure 2A is a plan view illustrating a vapor organic material
deposition apparatus according to the present invention.
The vapor organic material deposition apparatus according to the
present invention includes a deposition chamber according to a first
embodiment of the present invention, an organic material chamber for
heating an organic material and changing to a vapor state, and an
assistant chamber which includes a driving apparatus for driving an
operation of a spraying unit which sprays a vapor organic material and an
organic material chamber.
A deposition chamber 100 according to a first embodiment of the
present invention includes an inner space which is separated from an
outside and has a structure so that a mother material 10 on which a vapor
organic material is deposited , is mounted in a bottom surface of the inner
space. In addition, the deposition chamber 100 includes a spraying unit
110 which is positioned in an upper portion of the mother material 10 and
is adapted to spray a vapor organic material to an upper surface of the
mother material 10, a guide rail 120 which is engaged with the spraying
unit 110 and is longitudinally extended to be slidably engaged with a guide
plate(not shown) adapted to guide a sliding movement of the spraying unit
110, a guide rail support plate 122 which is adapted to fixedly support the
guide rail 120, and more than at least one warm keeping heater 130
adapted to maintain the temperature of the interior of the deposition
chamber 100 at a certain degree by radiating heat to the outside.
The organic chamber 200 is constructed in such a manner that an
organic material is evaporated by applying heat to an organic material
stored in the interior and is formed in a pipe shape and is connected with a
vapor organic material carry pipe 210 connected with the spraying unit 110
through the deposition chamber 100 for thereby carrying a vapor organic
material to the spraying unit 110.
The assistant chamber 300 includes a moving shaft 130 which is
engaged with the spraying unit 110 in a direction parallel with the guide rail
120 through the deposition chamber 100 in order for the spraying unit 100
is moved along the guide rail 120, a moving block 312 which is engaged
with the moving shaft 130 and is moved in a direction parallel with the
guide rail 120 based on an engagement with the carry unit 314, and a
sealing flange 320, a bellows 322 and an organic material chamber 200
which are positioned in a portion in which the vapor organic material carry
pipe 210 and the moving shaft 130 pass through the deposition chamber
100 and are directed to buffering a vacuum difference between a high
vacuum state of the deposition chamber and a low vacuum chamber or
standby state of an assistant chamber 300 and to separating the same for
thereby connecting above two chambers.
Figure 2B is a cross sectional view taken along line A-A of Figure
2A according to the present invention.
As shown therein, a warm keeping heater 130 is installed in the
interior of the deposition chamber 100 for constantly maintaining an inner
temperature of the deposition chamber 100 in an upper and side surface
therein. A mother material mounting portion 140 is provided in the bottom
surface of the deposition chamber 100 for mounting the mother material
10 on which an organic material is deposited. A spraying unit 110 is
provided in an upper portion of the mother material mounting unit 140 for
spraying a vapor organic material. In addition, a vacuum pump 150 is
provided in a lower outer surface of the deposition chamber 100 for
making the interior of the deposition chamber 100 a high vacuum state.
An organic material chamber 200 is provided in an inner lower
portion of the assistant chamber 300 for evaporating an organic material.
A vapor organic material carry pipe 210 is connected to an upper portion
of the organic material chamber 200 for carrying a vapor organic material
from the organic material chamber 200 to the spraying unit 110. A carry
unit 314 is provided between the organic material chamber 200 and the
vapor organic material carry pipe 210 for controlling the movement of the
spraying unit 110. In addition, the assistant chamber 300 is adapted to
input an inert gas into the interior of the organic material chamber 200,
and a flow amount controller is provided in the outer portion of the same
for thereby controlling the amount of the input of the inert gas. The inert
gas inputted into the organic material chamber 200 plays a role of a
moving medium of the vapor organic material. Therefore, it is possible to
finely control the amount of carry of the vapor organic material, and it is
possible to uniformly distribute the vapor organic material.
Figure 2C is a cross sectional view taken along line B-B of Figure
2A according to the present invention.
As shown therein, the guide plate 112 engaged with the spraying
unit 110 is slidably engaged with the guide rail 120 adapted to guide the
moving direction of the spraying unit 110. The mother material mounting
unit 140 adapted to mount the mother material 10 therein includes an
electric magnet moving apparatus using an electric magnet 142 for
thereby implementing a fine movement in the horizontal direction.
The electric magnet moving apparatus adapted to the mother
material mounting unit 140 may be implemented based on the technology
of the patent "A deposition apparatus for fabricating an electro-luminance
device using an electric magnet and a deposition method using the
same(Patent application No. 10-2001-0077739). The same is not limited
thereby. In addition, a conventional moving apparatus may be adapted
instead of using the electric magnet moving apparatus.
It is possible to more accurately arrange the positions of the
spraying unit 110 and the mother material 10 in such a manner that the
position of the spraying unit 110 is adjusted based on the guide rail 120,
and the position of the mother material mounting unit 140 is adjusted using
an electric magnet moving apparatus, so that it is possible to implement
an accurate and effective organic material spraying operation thereby.
Figure 2D is a view illustrating an organic material chamber of the
portion C of Figure 2B according to the present invention.
The organic material chamber 200 is formed of a heat-resisting
material in a sealed shape having an inner space for storing an organic
material therein and includes a furnace 220 which has a carry gas inlet
hole 222 formed in a hole shape in order for a carry gas adapted to carry a
vapor organic material to be flown in and a vapor organic material inlet
hole 224 formed in a hole shape in order for an organic material vapor and
carry gas to be flown out, and an organic material heating heater 230
which surrounds an outer portion of the furnace 220 and is adapted to
heat the interior of the organic material chamber to a temperature at which
the organic material is evaporated.
The inlet pipe 240 which is formed in a pipe shape and is
connected with a flow amount controller 400 of Figure 2B is connected
with the carry gas inlet hole 222 formed in the furnace 220 through the
organic material chamber 200, so that an inert gas inputted from the flow
amount controller 400 is flown into the interior of the furnace 220.
In addition, the vapor organic material carry pipe 210 which is
formed in a pipe shape and is connected with the spraying unit 110 of
Figure 2B is connected with the carry gas outlet hole 224 formed in the
furnace 220 through the organic material chamber 200, so that the organic
material which is heated and evaporated by the organic material heating
heater 230 is carried to the spraying unit 110 adapted to spray a vapor
organic material to the mother material.
Figure 3 is a view illustrating various operation types of a vapor
organic material deposition apparatus according to the present invention.
Figure 3A is a view illustrating a state that a spraying unit of a
shower head shape is moved and sprays a vapor organic material
according to the present invention.
The spraying unit adapted to spray a vapor organic material 22
may be fabricated to have various shapes of a spraying port through which
the vapor organic material 22 is sprayed for thereby uniformly spraying the
vapor organic material 22. Figure 3A is a view illustrating a state that a
deposition operation is performed using a shower head shaped spraying
unit having a plurality of spraying ports(not shown) each having a smaller
diameter.
In the case that the spraying unit is fixed to a certain position for
thereby spraying a vapor organic material, there is a problem that the
vapor organic material is not uniformly sprayed onto the mother material.
As shown in Figure 3A, the spraying unit 110 adapted to spray the vapor
organic material 22 to the upper surface of the mother material 10 is
horizontally moved along the guide rail and sprays the vapor organic
material 22, so that the vapor organic material 22 is uniformly deposited
on the entire surfaces of the mother material 10. At this time, in the case
that the vapor organic material 22 deposited on the mother material 10 is
more than at least two kinds, there is provided a mixing tank 250 in the
vapor organic material carry pipe 210 for uniformly mixing the different
kinds of the vapor organic materials before the vapor organic material is
carried to the spraying unit 110. In addition, the mixing tank 250 includes
more than at least one partition in the interior of the same for uniformly
mixing more than at least two vapor organic materials while the same is
flown into the interior of the mixing tank 250 and is flown to the outside of
the mixing tank 250.
Figure 3B is a view illustrating a state that a mother material
mounting unit with a mother material is horizontally moved based on a
carrying method using an electric magnet when a spraying unit which is
formed in a shower head shape sprays a vapor spraying material.
On the contrary to the operation that the spraying unit 110 is
horizontally moved when the spraying unit 110 sprays a vapor organic
material 22 as shown in Figure 2A, when the mother material mounting
unit 140 with the mother material 10 is horizontally moved when the
spraying unit 110 sprays a vapor organic material 22 as shown in Figure
3B, it is possible to obtain the same effect as the effect of Figure 2A in
which the vapor organic material 22 is uniformly deposited on the upper
surface of the mother material 10. In addition, differently from the
operation that the spraying unit 110 is moved by the guide rail as shown in
Figure 3A, the method in which the mother material mounting unit 140 is
horizontally moved when the spraying unit 110 sprays a vapor organic
material 22 uses a carrying method using an electric magnet, so that it is
possible to accurately control the movement of the mother material
mounting unit 140.
Figure 3C is a view illustrating a state that a vapor organic material
is deposited on a mother material using a spraying tube according to the
present invention.
As shown therein, in a deposition apparatus using a spraying tube,
a vapor organic material 22 which is carried into the interior of the
deposition chamber 100 through a mixing tank 250 adapted to uniformly
mix more than at least two vapor organic materials is formed of quartz,
ceramic or metallic material and is formed in a structure in such a manner
that the thusly formed organic materials are deposited on an upper surface
of the mother material 10 through the spraying tube 112 which has a
diameter of 3~20mm. The vapor organic material deposition apparatus
using the spraying tube 112 is capable of forming a flat organic thin film at
a high rate.
Figure 3D is a view illustrating a state that a vapor organic material
is deposited on a mother material as the spraying tube is rotated and
moved upwardly and downwardly according to the present invention.
As shown in Figure 3C, the deposition apparatus includes a
rotation motor 114 installed in an upper portion of the deposition chamber
100 and adapted to rotate the spraying tube 112, and a vertical moving
motor 116 adapted to vertically moving the spraying tube 112. In the above
construction, the spraying tube 112 is rotated and is moved upwardly and
downwardly and at the same time sprays a vapor organic material 22 on
an upper surface of the mother material 10. In addition, the spraying tube
112 may have a step shaped bent portion in such a manner that an end
portion of the spraying tube 112 through which a vapor organic material 22
is sprayed, moves in a circular shape when the same is rotated by the
rotation motor 114.
In this embodiment, since it is possible to freely adjust the position
of the spraying tube 112 by the rotation motor 114 and the vertical moving
motor 116, the deposition apparatus of Figure 3C is possible to uniformly
spraying a vapor organic material.
Figure 4 is a view illustrating a process that a carry gas is mixed
with a vapor organic material which is obtained by heating an organic
material.
Figure 4A is a view illustrating a state that a vapor organic material
and a carry gas are mixed in the interior of a furnace according to the
present invention.
As shown in Figure 4A, the organic material 20 heated and
evaporated by the organic material heating heater 230 is mixed with a
carry gas flown in along the inlet pipe 240 connected with the interior of
the furnace 220 in the interior of the furnace 220. When the vapor organic
material and the carry as are mixed in a such a manner of Figure 4a, since
the organic material is evaporated and at the same time is mixed with a
carry gas, it is possible to implement an easier mixing and uniform mixing
operation.
Figure 4B is a view illustrating a state that a vapor organic material
and a carry gas are mixed in the outside of a furnace according to the
present invention.
As shown therein, the mixing apparatus is constituted in such a
manner that a carry gas inlet pipe 240 is connected with a vapor organic
material carry pipe 210 positioned in the outside of the vapor organic
material chamber 200. The vapor organic material 20 which is heated and
evaporated by the vapor organic material heating heater 230 is carried
along the vapor organic material carry pipe 210 and is mixed with a carry
gas flown in through the carry gas inlet pipe 240 connected with the vapor
organic material carry pipe 210. Since the thusly constituted mixing
apparatus does not have an additional structure for engaging the carry gas
inlet pipe 240 to the furnace 220 and the organic material chamber 200, it
is possible to implement an easier fabrication of the system.
Figure 5 is a view illustrating various constructions of a furnace
and a vapor organic material outlet hole according to the present invention.
Figure 5A is a view illustrating the construction of a furnace which
is formed in a rectangular parallelepiped shape and has one vapor organic
material outlet hole in an upper portion of the same according to the
present invention.
As shown therein, the outer surfaces of the rectangular
parallelepiped shape furnace 220 are surrounded by the organic material
heating heater 230 adapted to heat the organic material in the interior of
the furnace 220, and a vapor organic material outlet hole 222 is provided
in an upper portion of the same for thereby discharging a vapor organic
material.
Figure 5B is a view illustrating the construction of a furnace which
is formed in a rectangular parallelepiped shape and has a plurality of
vapor organic material outlet holes in an upper portion of the same.
A large amount of the vapor organic material must be discharged
for a high rate film growth in which a vapor organic material is deposited
on a mother material at a high rate. Namely, there is a problem that it is
impossible to discharge a large amount of vapor organic material by
providing only one vapor organic material outlet hole 222 in the upper
portion of the furnace 220. In order to overcome the above problem, as
shown in Figure 5B, there are provided a plurality of vapor organic
material outlet holes 222 in an upper portion of the furnace 220.
Figure 5C is a view illustrating the construction of a furnace which
is formed in a cylindrical shape and has one vapor organic material outlet
hole in an upper portion of the same.
In order to more effectively evaporate the organic material in the
interior of the furnace 220, the furnace 220 may be fabricated in various
shapes. In the case that the furnace 220 is formed in a rectangular
parallelepiped shape, since the heat generated in the organic material
heating heater 230 surrounding the furnace 220 is not uniformly
transferred to the outer surfaces of the furnace 220, a lot of heat loss
occurs. Therefore, it is impossible to accurately adjust the amount of the
vapor organic material generated. As shown in Figure 5C, the furnace 220
is formed in a cylindrical shape, so that the heat generated in the organic
material heating heater 230 is uniformly transferred to the outer surfaces
of the furnace 220. Therefore, it is possible to effectively use the heat
generated in the organic material heating heater 230 by changing the
construction of the furnace 220 and to easily adjust the amount of the
generation of the vapor organic material. In addition, the furnace 220 is not
limited to the rectangular parallelepiped and cylindrical shapes. Namely,
the furnace 220 may be formed in a polygonal hexahedron and spherical
shape.
Figure 5D is a view illustrating the construction of the furnace
which is formed in a cylindrical shape and has a plurality of vapor organic
material outlet holes in an upper portion of the same.
In order to discharge a large amount of the vapor organic material
from the cylindrical furnace 220 as shown in Figure 5C, there may be
provided a plurality of vapor organic material outlet holes in the upper
surface of the furnace 220 in the same manner as Figure 5B.
Figure 6 is a view illustrating the construction that a fixed
temperature heater is provided in the outside of the vapor organic material
carry pipe according to the present invention.
When the vapor organic material from the furnace 220 is carried
through the vapor organic material carry pipe 210, when the vapor organic
material carry pipe 210 is contacted with an external air and is cooled, the
vapor organic material flowing in the interior of the vapor organic material
carry pipe 210 is also cooled. In this case, when the vapor organic
material is cooled to a certain temperature below a proper temperature,
the deposition on the mother material becomes bad. As shown in Figure 6,
in order to overcome the above problem, a fixed temperature heater 260
having a heating wire 262 adapted to generate heat and accurately
maintain and adjust the heating temperature is provided in the outer
portion of the vapor organic material carry pipe 210.
In addition, the fixed temperature heater 260 may be provided in
the organic material chamber 220 for thereby constantly maintaining the
temperature of the organic material chamber 200.
<Second embodiment
A fabrication apparatus of an organic semiconductor apparatus
and a fabrication method of the same which may use a wider area
substrate used when an organic semiconductor is fabricated according to
a second embodiment of the present invention will be described with
reference to Figure 7.
In the organic semiconductor system of Figure 7, the vapor
organic material deposition apparatus 700 of the wider area substrate of
the second embodiment of the present invention includes a gas reservoir
701 adapted to reserve an inert gas therein, a gas heater 703 which is
installed between the gas reservoir 701 and a MFC(Mass Flow Controller)
702 and is adapted to heat the inert gas, a connection pipe 707 installed in
the interior of the heater pipe 706, at least one deposition source tank 714,
a deposition source tank 714 which includes a gas deposited and an
organic material therein, a scan head 709 which has a deposition rate
adjusting unit 715 for checking and adjusting the flow of the deposition gas,
a buffer chamber 711 , a gate valve 711 adapted to gate the flow of the
deposition gas and open and close the same, and a deposition chamber
713 adapted to deposit a gas flown in from at least one deposition source
tank 714 on a wider area substrate 712.
As shown in Figure 7, the gas reservoir 701 may store an inert gas
such s Ar, He, N2, etc. and oxygen and all kinds of gases used in a
conventional CVD and which is not explosive. The amount of the gas is
adjusted, and the gas is flown into the interior of the heat deposition
source tank 714 through the MFC 702. The thusly flown-in gas is heated
to a high temperature of 200~600°C using the gas heater 703 and is flown
into the interior of the heat source.
In the present invention, a state that an organic material particle
and a high temperature gas co-exist, namely, a non-uniform state of a
solid and gas is assumed as a solid-gas heterogeneous phase(SGHP),
and a material of a diluted state is assumed as a material of the SGHP. In
addition, the organic material in the interior of the deposition source tank
714, for example, the organic material is diluted with a certain material
such as Alq3 and exists in the interior of the deposition source tank 714.
The material of the inert SGHP is heated by a heat source in the
deposition source tank 714, and the SGHP in the interior of the deposition
source tank 714 is heated by a convention current effect for thereby
generating a large amount of the organic material gas phase. In addition,
the SGHP material of the organic semiconductor is inputted into the
interior of the deposition chamber 713 using a pressure difference
between the deposition chamber 713 and the deposition source tank 714
through a connection pipe 707 of the organic semiconductor deposition
chamber 713. In the above process, the connection pipe 707 is heated to
a high temperature for preventing the vapor organic material from being
accumulated in the interior of the connection pipe 707. In particular, when
using Alq3, it is preferably heated to 320°C. In the above heating process,
in order to prevent a heat loss of the connection pipe 707, a double pipe is
formed for thereby constantly maintaining the temperature gradient. In
addition, the vacuum state is maintained in the connection pipe 707 for
thereby maintaining a temperature of the connection pipe 707. In addition,
in the downward type method, since the shadow effect by the mask may
be eliminated by adapting the deposition source tank capable of storing a
large amount of materials, the thick shadow mask may be used. Namely, it
is possible to implement a long time process by decreasing the alignment
error of the aligning portions of the shadow mask.
The vapor organic material inputted into the scan head 709
through the connection pipe 707 is deposited on the upper portion of the
substrate 712. At this time, the inner portions of the scan head 709 are
heated using a resistance type heat source based on the same method as
the connection pipe 707 for preventing a vapor organic material deposition.
In addition, in the case that the deposition process is not performed in the
substrate in the scan head 709, the scan head 709 is moved to the buffer
chamber 710. In addition, the buffer chamber 710 and the deposition
chamber 713 are fully separated, so that a temperature increase is
prevented in the substrate in which the heat source of the scan head 709
is wider and in the interior of the deposition chamber 713.
When the scan head 709 is positioned in the buffer chamber 710,
the amount of the vapor organic material sprayed from the scan head 709
is adjusted and stabilized using a crystal sensor 715 of the monitor in the
interior of the buffer chamber 710. Actually, a thickness measuring system
does not exist in the interior of the deposition chamber. The adjustment of
the thickness in the process is performed based on a process time.
Figure 8 is a view illustrating a plurality of deposition source tanks
and scan heads capable of effectively processing a SGHP organic
material in the interior of the system of Figure 7.
As shown therein, first, second and third deposition source tanks
741 , 742 and 743 supply a large amount of the organic material through
the first, second and third connection pipes 771 , 772 and 773 connected
with the tanks and the first, second and third scan heads 791 , 792 and 793.
In addition, in the buffer chamber, there is provided an assistant furnace
745 in such a manner that as the scan head is moved, the organic
material is collected and re-circulated,.
Figure 9 is a view of an operation method of a scan head in the
deposition chamber capable of carrying a SGHP organic material
according to the present invention.
As shown therein, in the deposition method using the scan head
709 according to the present invention, the vapor organic material itself is
performed based on a laminar flow pumping operation by the HIVAC pump
714 and is moved in the directions indicated by arrows of L, L', L" and L'".
Therefore, the deposition is performed based on the opening and closing
operation of the gate valve 71. Since the pumping port 732 is provided in a
lower portion of the substrate, the flow of the vapor organic material is
stably implemented, so that it is possible to implement a uniform thickness
of the organic material thin film deposited on a wider area substrate.
Therefore, since there is not any loss in the deposition in the directions of
arrows of L, L', L" and L'", it is possible to significantly increase the
efficiency of the material.
Figure 1-0 is a view of a moving method of a scan head capable of
carrying a SGHP organic material of the interior of Figure 8. The
movement of the longitudinal direction of the scam head 709 in the
deposition process of Figure 10 is implemented in such a manner that the
piston rod 718 reciprocates between P through P' at a constant speed
using the motor 717. The length of the scan head 719 and the moving
length of the longitudinal direction of the scan head 709 using the motor
717 are determined based on the size of the substrate. In addition, the
scan head adjusts the amount of the generation of the vapor organic
material by a flow rate adjusting unit 716.
Figure 11 is a view for explaining a vapor organic material
generation method of an organic semiconductor apparatus according to
the present invention.
As shown therein, there are provided a deposition source tank 714,
an external heat source heater 701 , an organic material particle 752 in a
deposition source tank 714, a high temperature gas 753 in the interior of
the deposition source tank 714, an organic material stored in the interior of
the deposition source tank 714 and a gas inputting pipe 755. In the vapor
organic material generation method of a semiconductor apparatus
according to the present invention, when a vapor organic material is
generated, since the heat conductivity of the materials used in the organic
semiconductor are low, when a common cell type heat source is used, an
evaporation of an organic material is difficult, and since a heat is
concentrated on a certain portion, the organic materials in the deposition
source tank 714 may be deteriorated.
As shown in Figure 11, a high temperature gas is sprayed into the
deposition source tank 714 through the gas input pipe 755, and in the
organic material itself, the gas and organic material are diluted in the
interior of the deposition source tank 714. Therefore, the organic material
particle 752 and high temperature gas 753 coexist in the deposition source
tank 714. In addition, The temperature of the deposition source tank 714 is
increased using the heat source heater 751 in the outer portion of the
deposition source tank 714. A heat conduction is performed in the diluting
portion of the coexisting state in the heating portion based on a convection
current method for thereby generating a large amount of the organic
materials. In addition, it is possible to generate a large amount of the
vapor organic material at an external temperature of a heat source lower
compared to the conventional method.
Figure 12 is a view illustrating a deposition method in the interior
of the deposition chamber based on a vapor organic material generated in
Figure 11 according to the present invention. The deposition and carrying
method of the vapor organic material of Figure 12 will be described. As
described above, it is possible to generate a large amount of the vapor
organic material in the interior of the deposition source tank 714.
Therefore, a difference between a vacuum pressure in the interior of the
deposition chamber 713 and the vacuum pressure of the interior of the
deposition source tank 714 is above 100 times. For example, if the
vacuum degree of the system is 10-4Torr and the pressure difference is
formed in such a manner that the pressure of the deposition source tank
714 is 10-1Torr, it is possible to induce the vapor organic material in the
deposition chamber in the interior of the deposition source tank 714. In
addition, the connection pipe is heated to a high temperature in order for
the vapor organic material not to be deposited. In the deposition chamber
of Figure 12, the scanning method including the scan head 761 and the
substrate 762 will be described. The vapor organic material induced by the
scanning method of Figure 12 is actually deposited on the substrate.
However, the vapor organic material is not deposited on a wider area
substrate at one time. As shown in Figure 12, the deposition process on a
wider area substrate is performed as the deposition is performed on a
certain region of the substrate, and the scan head 709 is moved at a
constant speed based on the movement of the scan head 709.
Figure 13 is a flow chart of an operation of a deposition apparatus.
In the deposition apparatus, the substrate 712 is loaded into the deposition
chamber 710(S710). The deposition source tank 714 is pre-heated, and a
high temperature gas of 200°C to 600°C is inputted into the deposition
source tank 714(S712). In addition, the high temperature of the interior of
the deposition source tank 714 and the organic material particles are
mixed for thereby forming a certain mixture. When the temperature of the
deposition source tank 714 is increased, a SGHP material is
generated(S714). A large amount of the generated SGHP material is
carried from the deposition source tank 714 to the buffer chamber 710
through the connection pipe 707(S716). At this time, in the buffer chamber
710, the flow amount of the vapor organic material is measured using a
vapor organic material sensor. When the amount of the vapor organic
material reached at a set amount, the buffer gate valve is opened(S718).
The deposition process of the vapor organic material is performed based
on the operation of the scan head 709(S720). After the set deposition time
is passed, the scan head 709 is moved(S722), and the buffer gate valve
711 is closed, and the substrate is unloaded(S724).
The vapor organic material deposition apparatus and method of a
wider area substrate according to the present invention will be described
with respect to the results of the experiments.
According to the experiments using the apparatus of Figure 13,
the graphs of Figures 7, 10, 15 and 16 will be described based on the
conditions: Used material: Alq3, substrate size: 370x470mm, used gas:
Ar(340°C), deposition source tank temperature: 300°C, uniformity of
deposition source tank: ±5%.
Figure 14 is a relative relationship graph of a temperature of a gas
diluted and a deposition amount according to the present invention, Figure
15 is a graph of a vapor organic material with respect to the amount of a
diluting gas according to the present invention, and Figure 16 is a graph of
a relationship of a deposition source tank temperature and a deposition
amount in the case that only a deposition source tank is heated without a
diluting gas according to the present invention.
As shown in Figure 14, it is checked that there is not any effect in
the temperature of the diluting gas with respect to the amount of the
deposition. As shown in Figure 15, as the amount of the diluting gas is
increased, the amount of the SGHP in the interior of the deposition source
tank 714 is increased, and the amount of the gaseous organic material is
increased by the heat of the deposition source tank 714, so that the
amount of the vapor organic material produced through the scan head 709
is increased. In addition, as shown in Figure 16, in the case that the
deposition source tank 714 itself is heated, it is checked that a small
amount of a gaseous organic material is generated.
In other words, as shown in Figures 13, 14, 15 and 16, in the case
that there is not a diluting gas, the amount of the SGHP of the interior of
the deposition source tank 714 is increased based on the input of the
diluting gas compared to the method of the conventional deposition source
tank 714 in which the amount of the generation of the vapor organic
material is small. In addition, it is checked that the SGHP generates a
large amount of the vapor organic material in the interior of the deposition
source tank 714 based on the conventional current principle.
Therefore, since the buffer chamber 710 and the deposition
chamber 713 are fully separated using the gate valve 711 , it is possible to
prevent a temperature increase in the substrate in which the heat source
of the scan head 709 is wider, and in the interior of the deposition chamber
713. In addition, the adhesive force with respect to the substrate of the
organic thin film is increased, and it is possible to adjust the thickness to a
common thickness accurately and stably. It is possible to store a large
amount of the materials.
As described above, in the vapor organic material deposition
method and a vapor organic material deposition apparatus using the same
according to the present invention, it is possible to uniformly deposit a
vapor organic material on a wider area substrate and to fast grow a film. In
addition, it is possible to implement a fine adjustment of the mixing amount
of the organic material. In addition, since a vapor organic material is
sprayed on only a portion on which a vapor organic material is deposited,
it is possible to effectively deposit a vapor organic material. The organic
material may be saved in the present invention.
In addition, in the vapor organic material deposition method and a
vapor organic material deposition apparatus using the same according to
the present invention, it is possible to increase an adhesive force with
respect to a substrate of an organic thin film by diluting an organic material
particle in the interior of the deposition source tank. In addition, it is
possible to prevent a temperature increase in a wider area substrate of a
heat source by a scan head and in the interior of the deposition chamber
by fully separating the buffer chamber and the deposition chamber using a
gate valve and continuously moving a heat source of a small side of the
scan head. In addition, in the present invention, since it is possible to
eliminate a shadow effect by a mask in a downward method by adapting a
deposition source tank which is capable of storing a large amount of
materials, it is possible to use a thick shadow mask. Namely, it is possible
to overcome a problem in an aligning portion of a shadow mask.
As the present invention may be embodied in several forms
without departing from the spirit or essential characteristics thereof, it
should also be understood that the above-described examples are not
limited by any of the details of the foregoing description, unless otherwise
specified, but rather should be construed broadly within its spirit and scope
as defined in the appended claims, and therefore all changes and
modifications that fall within the meets and bounds of the claims, or
equivalences of such meets and bounds are therefore intended to be
embraced by the appended claims.