TECHNICAL FIELD
[0001] The present invention relates in general to the field of applying a liquid to a surface
of an object located in a vacuum environment.
BACKGROUND
[0002] In industry and science, there is a need to modify surfaces of objects by applying
a specific material to the surface. This may aim to obtain unique surface properties
of the object, to protect the surface, to prepare the surface for a further processing
stage, etc. Modification of the surface by coating it with a material can be performed
using gases, liquids and solid matter.
[0003] There are known vacuum systems that provide high purity of the application process.
These systems allow removal of air and contaminants contained in the air from the
surroundings of the object, so that the surface of the object can be properly modified.
So far, modification of the surface of an object located in a vacuum by exposing it
to gases or by applying materials in a solid state to the surface has been well mastered.
However, effective methods for applying materials in a liquid form to an object, particularly
in a high vacuum environment, have not been satisfactorily developed yet.
[0004] There is a particular need for systems that would enable solutions of organic molecules
and their complexes, ionic liquids and other similar compositions to be effectively
applied to objects. Applying liquids to an object in a high vacuum environment is
problematic because liquids introduced into the vacuum begin to boil, i.e. evaporate
dynamically throughout their volume.
[0005] The systems for applying liquids to an object in a vacuum environment that have been
developed so far have some disadvantages.
[0006] A common feature of most of the known systems is that they use a needle positioned
above the object to apply the liquid to the object. For example, such solutions are
described in the publications "
Real Space Observation of Double-Helix DNA Structure Using a Low Temperature Scanning
Tunnelling Microscopy" (by Takashi KANNO et al., in Jpn. J. Appl. Phys. Vol. 38 (1999)
pp. L 606-L 607), "
Controlled injection of a liquid into ultra-high vacuum: Submonolayers of adenosine
triphosphate deposited on Cu (110)" (by Sobrado, J. M. et al., in Journal of Applied
Physics 120.14 (2016): 145307), "
Microcontroller design for solution-phase molecular deposition in vacuum via a pulsed
solenoid valve" (by Margaret Wolf et al., in J. Vac. Sci. Technol. A 38, 022413 (2020)), "
The direct injection of liquid droplets into low pressure plasmas" (by Ogawa, D. et
al., in Journal of Vacuum Science & Technology A: Vacuum, Surfaces, and Films 27.2
(2009): 342-351). The disadvantage of this type of solutions is that a droplet of liquid may form
on the tip of the needle from which the liquid is injected, wherein this droplet may
fall onto the object in an undispersed form, which makes it necessary to resume the
process all over again.
[0007] A European patent application
EP3034182A1 discloses a coating system comprising a coating chamber having arranged therein a
coating apparatus for providing a substrate with an organic coating layer. The substrate
has a form of a tape that is moved on rollers near a horizontally positioned needle
that sprays a liquid substance in a vacuum chamber onto the moving tape. This poses
a risk of contamination of the tape being coated with the drop of liquid that could
form on the tip of the needle and fall therefrom onto the tape. A system for adjusting
the distance between the needle and the object being coated is also used, wherein
the system is installed in the same vacuum chamber wherein the coating is carried
out, which introduces a risk of carrying contamination from the adjustment system
mechanisms into the operating chamber where the coating is carried out, and exposes
the mechanical components of the adjustment system to harmful fumes of the substance
being sprayed, which can be detrimental to the adjustment system mechanisms.
SUMMARY
[0008] There is a need to improve vacuum systems for applying liquids to an object, to at
least reduce the drawbacks of the state-of-the-art systems described above.
[0009] In one aspect, the invention relates to a vacuum system for applying a liquid to
an object, the vacuum system comprising a first module for generating a vacuum; a
second module with a user chamber and an injection chamber for applying the liquid
to the object under vacuum conditions; and a third module comprising a set of components
for preparing the liquid and supplying the liquid to an injection needle. The first
module is tightly connected to the second module and the second module is tightly
connected to the third module. The second module is connected to the third module
via a sealed linear movement system. The injection needle passes through the sealed
linear movement system to inject the liquid prepared in the third module, so that
the injection needle protrudes from the linear movement system into the interior of
the injection chamber in the second module and is movable in the horizontal axis relative
to the object located in the second module onto which the liquid from the injection
needle is to be sprayed.
[0010] The system according to the invention ensures that objects can be coated by very
thin layers, of the order of even a few nanometers, by maintaining conditions of controlled
needle-to-object distance under conditions of high vacuum. In the injection chamber,
there are no unnecessary components; it basically contains only the object to be processed
and the injection needle, while the components for preparing the liquid and for moving
the injection needle are located outside the injection chamber.
[0011] The sealed linear movement system can be a linear bellows manipulator. This is a
particularly preferable solution with regard to ensuring high vacuum conditions. Moreover,
it allows the needle-to-object distance to be adjusted.
[0012] The injection chamber may comprise a manipulator to rotate the object. This allows
the object to be coated from different sides. When the surface of the object is uneven,
the uniformity of the coated layer can be achieved by adjusting the needle-to-object
distance.
[0013] The second module may further comprise a user chamber separated from the injection
chamber by a vacuum-tight gate valve. This allows a clean object to be prepared in
the user chamber, moved to the injection chamber in a tight manner and, after the
coating has been applied, moved again in a tight manner to the user chamber, where
it can be further tested under tight conditions with regard to the applied coating.
[0014] The system may comprise an externally controlled manipulator to move the object between
the user chamber and the injection chamber. Controlling the manipulator from the outside
ensures tightness between the chambers.
[0015] The injection chamber may be separated from the user chamber by a high-tightness
gate valve mounted on a ConFlat class fitting. The injection chamber can be separated
from a pumping chamber in the first module by a high-tightness gate valve mounted
on a ConFlat class fitting. Preferably, the linear movement system ensures tightness
through mounting on a ConFlat class fitting. The use of components mounted on the
ConFlat class fittings allows high vacuum conditions to be maintained in the injection
chamber.
[0016] In another aspect, the invention relates to a method for applying a liquid to an
object in the vacuum system as described herein. The method comprises: in the injection
chamber in the second module, generating vacuum conditions with a pressure of p <
9E-9 mbar; moving the object from the user chamber, with pre-generated pressure of
p < 9E-9 mbar, to the injection chamber; closing the valve that separates the injection
chamber from the user chamber; preparing the liquid to be injected in the third module;
equalizing the pressure between the injection chamber and a reservoir with the liquid
to a value between 1E-1 and 1E1 mbar; spraying the object with the liquid using the
injection needle, and adjusting the spraying parameters while spraying, by adjusting
a distance of the injection needle from the object and parameters of a pulsed operation
of a valve supplying a gaseous medium to the reservoir with the liquid; after the
spraying is finished, sealing the injection chamber against the reservoir with the
liquid, reducing the pressure in the injection chamber to below 9E-9 mbar and opening
the valve that separates the injection chamber from the user chamber; and moving the
object from the injection chamber to the user chamber.
[0017] Starting the process under conditions of high vacuum and maintaining tightness throughout
the process ensures that a high degree of purity is maintained in the injection chamber,
so that, through the operation of the valve and the needle-to-object distance, only
a precisely defined amount of sprayed liquid is delivered to the object. This allows
for very good control over the parameters of the applied layer. The object is not
exposed at any stage to any liquid or gas other than that used intentionally during
the application process; in particular, it is not exposed to air and contaminants
contained therein.
BRIEF DESCRIPTION OF DRAWINGS
[0018] The object of the invention is presented by means of example embodiments in the drawing,
wherein:
Fig. 1 shows schematically a structure of an embodiment of the system according to
the invention in a cross-sectional view.
Fig. 2 shows a diagram of sealings between individual elements of the system according
to the embodiment of Fig. 1.
Fig. 3A-3C, 4A-4C show test results related to a first embodiment.
Fig. 5A-5D, 6A-6B show test results related to a second embodiment.
DETAILED DESCRIPTION OF EMBODIMENTS
[0019] An example embodiment of the system according to the invention is shown in Fig. 1.
The system comprises three modules: a first module (A), referred to as a vacuum generation
module; a second module (B), referred to as a operating module; and a third module
(C) referred to as a liquid dispensing module. The structure of the individual modules
is schematically shown in a cross-section in two different planes in Fig. 1: the first
module (A) is shown in a vertical cross section (in the yz plane), the second module
(B) is shown in a horizontal cross section (in the xy plane) and the third module
(C) is shown in a vertical cross section (in the yz plane). It is important to note
that the third module (C) is positioned next to the second module (B) and is movable
with respect to the second module (B) in a horizontal plane on the y-axis. The first
module (A) can be positioned anywhere relative to the second module (B) - for example,
next to, above or under the second module (B).
[0020] Individual components of the modules A, B and C should be made of vacuum-compatible
materials, for example made of stainless steel. The sealing elements should be made
of materials that are resistant to solvents used in the process.
[0021] The first module (A) comprises components for vacuum generation. The detailed structure
of this module is not essential for the invention and different types of vacuum generation
modules that will be capable of ensuring high vacuum conditions, in particular capable
of providing a pressure p < 9E-9 mbar in the second module (B), can be used. In the
embodiment shown here, the first module (A) comprises a pumping chamber 2 connected
by a gate valve 7a to the second module (B). A wide-range vacuum gauge 1 (which allows
accurate measurement of high vacuum) and a turbomolecular pump 3 are connected to
the pumping chamber 2, the turbomolecular pump 3 being connected by a manual isolation
valve 4a, 4b to a dry pump 5 that, in turn, is connected to the pumping chamber via
an infiltration valve 6.
[0022] The second module (B) is the operating module comprising a user chamber 8 into which
the user can introduce the object onto which the liquid layer is to be applied. In
the user chamber 8, tests may be carried out on an object with a layer applied thereon.
The user chamber 8 is connected by a gate valve 7b to an injection chamber 9, where
the liquid is sprayed onto an object 10 from a needle 11, also known as an injection
needle. The object can be moved between the user chamber 8 and the injection chamber
9 using a manipulator 12, allowing movement along the x-axis and rotation of the object
around the x-axis.
[0023] The third module (C) is a module for preparing liquid to be injected through the
needle 11. The detailed specification of its components is irrelevant to the essence
of the invention, and various types of liquid preparation components well known in
prior solutions for applying liquids to an object under vacuum conditions, including
those in which the needle is positioned vertically above the object, can be used.
For example, the components for preparing liquid to be injected include a container
14 (for example, a syringe) with liquid, connected to isolation valves 4c, 4d, 4e
and a solenoid valve 15, between which a reservoir 18 with liquid to be injected is
formed. The amount of liquid being injected is adjusted by the solenoid valve 15 with
a pulse length controller, also connected to a reservoir 17 with a gaseous medium.
The gaseous medium can be noble gases (for example, argon) or other gases, such as
those that do not react with a given object and liquid (for example, nitrogen).
[0024] It is important that between the second module (B) and the third module (C), a linear
movement system 13 is mounted and it allows the third module (C) to be moved relative
to the second module (B) in a horizontal plane along the y-axis. For example, it could
be a bellows-based system that can be precisely stretched and compressed. For example,
a linear bellows manipulator can be used that comprises vacuum-tight metal bellows
that can be accurately compressed and stretched, causing a change in the distance
between the connection points located at the ends of the bellows. Thus, the bellows
may comprise the injection needle 11, one end of which extends above the first end
of the bellows in the injection chamber 9, and the other end of which extends above
the second end of the bellows in the third module (C) for preparing liquid and is
connected there to liquid preparation components which, in turn, are connected by
flexible hoses 16 to the reservoir 17 with gaseous medium and a pump 19. Thus, the
entire third module (C) or an assembly of components for preparing liquid to be injected
(in particular, the assembly of valves 4c, 4d, 4e and 15, between which the reservoir
18 with liquid to be injected, preferably also the container 14 with liquid, is formed)
connected by the flexible tubes 16 to the reservoir 17 with gaseous medium may be
mobile.
[0025] The coating parameters to be obtained on the object to be coated are adjusted by
selecting the distance of the needle 11 from the object and the amount of liquid to
be supplied via the valve 15, by selecting the opening pulse length (manually or automatically).
[0026] Fig. 2 schematically shows a diagram of sealings between individual elements of the
system according to the embodiment of Fig. 1. The following sealings are used:
- CF class (ConFlat), i.e. with very high tightness, dedicated to ultra-high vacuum,
according to ISO 3669:2020;
- SW class (Swagelok standard, these are high-tightness connections, suitable for liquids
and gases)
- KF class (with medium tightness, according to ISO 2861:2020)
- LL class (Luer Lock, i.e. with low tightness, used for components requiring cyclic
replacement due to ease of use, according to ISO 80369-7:2021)
[0027] In particular, to maintain high vacuum conditions, it is advisable that the injection
chamber 9 be separated from the pumping chamber 2 and the user chamber 8 by ConFlat
class gate valves, as well as that the manipulator 12 and the linear movement system
13 provide a ConFlat class tightness.
[0028] The tip of the needle 11 can be mounted using a connection with a tightness of LL
to CF, as the linear movement system 13 provides a CF class tightness.
[0029] The use of Swagelok connections (and valves of this standard) at the connection of
the elements 6, 4b and the chamber 9 results from the need to use elements with a
smaller internal cross-section. The effective pumping speed (EPS) is, in practice
and to the greatest extent, a function of the cross-sectional area at the narrowest
point of the system and the length of that narrowing. In the present device, the influence
of the narrowing length is not of much importance as all the elements are close together.
However, the cross-section is of great importance. The smallest internal diameter
available in the CF standard is DN16CF (i.e. a nominal diameter of 16 mm), while in
the SW standard, it is possible to use pipes with an internal diameter of 3 to 4 mm.
This combination of cross-sections and valves allows so-called differential pumping
and precise control until the valve 7a, which connects the chambers 2 and 9 (where
the cross-section is already considerably larger, for example, nominally equal to
63 mm - DN63CF), is fully opened. When this valve is fully opened, it is possible
to pump at the full efficiency of the turbomolecular pump. For example, the turbomolecular
pump can also be connected with a DN63CF connector - in this situation, pressures
of E-9 mbar and below are easily achieved.
[0030] The SW connections, in turn, are used under ultra-high vacuum conditions. Because
at the point of their use, there are small cross-sections and a metal-to-metal sealing
(in particular, a clamped conical sleeve), it is possible to work with pressures of
E-9 mbar and below. In practice, connections of this type exhibit so-called infiltration
rates of 10E-11 mbar *l/s, i.e. comparable to the CF standard.
[0031] The system shown in Fig. 1 can be used as follows. At first, the valve 7b in the
second module (B) that separates the user chamber 8 from the injection chamber 9 is
closed. At this stage, the valves 6 and 4b in the first module (A) and the valves
4c, 4d, 4e, 15 located in the third module (C) are closed, the third module (C) being
thus isolated from the second module (B). In the user chamber 8, the user creates
or maintains, by any known means, ultra-high vacuum conditions, i.e. p < 9E-9 mbar.
In the user chamber 8, there is the object. Before starting the operation, the valve
4a and the valve 7a in the first module (A) are opened. A pump set consisting of the
dry pump 5 and the turbomolecular pump 3 is activated. The chambers 2 and 9 are pumped
out of the atmospheric pressure level and a vacuum of p < 9E-9 mbar is then generated.
Pressure measurement in the chambers 2 and 9 is carried out continuously by the wide-range
vacuum gauges 1. At this stage, the pressures in the user chamber 8 and in the injection
chamber 9 are in the same range, i.e. p < 9E-9 mbar. The valve 7b is opened and the
object prepared for coating is then moved from the user chamber 8 to the injection
chamber 9 using the manipulator 12. Then, the valve 7b between the chambers 8 and
9 is closed and the pressure in the injection chamber 9 is set at p < 9E-9 mbar. Subsequently,
the valve 7a is closed, cutting off the first module (A) from the second module (B),
resulting in a gradual increase in pressure in the injection chamber and setting the
pressure in the chamber in the range of 1E-1 > p > 9E-9 mbar, for example to a vacuum
of E-5 mbar. The increase in pressure in the chamber 9 is due to the lack of access
to the first module (A) and the establishment of the related equilibrium (static vacuum).
The third module (C) is then pumped until the pressure is below 1E-1 mbar, by opening
the valve 4e connected to the pump 19, which has the ability to determine the pressure.
The first sequence is then carried out, wherein the liquid in the syringe 14 is refilled,
the valve 4e is closed, the valve 4c is opened, the liquid is introduced into the
reservoir 18 and the valve 4c is closed; the valve 4d is then opened and the pressures
in the injection chamber 9 and the reservoir 18 are equalized - the final pressure
depends on the amount of liquid introduced and its physical characteristics, and will
generally be between 1E-1 and 1E1 mbar; the valve 4d is then closed. A second sequence
is then carried out, wherein the liquid in the syringe 14 is refilled, the valve 4c
is opened, the liquid is introduced into the reservoir 18 and the valve 4c is closed;
after that the valve 4d is opened and the pressure in the reservoir 18 is increased
by a controlled, gradual supply of gaseous medium induced by the pulsed operation
of the valve 15 (the valve 15 is a normally closed valve). For example, the gaseous
medium can be supplied at a pressure of 5 bar. Using the manipulator 12, the object
is placed in position for liquid application. As a result of the pulsed operation
of the valve 15, the liquid is discharged (injected) through the needle 11 towards
the object. At the end of the object spraying process (the end of operation of the
valve 15), the pressure in the chamber 2 is in the range of 1E-1 > p > 5E3 mbar. In
the next step, a differential pumping stage takes place using the first module (A)
and supportively the third module (C). To this end, the valves 4b and 4e are opened
and the injection chamber 9 is pumped to a pressure below 1E-2 mbar using the dry
pumps 5 and 19. The valves 4b and 4d are then closed and the valve 6 is opened until
the pressure reaches below 1E-3 mbar. The valve 6 is a valve with a smaller cross-section
than the valve 7a and is also more accurate than the valve 7a in terms of controlling
its opening. Opening of the valve 6 means that the chamber 9 is gradually pumped by
the turbomolecular pump 3 and, at the same time, there is no possibility of damage
and stopping of the pump due to overloads that could arise from the pressure difference
in the chambers 2 and 9. When a pressure of p < 1E-3 mbar is reached, the valve 7a
gradually opens and, when it is fully opened, the turbomolecular pump 3 pumps the
system, i.e. the chambers 2 and 9, to a pressure below 9E-9 mbar. The pressure in
the injection chamber 9 is therefore low again, and the object can thus be brought
out into the user chamber 8 by opening the gate valve 7b, while maintaining high vacuum
conditions.
[0032] In the above method, differential pumping is used, with the use of different valve
cross-sections: the valve 6 connects the chambers 2 and 9 through a small cross-section
channel, while the valve 7a connects the chambers 2 and 9 through a large cross-section
channel, where the EPS is close to the maximum value provided by the pump. Immediately
after the injection, the chamber 2 has a pressure of p < 9E-9 mbar, while the chamber
9 has a pressure of 5E3 mbar > p > E-1 mbar. With such a high differential pressure,
the valve 7a could be damaged and the turbomolecular pump could be "throttled" (a
rapid increase in pressure in the chamber 2 would cause the turbomolecular pump to
decelerate rapidly, the pump impeller would experience overloads so great that it
would stall, in extreme cases the impeller arms could be twisted or the bearings could
be knocked out). For this reason, differential pumping was used. In the present system,
differential pumping is first carried out with the dry pumps, which are resistant
to overloads associated with differential pressure (these are the valves 4b and 4d).
When they are closed and the valve 6 is opened, the turbomolecular pump 3 is already
used through a narrow channel. There is little pumping efficiency here, so the pump
is not subjected to high overloads associated with pressure difference. When the pressure
reaches a sufficient level to open the valve 7a, i.e. p < 1E-3 mbar, this valve is
opened and the chamber 9 is pumped with its full capacity (maximum EPS) by the turbomolecular
pump 3.
First embodiment
[0033] The system was prepared to apply ethanol 99.8% to the surface of the object in the
form of single-crystal rutile TiO
2 (011), which is a test sample. The system, consisting of the modules A, B and C,
was connected to the user chamber 8 containing a scanning tunnelling microscope to
allow observation of the object and a component that allows thermally programmed desorption
to be carried out to prove that ethanol was applied to the sample as a result of the
process. Fig. 3A shows the surface of a 100x100nm object before ethanol application,
imaged with a scanning tunnelling microscope (It = 2pA, U = 1.7V)). It shows the local
density of unoccupied electronic states on the surface. The procedure was carried
out as discussed above. The needle 11 was maintained at a distance of 20 mm from the
surface of the object. In the first sequence, 0.2ml of ethanol was consumed, so that
the pressure in the injection chamber 9 relative to the reservoir 18 with liquid was
equalized to 1.5E0 mbar prior to spraying. In the second sequence, i.e. the sequence
wherein liquid is injected towards the sample, 0.2 ml of ethanol was consumed, and
the solenoid valve 15 was controlled with 150 ms pulses, delivering a total of 3 pulses
every 2 seconds. Once the liquid had been applied and the pressure in chamber 9 had
settled at 2E2 mbar, pumping was started according to the procedure described above.
After pumping out the chamber 9, when a pressure of p < 9E-9 mbar was reached, the
sample was brought out to the user chamber 8, where the imaging was performed again
with the scanning tunnelling microscope. Fig. 3B shows the surface of a 100x100 nm
sample with ethanol applied (imaging parameters: It = 2pA, U = 1.7V), whereas Fig.
3C shows a magnified view of the portion indicated by a rectangle in Fig. 3B, with
dimensions of 30×30nm (imaging parameters: It = 3pA, U = 1.7V). From Fig. 3B, 3C it
can be seen that the maximum molecular multilayer was obtained, as otherwise it would
not be possible to measure with the STM microscope with the quality and resolution
presented. The surface is evenly covered, with additional agglomerates (Fig. 3B -
arrows) and defects that are probably impurities (Fig. 3C - arrow). The said agglomerates
and defects occur randomly on the surface of the sample, but their number is small
and their occurrence on a molecular or nanometric scale is inevitable.
[0034] Furthermore, to confirm the presence of ethanol molecules on the surface, thermally
programmed desorption (TPD) was performed on the sample in the user chamber. While
the sample was gradually heated at a controlled rate, a signal was collected from
a mass spectrometer positioned directly above the sample surface. This resulted in
plots of I(T), i.e. the equivalent intensity of a given atomic mass as a function
of temperature T. The result is shown in Fig. 4A which shows the TPD signal collected
simultaneously for masses of 31, 45 and 46 amu, the atomic mass of the ethanol molecule
is 46.07 g/mol - the existence of a distinguishable maximum when testing the mass
of 46 amu is clear evidence that ethanol is present on the surface of the prepared
sample. The liquid application method according to the invention therefore ensures
even coverage of the sample on a microscale - it can be assumed that a constant degree
of coverage θ is achieved every time for the same application parameters.
[0035] Therefore, the experiment was extended to include a series of TPD measurements with
different sample heating rates, the result of which is shown in Fig. 4B. This allowed
temperatures (Tpeak) corresponding to the maximum desorption at a given heating rate
of the sample to be determined. Using the assumptions of the HRV (heating rate variable)
method (Fig. 4C), the desorption activation energy Edes and the value of parameter
v (pre-exponential factor) were determined for an ethanol molecule on rutile TiO2
(011).
Second embodiment
[0036] An ethanol solution was made that comprises tin phthalocyanine (SnPc) molecules having
a structure as shown in Fig. 5D. Because phthalocyanines are poorly soluble in ethanol,
the solution was supersaturated and settled down - thus obtaining a mixture with the
maximum SnPc concentration under normal conditions.
[0037] The reference sample was the ethanol-applied sample described in the first embodiment.
[0038] In the next stage, the rutile crystal obtained in the first embodiment was purified.
Then, using the same application parameters as in the first embodiment, a solution
of ethanol and SnPc molecules was introduced onto the surface.
[0039] In this embodiment, it was possible to carry out an additional specialized study
of the samples using secondary ion mass spectrometry (SIMS). This method allows the
chemical composition of the surface to be accurately inspected, the local concentration
of a selected component to be determined, depth profiles to be made and chemical mapping
(distribution of a given mass over a selected area of the surface) to be carried out.
Figs. 5A and 5B show dependences of signal intensity (counts) for masses characteristic
for the SnPc molecule, in the case of ethanol (Fig. 5A) and the solution of ethanol
and SnPc molecules (Fig. 5B), respectively. As is evident from the data presented,
selected molecules were successfully applied to the surface of the sample. The signal
in the experiment was collected from randomly selected areas of the sample with dimensions
of 500 × 500 µm. The images can be interpreted as chemical maps for the peak of 632
amu - Fig. 5C. According to the accompanying scale, the brighter the spots on the
map, the higher the concentration of molecules. It can be seen that, in addition to
the bright agglomerates of molecules, individual points can be seen throughout the
area - these are nanometre-sized clusters of molecules.
[0040] Additional STM mapping was carried out to support the above conclusion. For comparison
purposes, the results obtained for ethanol (Fig. 6A, a sample size of 100x100 nm,
It = 2pA, U = 1.7V) and the solution of ethanol and SnPc molecules (Fig. 6B, a sample
size of 100×100 nm, It = 2pA, U = 1.7V) are collated. Upon application of the solution
of ethanol and SnPc molecules, an ethanol-specific structure forms on the surface
(indicated by the rectangle in Fig. 6B) and clusters of molecules (diameter < 20 nm)
are visible. The poorer quality of the map seen in Fig. 6B is associated with the
presence of agglomerates formed by SnPc molecules which are unstable under scanning
conditions.
[0041] The embodiments presented here relate to tests on the surface of single-crystal rutile
TiO2 only to illustrate the effects obtained by the method according to the invention.
However, this method does not have any limitations related to the application of liquids
to other surfaces of metals, semiconductors and insulators.
1. A vacuum system for applying a liquid to an object, the vacuum system comprising:
- a first module (A) for generating a vacuum;
- a second module (B) with a user chamber (8) and an injection chamber (9) for applying
the liquid to the object under vacuum conditions; and
- a third module (C) comprising a set of components for preparing the liquid and supplying
the liquid to an injection needle (11);
- wherein the first module (A) is tightly connected to the second module (B) and the
second module (B) is tightly connected to the third module (C);
the vacuum system
characterized in that:
- the second module (B) is connected to the third module (C) via a sealed linear movement
system (13);
- wherein the injection needle (11) passes through the sealed linear movement system
(13) to inject the liquid prepared in the third module (C), so that the injection
needle (11) protrudes from the linear movement system (13) into the interior of the
injection chamber (9) in the second module (B) and is movable in the horizontal axis
relative to the object (10) located in the second module (B) onto which the liquid
from the injection needle (11) is to be sprayed.
2. The system according to claim 1, wherein the sealed linear movement system (13) is
a linear bellows manipulator.
3. The system according to any of previous claims, wherein the injection chamber (9)
comprises a manipulator (12) for rotating the object.
4. The system according to any of previous claims, wherein the second module (B) further
comprises a user chamber (8) separated from the injection chamber (9) by a vacuum-tight
gate valve (7b).
5. The system according to claim 4, wherein the manipulator (12) to move the object between
the user chamber (8) and the injection chamber (9) is externally controlled.
6. The system according to any of previous claims, wherein the injection chamber (9)
is separated from the user chamber (8) by a high-tightness gate valve (7a) mounted
on a ConFlat class fitting.
7. The system according to any of previous claims, wherein the injection chamber (9)
is separated from a pumping chamber (2) in the first module (A) by a high-tightness
gate valve mounted on a ConFlat class fitting.
8. The system according to any of claims 1 to 7, wherein the linear movement system (13)
is mounted on a ConFlat class fitting.
9. A method for applying a liquid to an object in the vacuum system according to any
of claims 1 to 8, the method comprising:
- in the injection chamber (9) in the second module (B), generating vacuum conditions
with a pressure of p < 9E-9 mbar;
- moving the object from the user chamber (8), with pre-generated pressure of p <
9E-9 mbar, to the injection chamber (9);
- closing the valve (7b) that separates the injection chamber (9) from the user chamber
(8);
- preparing the liquid to be injected in the third module (C);
- equalizing the pressure between the injection chamber (9) and a reservoir (18) with
the liquid to a value between 1E-1 and 1E1 mbar;
- spraying the object with the liquid using the injection needle (11), and adjusting
the spraying parameters while spraying, by adjusting a distance of the injection needle
(11) from the object and parameters of a pulsed operation of a valve (15) supplying
a gaseous medium to the reservoir (18) with the liquid;
- after the spraying is finished, sealing the injection chamber (9) against the reservoir
(18) with the liquid, reducing the pressure in the injection chamber (9) to below
9E-9 mbar and opening the valve (7b) that separates the injection chamber (9) from
the user chamber (8); and
- moving the object from the injection chamber (9) to the user chamber (8).