WO2016203504A1 - Coating carrier gas control device - Google Patents

Coating carrier gas control device Download PDF

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Publication number
WO2016203504A1
WO2016203504A1 PCT/JP2015/002995 JP2015002995W WO2016203504A1 WO 2016203504 A1 WO2016203504 A1 WO 2016203504A1 JP 2015002995 W JP2015002995 W JP 2015002995W WO 2016203504 A1 WO2016203504 A1 WO 2016203504A1
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WO
WIPO (PCT)
Prior art keywords
carrier gas
coating
paint
pressure
heating
Prior art date
Application number
PCT/JP2015/002995
Other languages
French (fr)
Japanese (ja)
Inventor
阿部 正一
裕司 小柴
Original Assignee
有限会社ミクロコスモス
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 有限会社ミクロコスモス filed Critical 有限会社ミクロコスモス
Priority to PCT/JP2015/002995 priority Critical patent/WO2016203504A1/en
Priority to JP2015530219A priority patent/JP6095081B6/en
Publication of WO2016203504A1 publication Critical patent/WO2016203504A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02Spray pistols; Apparatus for discharge
    • B05B7/04Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02Spray pistols; Apparatus for discharge
    • B05B7/12Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/16Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas incorporating means for heating or cooling the material to be sprayed

Definitions

  • the present invention relates to a coating carrier gas control device. More specifically, the present invention relates to a technique for controlling the carrier gas for coating supplied to the coating means for performing spray coating so as to keep it in a good state.
  • compressed air from an air compressor 101 is applied to a paint tank via a pipe 102, a manual air regulator 103, and a pipe 104.
  • the inorganic paint in the paint tank 105 is introduced into the pipe 105 and sent out to the pipe 106 by the compressed air and supplied to the spray gun 107.
  • a pipe 108 for supplying compressed air to the spray gun 107 is provided in the pipe 102.
  • the pressure of the compressed air supplied to the spray gun 107 is adjusted by an air regulator 108a that is branched from the pipe 108 and provided in the pipe 108 (Patent Document 1).
  • the pressure adjustment of the compressed air is only the pressure setting of the air regulator 108a, which tends to be a high setting, and there is a problem that the paint and diluent are excessively used.
  • compressed air of about 0.5 to 1.0 MPa is sent from the air compressor 101 so that the pressure of the compressed air in the spray gun 107 (that is, the pressure of the blowout) becomes about 0.25 MPa.
  • the coating operation is performed in the temperature state of the compressed air sent from the air compressor 101, and the temperature of the carrier gas (that is, the compressed air) varies depending on the season and the working environment.
  • the temperature of the carrier gas that is, the compressed air
  • the present invention can reduce the amount of paint and diluent used, and thus improve the working environment at the painting site and suppress the diffusion of volatile organic compounds, as well as a coating carrier gas control device.
  • the purpose is to provide.
  • the coating carrier gas control device of the present invention has a predetermined pressure in the drying mechanism for dehumidifying and drying the carrier gas delivered from the gas supply source unit and the coating means to which the carrier gas is supplied.
  • Pressure adjusting means for adjusting the pressure of the carrier gas so that the pressure of the carrier gas becomes equal to, a heating means for heating the carrier gas so that the temperature in the coating means becomes a predetermined temperature, and for supplying the carrier gas to the coating means Heating means for heating the atmosphere in the housing having a space for housing the hose.
  • the humidity, temperature, and pressure of the carrier gas supplied to the coating means are managed and controlled in an appropriate state, so that it is suitable for spraying paint with uniform quality. Is supplied to the coating means.
  • this coating carrier gas control device when the carrier gas supplied to the coating means is appropriately heated, the paint blown out together with the carrier gas is heated, whereby the paint is applied to the coating. Since it becomes easy to be in an appropriate spraying state, coating is performed with a lower spraying pressure than in the past.
  • the coating carrier gas control device of the present invention may further include a storage unit that temporarily stores the carrier gas after passing through the drying mechanism in a pressurized state and then sends it to the pressure adjusting means. Since the carrier gas delivery pressure is smoothed, the pressure of the carrier gas blown out from the coating means, and the pressure of the paint blowout from the painting means together with the carrier gas is increased. It becomes smooth.
  • the hose may be covered with a heat insulating material.
  • the temperature drop due to the heat radiation of the carrier gas in the hose is suppressed, The temperature drop of the blown carrier gas is suppressed, and the temperature drop of the paint blown out from the coating means together with the carrier gas is suppressed.
  • the control device for the coating carrier gas of the present invention may further include a device branched from the hose so that the carrier gas is blown out toward the coating means.
  • the coating means is warmed and the coating is performed. Since the temperature is kept during the work, the temperature drop of the paint blown out from the coating means is suppressed.
  • the control device for the coating carrier gas of the present invention may further include a paint heating unit for storing the paint supplied to the painting means and for heating the paint before the painting operation using the atmosphere in the housing.
  • a paint heating unit for storing the paint supplied to the painting means and for heating the paint before the painting operation using the atmosphere in the housing.
  • the coating carrier gas control device includes an airflow adjustment unit including a drying mechanism and a pressure adjustment unit, a heating unit including a heating unit and a heating unit, and a storage unit, or a storage unit of these units.
  • a moving means may be provided for any combination of a plurality of units, and in this case, the unit can be moved for each unit or for each combination of a plurality of units. Equipment can be easily moved and installed according to the location (painting site).
  • a carrier gas suitable for spraying paint and having a uniform quality can be supplied to the coating means, so that the finish of spray coating is improved. Is possible.
  • the coating carrier gas control device of the present invention since coating can be performed with a lower spray pressure than before, it is possible to reduce the amount of paint and diluent used when spraying liquid paint. In addition, the amount of paint used in the case of spraying a powder paint can be reduced.
  • the coating carrier gas control device of the present invention has a storage unit for temporarily storing the carrier gas, the coating gas blowing pressure blown from the coating means together with the carrier gas is smoothed. As a result, it is possible to prevent fluctuations in the amount of paint blown out, thereby preventing uneven coating of the paint and improving the finish of the spray painting.
  • the coating carrier gas control device of the present invention can suppress the temperature drop of the paint blown from the coating means together with the carrier gas.
  • the temperature control of the paint becomes easy, and as a result, the paint temperature can be maintained in an appropriate state and good coating can be performed.
  • the coating carrier gas control device of the present invention When the coating carrier gas control device of the present invention has an appliance branched from the hose, it can suppress the temperature drop of the paint blown out from the painting means, so that the temperature management of the paint is easy. As a result, it is possible to perform satisfactory coating while maintaining the temperature of the coating material in an appropriate state.
  • the paint carrier gas control device of the present invention has a paint heating unit for warming the paint before the painting operation, it is a mixture of the paint and the carrier gas when blown out from the painting means. Therefore, it is possible to easily control the temperature of the coating material, and to maintain the temperature of the coating material in an appropriate state and perform good coating.
  • the moving means when the moving means is provided in the units constituting the apparatus, the movement of the apparatus in accordance with the movement of the painting place (painting place) by the painting work process. -Since installation can be performed easily, it becomes possible to improve the ease of handling of the apparatus and to reduce the labor of painting work.
  • FIG. 1 It is a functional block diagram (in other words, piping system diagram) showing an example of the embodiment of the control device for the coating carrier gas of the present invention. It is a figure which shows the table
  • FIG. 1 shows an example of an embodiment of a coating carrier gas control device of the present invention.
  • the control device for the coating carrier gas of the present embodiment includes an airflow adjustment unit 10, a storage unit 4, and a heating unit 20 as a rough configuration. Then, the paint is blown out from the coating means 7 by the pressure of the carrier gas 9 supplied from the gas supply source unit 1 and subjected to necessary processing through these units 10, 4, 20 (in other words, sprayed / discharged). ).
  • the coating means 7 in the present invention for example, a spray gun similar to a conventional spray gun for painting can be used.
  • a hand-blown spray gun (also referred to as a cup gun in terms of having a paint cup 7a) may be used.
  • the paint cup 7a is filled with a liquid paint (also referred to as a solvent paint) adjusted to an appropriate concentration with a diluent / solvent.
  • a liquid paint also referred to as a solvent paint
  • the pressurized carrier gas 9 is introduced from the hose 6 and mixed with the pressurized carrier gas 9 (in other words, the pressurized carrier gas 9 is mixed). At the same time, the paint is blown out from the nozzle (by the pressure of the pressurized carrier gas 9).
  • control apparatus of the coating carrier gas of this embodiment is the air-water separation means 13 and the dehumidification drying means 15 as a drying mechanism which dehumidifies and dries the carrier gas 9 sent from the gas supply source unit 1, and carrier gas.
  • Pressure adjusting means 16 for adjusting the pressure of the carrier gas 9 so that the pressure in the spray gun 7 as the coating means to which 9 is supplied becomes a predetermined pressure, and the temperature in the spray gun 7 as the coating means is set to a predetermined temperature.
  • Heating means 21 for heating the atmosphere in the housing provided with a heating means 21 for heating the carrier gas 9 and a space 24 for housing the hose 6 for supplying the carrier gas 9 to the spray gun 7 as a coating means.
  • the coating carrier gas control device of the present embodiment further stores the carrier gas 9 after passing through the steam-water separating means 13 as a drying mechanism, temporarily stored in a pressurized state and then sent to the pressure adjusting means 16.
  • the unit 4 is provided.
  • the gas supply source unit 1 is for sending a carrier gas 9 used for blowing paint from a spray gun 7 as a coating means at a predetermined pressure and supplying the carrier gas 9 to the airflow adjusting unit 10.
  • the carrier gas 9 in the present invention a gas similar to the gas supplied to the conventional spray gun can be used.
  • air, inert gas, specifically air, nitrogen (N 2 ) gas, or Helium (He) gas or the like can be used (which is supplied as a compressed gas).
  • a mechanism is used that has a capability of delivering gas at a pressure that can cause the storage unit 4 to store the carrier gas 9 in a predetermined pressurized state.
  • the pressure of the carrier gas 9 delivered from the gas supply source unit 1 is not limited to a specific value.
  • the carrier gas 9 passes through the airflow adjustment unit 10 and is stored in a predetermined pressurized state.
  • it is appropriately set to an appropriate value. Specifically, for example, as an example, it is appropriately set to an appropriate value in a range of about 0.50 to 1.0 MPa.
  • the gas supply source unit 1 for example, an air compressor is used, or a gas cylinder filled with a carrier gas 9 as a compressed gas, and a pressure regulator for adjusting the pressure of the gas output from the gas cylinder Or a combination of
  • the carrier gas 9 sent out from the gas supply source unit 1 is supplied to the airflow adjustment unit 10 through the gas input pipe 2.
  • the allowance and restriction of the inflow of the carrier gas 9 to the airflow adjustment unit 10 are controlled by opening and closing the gas input valve 11 provided in the gas input pipe 2.
  • the air flow adjusting unit 10 performs a cleaning process, a water / water separation process and a dehumidifying and drying process on the carrier gas 9 supplied from the gas supply source unit 1, and a spray gun 7 through a heating unit 20 and a hose 6. This is for adjusting the pressure of the carrier gas 9 supplied to the air.
  • the airflow adjustment unit 10 includes a cleaning mechanism for performing a cleaning process, and a drying mechanism for performing a steam-water separation process and a dehumidifying and drying process. And it comprises the primary cleaning means 12 and the secondary cleaning means 14 as the cleaning processing mechanism, and the steam-water separating means 13 and the dehumidifying and drying means 15 as the drying mechanism.
  • the carrier gas 9 is first introduced into the primary cleaning means 12 provided in the airflow adjustment unit 10.
  • the primary cleaning means 12 is for removing contaminants such as dust in the carrier gas 9 to clean the carrier gas 9 (primary cleaning process).
  • the primary cleaning means 12 is not limited to a specific type or specification, and is appropriate in consideration of, for example, the degree of cleaning required when storing the carrier gas 9 in the storage unit 4. Is appropriately selected.
  • the primary cleaning means 12 specifically, for example, an air filter having appropriate filtration performance (filtration degree) can be used.
  • the carrier gas 9 is also introduced into the steam / water separation means 13 provided in the airflow adjustment unit 10.
  • the air / water separation means 13 is for dehydrating the carrier gas 9 by separating and removing drains and water droplets in the carrier gas 9.
  • the steam-water separation means 13 is not limited to a specific type or specification, and for example, the degree of drying (dehydration) required when storing the carrier gas 9 in the storage unit 4 at a predetermined pressure. Appropriate ones are selected as appropriate.
  • the steam-water separation means 13 specifically, for example, a steam-water separator having proper drain / water droplet separation / exclusion performance can be used.
  • the foreign matter, moisture, and the like separated and removed by the primary cleaning means 12 and the air / water separation means 13 are collected, for example, in a drain pan (not shown) installed outside the airflow adjustment unit 10 and appropriately discarded. .
  • the air / water separation process is performed after the primary cleaning process, but the order is not limited to this, and the primary cleaning process is performed next to the air / water separation process. You may make it.
  • the carrier gas 9 subjected to the primary cleaning process and the steam separation process in the airflow adjustment unit 10 is sent out from the airflow adjustment unit 10 via the introduction pipe 3A and introduced into the storage unit 4.
  • the storage unit 4 is a carrier gas 9 in a predetermined (or within a predetermined range) pressurized state for the purpose of smoothing the delivery pressure of the carrier gas 9 and stabilizing the fluidity of the carrier gas 9. Is for temporary storage.
  • the carrier gas 9 sent from the air compressor is accompanied by wave fluctuations and pulsations.
  • the wave fluctuation and pulsation are eliminated (that is, suppressed)
  • the pressure of delivery of the carrier gas 9 is smoothed
  • the fluidity is stabilized
  • the discharge of the paint from the spray gun 7 is stabilized.
  • a tank having at least strength (specifically, airtightness) that can store gas in a predetermined pressurized state may be used.
  • the gas pressure in the storage unit 4 is adjusted so as to be in the range of, for example, about 0.50 to 1.0 mm2 for example as an example.
  • the internal volume and the maximum operating pressure of the storage unit 4 are not limited to a specific size or numerical value.
  • the volume or spray gun required for performing a continuous painting operation for a certain time without trouble In consideration of the final pressure of the carrier gas 9 supplied to 7, it is appropriately set to an appropriate size and value.
  • the internal volume of the storage unit 4 can be set to an appropriate size in a range of, for example, about 40 to 80 L, specifically as an example. Further, the working pressure of the storage unit 4 can be set to an appropriate numerical value within a range of, for example, about 0.50 to 1.0 kgpa, for example.
  • the carrier gas 9 is delivered from the delivery valve of the storage unit 4 with a smooth pressure that does not vary periodically.
  • the carrier gas 9 sent out from the storage unit 4 is supplied again to the air flow adjusting unit 10 through the sending pipe 3B.
  • the carrier gas 9 is introduced into the secondary cleaning means 14 provided in the airflow adjustment unit 10.
  • the secondary cleaning means 14 is for removing dust / impurities such as oil fine particles (oil mist) and fine solids in the carrier gas 9 to clean the carrier gas 9 (secondary cleaning treatment). .
  • the secondary cleaning means 14 is not limited to a specific type or specification.
  • the desired degree of cleaning as the carrier gas 9 supplied to the dehumidifying and drying means 15 and the carrier gas 9 supplied to the spray gun 7 are used.
  • an appropriate one is appropriately selected.
  • the secondary cleaning means 14 for example, a mist filter, a micro mist filter, and a super mist filter having appropriate dust removal / absorption performance (each of which is a mist separator, a micro mist separator, and a super mist separator, respectively) Any one of them may be used, or two or more may be used in combination.
  • the carrier gas 9 is then introduced into the dehumidifying and drying means 15 provided in the airflow adjusting unit 10.
  • the dehumidifying and drying means 15 is for removing moisture in the carrier gas 9 and dehumidifying and drying the carrier gas 9.
  • the dehumidifying and drying means 15 is not limited to a specific type or specification.
  • the degree of drying (dehumidifying and drying) desirable as the carrier gas 9 supplied to the spray gun 7 is considered. An appropriate one is appropriately selected.
  • the dehumidifying and drying means 15 specifically, for example, an air dryer having an appropriate moisture removal performance can be used.
  • the carrier gas 9 is then introduced into the pressure adjusting means 16 provided in the airflow adjusting unit 10.
  • the pressure adjusting means 16 is configured so that the pressure of the carrier gas 9 becomes an appropriate pressure to be supplied to the spray gun 7 via the hose 6 via the heating unit 20, in other words, the carrier from the spray gun 7. This is for adjusting the pressure of the carrier gas 9 delivered to the heating unit 20 so that the blowing pressure of the gas 9 becomes appropriate.
  • the set pressure for delivery of the carrier gas 9 by the pressure adjusting means 16 is not limited to a specific value.
  • the carrier gas 9 is discharged from the spray gun 7 while the carrier gas 9 passes through the appropriate pressure or hose 6.
  • An appropriate value is appropriately set in consideration of the pressure loss of the gas 9 and the like. Specifically, for example, as an example, it is appropriately set to an appropriate value in a range of about 0.3 to 0.5 MPa.
  • the pressure adjusting means 16 is not limited to a specific type or specification, and functions to output the carrier gas 9 sent and input from the storage unit 4 at a predetermined pressure at a predetermined constant pressure. An appropriate mechanism to be obtained is appropriately selected.
  • the pressure adjusting means 16 for example, there is a pressure regulator (also called a pressure regulating valve or a regulator) that can keep the pressure of the output gas constant even if the pressure of the input gas fluctuates. Can be used.
  • a pressure regulator also called a pressure regulating valve or a regulator
  • the carrier gas 9 that has been subjected to the cleaning process, the steam separation process, and the dehumidifying drying process in the airflow adjustment unit 10 and whose pressure has been adjusted is transferred from the airflow adjustment unit 10 to the heating unit 20 via the connection pipe 5. Is sent out.
  • the heating unit 20 performs a heating process on the carrier gas 9 delivered from the airflow adjustment unit 10 and is connected to the spray gun 7 to provide a hose 6 for supplying the carrier gas 9 to the spray gun 7. This is to heat and keep the carrier gas 9 in the hose 6 warm.
  • the heating unit 20 has a casing, and includes a heating means 21 and a heating means 23 inside the casing.
  • the carrier gas 9 is introduced into the heating means 21 provided in the heating unit 20.
  • the heating means 21 adjusts the blowing temperature of the carrier gas 9 from the spray gun 7 so that the temperature of the carrier gas 9 becomes an appropriate temperature to be supplied to the spray gun 7 via the hose 6. It is for adjusting the temperature of the carrier gas 9 delivered to the hose 6 so as to be appropriate.
  • the set temperature of the heating process of the carrier gas 9 by the heating means 21 is not limited to a specific value, for example, while passing through an appropriate blowing temperature of the carrier gas 9 from the spray gun 7 or the hose 6 or the like.
  • it is preferably set in a range of about 30 to 60 ° C., more preferably in a range of about 40 to 55 ° C., and most preferably about 50 ° C.
  • the heating means 21 is not limited to a specific type or specification, and an appropriate mechanism that can function to output the input carrier gas 9 at various temperatures at the above temperature is appropriately selected.
  • the heating means 21 specifically, for example, a gas warmer capable of supplying a desired amount of heat to the gas according to the flow rate of the passing gas can be used.
  • a gas output valve 22 is provided in the piping on the output side of the heating means 21, and the allowance and limitation of the outflow of the carrier gas 9 from the heating unit 20 are controlled by opening and closing the gas output valve 22.
  • the hose 6 is connected to the gas output valve 22, and the hose 6 and the spray gun 7 are connected via a coupler 8 including a socket 8A at the end of the hose 6 and a plug 8B coupled to the socket 8A.
  • the carrier gas 9 is sent from the heating means 21 to the hose 6, and the carrier gas 9 that has passed through the hose 6 is supplied to the spray gun 7.
  • hose 6 a hose having a performance capable of withstanding a predetermined pressure of the carrier gas 9 supplied to the spray gun 7 is used.
  • the hose 6 has a function / mechanism for rectifying the carrier gas 9.
  • a concave groove continuous in a spiral shape or a convex portion continuous in a spiral shape is formed on the inner peripheral surface of the hose 6, or a spiral shape (in other words, a spiral shape) in a portion near the spray gun 7 in the hose 6.
  • a coil spring-like member may be mounted.
  • the carrier gas 9 supplied to the spray gun 7 is heated so that the paint blown out together with the carrier gas 9 from the spray gun 7 has a predetermined temperature.
  • the temperature drop of the carrier gas 9 heated by the heating means 21 can be suppressed.
  • the hose housing space 24 is secured in the casing of the heating unit 20 so that the hose 6 can be accommodated, and the hose 6 is wound or laminated. A mechanism to do this is provided.
  • the heating means 23 is provided in a housing
  • the set temperature of heating in the casing of the heating unit 20 by the heating means 23 is not limited to a specific value, and for example, appropriately suppressing a temperature drop of the carrier gas 9 while passing through the hose 6. Is properly set to an appropriate value. Specifically, for example, it is preferably set in a range of about 20 to 45 ° C., more preferably in a range of about 25 to 40 ° C., and a range of about 30 to 35 ° C. Most preferred.
  • the heating means 23 is not limited to a specific type or specification, and an appropriate mechanism capable of heating the atmosphere in the casing of the heating unit 20 to the above temperature is appropriately selected.
  • the heating means 23 specifically, for example, an electric heater that can supply a necessary amount of heat to the atmosphere in the casing in accordance with the volume in the casing of the heating unit 20 can be used.
  • an electric heater with a fan is preferable so that heat can be supplied while stirring the atmosphere in the housing.
  • the painting operation can be started at an appropriate time.
  • the hose 6 By housing the hose 6 in the casing of the heating unit 20, the hose 6 is also warmed by the atmosphere warmed by the heating means 23. Therefore, the hose 6 can be warmed in a shorter time than the case where the heated carrier gas 9 is warmed by passing through the hose 6, and the painting operation can be performed quickly.
  • the hose 6 is covered with a heat insulating material / heat insulating material, or a hose formed of the heat insulating material / heat insulating material is used as the hose 6. It is preferable that
  • the casing is formed of a heat insulating material or a heat insulating material, or a part or the whole of the case is covered with a heat insulating material or a heat insulating material. Is preferable.
  • a plug 8B ′ having an exhaust port connected to the socket 8A at the end of the hose 6 and communicating with the inside of the casing of the heating unit 20 is attached to a side wall constituting the casing, and the end of the hose 6 is connected to the plug 8B ′.
  • the carrier gas 9 delivered from the hose 6 may be introduced into the casing of the heating unit 20 by coupling the sockets 8 ⁇ / b> A.
  • the carrier gas 9 heated by the heating means 21 and delivered to the hose 6 can be introduced into the casing of the heating unit 20 via the hose 6.
  • the atmosphere pressure in the casing rises, so the atmosphere in the casing (the hose 6) (Including the carrier gas 9 delivered from the outside) is provided.
  • a suspension type swingable openable / closable door for example, a pet door or a cat door
  • a small-sized one is installed in an appropriate place such as a side wall constituting the casing of the heating unit 20.
  • the opening for pulling out the hose 6 from the inside of the casing of the heating unit 20 may also be configured to serve as a mechanism for releasing the atmosphere in the casing to the outside.
  • an instrument branching from the hose 6 is further provided at a position near the spray gun 7 of the hose 6 (for example, in the vicinity of the socket 8A at the end of the hose 6 in the example shown in FIG. 1) (FIG. (Not shown), the carrier gas 9 heated toward the surface of the main body of the spray gun 7 or the paint cup 7a may be blown out from the branch device.
  • a cover is further provided around the body of the spray gun 7 or the paint cup 7a after an appropriate space (gap) is secured between them.
  • the heated carrier gas 9 may be blown out and stay in the cover.
  • the main body of the spray gun 7, the paint cup 7a and the paint in the paint cup 7a are warmed and kept warm during the painting work, and even when the temperature at the painting site is low, Temperature management becomes easy, and it becomes possible to maintain the temperature of the paint blown out from the spray gun 7 in an appropriate range.
  • the coating carrier gas control device of the present invention accommodates the coating material supplied to the coating means 7 and uses the atmosphere in the casing of the heating unit 20 to warm the coating material before the coating operation. You may make it have the part 25 further.
  • the paint cup 7a ′ containing the paint to be supplied to the spray gun 7 is accommodated, and the warm air atmosphere in the casing of the heating unit 20 is used to put the paint cup 7a ′.
  • a paint heating unit 25 is provided for heating the applied paint before the painting operation.
  • the paint heating unit 25 may be provided adjacent to the side surface or the upper surface of the casing of the heating unit 20, or may be provided within the casing of the heating unit 20, or You may make it provide separately from the housing
  • the side plate of the casing It is attached to the top plate and the top plate (At this time, these side plates and the top plate are used as one surface), and is configured as a box having a door that can be opened and closed on either the side surface or the top surface. It is possible.
  • the side plate and the ceiling of the casing are arranged so that the space in the casing of the heating unit 20 communicates with the space in the box as the paint heating section 25 so that the warm atmosphere in the casing can enter.
  • a structure (reference numeral 25a in FIG. 1) for ventilation such as a louver or a through hole is provided at a position of the plate where the box is attached.
  • a heat insulating material / heat insulating material may be used as a member constituting the box as the paint heating unit 25, or a part or the whole of the box may be covered with the heat insulating material / heat insulating material. preferable.
  • the paint heating unit 25 is provided in the casing of the heating unit 20, it is conceivable that the paint heating unit 25 is configured as a partial section in which the space in the casing is partitioned. In this case, a structure for ventilation such as a louver or a through hole is provided in the partition member constituting the compartment so that the warm atmosphere in the casing can enter the compartment as the paint heating unit 25. . In addition, an openable / closable door connected to the section as the paint heating unit 25 is provided on a side plate or a part of the top plate of the casing of the heating unit 20.
  • the paint heating unit 25 is provided separately from the casing of the heating unit 20, it is conceivable that the paint heating unit 25 is configured as an independent box having an openable / closable door.
  • the casing and the box are connected to the space in the casing of the heating unit 20 and the space in the box as the paint heating unit 25 by the tubes communicating at both ends, respectively. An atmosphere is introduced into the box.
  • a heat insulating material / heat insulating material may be used as a member constituting the box as the paint heating unit 25, or a part or the whole of the box may be covered with the heat insulating material / heat insulating material.
  • the tube is covered with a heat insulating material / heat insulating material, or a hose formed of a heat insulating material / heat insulating material is used as the tube.
  • the temperature of the paint blown out together with the carrier gas 9 is low even if the carrier gas 9 is heated. It is prevented that the temperature of the paint when it is blown out from the spray gun 7 is lowered, the temperature management of the paint is facilitated, and the temperature of the paint to be blown out is maintained within an appropriate range. It becomes possible.
  • the paint heating unit 25 may store the paint in a state other than the paint put in the paint cup 7a ′.
  • the airflow adjustment unit 10, the storage unit 4, and the heating unit 20 described above may be a fixed type that is installed and installed for each unit or after a plurality of arbitrary units are combined. Further, it may be a movable type provided with a moving means. In the case of a movable type, it becomes a structure which can move for every unit or for every combination of a some unit, and installation of the apparatus according to the field condition is attained.
  • the moving means for making the unit movable for example, a carriage including a pedestal on which the unit is placed and a wheel provided on the lower side of the pedestal, or a pedestal on which the unit is placed And a mechanism having a wheel provided below the pedestal and a rail with which the wheel engages.
  • the heating unit 20 (and other units) can be installed in a safe area away from the explosive atmosphere at the site of painting by the spray gun 7 (that is, an area having a non-explosive atmosphere). Therefore, it is not necessary to make the heating unit 20 (and other units) have a structure that satisfies the standard as an explosion-proof device, and safety can be ensured. Further, as described above, the heating unit 20 (and other units) is provided with the moving means, so that the heating unit 20 (and other units) according to the movement of the painting place (painting site) by the painting work process. The unit can be easily moved and installed.
  • the carrier gas 9 is cleaned and dried by the airflow adjusting unit 10, and further fluidized by being temporarily stored in a pressurized state in the storage unit 4. It is delivered at a stable and smooth pressure, and is heated by the heating unit 20 and then supplied to the spray gun 7.
  • the atomization temperature of the paint in the spray gun 7 is about 20 to 30 ° C. by adjusting the temperature of the heating means 21 and the delivery pressure of the pressure adjusting means 16.
  • the spray pressure from the nozzle of the spray gun 7 is preferably in the range of about 0.15 to 0.20 MPa, and the atomization temperature of the paint is in the range of about 23 to 27 ° C and the blowout pressure. Is more preferably in the range of about 0.165 to 0.185 MPa, most preferably the atomization temperature of the paint is about 25 ° C and the blowing pressure is in the range of about 0.170 to 0.180 MPa. preferable.
  • the blowing pressure from the nozzle of the spray gun 7 is in the range of about 0.050 to 0.10 MPa, and the blowing pressure is about 0.065 to 0.085 MPa. More preferably, the blowing pressure is in the range of about 0.07 to 0.08 kgpa.
  • the coating carrier gas control device having the above-described configuration, it is possible to ensure a clean carrier gas 9 free from contaminants, and to keep the temperature of the carrier gas 9 within an appropriate range regardless of the season and working environment.
  • the humidity can be maintained within an appropriate range (in other words, the carrier gas 9 can be appropriately dried), and in addition, the blowing pressure of the carrier gas 9 can be maintained within the appropriate range. That is, the three elements of the temperature, humidity, and pressure of the carrier gas 9 can be managed and controlled in an appropriate state. For this reason, compared with the conventional spray coating method in which the pressure of the carrier gas 9 is set higher because the temperature and humidity are not controlled, the amount of paint and diluent used is reduced, and the working environment at the painting site is reduced. And the diffusion of volatile organic compounds can be suppressed. Furthermore, the paint blown out from the spray gun 7 together with the carrier gas 9 can be made into a good state suitable for painting by blowing, and the quality of the finish of spray painting can be improved.
  • the coating means 7 to which the carrier gas 9 is supplied is a hand-blown spray gun
  • the painting means to which the present invention can be applied is limited to the hand-blown spray gun.
  • the present invention can be widely applied in combination with various coating means in which paint is blown out by the pressure of the carrier gas 9 (in other words, sprayed / discharged).
  • the present invention can also be applied when the coating means to which the carrier gas 9 is supplied is an automated coating module having a mechanism in which the coating material is blown out together with the coating carrier gas.
  • the liquid paint prepared in an appropriate concentration by the diluent / solvent and put in the paint cup 7a is blown out.
  • the paint to which the present invention can be applied is a liquid paint.
  • the present invention is not limited, and the present invention can also be applied as a control device for the coating carrier gas supplied to the coating means when the powder paint is blown out from the coating means.
  • the primary cleaning means 12 and the steam / water separation means 13 are disposed on the upstream side of the storage unit 4, and the secondary cleaning means 14 and the dehumidifying and drying means 15 are disposed on the downstream side.
  • the presence or absence of these means 12, 13, 14, and 15 is not limited to that in the above-described embodiment.
  • the airflow adjustment unit 10 is required to clean or dry (dehydrate) the carrier gas 9 to the extent required when storing the carrier gas 9 in the storage unit 4 and to supply the carrier gas 9 to the spray gun 7. As long as such cleaning or drying is achieved, the presence of the means 12, 13, 14, 15 is appropriately determined. Can be adjusted.
  • the primary cleaning means 12 and the secondary cleaning means 12 may not be disposed, and when a gas cylinder is used as the gas supply source unit 1, the gas filled in the gas cylinder has a certain condition regarding cleanliness and humidity. Even when the above conditions are satisfied, the primary cleaning means 12, the secondary cleaning means 14, and the steam-water separation means 13 may not be provided. Therefore, the cleaning processing mechanism of the airflow adjustment unit 10 may be configured only by the secondary cleaning means 14, and more specifically, the airflow adjustment unit 10 may not have the cleaning processing mechanism, The adjusting mechanism may be composed of only the dehumidifying and drying means 15.
  • the primary cleaning means 12 and the steam-water separation means 13 are disposed on the upstream side of the storage unit 4, and the secondary cleaning means 14 and the dehumidifying and drying means 15 are disposed on the downstream side (in other words, in other words).
  • a cleaning mechanism and a drying mechanism are arranged on both the upstream side and the downstream side of the storage unit 4), but the relationship of these means 12, 13, 14, 15 with the storage unit 4.
  • the arrangement position is not limited to that in the above-described embodiment.
  • one or both of the secondary cleaning unit 14 and the dehumidifying / drying unit 15 may be arranged on the upstream side of the storage unit 4.
  • the cleaning mechanism and the drying mechanism of the airflow adjustment unit 10 may be disposed only on the upstream side of the storage unit 4.
  • the secondary cleaning means 14 and dehumidifying and drying are provided between these means 12 and 13 and the storage unit 4.
  • Means 15 are arranged.
  • the storage unit 4 is provided, but the storage unit 4 may not be provided.
  • the storage unit 4 may not be provided.
  • the pressure is adjusted by the pressure adjusting means 16, and the heating by the heating means 21.
  • the heating means 23 by heating the atmosphere in the casing of the heating unit 20 including the hose housing space 24 by the heating means 23, the effect of the present invention of reducing the amount of paint and diluent used can be exhibited. .
  • hand spray painting by an operator using a spray gun (cup gun) was performed.
  • the operator is a person who has sufficient experience with hand-blown painting and can perform appropriate painting work under the painting conditions in accordance with the difference in painting conditions.
  • a comparative example 1 for comparison with the embodiment according to the present invention it is a conventional spray coating system, and the compressed air sent from the air compressor is directly supplied to the spray gun. When used as a gas, it was painted.
  • the dilution ratio of the paint with the solvent (that is, the ratio of the weight of the solvent to the weight of the paint) is the standard for the paint used in this example in both Comparative Example 1-1 and Comparative Example 1-2.
  • the dilution rate was set to 70 %%.
  • Example 1 the compressed air delivered from the air compressor is processed by the coating carrier gas control device of the present invention and then used as the carrier gas supplied to the spray gun.
  • the configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
  • Example 1 when the dilution ratio of the paint with the solvent is set to 70% by weight, which is the same as Comparative Example 1 (Example 1-1), it is set to 35% by weight, which is half of Comparative Example 1. In two cases (ie, the viscosity of the paint is high; Example 1-2).
  • Example 1-1 and Example 1-2 The coating pressure for both Example 1-1 and Example 1-2 was set at 0.175 MPa MPa, which is lower than the standard pressure.
  • Example 1-1 and Example 1-2 the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
  • the number of coats (that is, the number of times the paint was applied) was basically four.
  • the amount of paint blown out due to the low coating pressure was extremely small, and the quality of the finished product could not be ensured when the number of coats was four, so the number was five. .
  • the finish of Comparative Example 1-2 was poor (in other words, a finish equivalent to that of the conventional coating of Example 1-1 was not achieved).
  • Example 1-1 and 1-2 although the coating pressure was lower than the standard, in addition, in Example 1-2, the dilution rate was small and the viscosity of the paint was low. Despite being high, the finish was good (in other words, a finish at least equivalent to the conventional coating of Example 1-1 was achieved).
  • Example 1-1 the reduction rate of the amount of paint used based on the amount of paint used in Comparative Example 1-1, which is a conventional standard coating condition, is the result of the coating pressure being low in Example 1-1.
  • Example 1-2 the coating pressure was low and the dilution rate was small, resulting in 43 %%%.
  • the coating carrier gas control device of the present invention it is possible to ensure a good finish even if the coating pressure is reduced, as compared with the conventional spray coating method, and dilution with a solvent. It was confirmed that it was possible to ensure a good finish even if the coating pressure was reduced when the rate was reduced and the viscosity of the paint was high.
  • a conventional spray painting system is used, and compressed air sent from an air compressor is supplied as it is to a painting module of a robot. When used as a carrier gas, it was painted.
  • the dilution ratio of the paint with the solvent is set to 70% by weight, which is the standard dilution ratio for the paint used in this example, and the carrier gas, paint, etc. from the paint module of the robot
  • the discharge pressure (painting pressure) was set to 0.250 kgpa, which is a conventional standard painting pressure.
  • Example 2 when compressed air delivered from an air compressor is processed by the coating carrier gas control device of the present invention and then used as a carrier gas supplied to a robot coating module Painting was done.
  • the configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
  • Example 2 the dilution ratio of the paint with the solvent was set to 50% by weight, which is smaller than that of Comparative Example 2, and the coating pressure was set to 0.175% MPa, which is lower than the standard.
  • Example 2 the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
  • Comparative Example 2 is 19.8 ⁇ m, while Example 2 is 28.7 ⁇ m, and in Example 2, the film thickness is increased by 45% by did.
  • the amount of paint used for Comparative Example 2 is less than that of Comparative Example 2 when coating with the same film thickness of 19.8 ⁇ m as in Comparative Example 2 under the conditions of Example 2. It was found that it was reduced by 31%.
  • the coating carrier gas control device of the present invention when the amount of paint used is the same, the coating film thickness can be increased by about 45% compared with the conventional spray coating method. It was confirmed that it was possible. That is, in other words, according to the present invention, it is possible to reduce the amount of paint and diluent used to make the coating film thickness the same as compared with the conventional spray coating method. Was confirmed.
  • a conventional spray painting method is used, and compressed air sent from an air compressor is supplied as it is to a painting module of a robot. When used as a carrier gas, it was painted.
  • the dilution ratio of the paint with the solvent is set to 70% by weight, which is the standard dilution ratio for the paint used in this example, and the carrier gas, paint, etc. from the paint module of the robot are set.
  • the discharge pressure (painting pressure) was set to 0.250 kgpa, which is a conventional standard painting pressure.
  • the viscosity of the paint of Comparative Example 3 the measured value at a temperature of 20 ° C. using an Iwata viscosity cup NK-2 was 11.7 seconds.
  • Example 3 when compressed air delivered from an air compressor is processed by the coating carrier gas control device of the present invention and then used as a carrier gas supplied to a robot coating module Painting was done.
  • the configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
  • Example 3 the dilution ratio of the paint with the solvent was set to 50% by weight, which is smaller than that of Comparative Example 3, and the coating pressure was set to 0.175% MPa, which is lower than the standard.
  • the viscosity of the coating material of Example 3 the measured value at a temperature of 20 ° C. using the Iwata viscosity cup NK-2 was 14.5 seconds.
  • Example 3 the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
  • Comparative Example 3 was 43.0 gr, while Example 3 was 28.3 gr, and in contrast to Comparative Example 3, the amount of paint used was 34. Reduced by%.
  • the amount of paint and diluent used to make the coating film thickness the same is 34 compared with the conventional spray coating method. It was confirmed that it was possible to reduce by about %%.

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Abstract

In order to allow a reduction in the amount of coating material or diluent used, the present invention comprises: a steam separation means (13) and a dehumidification and drying means (15), which act as drying mechanisms to dehumidify and dry a carrier gas (9) sent from a gas supply source unit (1); a pressure adjustment means (16) that adjusts the pressure of the carrier gas (9) such that the pressure in a spray gun (7) acting as a coating means, to which the carrier gas (9) is supplied, matches a prescribed pressure; a heating means (21) that heats the carrier gas (9) such that the temperature in the spray gun (7) acting as a coating means matches a prescribed temperature; and a warming means (23) that warms the atmosphere inside a housing provided with a space (24) that accommodates a hose (6) for supplying the carrier gas (9) to the spray gun (7) acting as a coating means.

Description

塗装キャリアガスの制御装置Control device for coating carrier gas
 本発明は、塗装キャリアガスの制御装置に関する。さらに詳述すると、本発明は、吹き付け塗装を行う塗装手段に供給される塗装用のキャリアガスを良好な状態に保つように制御するための技術に関する。 The present invention relates to a coating carrier gas control device. More specifically, the present invention relates to a technique for controlling the carrier gas for coating supplied to the coating means for performing spray coating so as to keep it in a good state.
 塗装手段としてスプレーガンを用いて吹き付け塗装を行う従来の装置として、例えば、図5に示すように、エアコンプレッサ101からの圧縮空気が配管102,手動エアレギュレータ103,及び配管104を介して塗料タンク105内に導入されて当該圧縮空気によって塗料タンク105内の無機塗料が配管106へ送り出されてスプレーガン107に供給されると共に、スプレーガン107へと圧縮空気を供給するための配管108が配管102から分岐して当該配管108に設けられたエアレギュレータ108aによってスプレーガン107へと供給される圧縮空気の圧力が調節されるものがある(特許文献1)。 As a conventional apparatus that performs spray painting using a spray gun as a painting means, for example, as shown in FIG. 5, compressed air from an air compressor 101 is applied to a paint tank via a pipe 102, a manual air regulator 103, and a pipe 104. The inorganic paint in the paint tank 105 is introduced into the pipe 105 and sent out to the pipe 106 by the compressed air and supplied to the spray gun 107. A pipe 108 for supplying compressed air to the spray gun 107 is provided in the pipe 102. The pressure of the compressed air supplied to the spray gun 107 is adjusted by an air regulator 108a that is branched from the pipe 108 and provided in the pipe 108 (Patent Document 1).
特開平10-235235号公報Japanese Patent Laid-Open No. 10-235235
 しかしながら、例えば特許文献1に挙げられているような従来の塗装装置では、周囲大気の圧縮空気をキャリアガスとしてスプレーガン107へと直接供給しているために湿気を含んだ状態での塗装作業になり、季節や作業環境によってキャリアガス(即ち、圧縮空気)の湿気状態が変動するので塗装仕上がりにむら(言い換えると、ばらつき)が生じ易いなどの問題がある。 However, for example, in a conventional coating apparatus such as that described in Patent Document 1, since compressed air in the surrounding atmosphere is directly supplied to the spray gun 107 as a carrier gas, the coating operation in a state including moisture is performed. Thus, the humidity state of the carrier gas (that is, compressed air) fluctuates depending on the season and work environment, so that there is a problem that unevenness (in other words, variation) is likely to occur in the finished paint.
 従来の塗装装置では、また、圧縮空気の圧力調整はエアレギュレータ108aの圧力設定のみであり、高めの設定になりがちになり、塗料及び希釈剤が過剰に使用されてしまうという問題がある。具体的には例えば、エアコンプレッサ101から0.5~1.0 MPa 程度の圧縮空気が送り出されてスプレーガン107における圧縮空気の圧力(即ち、吹き出しの圧力)が0.25 MPa 程度になるように設定される。 In the conventional coating apparatus, the pressure adjustment of the compressed air is only the pressure setting of the air regulator 108a, which tends to be a high setting, and there is a problem that the paint and diluent are excessively used. Specifically, for example, compressed air of about 0.5 to 1.0 MPa is sent from the air compressor 101 so that the pressure of the compressed air in the spray gun 107 (that is, the pressure of the blowout) becomes about 0.25 MPa. Set to
 従来の塗装装置では、さらに、エアコンプレッサ101から送出される圧縮空気の温度状態での塗装作業になり、季節や作業環境によってキャリアガス(即ち、圧縮空気)の温度が変動するので塗料の適正温度での塗料及び希釈剤の使用になっておらず、このために塗料及び希釈剤が過剰に使用されてしまう(言い換えると、歩留まりが悪い)という問題がある。 Further, in the conventional coating apparatus, the coating operation is performed in the temperature state of the compressed air sent from the air compressor 101, and the temperature of the carrier gas (that is, the compressed air) varies depending on the season and the working environment. However, there is a problem in that the paint and diluent are excessively used (in other words, the yield is poor).
 そして、塗料及び希釈剤の過剰な使用が、塗装現場の作業環境悪化の原因になり、且つ、揮発性有機化合物(VOCとも表記される)の拡散の一因になるという問題がある。 Further, there is a problem that excessive use of the paint and diluent causes deterioration of the working environment at the painting site and contributes to diffusion of volatile organic compounds (also expressed as VOC).
 そこで、本発明は、塗料及び希釈剤の使用量を低減させることができ、延いては塗装現場の作業環境を改善すると共に揮発性有機化合物の拡散を抑制することができる塗装キャリアガスの制御装置を提供することを目的とする。 Therefore, the present invention can reduce the amount of paint and diluent used, and thus improve the working environment at the painting site and suppress the diffusion of volatile organic compounds, as well as a coating carrier gas control device. The purpose is to provide.
 かかる目的を達成するため、本発明の塗装キャリアガスの制御装置は、ガス供給源ユニットから送出されるキャリアガスを除湿し乾燥させるドライ化機構と、キャリアガスが供給される塗装手段における圧力が所定の圧力になるようにキャリアガスの圧力を調整する圧力調整手段と、塗装手段における温度が所定の温度になるようにキャリアガスを加温する加温手段と、塗装手段にキャリアガスを供給するためのホースを収容するスペースを備える筐体内の雰囲気を温める暖房手段とを有するようにしている。 In order to achieve such an object, the coating carrier gas control device of the present invention has a predetermined pressure in the drying mechanism for dehumidifying and drying the carrier gas delivered from the gas supply source unit and the coating means to which the carrier gas is supplied. Pressure adjusting means for adjusting the pressure of the carrier gas so that the pressure of the carrier gas becomes equal to, a heating means for heating the carrier gas so that the temperature in the coating means becomes a predetermined temperature, and for supplying the carrier gas to the coating means Heating means for heating the atmosphere in the housing having a space for housing the hose.
 したがって、この塗装キャリアガスの制御装置によると、塗装手段に供給されるキャリアガスの湿度,温度,及び圧力が適切な状態に管理・制御されるので、塗料の吹き付けに適切であり且つ均一な品質であるキャリアガスが塗装手段に供給される。 Therefore, according to this coating carrier gas control device, the humidity, temperature, and pressure of the carrier gas supplied to the coating means are managed and controlled in an appropriate state, so that it is suitable for spraying paint with uniform quality. Is supplied to the coating means.
 この塗装キャリアガスの制御装置によると、また、塗装手段に供給されるキャリアガスが適切に加温されることによって当該キャリアガスと一緒に吹き出される塗料が加温され、これによって塗料が塗装に適正な噴霧状態になり易くなるので、従来よりも低い吹き付けの圧力によって塗装が行われる。 According to this coating carrier gas control device, when the carrier gas supplied to the coating means is appropriately heated, the paint blown out together with the carrier gas is heated, whereby the paint is applied to the coating. Since it becomes easy to be in an appropriate spraying state, coating is performed with a lower spraying pressure than in the past.
 本発明の塗装キャリアガスの制御装置は、ドライ化機構を通過した後のキャリアガスを加圧状態で一時貯蔵した上で圧力調整手段に送出する貯留ユニットを更に有するようにしても良く、この場合には、キャリアガスの送出の圧力が平滑にされるので、塗装手段から吹き出されるキャリアガスの吹き出しの圧力が、延いてはキャリアガスと一緒に塗装手段から吹き出される塗料の吹き出しの圧力が平滑になる。 The coating carrier gas control device of the present invention may further include a storage unit that temporarily stores the carrier gas after passing through the drying mechanism in a pressurized state and then sends it to the pressure adjusting means. Since the carrier gas delivery pressure is smoothed, the pressure of the carrier gas blown out from the coating means, and the pressure of the paint blowout from the painting means together with the carrier gas is increased. It becomes smooth.
 本発明の塗装キャリアガスの制御装置は、ホースが保温材で覆われているようにしても良く、この場合には、ホース内のキャリアガスの放熱による温度低下が抑制されるので、塗装手段から吹き出されるキャリアガスの温度低下が、延いてはキャリアガスと一緒に塗装手段から吹き出される塗料の温度低下が抑制される。 In the coating carrier gas control device of the present invention, the hose may be covered with a heat insulating material. In this case, since the temperature drop due to the heat radiation of the carrier gas in the hose is suppressed, The temperature drop of the blown carrier gas is suppressed, and the temperature drop of the paint blown out from the coating means together with the carrier gas is suppressed.
 本発明の塗装キャリアガスの制御装置は、塗装手段に向けてキャリアガスが吹き出されるようにホースから分岐する器具を更に有するようにしても良く、この場合には、塗装手段が温められると共に塗装作業の間に亙って保温されるので、塗装手段から吹き出される塗料の温度低下が抑制される。 The control device for the coating carrier gas of the present invention may further include a device branched from the hose so that the carrier gas is blown out toward the coating means. In this case, the coating means is warmed and the coating is performed. Since the temperature is kept during the work, the temperature drop of the paint blown out from the coating means is suppressed.
 本発明の塗装キャリアガスの制御装置は、塗装手段に供給される塗料を収容すると共に筐体内の雰囲気を利用して塗料を塗装作業前に温めるための塗料加温部を更に有するようにしても良く、この場合には、予め温められた塗料が塗装手段に供給されるので、塗装手段から吹き出される際の塗料とキャリアガスとの混合体としての温度低下が抑制される。 The control device for the coating carrier gas of the present invention may further include a paint heating unit for storing the paint supplied to the painting means and for heating the paint before the painting operation using the atmosphere in the housing. Well, in this case, since the preheated paint is supplied to the coating means, the temperature drop as a mixture of the paint and the carrier gas when blown out from the coating means is suppressed.
 本発明の塗装キャリアガスの制御装置は、ドライ化機構及び圧力調整手段を含む気流調整ユニットと、加温手段及び暖房手段を含む加温ユニットと、貯留ユニットとのそれぞれに、または、これらユニットのうちの任意の複数のユニットの組み合わせに対し、移動手段が備えられるようにしても良く、この場合には、ユニット毎若しくは複数のユニットの組み合わせ毎に移動可能になるので、塗装作業の工程による塗装場所(塗装の現場)の移動に合わせての装置の移動・設置が容易に行われる。 The coating carrier gas control device according to the present invention includes an airflow adjustment unit including a drying mechanism and a pressure adjustment unit, a heating unit including a heating unit and a heating unit, and a storage unit, or a storage unit of these units. A moving means may be provided for any combination of a plurality of units, and in this case, the unit can be moved for each unit or for each combination of a plurality of units. Equipment can be easily moved and installed according to the location (painting site).
 本発明の塗装キャリアガスの制御装置によれば、塗料の吹き付けに適切であり且つ均一な品質であるキャリアガスを塗装手段に供給することができるので、吹き付け塗装の仕上がりを良好なものにすることが可能になる。 According to the coating carrier gas control device of the present invention, a carrier gas suitable for spraying paint and having a uniform quality can be supplied to the coating means, so that the finish of spray coating is improved. Is possible.
 本発明の塗装キャリアガスの制御装置によれば、従来よりも低い吹き付けの圧力によって塗装を行うことができるので、液体塗料を吹き付ける場合の塗料及び希釈剤の使用量を低減させることが可能になり、また、粉体塗料を吹き付ける場合の塗料の使用量を低減させることが可能になる。 According to the coating carrier gas control device of the present invention, since coating can be performed with a lower spray pressure than before, it is possible to reduce the amount of paint and diluent used when spraying liquid paint. In addition, the amount of paint used in the case of spraying a powder paint can be reduced.
 また、本発明の塗装キャリアガスの制御装置は、キャリアガスを一時貯蔵する貯留ユニットを有するようにした場合には、キャリアガスと一緒に塗装手段から吹き出される塗料の吹き出しの圧力を平滑にすることができるので、塗料の吹き出し量の変動を防止することが可能になり、延いては塗料の塗装のむらを防いで吹き付け塗装の仕上がりを良好なものにすることが可能になる。 In addition, when the coating carrier gas control device of the present invention has a storage unit for temporarily storing the carrier gas, the coating gas blowing pressure blown from the coating means together with the carrier gas is smoothed. As a result, it is possible to prevent fluctuations in the amount of paint blown out, thereby preventing uneven coating of the paint and improving the finish of the spray painting.
 本発明の塗装キャリアガスの制御装置は、ホースが保温材で覆われているようにした場合には、キャリアガスと一緒に塗装手段から吹き出される塗料の温度低下を抑制することができるので、塗料の温度管理が容易になり、延いては塗料の温度を適切な状態に維持して良好な塗装を行うことが可能になる。 When the hose is covered with a heat insulating material, the coating carrier gas control device of the present invention can suppress the temperature drop of the paint blown from the coating means together with the carrier gas. The temperature control of the paint becomes easy, and as a result, the paint temperature can be maintained in an appropriate state and good coating can be performed.
 本発明の塗装キャリアガスの制御装置は、ホースから分岐する器具を有するようにした場合には、塗装手段から吹き出される塗料の温度低下を抑制することができるので、塗料の温度管理が容易になり、延いては塗料の温度を適切な状態に維持して良好な塗装を行うことが可能になる。 When the coating carrier gas control device of the present invention has an appliance branched from the hose, it can suppress the temperature drop of the paint blown out from the painting means, so that the temperature management of the paint is easy. As a result, it is possible to perform satisfactory coating while maintaining the temperature of the coating material in an appropriate state.
 本発明の塗装キャリアガスの制御装置は、塗料を塗装作業前に温めるための塗料加温部を有するようにした場合には、塗装手段から吹き出される際の塗料とキャリアガスとの混合体としての温度低下を抑制することができるので、塗料の温度管理が容易になり、延いては塗料の温度を適切な状態に維持して良好な塗装を行うことが可能になる。 When the paint carrier gas control device of the present invention has a paint heating unit for warming the paint before the painting operation, it is a mixture of the paint and the carrier gas when blown out from the painting means. Therefore, it is possible to easily control the temperature of the coating material, and to maintain the temperature of the coating material in an appropriate state and perform good coating.
 本発明の塗装キャリアガスの制御装置は、装置を構成するユニットに移動手段が備えられるようにした場合には、塗装作業の工程による塗装場所(塗装の現場)の移動に合わせての装置の移動・設置を容易に行うことができるので、装置の扱い易さを向上させ、延いては塗装作業の手間を軽減させることが可能になる。 In the coating carrier gas control apparatus according to the present invention, when the moving means is provided in the units constituting the apparatus, the movement of the apparatus in accordance with the movement of the painting place (painting place) by the painting work process. -Since installation can be performed easily, it becomes possible to improve the ease of handling of the apparatus and to reduce the labor of painting work.
本発明の塗装キャリアガスの制御装置の実施形態の一例を示す機能ブロック図(言い換えると、配管系統図)である。It is a functional block diagram (in other words, piping system diagram) showing an example of the embodiment of the control device for the coating carrier gas of the present invention. 実施例1の結果を整理した表を示す図である。It is a figure which shows the table | surface which arranged the result of Example 1. FIG. 実施例2の結果を整理した表を示す図である。It is a figure which shows the table | surface which arranged the result of Example 2. FIG. 実施例3の結果を整理した表を示す図である。It is a figure which shows the table | surface which arranged the result of Example 3. FIG. 従来の塗装装置を示す配管系統図である。It is a piping system diagram which shows the conventional coating apparatus.
 以下、本発明の構成を図面に示す実施の形態の一例に基づいて詳細に説明する。 Hereinafter, the configuration of the present invention will be described in detail based on an example of an embodiment shown in the drawings.
 図1に、本発明の塗装キャリアガスの制御装置の実施形態の一例を示す。 FIG. 1 shows an example of an embodiment of a coating carrier gas control device of the present invention.
 本実施形態の塗装キャリアガスの制御装置は、大まかな構成として、気流調整ユニット10と貯留ユニット4と加温ユニット20とを有する。そして、ガス供給源ユニット1から供給されてこれらユニット10,4,20を経て必要な処理をされたキャリアガス9の圧力によって塗装手段7から塗料が吹き出される(言い換えると、噴霧・吐出される)。 The control device for the coating carrier gas of the present embodiment includes an airflow adjustment unit 10, a storage unit 4, and a heating unit 20 as a rough configuration. Then, the paint is blown out from the coating means 7 by the pressure of the carrier gas 9 supplied from the gas supply source unit 1 and subjected to necessary processing through these units 10, 4, 20 (in other words, sprayed / discharged). ).
 本発明における塗装手段7としては、例えば、従来の塗装用のスプレーガンと同様のスプレーガンが使用可能である。 As the coating means 7 in the present invention, for example, a spray gun similar to a conventional spray gun for painting can be used.
 具体的には例えば、塗料が吹き出されるノズルと、作業時に把持されるグリップと、塗料の吹き出しの開始及び停止並びに程度を制御するトリガーと、塗料カップ7aとを有すると共に、ホース6が接続される手吹きスプレーガン(なお、塗料カップ7aを有する点においてカップガンとも呼ばれる)が使用され得る。 Specifically, for example, it has a nozzle that sprays paint, a grip that is gripped during work, a trigger that controls the start, stop, and degree of paint blowing, a paint cup 7a, and a hose 6 connected thereto. A hand-blown spray gun (also referred to as a cup gun in terms of having a paint cup 7a) may be used.
 塗料カップ7aには、希釈剤・溶剤などによって適宜の濃度に調製された液体塗料(溶剤塗料とも呼ばれる)が入れられる。 The paint cup 7a is filled with a liquid paint (also referred to as a solvent paint) adjusted to an appropriate concentration with a diluent / solvent.
 そして、トリガーが操作されることにより、加圧されたキャリアガス9がホース6から導入され、当該加圧されたキャリアガス9と一緒に(言い換えると、加圧されたキャリアガス9と混合されると共に当該加圧されたキャリアガス9の圧力によって)塗料がノズルから吹き出されることによって塗装が行われる。 Then, when the trigger is operated, the pressurized carrier gas 9 is introduced from the hose 6 and mixed with the pressurized carrier gas 9 (in other words, the pressurized carrier gas 9 is mixed). At the same time, the paint is blown out from the nozzle (by the pressure of the pressurized carrier gas 9).
 そして、本実施形態の塗装キャリアガスの制御装置は、ガス供給源ユニット1から送出されるキャリアガス9を除湿し乾燥させるドライ化機構としての気水分離手段13及び除湿乾燥手段15と、キャリアガス9が供給される塗装手段としてのスプレーガン7における圧力が所定の圧力になるようにキャリアガス9の圧力を調整する圧力調整手段16と、塗装手段としてのスプレーガン7における温度が所定の温度になるようにキャリアガス9を加温する加温手段21と、塗装手段としてのスプレーガン7にキャリアガス9を供給するためのホース6を収容するスペース24を備える筐体内の雰囲気を温める暖房手段23とを有するようにしている。 And the control apparatus of the coating carrier gas of this embodiment is the air-water separation means 13 and the dehumidification drying means 15 as a drying mechanism which dehumidifies and dries the carrier gas 9 sent from the gas supply source unit 1, and carrier gas. Pressure adjusting means 16 for adjusting the pressure of the carrier gas 9 so that the pressure in the spray gun 7 as the coating means to which 9 is supplied becomes a predetermined pressure, and the temperature in the spray gun 7 as the coating means is set to a predetermined temperature. Heating means 21 for heating the atmosphere in the housing provided with a heating means 21 for heating the carrier gas 9 and a space 24 for housing the hose 6 for supplying the carrier gas 9 to the spray gun 7 as a coating means. And have
 本実施形態の塗装キャリアガスの制御装置は、さらに、ドライ化機構としての気水分離手段13を通過した後のキャリアガス9を加圧状態で一時貯蔵した上で圧力調整手段16に送出する貯留ユニット4を有するようにしている。 The coating carrier gas control device of the present embodiment further stores the carrier gas 9 after passing through the steam-water separating means 13 as a drying mechanism, temporarily stored in a pressurized state and then sent to the pressure adjusting means 16. The unit 4 is provided.
 ガス供給源ユニット1は、塗装手段としてのスプレーガン7からの塗料の吹き出しに利用されるキャリアガス9を所定の圧力で送出して気流調整ユニット10へと供給するためのものである。 The gas supply source unit 1 is for sending a carrier gas 9 used for blowing paint from a spray gun 7 as a coating means at a predetermined pressure and supplying the carrier gas 9 to the airflow adjusting unit 10.
 本発明におけるキャリアガス9としては、従来のスプレーガンに供給されていた気体と同様の気体が使用可能であり、例えば空気や不活性ガス、具体的には空気,窒素(N)ガス,或いはヘリウム(He)ガスなどが使用され得る(なお、圧縮ガスとして供給される)。 As the carrier gas 9 in the present invention, a gas similar to the gas supplied to the conventional spray gun can be used. For example, air, inert gas, specifically air, nitrogen (N 2 ) gas, or Helium (He) gas or the like can be used (which is supplied as a compressed gas).
 また、ガス供給源ユニット1としては、キャリアガス9を所定の加圧状態にて貯留ユニット4に貯留させ得る圧力にてガスを送出する性能を有する仕組みが用いられる。 Further, as the gas supply source unit 1, a mechanism is used that has a capability of delivering gas at a pressure that can cause the storage unit 4 to store the carrier gas 9 in a predetermined pressurized state.
 ガス供給源ユニット1から送出されるキャリアガス9の圧力は、特定の値に限定されるものではなく、例えばキャリアガス9が気流調整ユニット10を経由した上で所定の加圧状態にて貯留ユニット4に貯留され得る圧力が考慮された上で適正な値に適宜設定される。具体的には例えば、あくまで一例として挙げると、0.50~1.0 MPa 程度の範囲で適正な値に適宜設定される。 The pressure of the carrier gas 9 delivered from the gas supply source unit 1 is not limited to a specific value. For example, the carrier gas 9 passes through the airflow adjustment unit 10 and is stored in a predetermined pressurized state. In consideration of the pressure that can be stored in 4, it is appropriately set to an appropriate value. Specifically, for example, as an example, it is appropriately set to an appropriate value in a range of about 0.50 to 1.0 MPa.
 ガス供給源ユニット1としては、具体的には例えば、エアコンプレッサが用いられたり、キャリアガス9が圧縮気体として充填されたガスボンベと当該ガスボンベから出力されるガスの圧力を調整するための圧力調整器との組み合わせが用いられたりする。 Specifically, as the gas supply source unit 1, for example, an air compressor is used, or a gas cylinder filled with a carrier gas 9 as a compressed gas, and a pressure regulator for adjusting the pressure of the gas output from the gas cylinder Or a combination of
 ガス供給源ユニット1から送出されたキャリアガス9は、ガス入力配管2を介して気流調整ユニット10に供給される。 The carrier gas 9 sent out from the gas supply source unit 1 is supplied to the airflow adjustment unit 10 through the gas input pipe 2.
 本実施形態では、ガス入力配管2に設けられたガス入力バルブ11の開閉によって気流調整ユニット10へのキャリアガス9の流入の許容と制限とが制御される。 In this embodiment, the allowance and restriction of the inflow of the carrier gas 9 to the airflow adjustment unit 10 are controlled by opening and closing the gas input valve 11 provided in the gas input pipe 2.
 気流調整ユニット10は、ガス供給源ユニット1から供給されたキャリアガス9に対して清浄処理並びに気水分離処理や除湿乾燥処理を施すと共に、加温ユニット20を経てホース6を介してスプレーガン7へと供給されるキャリアガス9の圧力を調整するためのものである。 The air flow adjusting unit 10 performs a cleaning process, a water / water separation process and a dehumidifying and drying process on the carrier gas 9 supplied from the gas supply source unit 1, and a spray gun 7 through a heating unit 20 and a hose 6. This is for adjusting the pressure of the carrier gas 9 supplied to the air.
 気流調整ユニット10は、本実施形態では、清浄処理を行うための清浄処理機構と、気水分離処理及び除湿乾燥処理を行うためのドライ化機構とを有する。そして、清浄処理機構として一次清浄手段12と二次清浄手段14とを備え、ドライ化機構として気水分離手段13と除湿乾燥手段15とを備える。 In the present embodiment, the airflow adjustment unit 10 includes a cleaning mechanism for performing a cleaning process, and a drying mechanism for performing a steam-water separation process and a dehumidifying and drying process. And it comprises the primary cleaning means 12 and the secondary cleaning means 14 as the cleaning processing mechanism, and the steam-water separating means 13 and the dehumidifying and drying means 15 as the drying mechanism.
 キャリアガス9は、まず、気流調整ユニット10に備えられる一次清浄手段12に導入される。 The carrier gas 9 is first introduced into the primary cleaning means 12 provided in the airflow adjustment unit 10.
 一次清浄手段12は、キャリアガス9中の粉塵などの夾雑物を取り除いて当該キャリアガス9を清浄化(一次清浄処理)するためのものである。 The primary cleaning means 12 is for removing contaminants such as dust in the carrier gas 9 to clean the carrier gas 9 (primary cleaning process).
 一次清浄手段12は、特定の種類や仕様のものに限定されるものではなく、例えばキャリアガス9を貯留ユニット4に貯留するに際して必要とされる清浄の程度などが考慮された上で適正なものが適宜選択される。 The primary cleaning means 12 is not limited to a specific type or specification, and is appropriate in consideration of, for example, the degree of cleaning required when storing the carrier gas 9 in the storage unit 4. Is appropriately selected.
 一次清浄手段12としては、具体的には例えば、適正な濾過性能(濾過度)を具備したエアフィルタが用いられ得る。 As the primary cleaning means 12, specifically, for example, an air filter having appropriate filtration performance (filtration degree) can be used.
 キャリアガス9は、また、気流調整ユニット10に備えられる気水分離手段13に導入される。 The carrier gas 9 is also introduced into the steam / water separation means 13 provided in the airflow adjustment unit 10.
 気水分離手段13は、キャリアガス9中のドレン・水滴を分離・排除して当該キャリアガス9を脱水するためのものである。 The air / water separation means 13 is for dehydrating the carrier gas 9 by separating and removing drains and water droplets in the carrier gas 9.
 気水分離手段13は、特定の種類や仕様のものに限定されるものではなく、例えばキャリアガス9を所定の圧力にて貯留ユニット4に貯留するに際して必要とされるドライ化(脱水)の程度などが考慮された上で適正なものが適宜選択される。 The steam-water separation means 13 is not limited to a specific type or specification, and for example, the degree of drying (dehydration) required when storing the carrier gas 9 in the storage unit 4 at a predetermined pressure. Appropriate ones are selected as appropriate.
 気水分離手段13としては、具体的には例えば、適正なドレン・水滴の分離・排除性能を具備した気水分離器が用いられ得る。 As the steam-water separation means 13, specifically, for example, a steam-water separator having proper drain / water droplet separation / exclusion performance can be used.
 なお、一次清浄手段12や気水分離手段13によって分離・排除された夾雑物や水分などは、例えば気流調整ユニット10の外部に設置されたドレンパン(図示省略)へと集められて適宜廃棄される。 Note that the foreign matter, moisture, and the like separated and removed by the primary cleaning means 12 and the air / water separation means 13 are collected, for example, in a drain pan (not shown) installed outside the airflow adjustment unit 10 and appropriately discarded. .
 また、図1に示す例では一次清浄処理の次に気水分離処理が施されるようにしているが、この順序に限られるものではなく、気水分離処理の次に一次清浄処理が施されるようにしても良い。 Further, in the example shown in FIG. 1, the air / water separation process is performed after the primary cleaning process, but the order is not limited to this, and the primary cleaning process is performed next to the air / water separation process. You may make it.
 気流調整ユニット10において一次清浄処理と気水分離処理とが施されたキャリアガス9は、当該気流調整ユニット10から導入配管3Aを介して送出されて貯留ユニット4へと導入される。 The carrier gas 9 subjected to the primary cleaning process and the steam separation process in the airflow adjustment unit 10 is sent out from the airflow adjustment unit 10 via the introduction pipe 3A and introduced into the storage unit 4.
 貯留ユニット4は、キャリアガス9の送出の圧力を平滑なものにして当該キャリアガス9の流動性を安定させる目的で、所定の(若しくは、所定の範囲内の)加圧状態にてキャリアガス9を一時的に貯蔵しておくためのものである。 The storage unit 4 is a carrier gas 9 in a predetermined (or within a predetermined range) pressurized state for the purpose of smoothing the delivery pressure of the carrier gas 9 and stabilizing the fluidity of the carrier gas 9. Is for temporary storage.
 特に、ガス供給源ユニット1としてエアコンプレッサが用いられる場合には、エアコンプレッサから送出されるキャリアガス9は波動変動や脈動を伴うものであるところ、貯留ユニット4に一旦貯蔵してから送出することによって前記波動変動や脈動が解消されて(つまり、抑制されて)キャリアガス9の送出の圧力が平滑になって流動性が安定し、延いてはスプレーガン7からの塗料の吐出が安定する。 In particular, when an air compressor is used as the gas supply source unit 1, the carrier gas 9 sent from the air compressor is accompanied by wave fluctuations and pulsations. Thus, the wave fluctuation and pulsation are eliminated (that is, suppressed), the pressure of delivery of the carrier gas 9 is smoothed, the fluidity is stabilized, and the discharge of the paint from the spray gun 7 is stabilized.
 貯留ユニット4としては、具体的には例えば、所定の加圧状態にてガスを貯蔵し得る程度の強度(具体的には、気密性)を少なくとも具備したタンクが用いられ得る。 As the storage unit 4, specifically, for example, a tank having at least strength (specifically, airtightness) that can store gas in a predetermined pressurized state may be used.
 貯留ユニット4内のガス圧は、あくまで一例として挙げると、具体的には例えば0.50~1.0 MPa 程度の範囲であるように調整される。 The gas pressure in the storage unit 4 is adjusted so as to be in the range of, for example, about 0.50 to 1.0 mm2 for example as an example.
 貯留ユニット4の内容積や最高使用圧力は、特定の大きさや数値に限定されるものではなく、例えば一定の時間に及ぶ連続的な塗装作業を支障なく行うために必要とされる容積やスプレーガン7に供給されるキャリアガス9の最終的な圧力などが考慮された上で適正な大きさや数値に適宜設定される。 The internal volume and the maximum operating pressure of the storage unit 4 are not limited to a specific size or numerical value. For example, the volume or spray gun required for performing a continuous painting operation for a certain time without trouble. In consideration of the final pressure of the carrier gas 9 supplied to 7, it is appropriately set to an appropriate size and value.
 貯留ユニット4の内容積は、あくまで一例として挙げると、具体的には例えば40~80 L 程度の範囲で適正な大きさに設定され得る。また、貯留ユニット4の使用圧力は、あくまで一例として挙げると、具体的には例えば0.50~1.0 MPa 程度の範囲で適正な数値に設定され得る。 The internal volume of the storage unit 4 can be set to an appropriate size in a range of, for example, about 40 to 80 L, specifically as an example. Further, the working pressure of the storage unit 4 can be set to an appropriate numerical value within a range of, for example, about 0.50 to 1.0 kgpa, for example.
 そして、貯留ユニット4の送出弁の開放の程度を一定で固定することにより、当該貯留ユニット4の送出弁から、周期的に変動することのない平滑な圧力でキャリアガス9が送出される。 Then, by fixing the degree of opening of the delivery valve of the storage unit 4 at a constant level, the carrier gas 9 is delivered from the delivery valve of the storage unit 4 with a smooth pressure that does not vary periodically.
 貯留ユニット4から送出されたキャリアガス9は、送出配管3Bを介して気流調整ユニット10にあらためて供給される。 The carrier gas 9 sent out from the storage unit 4 is supplied again to the air flow adjusting unit 10 through the sending pipe 3B.
 そして、キャリアガス9は、気流調整ユニット10に備えられる二次清浄手段14に導入される。 Then, the carrier gas 9 is introduced into the secondary cleaning means 14 provided in the airflow adjustment unit 10.
 二次清浄手段14は、キャリアガス9中の油微粒子(オイルミスト)や微粒固形物等のダスト・不純物などを取り除いて当該キャリアガス9を清浄化(二次清浄処理)するためのものである。 The secondary cleaning means 14 is for removing dust / impurities such as oil fine particles (oil mist) and fine solids in the carrier gas 9 to clean the carrier gas 9 (secondary cleaning treatment). .
 二次清浄手段14は、特定の種類や仕様のものに限定されるものではなく、例えば除湿乾燥手段15に供給されるキャリアガス9として望ましい清浄の程度やスプレーガン7に供給されるキャリアガス9として望ましい清浄の程度などが考慮された上で適正なものが適宜選択される。 The secondary cleaning means 14 is not limited to a specific type or specification. For example, the desired degree of cleaning as the carrier gas 9 supplied to the dehumidifying and drying means 15 and the carrier gas 9 supplied to the spray gun 7 are used. In consideration of a desirable degree of cleaning, an appropriate one is appropriately selected.
 二次清浄手段14としては、具体的には例えば、適正なダスト除去・吸収性能を具備したミストフィルタ,マイクロミストフィルタ,及びスーパーミストフィルタ(それぞれ、ミストセパレータ,マイクロミストセパレータ,及びスーパーミストセパレータとも呼ばれる)のうちのいずれか一つが用いられたり二つ以上が組み合わされて用いられたりされ得る。 Specifically, as the secondary cleaning means 14, for example, a mist filter, a micro mist filter, and a super mist filter having appropriate dust removal / absorption performance (each of which is a mist separator, a micro mist separator, and a super mist separator, respectively) Any one of them may be used, or two or more may be used in combination.
 キャリアガス9は、続いて、気流調整ユニット10に備えられる除湿乾燥手段15に導入される。 The carrier gas 9 is then introduced into the dehumidifying and drying means 15 provided in the airflow adjusting unit 10.
 除湿乾燥手段15は、キャリアガス9中の湿気分を除去して当該キャリアガス9を除湿し乾燥させるためのものである。 The dehumidifying and drying means 15 is for removing moisture in the carrier gas 9 and dehumidifying and drying the carrier gas 9.
 除湿乾燥手段15は、特定の種類や仕様のものに限定されるものではなく、例えばスプレーガン7に供給されるキャリアガス9として望ましいドライ化(除湿,乾燥)の程度などが考慮された上で適正なものが適宜選択される。 The dehumidifying and drying means 15 is not limited to a specific type or specification. For example, the degree of drying (dehumidifying and drying) desirable as the carrier gas 9 supplied to the spray gun 7 is considered. An appropriate one is appropriately selected.
 除湿乾燥手段15としては、具体的には例えば、適正な湿気分の除去性能を具備したエアドライヤが用いられ得る。 As the dehumidifying and drying means 15, specifically, for example, an air dryer having an appropriate moisture removal performance can be used.
 キャリアガス9は、続いて、気流調整ユニット10に備えられる圧力調整手段16に導入される。 The carrier gas 9 is then introduced into the pressure adjusting means 16 provided in the airflow adjusting unit 10.
 圧力調整手段16は、キャリアガス9の圧力が加温ユニット20を経てホース6を介してスプレーガン7へと供給されるのに適切な圧力になるように、言い換えると、スプレーガン7からのキャリアガス9の吹き出し圧力が適切なものになるように、加温ユニット20へと送出するキャリアガス9の圧力を調整するためのものである。 The pressure adjusting means 16 is configured so that the pressure of the carrier gas 9 becomes an appropriate pressure to be supplied to the spray gun 7 via the hose 6 via the heating unit 20, in other words, the carrier from the spray gun 7. This is for adjusting the pressure of the carrier gas 9 delivered to the heating unit 20 so that the blowing pressure of the gas 9 becomes appropriate.
 圧力調整手段16によるキャリアガス9の送出の設定圧力は、特定の値に限定されるものではなく、例えばスプレーガン7からのキャリアガス9の適切な吹き出し圧力やホース6等を通過する間におけるキャリアガス9の圧力損失などが考慮された上で適正な値に適宜設定される。具体的には例えば、あくまで一例として挙げると、0.3~0.5 MPa 程度の範囲で適正な値に適宜設定される。 The set pressure for delivery of the carrier gas 9 by the pressure adjusting means 16 is not limited to a specific value. For example, the carrier gas 9 is discharged from the spray gun 7 while the carrier gas 9 passes through the appropriate pressure or hose 6. An appropriate value is appropriately set in consideration of the pressure loss of the gas 9 and the like. Specifically, for example, as an example, it is appropriately set to an appropriate value in a range of about 0.3 to 0.5 MPa.
 圧力調整手段16は、特定の種類や仕様のものに限定されるものではなく、貯留ユニット4から所定の圧力で送出されて入力されたキャリアガス9を所定の一定の圧力で出力する働きをし得る適正な仕組みが適宜選択される。 The pressure adjusting means 16 is not limited to a specific type or specification, and functions to output the carrier gas 9 sent and input from the storage unit 4 at a predetermined pressure at a predetermined constant pressure. An appropriate mechanism to be obtained is appropriately selected.
 圧力調整手段16としては、具体的には例えば、入力されるガスの圧力が変動しても出力するガスの圧力を一定に保つ働きをし得る圧力調整器(圧力調整弁やレギュレータとも呼ばれる)が用いられ得る。 Specifically, as the pressure adjusting means 16, for example, there is a pressure regulator (also called a pressure regulating valve or a regulator) that can keep the pressure of the output gas constant even if the pressure of the input gas fluctuates. Can be used.
 そして、気流調整ユニット10において清浄処理と気水分離処理と除湿乾燥処理とが施され且つ圧力が調整されたキャリアガス9は、当該気流調整ユニット10から接続配管5を介して加温ユニット20へと送出される。 Then, the carrier gas 9 that has been subjected to the cleaning process, the steam separation process, and the dehumidifying drying process in the airflow adjustment unit 10 and whose pressure has been adjusted is transferred from the airflow adjustment unit 10 to the heating unit 20 via the connection pipe 5. Is sent out.
 加温ユニット20は、気流調整ユニット10から送出されたキャリアガス9に対して加温処理を施すと共に、スプレーガン7に接続されて当該スプレーガン7にキャリアガス9を供給するためのホース6を(延いては、ホース6内のキャリアガス9を)加温して保温するためのものである。 The heating unit 20 performs a heating process on the carrier gas 9 delivered from the airflow adjustment unit 10 and is connected to the spray gun 7 to provide a hose 6 for supplying the carrier gas 9 to the spray gun 7. This is to heat and keep the carrier gas 9 in the hose 6 warm.
 加温ユニット20は、このため、筐体を有し、当該筐体の内部に加温手段21及び暖房手段23を備える。 For this reason, the heating unit 20 has a casing, and includes a heating means 21 and a heating means 23 inside the casing.
 そして、キャリアガス9は、加温ユニット20に備えられる加温手段21に導入される。 Then, the carrier gas 9 is introduced into the heating means 21 provided in the heating unit 20.
 加温手段21は、キャリアガス9の温度がホース6を介してスプレーガン7へと供給されるのに適切な温度になるように、言い換えると、スプレーガン7からのキャリアガス9の吹き出し温度が適切なものになるように、ホース6へと送出するキャリアガス9の温度を調整するためのものである。 The heating means 21 adjusts the blowing temperature of the carrier gas 9 from the spray gun 7 so that the temperature of the carrier gas 9 becomes an appropriate temperature to be supplied to the spray gun 7 via the hose 6. It is for adjusting the temperature of the carrier gas 9 delivered to the hose 6 so as to be appropriate.
 加温手段21によるキャリアガス9の加温処理の設定温度は、特定の値に限定されるものではなく、例えばスプレーガン7からのキャリアガス9の適切な吹き出し温度やホース6等を通過する間におけるキャリアガス9の温度低下などが考慮された上で適正な値に適宜設定される。具体的には例えば、30~60 ℃ 程度の範囲に設定されることが好ましく、40~55 ℃ 程度の範囲に設定されることが更に好ましく、50 ℃ 程度に設定されることが最も好ましい。 The set temperature of the heating process of the carrier gas 9 by the heating means 21 is not limited to a specific value, for example, while passing through an appropriate blowing temperature of the carrier gas 9 from the spray gun 7 or the hose 6 or the like. In consideration of the temperature drop of the carrier gas 9 in FIG. Specifically, for example, it is preferably set in a range of about 30 to 60 ° C., more preferably in a range of about 40 to 55 ° C., and most preferably about 50 ° C.
 加温手段21は、特定の種類や仕様のものに限定されるものではなく、入力される種々の温度のキャリアガス9を上記温度で出力する働きをし得る適正な仕組みが適宜選択される。 The heating means 21 is not limited to a specific type or specification, and an appropriate mechanism that can function to output the input carrier gas 9 at various temperatures at the above temperature is appropriately selected.
 加温手段21としては、具体的には例えば、通過するガスの流量に応じて所望の熱量を当該ガスに対して供給し得るガス加温器が用いられ得る。 As the heating means 21, specifically, for example, a gas warmer capable of supplying a desired amount of heat to the gas according to the flow rate of the passing gas can be used.
 本実施形態では、加温手段21の出力側の配管にガス出力バルブ22が設けられ、当該ガス出力バルブ22の開閉によって加温ユニット20からのキャリアガス9の流出の許容と制限とが制御される。 In the present embodiment, a gas output valve 22 is provided in the piping on the output side of the heating means 21, and the allowance and limitation of the outflow of the carrier gas 9 from the heating unit 20 are controlled by opening and closing the gas output valve 22. The
 ガス出力バルブ22にはホース6が接続され、当該ホース6端部のソケット8Aと当該ソケット8Aと結合するプラグ8Bとからなるカプラ8を介して当該ホース6とスプレーガン7とが連結される。 The hose 6 is connected to the gas output valve 22, and the hose 6 and the spray gun 7 are connected via a coupler 8 including a socket 8A at the end of the hose 6 and a plug 8B coupled to the socket 8A.
 そして、ガス出力バルブ22が開放されると、加温手段21からホース6へとキャリアガス9が送出され、ホース6を通過したキャリアガス9がスプレーガン7へと供給される。 When the gas output valve 22 is opened, the carrier gas 9 is sent from the heating means 21 to the hose 6, and the carrier gas 9 that has passed through the hose 6 is supplied to the spray gun 7.
 ホース6としては、スプレーガン7に供給されるキャリアガス9の所定の圧力に耐え得る性能を有するものが用いられる。 As the hose 6, a hose having a performance capable of withstanding a predetermined pressure of the carrier gas 9 supplied to the spray gun 7 is used.
 また、ホース6が、キャリアガス9を整流させる機能・仕組みを備えることが好ましい。具体的には例えば、ホース6の内周面に螺旋状に連続する凹溝若しくは螺旋状に連なる凸部が形成されたり、ホース6内のスプレーガン7寄りの部分に螺旋状(言い換えると、渦巻状,コイルスプリング状)の部材が装着されたりすることが考えられる。これにより、ホース6からスプレーガン7へと送出されるキャリアガス9の流動が整えられ、安定した流れのキャリアガス9がスプレーガン7へと供給され、延いてはスプレーガン7からの塗料の吐出が安定する。 Further, it is preferable that the hose 6 has a function / mechanism for rectifying the carrier gas 9. Specifically, for example, a concave groove continuous in a spiral shape or a convex portion continuous in a spiral shape is formed on the inner peripheral surface of the hose 6, or a spiral shape (in other words, a spiral shape) in a portion near the spray gun 7 in the hose 6. Or a coil spring-like member may be mounted. As a result, the flow of the carrier gas 9 sent from the hose 6 to the spray gun 7 is adjusted, the carrier gas 9 having a stable flow is supplied to the spray gun 7, and then the paint is discharged from the spray gun 7. Is stable.
 ここで、本発明ではスプレーガン7に供給されるキャリアガス9を加温することによってスプレーガン7からキャリアガス9と一緒に吹き出される塗料が所定の温度になるようにしているところ、ホース6自体を温めることにより、加温手段21によって温められたキャリアガス9の温度低下を抑制することができる。 Here, in the present invention, the carrier gas 9 supplied to the spray gun 7 is heated so that the paint blown out together with the carrier gas 9 from the spray gun 7 has a predetermined temperature. By heating itself, the temperature drop of the carrier gas 9 heated by the heating means 21 can be suppressed.
 そこで、本発明の塗装キャリアガスの制御装置は、加温ユニット20の筐体内に、ホース6が収容可能であるようにホース収容スペース24が確保されると共にホース6が巻き回されたり積層されたりする仕組みが備えられる。 Therefore, in the coating carrier gas control device of the present invention, the hose housing space 24 is secured in the casing of the heating unit 20 so that the hose 6 can be accommodated, and the hose 6 is wound or laminated. A mechanism to do this is provided.
 そして、加温ユニット20の筐体内の雰囲気を温めるため、筐体内に暖房手段23が備えられる。 And in order to warm the atmosphere in the housing | casing of the heating unit 20, the heating means 23 is provided in a housing | casing.
 暖房手段23による加温ユニット20の筐体内の暖房の設定温度は、特定の値に限定されるものではなく、例えばホース6を通過する間におけるキャリアガス9の温度低下を適切に抑制することなどが考慮された上で適正な値に適宜設定される。具体的には例えば、20~45 ℃ 程度の範囲に設定されることが好ましく、25~40 ℃ 程度の範囲に設定されることが更に好ましく、30~35 ℃ 程度の範囲に設定されることが最も好ましい。 The set temperature of heating in the casing of the heating unit 20 by the heating means 23 is not limited to a specific value, and for example, appropriately suppressing a temperature drop of the carrier gas 9 while passing through the hose 6. Is properly set to an appropriate value. Specifically, for example, it is preferably set in a range of about 20 to 45 ° C., more preferably in a range of about 25 to 40 ° C., and a range of about 30 to 35 ° C. Most preferred.
 暖房手段23は、特定の種類や仕様のものに限定されるものではなく、加温ユニット20の筐体内の雰囲気を上記温度まで温める働きをし得る適正な仕組みが適宜選択される。 The heating means 23 is not limited to a specific type or specification, and an appropriate mechanism capable of heating the atmosphere in the casing of the heating unit 20 to the above temperature is appropriately selected.
 暖房手段23としては、具体的には例えば、加温ユニット20の筐体内の容積に合わせて必要な熱量を筐体内雰囲気に対して供給し得る電気ヒータが用いられ得る。なお、この場合、筐体内雰囲気を攪拌しつつ熱を供給し得るようにファン付きの電気ヒータであることが好ましい。 As the heating means 23, specifically, for example, an electric heater that can supply a necessary amount of heat to the atmosphere in the casing in accordance with the volume in the casing of the heating unit 20 can be used. In this case, an electric heater with a fan is preferable so that heat can be supplied while stirring the atmosphere in the housing.
 なお、加温ユニット20の筐体内の雰囲気が適正温度(具体的には20~45 ℃ 程度の範囲)であることを外部から確認して塗装作業を適正時機に開始し得るようにするため、前記筐体内に挿し込まれた温度検知部と筐体の外部から視認可能な温度表示部とを有する温度計26が設けられるようにしても良い。 In order to ensure that the atmosphere in the casing of the heating unit 20 is at an appropriate temperature (specifically, in the range of about 20 to 45 ° C.), the painting operation can be started at an appropriate time. You may make it provide the thermometer 26 which has the temperature detection part inserted in the said housing | casing and the temperature display part visible from the exterior of a housing | casing.
 加温ユニット20の筐体内にホース6を収容することにより、暖房手段23によって温められた雰囲気によってホース6も温められる。したがって、加温されたキャリアガス9をホース6内を通過させることによって温める場合よりも短時間でホース6を温めることができ、塗装作業を迅速に行うことが可能になる。 By housing the hose 6 in the casing of the heating unit 20, the hose 6 is also warmed by the atmosphere warmed by the heating means 23. Therefore, the hose 6 can be warmed in a shorter time than the case where the heated carrier gas 9 is warmed by passing through the hose 6, and the painting operation can be performed quickly.
 また、塗装作業に必要な長さだけホース6を加温ユニット20の筐体内から引き出すようにすることにより、ホース6からの放熱を最小限に抑えることが可能なる。 In addition, by extracting the hose 6 from the casing of the heating unit 20 by a length necessary for the painting work, it is possible to minimize heat radiation from the hose 6.
 なお、ホース6内の加温状態のキャリアガス9の放熱による温度低下を防ぐため、ホース6が保温材・断熱材で覆われたり、ホース6として保温材・断熱材で形成されたホースが用いられたりすることが好ましい。 In addition, in order to prevent the temperature drop due to heat radiation of the heated carrier gas 9 in the hose 6, the hose 6 is covered with a heat insulating material / heat insulating material, or a hose formed of the heat insulating material / heat insulating material is used as the hose 6. It is preferable that
 また、加温ユニット20の筐体内の暖気雰囲気の放熱による温度低下を防ぐため、筐体が保温材・断熱材によって形成されたり、筐体の一部若しくは全体が保温材・断熱材で覆われたりすることが好ましい。 In addition, in order to prevent a temperature drop due to heat radiation of the warm air atmosphere in the casing of the heating unit 20, the casing is formed of a heat insulating material or a heat insulating material, or a part or the whole of the case is covered with a heat insulating material or a heat insulating material. Is preferable.
 また、ホース6端部のソケット8Aと結合すると共に加温ユニット20の筐体内に連通する排気口を備えるプラグ8B'が前記筐体を構成する側壁に取り付けられ、当該プラグ8B'にホース6端部のソケット8Aが結合させられることにより、ホース6から送出されるキャリアガス9が加温ユニット20の筐体内に導入されるようにしても良い。 Further, a plug 8B ′ having an exhaust port connected to the socket 8A at the end of the hose 6 and communicating with the inside of the casing of the heating unit 20 is attached to a side wall constituting the casing, and the end of the hose 6 is connected to the plug 8B ′. The carrier gas 9 delivered from the hose 6 may be introduced into the casing of the heating unit 20 by coupling the sockets 8 </ b> A.
 上記の構成により、加温手段21によって加温されてホース6へと送出されるキャリアガス9が前記ホース6を介して加温ユニット20の筐体内へと導入され得るようになり、暖房手段23のみによって温める場合よりも短時間で加温ユニット20の筐体内雰囲気を温めることができ、塗装作業を迅速に行うことが可能になる。 With the above configuration, the carrier gas 9 heated by the heating means 21 and delivered to the hose 6 can be introduced into the casing of the heating unit 20 via the hose 6. As a result, it is possible to warm the atmosphere in the casing of the heating unit 20 in a shorter time than when warming only by heating, and it is possible to perform the painting work quickly.
 なお、ホース6から送出されるキャリアガス9が加温ユニット20の筐体内に導入される場合には、当該筐体内の雰囲気の圧力が上昇することになるので、当該筐体内の雰囲気(ホース6から送出されたキャリアガス9を含む)を外部に放出する仕組みが備えられる。具体的には例えば、板状部材と当該板状部材の上端部に取り付けられた蝶番との組み合わせによる懸垂型揺動開閉自在のドア(例えばペットドアやキャットドアなどと呼ばれるものと同様の仕組みの小型のもの)が加温ユニット20の筐体を構成する側壁などの適正な場所に設置されることが考えられる。あくまで一例として付け加えると、加温ユニット20の筐体内からホース6を引き出すための開口が、当該筐体内の雰囲気を外部に放出するための仕組みを兼ねて構成されるようにしても良い。 In addition, when the carrier gas 9 delivered from the hose 6 is introduced into the casing of the heating unit 20, the atmosphere pressure in the casing rises, so the atmosphere in the casing (the hose 6) (Including the carrier gas 9 delivered from the outside) is provided. Specifically, for example, a suspension type swingable openable / closable door (for example, a pet door or a cat door) having a combination of a plate-like member and a hinge attached to the upper end of the plate-like member. It is conceivable that a small-sized one is installed in an appropriate place such as a side wall constituting the casing of the heating unit 20. As an example only, the opening for pulling out the hose 6 from the inside of the casing of the heating unit 20 may also be configured to serve as a mechanism for releasing the atmosphere in the casing to the outside.
 また、ホース6のスプレーガン7寄りの位置に(例えば、図1に示す例ではホース6端部のソケット8Aの近傍位置に)、当該ホース6から分岐する器具が更に設けられ(図1では図示していない)、当該分岐器具からスプレーガン7の本体や塗料カップ7aなどの表面に向けて加温されたキャリアガス9が吹き出されるように構成されても良い。 Further, an instrument branching from the hose 6 is further provided at a position near the spray gun 7 of the hose 6 (for example, in the vicinity of the socket 8A at the end of the hose 6 in the example shown in FIG. 1) (FIG. (Not shown), the carrier gas 9 heated toward the surface of the main body of the spray gun 7 or the paint cup 7a may be blown out from the branch device.
 ホース6から分岐する器具としては、具体的には例えば、一口である一方の端部と二股に分かれて二口になっている他方の端部とを有するY字形の分岐管やチューブ(この場合、前記一方の端部はホース6と接続され、前記他方の端部の片方はスプレーガン7と接続され、もう片方からキャリアガス9が吹き出される)が用いられたり、前記Y字形の分岐管と一本のチューブとの組み合わせが用いられたりされ得る。 Specifically, the device branched from the hose 6 is, for example, a Y-shaped branch pipe or tube having one end which is a single mouth and the other end which is bifurcated and has two ends (in this case) The one end is connected to the hose 6, one end of the other end is connected to the spray gun 7, and the carrier gas 9 is blown from the other end) or the Y-shaped branch pipe Or a single tube combination may be used.
 上述の分岐器具が用いられる場合には、さらに、スプレーガン7の本体や塗料カップ7aなどの周囲に、これらとの間に適正な空間(隙間)が確保された上でカバーが設けられ、当該カバー内に加温されたキャリアガス9が吹き出されて滞留し得るようにしても良い。 When the above-described branching device is used, a cover is further provided around the body of the spray gun 7 or the paint cup 7a after an appropriate space (gap) is secured between them. The heated carrier gas 9 may be blown out and stay in the cover.
 これにより、スプレーガン7の本体や塗料カップ7a及び当該塗料カップ7a内の塗料が温められると共に塗装作業の間に亙って保温され、特に塗装現場の気温が低い場合であっても、塗料の温度管理が容易になり、延いてはスプレーガン7から吹き出される塗料の温度が適正範囲に維持されるようにすることが可能になる。 As a result, the main body of the spray gun 7, the paint cup 7a and the paint in the paint cup 7a are warmed and kept warm during the painting work, and even when the temperature at the painting site is low, Temperature management becomes easy, and it becomes possible to maintain the temperature of the paint blown out from the spray gun 7 in an appropriate range.
 また、本発明の塗装キャリアガスの制御装置は、塗装手段7に供給される塗料を収容すると共に加温ユニット20の筐体内の雰囲気を利用して塗料を塗装作業前に温めるための塗料加温部25を更に有するようにしても良い。 In addition, the coating carrier gas control device of the present invention accommodates the coating material supplied to the coating means 7 and uses the atmosphere in the casing of the heating unit 20 to warm the coating material before the coating operation. You may make it have the part 25 further.
 本実施形態では、具体的には、スプレーガン7に供給される塗料が入れられた塗料カップ7a'を収容すると共に加温ユニット20の筐体内の暖気雰囲気を利用し、塗料カップ7a'に入れられた塗料を塗装作業前に温めるための塗料加温部25が設けられる。 Specifically, in the present embodiment, the paint cup 7a ′ containing the paint to be supplied to the spray gun 7 is accommodated, and the warm air atmosphere in the casing of the heating unit 20 is used to put the paint cup 7a ′. A paint heating unit 25 is provided for heating the applied paint before the painting operation.
 塗料加温部25は、加温ユニット20の筐体の側面や上面に隣接して設けられるようにしても良いし、加温ユニット20の筐体内に設けられるようにしても良いし、或いは、加温ユニット20の筐体とは別個に設けられるようにしても良い。 The paint heating unit 25 may be provided adjacent to the side surface or the upper surface of the casing of the heating unit 20, or may be provided within the casing of the heating unit 20, or You may make it provide separately from the housing | casing of the heating unit 20. FIG.
 塗料加温部25は、加温ユニット20の筐体の側面や上面に隣接して設けられる場合には(図1に示す例は、この場合に対応するイメージである)、前記筐体の側板や天板に対して取り付けられる(このとき、これら側板や天板を自身の一面として利用する)と共に、側面と上面とのうちのいずれか一面に開閉自在の扉を備える箱体として構成されることが考えられる。 When the paint heating unit 25 is provided adjacent to the side or upper surface of the casing of the heating unit 20 (the example shown in FIG. 1 is an image corresponding to this case), the side plate of the casing It is attached to the top plate and the top plate (At this time, these side plates and the top plate are used as one surface), and is configured as a box having a door that can be opened and closed on either the side surface or the top surface. It is possible.
 この場合には、加温ユニット20の筐体内の空間と塗料加温部25としての箱体内の空間とが連通して前記筐体内の暖気雰囲気が進入し得るように、筐体の側板や天板の、箱体が取り付けられた位置に、ガラリや貫通孔などの通気のための構造(図1の符号25a)が設けられる。なお、この場合、塗料加温部25としての箱体を構成する部材として保温材・断熱材が用いられたり、前記箱体の一部若しくは全体が保温材・断熱材で覆われたりすることが好ましい。 In this case, the side plate and the ceiling of the casing are arranged so that the space in the casing of the heating unit 20 communicates with the space in the box as the paint heating section 25 so that the warm atmosphere in the casing can enter. A structure (reference numeral 25a in FIG. 1) for ventilation such as a louver or a through hole is provided at a position of the plate where the box is attached. In this case, a heat insulating material / heat insulating material may be used as a member constituting the box as the paint heating unit 25, or a part or the whole of the box may be covered with the heat insulating material / heat insulating material. preferable.
 また、塗料加温部25は、加温ユニット20の筐体内に設けられる場合には、前記筐体内の空間が仕切られた一部区画として構成されることが考えられる。この場合には、前記筐体内の暖気雰囲気が塗料加温部25としての区画に進入し得るように、前記区画を構成する仕切り部材に、ガラリや貫通孔などの通気のための構造が設けられる。また、塗料加温部25としての区画に繋がる開閉自在の扉が、加温ユニット20の筐体の側板や天板の一部に設けられる。 Further, when the paint heating unit 25 is provided in the casing of the heating unit 20, it is conceivable that the paint heating unit 25 is configured as a partial section in which the space in the casing is partitioned. In this case, a structure for ventilation such as a louver or a through hole is provided in the partition member constituting the compartment so that the warm atmosphere in the casing can enter the compartment as the paint heating unit 25. . In addition, an openable / closable door connected to the section as the paint heating unit 25 is provided on a side plate or a part of the top plate of the casing of the heating unit 20.
 また、塗料加温部25は、加温ユニット20の筐体とは別個に設けられる場合には、開閉自在の扉を備える独立した箱体として構成されることが考えられる。この場合には、加温ユニット20の筐体内の空間と塗料加温部25としての箱体内の空間とに両端部がそれぞれ連通するチューブによってこれら筐体及び箱体が接続され、筐体内の暖気雰囲気が箱体内に導入される。 Further, when the paint heating unit 25 is provided separately from the casing of the heating unit 20, it is conceivable that the paint heating unit 25 is configured as an independent box having an openable / closable door. In this case, the casing and the box are connected to the space in the casing of the heating unit 20 and the space in the box as the paint heating unit 25 by the tubes communicating at both ends, respectively. An atmosphere is introduced into the box.
 なお、この場合、塗料加温部25としての箱体を構成する部材として保温材・断熱材が用いられたり、前記箱体の一部若しくは全体が保温材・断熱材で覆われたりすることが好ましく、また、前記チューブが保温材・断熱材で覆われたり、前記チューブとして保温材・断熱材で形成されたホースが用いられたりすることが好ましい。 In this case, a heat insulating material / heat insulating material may be used as a member constituting the box as the paint heating unit 25, or a part or the whole of the box may be covered with the heat insulating material / heat insulating material. Preferably, the tube is covered with a heat insulating material / heat insulating material, or a hose formed of a heat insulating material / heat insulating material is used as the tube.
 塗料加温部25によって塗装作業前に塗料カップ7a'と共に塗料を温めておくことにより、キャリアガス9がたとえ加温されていてもキャリアガス9と一緒に吹き出される塗料の温度が低いためにスプレーガン7から吹き出される際の塗料の温度が低下してしまうことが防止され、塗料の温度管理が容易になり、延いては吹き出される塗料の温度が適正範囲に維持されるようにすることが可能になる。 By heating the paint together with the paint cup 7a ′ by the paint heating unit 25 before the painting operation, the temperature of the paint blown out together with the carrier gas 9 is low even if the carrier gas 9 is heated. It is prevented that the temperature of the paint when it is blown out from the spray gun 7 is lowered, the temperature management of the paint is facilitated, and the temperature of the paint to be blown out is maintained within an appropriate range. It becomes possible.
 なお、塗料加温部25には、塗料カップ7a'に入れられた状態の塗料ではなく、他の容器に入れられた状態の塗料が収容されるようにしても良い。 Note that the paint heating unit 25 may store the paint in a state other than the paint put in the paint cup 7a ′.
 上述した気流調整ユニット10と貯留ユニット4と加温ユニット20とは、これらユニット毎に若しくは任意の複数のユニットが組み合わされた上で、据え置かれて設置される固定型であるようにしても良く、また、移動手段が備えられる可動型であるようにしても良い。可動型の場合には、ユニット毎に、若しくは、複数のユニットの組み合わせ毎に、移動可能の構成となり、現場状況に応じた装置の設置が可能になる。 The airflow adjustment unit 10, the storage unit 4, and the heating unit 20 described above may be a fixed type that is installed and installed for each unit or after a plurality of arbitrary units are combined. Further, it may be a movable type provided with a moving means. In the case of a movable type, it becomes a structure which can move for every unit or for every combination of a some unit, and installation of the apparatus according to the field condition is attained.
 ユニットを可動型にするための移動手段としては、具体的には例えば、ユニットが載置される台座と当該台座の下側に設けられた車輪とを備える台車や、ユニットが載置される台座と当該台座の下側に設けられた車輪と当該車輪が係合するレールとを有する仕組みなどが挙げられる。 Specifically, as the moving means for making the unit movable, for example, a carriage including a pedestal on which the unit is placed and a wheel provided on the lower side of the pedestal, or a pedestal on which the unit is placed And a mechanism having a wheel provided below the pedestal and a rail with which the wheel engages.
 また、加温ユニット20の筐体内にホース収容スペース24が確保されてホース6が収容されるようにしていることに関連し、塗装作業時には加温ユニット20の筐体内からホース6を引き出すことにより、スプレーガン7による塗装の現場の爆発性雰囲気から離れた安全なエリア(即ち、非爆発性雰囲気であるエリア)に加温ユニット20(及び他のユニット)を設置することが可能になる。したがって、加温ユニット20(及び他のユニット)を防爆機器としての基準を満たす構造とする必要がなく、且つ、安全性の確保が図られる。そして、上記のように加温ユニット20(及び他のユニット)に移動手段が備えられることにより、塗装作業の工程による塗装場所(塗装の現場)の移動に合わせての加温ユニット20(及び他のユニット)の移動・設置を容易に行うことが可能になる。 Further, in connection with the fact that the hose housing space 24 is secured in the housing of the heating unit 20 and the hose 6 is housed, the hose 6 is pulled out from the housing of the heating unit 20 during painting work. The heating unit 20 (and other units) can be installed in a safe area away from the explosive atmosphere at the site of painting by the spray gun 7 (that is, an area having a non-explosive atmosphere). Therefore, it is not necessary to make the heating unit 20 (and other units) have a structure that satisfies the standard as an explosion-proof device, and safety can be ensured. Further, as described above, the heating unit 20 (and other units) is provided with the moving means, so that the heating unit 20 (and other units) according to the movement of the painting place (painting site) by the painting work process. The unit can be easily moved and installed.
 上述した塗装キャリアガスの制御装置によれば、キャリアガス9が、気流調整ユニット10によって清浄化されると共にドライ化され、さらに、貯留ユニット4において加圧状態で一時貯蔵されることによって流動性が安定して平滑な圧力で送出され、加えて、加温ユニット20によって加温された上で、スプレーガン7に供給される。 According to the coating carrier gas control device described above, the carrier gas 9 is cleaned and dried by the airflow adjusting unit 10, and further fluidized by being temporarily stored in a pressurized state in the storage unit 4. It is delivered at a stable and smooth pressure, and is heated by the heating unit 20 and then supplied to the spray gun 7.
 このとき、液体塗料(溶剤塗料)の場合には、加温手段21の温度や圧力調整手段16の送出圧力が調節されることにより、スプレーガン7における塗料の霧化温度が20~30 ℃ 程度の範囲であると共にスプレーガン7のノズルからの吹き出し圧力が0.15~0.20 MPa 程度の範囲であることが好ましく、塗料の霧化温度が23~27 ℃ 程度の範囲であると共に吹き出し圧力が0.165~0.185 MPa 程度の範囲であることが更に好ましく、塗料の霧化温度が25 ℃ 程度であると共に吹き出し圧力が0.170~0.180 MPa 程度の範囲であることが最も好ましい。 At this time, in the case of a liquid paint (solvent paint), the atomization temperature of the paint in the spray gun 7 is about 20 to 30 ° C. by adjusting the temperature of the heating means 21 and the delivery pressure of the pressure adjusting means 16. The spray pressure from the nozzle of the spray gun 7 is preferably in the range of about 0.15 to 0.20 MPa, and the atomization temperature of the paint is in the range of about 23 to 27 ° C and the blowout pressure. Is more preferably in the range of about 0.165 to 0.185 MPa, most preferably the atomization temperature of the paint is about 25 ° C and the blowing pressure is in the range of about 0.170 to 0.180 MPa. preferable.
 また、粉体塗料の場合には、スプレーガン7のノズルからの吹き出し圧力が0.050~0.10 MPa 程度の範囲であることが好ましく、吹き出し圧力が0.065~0.085 MPa 程度の範囲であることが更に好ましく、吹き出し圧力が0.07~0.08 MPa 程度の範囲であることが最も好ましい。 In the case of a powder paint, it is preferable that the blowing pressure from the nozzle of the spray gun 7 is in the range of about 0.050 to 0.10 MPa, and the blowing pressure is about 0.065 to 0.085 MPa. More preferably, the blowing pressure is in the range of about 0.07 to 0.08 kgpa.
 上述の構成を有する塗装キャリアガスの制御装置によれば、夾雑物のない清浄なキャリアガス9を確保することができ、さらに、季節や作業環境に拘わらずキャリアガス9の温度を適正範囲に保つことができると共に湿度を適正範囲に保つ(言い換えると、キャリアガス9のドライ化を適切に達成する)ことができ、加えて、キャリアガス9の吹き出し圧力を適正範囲に保つことができる。すなわち、キャリアガス9の温度,湿度,及び圧力という三要素を一体として適切な状態に管理・制御することができる。このため、温度や湿度を制御していないためにキャリアガス9の圧力が高めの設定になってしまう従来の吹き付け塗装方式と比べ、塗料及び希釈剤の使用量を低減させ、塗装現場の作業環境を改善すると共に、揮発性有機化合物の拡散を抑制することが可能になる。さらに、キャリアガス9と一緒にスプレーガン7から吹き出される塗料を吹き出しによる塗装に適した良好な状態にし、吹き付け塗装の仕上がりの品質を向上させることが可能になる。 According to the coating carrier gas control device having the above-described configuration, it is possible to ensure a clean carrier gas 9 free from contaminants, and to keep the temperature of the carrier gas 9 within an appropriate range regardless of the season and working environment. In addition, the humidity can be maintained within an appropriate range (in other words, the carrier gas 9 can be appropriately dried), and in addition, the blowing pressure of the carrier gas 9 can be maintained within the appropriate range. That is, the three elements of the temperature, humidity, and pressure of the carrier gas 9 can be managed and controlled in an appropriate state. For this reason, compared with the conventional spray coating method in which the pressure of the carrier gas 9 is set higher because the temperature and humidity are not controlled, the amount of paint and diluent used is reduced, and the working environment at the painting site is reduced. And the diffusion of volatile organic compounds can be suppressed. Furthermore, the paint blown out from the spray gun 7 together with the carrier gas 9 can be made into a good state suitable for painting by blowing, and the quality of the finish of spray painting can be improved.
 なお、上述の形態は本発明を実施する際の好適な形態の一例ではあるものの本発明の実施の形態が上述のものに限定されるものではなく、本発明の要旨を逸脱しない範囲において本発明は種々変形実施可能である。 Although the above-described embodiment is an example of a preferred embodiment for carrying out the present invention, the embodiment of the present invention is not limited to the above-described embodiment, and the present invention is not deviated from the gist of the present invention. Various modifications can be made.
 例えば、上述の実施形態ではキャリアガス9が供給される塗装手段7が手吹きスプレーガンである場合を例に挙げているが、本発明が適用され得る塗装手段は手吹きスプレーガンに限定されるものではなく、キャリアガス9の圧力によって塗料が吹き出される(言い換えると、噴霧・吐出される)種々の塗装手段と組み合わせて本発明は広く適用可能である。具体的には例えば、キャリアガス9が供給される塗装手段が、塗装キャリアガスと一緒に塗料が吹き出される仕組みを備える自動化の塗装モジュールである場合にも本発明は適用され得る。 For example, in the above-described embodiment, the case where the coating means 7 to which the carrier gas 9 is supplied is a hand-blown spray gun, but the painting means to which the present invention can be applied is limited to the hand-blown spray gun. The present invention can be widely applied in combination with various coating means in which paint is blown out by the pressure of the carrier gas 9 (in other words, sprayed / discharged). Specifically, for example, the present invention can also be applied when the coating means to which the carrier gas 9 is supplied is an automated coating module having a mechanism in which the coating material is blown out together with the coating carrier gas.
 また、上述の実施形態では希釈剤・溶剤などによって適宜の濃度に調製されて塗料カップ7aに入れられた液体塗料が吹き出されるようにしているが、本発明が適用され得る塗料は液体塗料に限定されるものではなく、粉体塗料が塗装手段から吹き出される場合の当該塗装手段に供給される塗装キャリアガスの制御装置としても本発明は適用され得る。 In the above-described embodiment, the liquid paint prepared in an appropriate concentration by the diluent / solvent and put in the paint cup 7a is blown out. However, the paint to which the present invention can be applied is a liquid paint. The present invention is not limited, and the present invention can also be applied as a control device for the coating carrier gas supplied to the coating means when the powder paint is blown out from the coating means.
 また、上述の実施形態では貯留ユニット4の上流側に一次清浄手段12及び気水分離手段13が配設されると共に下流側に二次清浄手段14及び除湿乾燥手段15が配設されるようにしているが、これら手段12,13,14,15の配設の有無(言い換えると、気流調整ユニット10の清浄処理機構とドライ化機構との構成)は上述の実施形態におけるものには限られない。すなわち、気流調整ユニット10は、キャリアガス9を、貯留ユニット4に貯留するに際して必要とされる程度に清浄化したりドライ化(脱水)したりすると共に、スプレーガン7に供給するに際して必要とされる程度に清浄化したりドライ化(除湿,乾燥)したりするものであり、このような清浄化やドライ化が達成されるのであれば前記手段12,13,14,15の配設の有無は適宜調整され得る。具体的には例えば、ガス供給源ユニット1としてエアコンプレッサが用いられる場合に当該エアコンプレッサに導入される雰囲気が一定程度清浄であったり湿度管理されていたりする場合には一次清浄手段12及び二次清浄手段14や気水分離手段13は配設されないようにしても良く、また、ガス供給源ユニット1としてガスボンベが利用される場合に当該ガスボンベに充填されているガスが清浄性や湿度について一定条件を満たしている場合にも一次清浄手段12及び二次清浄手段14や気水分離手段13は配設されないようにしても良い。したがって、気流調整ユニット10の清浄処理機構は二次清浄手段14のみから構成されるようにしても良く、更に言えば気流調整ユニット10が清浄処理機構を有しないようにしても良く、また、ドライ化機構は除湿乾燥手段15のみから構成されるようにしても良い。 In the above-described embodiment, the primary cleaning means 12 and the steam / water separation means 13 are disposed on the upstream side of the storage unit 4, and the secondary cleaning means 14 and the dehumidifying and drying means 15 are disposed on the downstream side. However, the presence or absence of these means 12, 13, 14, and 15 (in other words, the configuration of the cleaning processing mechanism and the drying mechanism of the airflow adjustment unit 10) is not limited to that in the above-described embodiment. . In other words, the airflow adjustment unit 10 is required to clean or dry (dehydrate) the carrier gas 9 to the extent required when storing the carrier gas 9 in the storage unit 4 and to supply the carrier gas 9 to the spray gun 7. As long as such cleaning or drying is achieved, the presence of the means 12, 13, 14, 15 is appropriately determined. Can be adjusted. Specifically, for example, when an air compressor is used as the gas supply source unit 1, when the atmosphere introduced into the air compressor is clean to a certain extent or humidity is controlled, the primary cleaning means 12 and the secondary cleaning means 12 The cleaning means 14 and the air / water separation means 13 may not be disposed, and when a gas cylinder is used as the gas supply source unit 1, the gas filled in the gas cylinder has a certain condition regarding cleanliness and humidity. Even when the above conditions are satisfied, the primary cleaning means 12, the secondary cleaning means 14, and the steam-water separation means 13 may not be provided. Therefore, the cleaning processing mechanism of the airflow adjustment unit 10 may be configured only by the secondary cleaning means 14, and more specifically, the airflow adjustment unit 10 may not have the cleaning processing mechanism, The adjusting mechanism may be composed of only the dehumidifying and drying means 15.
 また、上述の実施形態では貯留ユニット4の上流側に一次清浄手段12及び気水分離手段13が配設されると共に下流側に二次清浄手段14及び除湿乾燥手段15が配設される(言い換えると、貯留ユニット4の上流側と下流側との両方に清浄処理機構及びドライ化機構が配設される)ようにしているが、これら手段12,13,14,15の貯留ユニット4との関係における配設位置は上述の実施形態におけるものには限られない。具体的には、二次清浄手段14と除湿乾燥手段15とのうちの一方若しくは両方が、貯留ユニット4の上流側に配設されるようにしても良い。したがって、気流調整ユニット10の清浄処理機構やドライ化機構は、貯留ユニット4の上流側のみに配設されるようにしても良い。なお、貯留ユニット4の上流側に一次清浄手段12や気水分離手段13が配設されている場合には、これら手段12,13と貯留ユニット4との間に二次清浄手段14や除湿乾燥手段15が配設されるようにする。 In the above-described embodiment, the primary cleaning means 12 and the steam-water separation means 13 are disposed on the upstream side of the storage unit 4, and the secondary cleaning means 14 and the dehumidifying and drying means 15 are disposed on the downstream side (in other words, in other words). And a cleaning mechanism and a drying mechanism are arranged on both the upstream side and the downstream side of the storage unit 4), but the relationship of these means 12, 13, 14, 15 with the storage unit 4. The arrangement position is not limited to that in the above-described embodiment. Specifically, one or both of the secondary cleaning unit 14 and the dehumidifying / drying unit 15 may be arranged on the upstream side of the storage unit 4. Therefore, the cleaning mechanism and the drying mechanism of the airflow adjustment unit 10 may be disposed only on the upstream side of the storage unit 4. When the primary cleaning means 12 and the air / water separation means 13 are disposed upstream of the storage unit 4, the secondary cleaning means 14 and dehumidifying and drying are provided between these means 12 and 13 and the storage unit 4. Means 15 are arranged.
 また、上述の実施形態では貯留ユニット4を有するようにしているが、貯留ユニット4を有しないようにしても良い。すなわち、貯留ユニット4によるキャリアガス9の一時貯蔵が行われなくても、少なくとも、キャリアガス9の、除湿乾燥手段15によるドライ化,圧力調整手段16による圧力調整,及び加温手段21による加温と、ホース収容スペース24を含む加温ユニット20の筐体内の雰囲気の、暖房手段23による加温とが行われることにより、塗料及び希釈剤の使用量の低減という本発明の効果は発揮され得る。 In the above-described embodiment, the storage unit 4 is provided, but the storage unit 4 may not be provided. In other words, even if the carrier gas 9 is not temporarily stored by the storage unit 4, at least the carrier gas 9 is dried by the dehumidifying and drying means 15, the pressure is adjusted by the pressure adjusting means 16, and the heating by the heating means 21. And, by heating the atmosphere in the casing of the heating unit 20 including the hose housing space 24 by the heating means 23, the effect of the present invention of reducing the amount of paint and diluent used can be exhibited. .
 本発明の塗装キャリアガスの制御装置による塗料及び希釈剤の使用量の低減効果の検証例を図2を用いて説明する。 A verification example of the effect of reducing the amount of paint and diluent used by the coating carrier gas control device of the present invention will be described with reference to FIG.
 本実施例では、スプレーガン(カップガン)を用いてのオペレータによる手吹き塗装(ハンド塗装)が行われた。なお、オペレータは、手吹き塗装に関して十分な経験を有し、塗装条件の違いに適応して当該塗装条件における適切な塗装作業を行い得る者であった。 In this example, hand spray painting (hand painting) by an operator using a spray gun (cup gun) was performed. The operator is a person who has sufficient experience with hand-blown painting and can perform appropriate painting work under the painting conditions in accordance with the difference in painting conditions.
 なお、本実施例では、関西ペイント社製の「PG80」(ウレタン系:主剤/硬化剤=10/1配合)の赤色(PG80III無鉛E05-40Xレッド)の塗料が用いられた。 In this example, a red (PG80III lead-free E05-40X red) paint of “PG80” (urethane type: main agent / curing agent = 10/1 blend) manufactured by Kansai Paint Co., Ltd. was used.
 本実施例では、まず、本発明に係る実施例と対比させるための比較例1として、従来の吹き付け塗装方式であり、エアコンプレッサから送出される圧縮空気を、そのまま、スプレーガンに供給されるキャリアガスとして使用した場合の塗装が行われた。 In this embodiment, first, as a comparative example 1 for comparison with the embodiment according to the present invention, it is a conventional spray coating system, and the compressed air sent from the air compressor is directly supplied to the spray gun. When used as a gas, it was painted.
 比較例1については、スプレーガンからのキャリアガス及び塗料等の吐出の圧力(塗装圧)が、従来の標準的な塗装圧である0.250 MPa 程度に調節された場合(比較例1-1)と、標準よりも低圧の0.175 MPa 程度に調節された場合(比較例1-2)との二つのケースについて行われた。 For Comparative Example 1, when the discharge pressure (coating pressure) of the carrier gas and paint from the spray gun was adjusted to about 0.250 MPa, which is the conventional standard coating pressure (Comparative Example 1-1) ) And the case where the pressure was adjusted to about 0.175 MPa lower than the standard (Comparative Example 1-2).
 溶剤による塗料の希釈率(即ち、塗料の重量に対する溶剤の重量の割合)は、比較例1-1と比較例1-2とのどちらも、本実施例で用いられた塗料についての標準的な希釈率である70 % に設定された。 The dilution ratio of the paint with the solvent (that is, the ratio of the weight of the solvent to the weight of the paint) is the standard for the paint used in this example in both Comparative Example 1-1 and Comparative Example 1-2. The dilution rate was set to 70 %%.
 一方、本発明に係る実施例1として、エアコンプレッサから送出される圧縮空気を、本発明の塗装キャリアガスの制御装置によって処理してから、スプレーガンに供給されるキャリアガスとして使用した場合の塗装が行われた。本発明としての塗装キャリアガスの制御装置の構成は、図1に示す例と同様のものとされた。 On the other hand, as Example 1 according to the present invention, the compressed air delivered from the air compressor is processed by the coating carrier gas control device of the present invention and then used as the carrier gas supplied to the spray gun. Was done. The configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
 本発明に係る実施例1については、溶剤による塗料の希釈率が、比較例1と同じ70 % に設定された場合(実施例1-1)と、比較例1の半分の35 % に設定された場合(つまり、塗料の粘度が高い;実施例1-2)との二つのケースについて行われた。 For Example 1 according to the present invention, when the dilution ratio of the paint with the solvent is set to 70% by weight, which is the same as Comparative Example 1 (Example 1-1), it is set to 35% by weight, which is half of Comparative Example 1. In two cases (ie, the viscosity of the paint is high; Example 1-2).
 塗装圧は、実施例1-1と実施例1-2とのどちらも、標準よりも低圧の0.175 MPa に設定された。 The coating pressure for both Example 1-1 and Example 1-2 was set at 0.175 MPa MPa, which is lower than the standard pressure.
 また、実施例1-1及び実施例1-2では、ホース6端部のソケット8Aから吹き出されるキャリアガス9の温度は、計測の結果、25~30 ℃ であった。 In Example 1-1 and Example 1-2, the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
 本実施例では、コート数(即ち、塗料の塗り重ね回数)は4回が基本とされた。しかしながら、比較例1-2については、塗装圧が低圧であることによって吹き出される塗料の量が極端に少なく、コート数が4回では仕上がりの品質の確保ができなかったために5回とされた。それでも、比較例1-2については、仕上がりが不良であった(言い換えると、実施例1-1の従来塗装と同等の仕上がりは達成されなかった)。 In this example, the number of coats (that is, the number of times the paint was applied) was basically four. However, for Comparative Example 1-2, the amount of paint blown out due to the low coating pressure was extremely small, and the quality of the finished product could not be ensured when the number of coats was four, so the number was five. . Nevertheless, the finish of Comparative Example 1-2 was poor (in other words, a finish equivalent to that of the conventional coating of Example 1-1 was not achieved).
 一方、本発明に係る実施例1-1及び実施例1-2については、塗装圧が標準よりも低圧であるにも拘わらず、加えて実施例1-2では希釈率が小さく塗料の粘度が高いにも拘わらず、仕上がりは良好であった(言い換えると、実施例1-1の従来塗装と少なくとも同等の仕上がりが達成された)。 On the other hand, in Examples 1-1 and 1-2 according to the present invention, although the coating pressure was lower than the standard, in addition, in Example 1-2, the dilution rate was small and the viscosity of the paint was low. Despite being high, the finish was good (in other words, a finish at least equivalent to the conventional coating of Example 1-1 was achieved).
 また、従来の標準的な塗装条件である比較例1-1の塗料の使用量を基準としたときの、塗料使用量の削減率は、実施例1-1では塗装圧が低圧である結果として29 % になり、実施例1-2では塗装圧が低圧であり且つ希釈率が小さい結果として43 % になった。 In addition, the reduction rate of the amount of paint used based on the amount of paint used in Comparative Example 1-1, which is a conventional standard coating condition, is the result of the coating pressure being low in Example 1-1. In Example 1-2, the coating pressure was low and the dilution rate was small, resulting in 43 %%%.
 なお、塗装圧が低圧である場合には、塗装の対象表面に向けて吹き出された塗料のうち、前記対象表面に衝突したキャリアガスによる気流の乱れによって前記対象表面に到達する前に吹き払われてしまう塗料が減少するので、前記対象表面に実際に定着する分が増えて拡散する分が減ると考えられた。すなわち、スプレーガンから吹き出される塗料の全量に対する塗膜として定着する量の割合が増加するために塗料使用量が減少すると考えられた。 When the coating pressure is low, the paint blown toward the target surface of the paint is blown off before reaching the target surface due to the turbulence of the airflow caused by the carrier gas that has collided with the target surface. Therefore, it is considered that the amount of the paint actually fixed on the target surface increases and the amount of diffusion decreases. That is, it was considered that the amount of paint used decreased because the ratio of the amount fixed as a coating film to the total amount of paint blown from the spray gun increased.
 以上の結果から、本発明の塗装キャリアガスの制御装置によれば、従来の吹き付け塗装方式と比べ、塗装圧を低減させても良好な仕上がりを確保することが可能であり、且つ、溶剤による希釈率を小さくして塗料の粘度が高い場合に塗装圧を低減させても良好な仕上がりを確保することが可能であることが確認された。 From the above results, according to the coating carrier gas control device of the present invention, it is possible to ensure a good finish even if the coating pressure is reduced, as compared with the conventional spray coating method, and dilution with a solvent. It was confirmed that it was possible to ensure a good finish even if the coating pressure was reduced when the rate was reduced and the viscosity of the paint was high.
 以上の結果から、また、従来の標準的な塗装条件の場合と少なくとも同等の仕上がりを確保するために必要とされる塗料及び希釈剤の使用量を30~40 % 程度削減することが可能であることが確認された。 From the above results, it is also possible to reduce the amount of paint and diluent used to ensure at least the same finish as in the case of conventional standard coating conditions by 30 to 40%. It was confirmed.
 本発明の塗装キャリアガスの制御装置による塗料及び希釈剤の使用量の低減効果の他の検証例を図3を用いて説明する。 Another verification example of the effect of reducing the amount of paint and diluent used by the coating carrier gas control device of the present invention will be described with reference to FIG.
 本実施例では、ロボットによる自動塗装が行われた。 In this example, automatic painting by a robot was performed.
 なお、本実施例でも、上述の実施例1と同様の塗料が用いられた。 In this example, the same paint as in Example 1 was used.
 本実施例では、まず、本発明に係る実施例と対比させるための比較例2として、従来の吹き付け塗装方式であり、エアコンプレッサから送出される圧縮空気を、そのまま、ロボットの塗装モジュールに供給されるキャリアガスとして使用した場合の塗装が行われた。 In this embodiment, first, as a comparative example 2 for comparison with the embodiment according to the present invention, a conventional spray painting system is used, and compressed air sent from an air compressor is supplied as it is to a painting module of a robot. When used as a carrier gas, it was painted.
 比較例2については、溶剤による塗料の希釈率が本実施例で用いられた塗料についての標準的な希釈率である70 % に設定されると共に、ロボットの塗装モジュールからのキャリアガス及び塗料等の吐出の圧力(塗装圧)が従来の標準的な塗装圧である0.250 MPa に設定された。 For Comparative Example 2, the dilution ratio of the paint with the solvent is set to 70% by weight, which is the standard dilution ratio for the paint used in this example, and the carrier gas, paint, etc. from the paint module of the robot The discharge pressure (painting pressure) was set to 0.250 kgpa, which is a conventional standard painting pressure.
 一方、本発明に係る実施例2として、エアコンプレッサから送出される圧縮空気を、本発明の塗装キャリアガスの制御装置によって処理してから、ロボットの塗装モジュールに供給されるキャリアガスとして使用した場合の塗装が行われた。本発明としての塗装キャリアガスの制御装置の構成は、図1に示す例と同様のものとされた。 On the other hand, as Example 2 according to the present invention, when compressed air delivered from an air compressor is processed by the coating carrier gas control device of the present invention and then used as a carrier gas supplied to a robot coating module Painting was done. The configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
 本発明に係る実施例2については、溶剤による塗料の希釈率が比較例2よりも小さい50 % に設定されると共に、塗装圧が標準よりも低圧の0.175 MPa に設定された。 For Example 2 according to the present invention, the dilution ratio of the paint with the solvent was set to 50% by weight, which is smaller than that of Comparative Example 2, and the coating pressure was set to 0.175% MPa, which is lower than the standard.
 また、実施例2では、ホース6端部のソケット8Aから吹き出されるキャリアガス9の温度は、計測の結果、25~30 ℃ であった。 In Example 2, the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
 上述の条件のもと、塗料の使用量を同じにしてコート数を2回とした塗装を行い、比較例2の場合と実施例2の場合とのそれぞれの塗装の膜厚が計測された。なお、比較例2と実施例2とのどちらも塗装の仕上がりは良好であった。 Under the above-mentioned conditions, coating was performed with the same amount of paint used and the number of coatings being twice, and the film thickness of each coating in the case of Comparative Example 2 and Example 2 was measured. In both Comparative Example 2 and Example 2, the finish of the coating was good.
 塗装の膜厚の計測の結果、比較例2は19.8 μm であるのに対して実施例2は28.7 μm であり、比較例2に対して実施例2では膜厚が45 % 増加した。 As a result of measuring the film thickness of the coating, Comparative Example 2 is 19.8 μm, while Example 2 is 28.7 μm, and in Example 2, the film thickness is increased by 45% by did.
 また、実施例2の実績に基づいて試算すると、実施例2の条件で比較例2と同じ19.8 μm の膜厚の塗装をする場合には、比較例2に対して塗料の使用量が31 % 削減されることが分かった。 Further, when a trial calculation is made based on the results of Example 2, the amount of paint used for Comparative Example 2 is less than that of Comparative Example 2 when coating with the same film thickness of 19.8 μm as in Comparative Example 2 under the conditions of Example 2. It was found that it was reduced by 31%.
 以上の結果から、本発明の塗装キャリアガスの制御装置によれば、塗料の使用量が同じである場合には、従来の吹き付け塗装方式と比べ、塗装の膜厚を45 % 程度増加させることが可能であることが確認された。すなわち、言い換えると、本発明によれば、塗装の膜厚を同じにするために必要とされる塗料及び希釈剤の使用量を、従来の吹き付け塗装方式と比べ、削減することが可能であることが確認された。 From the above results, according to the coating carrier gas control device of the present invention, when the amount of paint used is the same, the coating film thickness can be increased by about 45% compared with the conventional spray coating method. It was confirmed that it was possible. That is, in other words, according to the present invention, it is possible to reduce the amount of paint and diluent used to make the coating film thickness the same as compared with the conventional spray coating method. Was confirmed.
 本発明の塗装キャリアガスの制御装置による塗料及び希釈剤の使用量の低減効果の更に他の検証例を図4を用いて説明する。 Referring to FIG. 4, still another verification example of the effect of reducing the amount of paint and diluent used by the coating carrier gas control device of the present invention will be described.
 本実施例では、ロボットによる自動塗装が行われた。 In this example, automatic painting by a robot was performed.
 なお、本実施例でも、上述の実施例1と同様の塗料が用いられた。 In this example, the same paint as in Example 1 was used.
 本実施例では、まず、本発明に係る実施例と対比させるための比較例3として、従来の吹き付け塗装方式であり、エアコンプレッサから送出される圧縮空気を、そのまま、ロボットの塗装モジュールに供給されるキャリアガスとして使用した場合の塗装が行われた。 In this embodiment, first, as a comparative example 3 for comparison with the embodiment according to the present invention, a conventional spray painting method is used, and compressed air sent from an air compressor is supplied as it is to a painting module of a robot. When used as a carrier gas, it was painted.
 比較例3については、溶剤による塗料の希釈率が本実施例で用いられた塗料についての標準的な希釈率である70 % に設定されると共に、ロボットの塗装モジュールからのキャリアガス及び塗料等の吐出の圧力(塗装圧)が従来の標準的な塗装圧である0.250 MPa に設定された。比較例3の塗料の粘度は、岩田粘度カップNK-2を使用した温度20 ℃ での計測値が11.7秒であった。 For Comparative Example 3, the dilution ratio of the paint with the solvent is set to 70% by weight, which is the standard dilution ratio for the paint used in this example, and the carrier gas, paint, etc. from the paint module of the robot are set. The discharge pressure (painting pressure) was set to 0.250 kgpa, which is a conventional standard painting pressure. As for the viscosity of the paint of Comparative Example 3, the measured value at a temperature of 20 ° C. using an Iwata viscosity cup NK-2 was 11.7 seconds.
 一方、本発明に係る実施例3として、エアコンプレッサから送出される圧縮空気を、本発明の塗装キャリアガスの制御装置によって処理してから、ロボットの塗装モジュールに供給されるキャリアガスとして使用した場合の塗装が行われた。本発明としての塗装キャリアガスの制御装置の構成は、図1に示す例と同様のものとされた。 On the other hand, as Example 3 according to the present invention, when compressed air delivered from an air compressor is processed by the coating carrier gas control device of the present invention and then used as a carrier gas supplied to a robot coating module Painting was done. The configuration of the coating carrier gas control device according to the present invention is the same as that shown in FIG.
 本発明に係る実施例3については、溶剤による塗料の希釈率が比較例3よりも小さい50 % に設定されると共に、塗装圧が標準よりも低圧の0.175 MPa に設定された。実施例3の塗料の粘度は、岩田粘度カップNK-2を使用した温度20 ℃ での計測値が14.5秒であった。 For Example 3 according to the present invention, the dilution ratio of the paint with the solvent was set to 50% by weight, which is smaller than that of Comparative Example 3, and the coating pressure was set to 0.175% MPa, which is lower than the standard. As for the viscosity of the coating material of Example 3, the measured value at a temperature of 20 ° C. using the Iwata viscosity cup NK-2 was 14.5 seconds.
 また、実施例3では、ホース6端部のソケット8Aから吹き出されるキャリアガス9の温度は、計測の結果、25~30 ℃ であった。 Further, in Example 3, the temperature of the carrier gas 9 blown out from the socket 8A at the end of the hose 6 was 25 to 30 ° C. as a result of measurement.
 上述の条件のもと、塗装の膜厚が同じになるようにしてコート数を2回とした塗装を行い、比較例3の場合と実施例3の場合とのそれぞれの塗料の使用量が計測された。なお、塗装作業の結果、比較例3の膜厚は11.0 μmであると共に実施例3の膜厚は11.3 μm であり、両者の膜厚は概ね同じであると判断された。また、比較例3と実施例3とのどちらも塗装の仕上がりは良好であった。 Under the above conditions, coating was performed with the number of coatings being twice so that the coating film thickness was the same, and the amount of paint used in each of Comparative Example 3 and Example 3 was measured. It was done. As a result of the coating operation, the film thickness of Comparative Example 3 was 11.0 μm and the film thickness of Example 3 was 11.3 μm μm. Moreover, the finish of the coating was favorable in both Comparative Example 3 and Example 3.
 塗料の使用量の計測の結果、比較例3は43.0 gr であるのに対して実施例3は28.3 gr であり、比較例3に対して実施例3では塗料の使用量が34 % 削減された。 As a result of the measurement of the amount of paint used, Comparative Example 3 was 43.0 gr, while Example 3 was 28.3 gr, and in contrast to Comparative Example 3, the amount of paint used was 34. Reduced by%.
 以上の結果から、本発明の塗装キャリアガスの制御装置によれば、塗装の膜厚を同じにするために必要とされる塗料及び希釈剤の使用量を、従来の吹き付け塗装方式と比べ、34 % 程度削減することが可能であることが確認された。 From the above results, according to the coating carrier gas control device of the present invention, the amount of paint and diluent used to make the coating film thickness the same is 34 compared with the conventional spray coating method. It was confirmed that it was possible to reduce by about %%.
 1 ガス供給源ユニット
 2 ガス入力配管
 3A 導入配管
 3B 送出配管
 4 貯留ユニット
 5 接続配管
 6 ホース
 7 スプレーガン
 7a 塗料カップ
 7a' 塗料カップ
 8 カプラ
 8A ソケット
 8B プラグ
 8B' プラグ
 9 キャリアガス
10 気流調整ユニット
11 ガス入力バルブ
12 一次清浄手段
13 気水分離手段
14 二次清浄手段
15 除湿乾燥手段
16 圧力調整手段
20 加温ユニット
21 加温手段
22 ガス出力バルブ
23 暖房手段
24 ホース収容スペース
25 塗料加温部
26 温度計
DESCRIPTION OF SYMBOLS 1 Gas supply source unit 2 Gas input piping 3A Introducing piping 3B Outgoing piping 4 Storage unit 5 Connection piping 6 Hose 7 Spray gun 7a Paint cup 7a 'Paint cup 8 Coupler 8A Socket 8B Plug 8B' Plug 9 Carrier gas 10 Airflow adjustment unit 11 Gas input valve 12 Primary cleaning means 13 Air-water separation means 14 Secondary cleaning means 15 Dehumidification drying means 16 Pressure adjusting means 20 Heating unit 21 Heating means 22 Gas output valve 23 Heating means 24 Hose storage space 25 Paint heating part 26 thermometer

Claims (6)

  1.  ガス供給源ユニットから送出されるキャリアガスを除湿し乾燥させるドライ化機構と、前記キャリアガスが供給される塗装手段における圧力が所定の圧力になるように前記キャリアガスの圧力を調整する圧力調整手段と、前記塗装手段における温度が所定の温度になるように前記キャリアガスを加温する加温手段と、前記塗装手段に前記キャリアガスを供給するためのホースを収容するスペースを備える筐体内の雰囲気を温める暖房手段とを有することを特徴とする塗装キャリアガスの制御装置。 A drying mechanism for dehumidifying and drying the carrier gas delivered from the gas supply source unit, and a pressure adjusting means for adjusting the pressure of the carrier gas so that the pressure in the coating means to which the carrier gas is supplied becomes a predetermined pressure. And an atmosphere in a housing comprising a heating unit for heating the carrier gas so that the temperature in the coating unit becomes a predetermined temperature, and a space for housing a hose for supplying the carrier gas to the coating unit And a heating means for heating the coating carrier gas control device.
  2.  前記ドライ化機構を通過した後の前記キャリアガスを加圧状態で一時貯蔵した上で前記圧力調整手段に送出する貯留ユニットを更に有することを特徴とする請求項1記載の塗装キャリアガスの制御装置。 2. The coating carrier gas control apparatus according to claim 1, further comprising a storage unit that temporarily stores the carrier gas after passing through the drying mechanism in a pressurized state and then sends the carrier gas to the pressure adjusting means. .
  3.  前記ホースが保温材で覆われていることを特徴とする請求項1記載の塗装キャリアガスの制御装置。 2. The coating carrier gas control device according to claim 1, wherein the hose is covered with a heat insulating material.
  4.  前記塗装手段に向けて前記キャリアガスが吹き出されるように前記ホースから分岐する器具を更に有することを特徴とする請求項1記載の塗装キャリアガスの制御装置。 2. The coating carrier gas control apparatus according to claim 1, further comprising a device branched from the hose so that the carrier gas is blown toward the coating means.
  5.  前記塗装手段に供給される塗料を収容すると共に前記筐体内の雰囲気を利用して前記塗料を塗装作業前に温めるための塗料加温部を更に有することを特徴とする請求項1記載の塗装キャリアガスの制御装置。 The paint carrier according to claim 1, further comprising a paint heating unit for containing the paint supplied to the painting means and heating the paint before painting using the atmosphere in the casing. Gas control device.
  6.  前記ドライ化機構及び前記圧力調整手段を含む気流調整ユニットと、前記加温手段及び前記暖房手段を含む加温ユニットと、前記貯留ユニットとのそれぞれに、または、これらユニットのうちの任意の複数のユニットの組み合わせに対し、移動手段が備えられることを特徴とする請求項2記載の塗装キャリアガスの制御装置。 Each of the airflow adjustment unit including the drying mechanism and the pressure adjustment unit, the heating unit including the heating unit and the heating unit, and the storage unit, or any plurality of these units 3. The coating carrier gas control device according to claim 2, wherein a moving means is provided for the combination of units.
PCT/JP2015/002995 2015-06-16 2015-06-16 Coating carrier gas control device WO2016203504A1 (en)

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PCT/JP2015/002995 WO2016203504A1 (en) 2015-06-16 2015-06-16 Coating carrier gas control device
JP2015530219A JP6095081B6 (en) 2015-06-16 2015-06-16 Control device for coating carrier gas

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JPS5469147A (en) * 1977-11-14 1979-06-02 Kansai Paint Co Ltd Coating method
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Publication number Priority date Publication date Assignee Title
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