EP1041348A2 - Méthode d'installation d'un dispositif de conditionnement d'air - Google Patents

Méthode d'installation d'un dispositif de conditionnement d'air Download PDF

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Publication number
EP1041348A2
EP1041348A2 EP00106823A EP00106823A EP1041348A2 EP 1041348 A2 EP1041348 A2 EP 1041348A2 EP 00106823 A EP00106823 A EP 00106823A EP 00106823 A EP00106823 A EP 00106823A EP 1041348 A2 EP1041348 A2 EP 1041348A2
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EP
European Patent Office
Prior art keywords
indoor unit
trap apparatus
heat exchanger
carbon dioxide
connecting pipe
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
EP00106823A
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German (de)
English (en)
Other versions
EP1041348A3 (fr
EP1041348B1 (fr
Inventor
Hironao Numoto
Shigehiro Sato
Hitoshi Motegi
Yukio Rm.1108 Co-op Nomura Kyoto Minami Watanabe
Hiroyuki Takeuchi
Eiji Nakatsuno
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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
Priority claimed from JP09180699A external-priority patent/JP3154986B2/ja
Priority claimed from JP09457599A external-priority patent/JP3154989B2/ja
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Publication of EP1041348A2 publication Critical patent/EP1041348A2/fr
Publication of EP1041348A3 publication Critical patent/EP1041348A3/fr
Application granted granted Critical
Publication of EP1041348B1 publication Critical patent/EP1041348B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
    • F24F1/06—Separate outdoor units, e.g. outdoor unit to be linked to a separate room comprising a compressor and a heat exchanger
    • F24F1/26—Refrigerant piping
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F1/00—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station
    • F24F1/0003—Room units for air-conditioning, e.g. separate or self-contained units or units receiving primary air from a central station characterised by a split arrangement, wherein parts of the air-conditioning system, e.g. evaporator and condenser, are in separately located units
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B45/00—Arrangements for charging or discharging refrigerant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00—Gas cycle refrigeration machines
    • F25B2309/06—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2345/00—Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/006—Details for charging or discharging refrigerants; Service stations therefor characterised by charging or discharging valves

Definitions

  • the present invention relates to a method for installing an air conditioner and particularly for connecting an indoor unit and an outdoor unit using connecting pipes.
  • an air conditioner is installed in such a manner that more than prescribed amount of refrigerant gas is charged into an outdoor unit for purging air; the air in the connecting pipes and an indoor unit is purged by the refrigerant gas introduced from a liquid-side two-way valve, and the refrigerant gas is discharged into the atmosphere from a valve called a service port of a gas-side three-way valve.
  • the air conditioner is installed in such a manner that after the connecting pipes and the indoor unit are brought into a sufficiently evacuated state using a vacuum pump from the valve called the service port of the gas-side three-way valve, the refrigerant gas is introduced into the connecting pipes and the indoor unit from the liquid-side two-way valve.
  • An installing method using a vacuum pump is recommended as an installing method which does not discharge the refrigerant gas.
  • the installing method using the vacuum pump takes more time to install the air conditioner as compared with a method using the conventional purging method using refrigerant gas of the outdoor unit and discharging the refrigerant gas into the atmosphere.
  • the present invention has been accomplished in view of the problems that conventional methods had;, and it is an object of the invention to provided an easy method for installing an air conditioner while taking an influence on environment into consideration.
  • an air conditioner which is comprised of an outdoor unit including a compressor and an outdoor unit heat exchanger into which refrigerant gas is charged, an indoor unit including an indoor unit heat exchanger which is opened to atmosphere, and a connecting pipe connecting said outdoor unit and said indoor unit which is also opened to atmosphere; and the method is comprised of: air in said indoor unit heat exchanger and said connecting pipe is replaced by carbon dioxide; said carbon dioxide is collected by a trap apparatus having zeolite; and after said carbon dioxide is collected, the refrigerant gas in the outdoor unit is charged into said indoor unit heat exchanger and said connecting pipe, wherein when said air in said indoor unit heat exchanger and said connecting pipe is replaced by said carbon dioxide, pressure in said indoor unit heat exchanger and said connecting pipe is brought into a positive pressure state.
  • the inside pressure is held at positive pressure when air is replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the positive pressure state of the inside becomes a trigger of convection of gas, the carbon dioxide is swiftly absorbed by the zeolite in the trap apparatus, and the carbon dioxide can be collected swiftly.
  • an air conditioner which is comprised of an outdoor unit including a compressor and an outdoor unit heat exchanger into which refrigerant gas is charged, an indoor unit including an indoor unit heat exchanger which is opened to atmosphere, and a connecting pipe connecting said outdoor unit and said indoor unit which is opened to atmosphere; and the method is comprised of: air in said indoor unit heat exchanger and said connecting pipe is replaced by carbon dioxide; said carbon dioxide is collected by a trap apparatus having zeolite; and after said carbon dioxide is collected, the refrigerant gas in the outdoor unit is charged into said indoor unit heat exchanger and said connecting pipe, wherein when said air in said indoor unit heat exchanger and said connecting pipe is replaced by said carbon dioxide, pressure in said indoor unit heat exchanger or said connecting pipe is brought into pressure higher than that in said trap apparatus.
  • the inside pressure is held at a higher pressure than that of the trap apparatus when air is replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the higher pressure state of the inside becomes a trigger of convection of gas, the carbon dioxide is swiftly absorbed by the zeolite in the trap apparatus, and the carbon dioxide can be collected swiftly.
  • said trap apparatus includes therein a structure body constructed with carriers which are coated with a layer mainly made of zeolite.
  • zeolite exists on the surface of the structure body, it is possible to increase the contact area with the carbon dioxide, and to swiftly collect the carbon dioxide.
  • said trap apparatus includes 60g or greater zeolite per one liter of a volume of a pipe of said indoor unit and said connecting pipe.
  • the trap apparatus is comprised of a structure body constructed with carriers which are coated with a layer mainly made of zeolite.
  • zeolite exists on the surface of the structure body, it is possible to increase the contact area with the carbon dioxide.
  • the structure body is a honeycomb structure body or a corrugated structure body. With this mode, it is possible to increase the contact area with the carbon dioxide, and to speed up the collection of the carbon dioxide.
  • a trap apparatus for installing an air conditioner wherein zeolite is charged such that a flow path space is larger on the inlet side than that of the bottom side.
  • a trap apparatus for installing an air conditioner wherein a hollow cylindrical zeolite is used.
  • a trap apparatus for installing an air conditioner wherein zeolite having surface area greater than that of zeolite disposed closer to a bottom of the trap apparatus is disposed closer to an inlet of the trap apparatus.
  • a trap apparatus for installing an air conditioner wherein spherical or columnar zeolite is used, and zeolite having diameter or length greater than that of zeolite disposed closer to a bottom of the trap apparatus is disposed closer to an inlet of the trap apparatus.
  • pressure in the trap apparatus is brought into a negative state equal to or lower than 1 mmHg.
  • this negative pressure state becomes a trigger of convection of gas, the carbon dioxide is swiftly absorbed by the zeolite in the trap apparatus, and the carbon dioxide can be collected swiftly.
  • an air conditioner which is comprised of an outdoor unit including a compressor and an outdoor unit heat exchanger into which refrigerant gas is charged, an indoor unit including an indoor unit heat exchanger which is opened to atmosphere, and a connecting pipe connecting said outdoor unit and said indoor unit which is opened to atmosphere; and the method is comprised of: air in said indoor unit heat exchanger and said connecting pipe is replaced by carbon dioxide; said carbon dioxide is collected by a trap apparatus having calcium hydroxide; and after said carbon dioxide is collected, the refrigerant gas in the outdoor unit is charged into said indoor unit heat exchanger and said connecting pipe, wherein when said air in said indoor unit beat exchanger and said connecting pipe is replaced by said carbon dioxide, pressure in said indoor unit heat exchanger and said connecting pipe is brought into a positive pressure state.
  • the inside pressure is held at positive pressure when air is replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the positive pressure state of the inside becomes a trigger of convection of gas, the chemical reaction with calcium hydroxide in the trap apparatus is swiftly caused, and the carbon dioxide can be collected swiftly.
  • an air conditioner which is comprised of an outdoor unit including a compressor and an outdoor unit heat exchanger into which refrigerant gas is charged, an indoor unit including an indoor unit heat exchanger which is opened to atmosphere, and a connecting pipe connecting said outdoor unit and said indoor unit which is opened to atmosphere; and the method is comprised of: air in said indoor unit heat exchanger and said connecting pipe is replaced by carbon dioxide; said carbon dioxide is collected by a trap apparatus having calcium hydroxide; and after said carbon dioxide is collected, the refrigerant gas in the outdoor unit is charged into said indoor unit heat exchanger and said connecting pipe, wherein when said air in said indoor unit heat exchanger and said connecting pipe is replaced by said carbon dioxide, pressure in said indoor unit heat exchanger and said connecting pipe is brought into pressure higher than that in said trap apparatus.
  • the inside pressure is held at a higher pressure than that of the trap apparatus when air is replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the higher pressure state of the inside becomes a trigger of convection of gas, the chemical reaction with calcium hydroxide in the trap apparatus is swiftly caused, and the carbon dioxide can be collected swiftly.
  • the trap apparatus in the above method for installing an air conditioner, includes therein a structure body constructed with carriers which are coated with a layer mainly made of calcium hydroxide.
  • a structure body constructed with carriers which are coated with a layer mainly made of calcium hydroxide.
  • the trap apparatus in the above method for installing an air conditioner, includes 6.6g or greater calcium hydroxide per one liter of a volume of a pipe of the indoor unit and the connecting pipe.
  • a trap apparatus for installing an air conditioner comprising a structure body constructed with carriers which are coated with a layer mainly made of calcium hydroxide.
  • the structure body is a honeycomb structure body or a corrugated structure body.
  • water in the amount of 0.1 to 10 wt% of calcium hydroxide is included.
  • the calcium hydroxide is mixed with at least one of zeolite, activated alumina and silica gel to form the coating layer.
  • zeolite, activated alumina or silica gel With this mode, it is possible to hold water by zeolite, activated alumina or silica gel, and this water becomes a catalytic trigger, and the chemical reaction speed from the calcium hydroxide to calcium carbonate can be accelerated, thereby, collection speed will be increased.
  • a heat radiating portion or a cooling portion is provided outside the trap apparatus.
  • reaction heat generated by the abrupt chemical reaction can efficiently be transmitted and diffused outside, and it is possible to prevent the reaction speed from being lowered.
  • Figs.1 and 2 are block diagrams of a refrigeration cycle of an air conditioner used in the embodiment.
  • Fig.1 shows a state where a carbon dioxide cylinder is connected
  • Fig.2 shows a state where a trap apparatus is connected.
  • the refrigeration cycle comprises a compressor 1, a four-way valve 2, an outdoor unit heat exchanger 3, an expansion device 4, a dryer 5 and an indoor unit heat exchanger 6.
  • the compressor 1, the four-way valve 2, the outdoor unit heat exchanger 3, the expansion device 4 and the dryer 5 are disposed in an outdoor unit A, and the indoor unit heat exchanger 6 is disposed in an indoor unit B.
  • the outdoor unit A is provided with a liquid-side two-way valve 7 and a gas-side three-way valve 8.
  • the outdoor unit A and the indoor unit B are connected to each other through connection pipes 9 and 10 using the liquid-side two-way valve 7 and the gas-side three-way valve 8.
  • the liquid-side two-way valve 7 includes a screw portion 7a, and a pipe on the side of the outdoor unit A and a connecting pipe 9 are brought into communication with each other by opening the screw portion 7a.
  • the gas-side three-way valve 8 includes a screw portion 8a and a service port 8b, and a pipe on the side of the outdoor unit A and a connecting pipe 10 are brought into communication with each other by opening this screw portion 8a.
  • a carbon dioxide cylinder 11 can be connected to the service port 8b using a connecting device 12, or as shown in Fig.2, a trap apparatus 13 can be connected to the service port 8b using a connecting device 14.
  • the carbon dioxide cylinder 11 or the trap apparatus 13 can be brought into communication with a connecting pipe 10 through the connecting device 12 or 14.
  • Fig.3 is a schematic view of the trap apparatus according to the first embodiment.
  • Spherical shape zeolite particles 15A and 15B are charged in the trap apparatus 13A.
  • the zeolite particles 15A have 6 to 8 mesh diameter, and the zeolite particles 15B have 4 to 6 mesh diameter.
  • the trap apparatus 13A is provided therein with a baffle 16 for separating an inlet C and the zeolite particles 15A so that the zeolite particles 15A and 15B are securely held.
  • This baffle 16 has holes of such diameters that the zeolite particles 15A and 15B cannot pass through. In the present embodiment, an opening ratio is set to 60%.
  • the zeolite particles 15A having greater diameter are charged closer to the inlet C, and the zeolite particles 15B having smaller diameter is charged in the deep side of the trap apparatus 13A.
  • this layout it is possible to form a flow path space which is greater on the side of the inlet C than that of the bottom side.
  • 100g of zeolite particles 15A and 15B in total were charged.
  • Fig.4 is a schematic view of the trap apparatus according to the second embodiment.
  • Hollow cylindrical zeolite particles 15C are charged in the trap apparatus 13B.
  • the zeolite particles 15C has size of ⁇ 5 ⁇ 7mm, and thickness of 2mm.
  • the trap apparatus 13B is provided therein with the baffle 16 for separating the inlet C and the zeolite particles 15C so that the zeolite particles 15C is securely held.
  • the opening ratio is set to 60%.
  • the hollow cylindrical zeolite particles 15C are charged in the trap apparatus 13B. Therefore, the flow path space can be enlarged, and the contact area can be increased. In the present embodiment, 100g of zeolite particles 15C were charged in total.
  • Figs.5 to 7 show a trap apparatus according to the third embodiment.
  • Fig.5 is a schematic view of the trap apparatus used in the third embodiment
  • Fig.6 is a sectional view taken along the line A-A in Fig.5
  • Fig.7 is an enlarged sectional view of an essential portion of an inside structure body in Fig.6.
  • a trap apparatus 13C is provided therein with a honeycomb structure body 17.
  • the honeycomb structure body 17 has 400 cells/inch 2 (see Fig.6), and volume of 70 ⁇ ⁇ 90mm; and is coated on its surface with a coating layer 15D that is mainly made of zeolite in the amount of 100g in total.
  • Figs.8 to 10 show the fourth embodiment.
  • Fig.8 is a schematic view of a trap apparatus according to the fourth embodiment
  • Fig.9 is a sectional view taken along the line A-A in Fig.8
  • Fig.10 is an enlarged sectional view of an essential portion of an inside structure body in Fig.8.
  • a trap apparatus 13D is provided therein with a honeycomb structure body 18.
  • An outer periphery of a body of the trap apparatus 13D is provided with radiating fins 19.
  • the honeycomb structure body 18 has 200 cells/inch 2 (see Fig.9), and volume of 50 ⁇ 65mm.
  • the honeycomb structure body 18 is coated on its surface with a coating layer 18A which is mainly made of calcium hydroxide in the amount of 10g in total. More specifically, the coating layer 18A is made of 90 wt% of calcium hydroxide, and 10 wt% of A-type zeolite.
  • the A-type zeolite which easily absorbs water is allowed to hold 10 wt% of water.
  • the zeolite is mixed in the coating layer 18A, the water held by the zeolite is less prone to be disassociated even if abrupt reaction heat is generated, and therefore, it acts effectively as a catalytic trigger.
  • refrigerant gas is charged in the outdoor unit A including in the compressor 1 as well as in the outdoor heat exchange unit 3. At that time, in addition to the refrigerant gas which is necessary for operation, the refrigerant gas to be used for purge operation is also charged in the outdoor unit A.
  • pipes in the indoor unit such as those in the indoor heat exchanger 6 and the connecting pipes 9 and 10 are not hermetically sealed but are opened to the atmosphere.
  • the outdoor unit A and the indoor unit B are connected through the connecting pipes 9 and 10. At that time, a screw portion 7a of a liquid-side two-way valve 7 and a screw portion 8a of a gas-side three-way valve 8 are closed.
  • the carbon dioxide cylinder 11 is mounted to the service port 8b of the gas-side three-way valve 8 using the connecting device 12.
  • the flare portion of the liquid-side two-way valve 7 is tightly closed keeping the pressure in the connecting pipes 9 and 10 and the indoor unit B at positive pressure (about 0.1 kgf/cm 2 ).
  • the connecting device 12 is removed from the service port 8b together with the carbon dioxide cylinder 11.
  • the trap apparatus 13 is mounted to the service port 8b using the connecting device 14.
  • the trap apparatus 13 is mounted to the connection device 14 by being pushed to the connection device 14 while being rotated. By this mounting operation, the interior of the trap apparatus 13 is brought into communication with the connecting pipe 10.
  • the introduced carbon dioxide is physically absorbed and collected by the zeolite in the trap apparatus 13, whereas in the fourth embodiment, the introduced carbon dioxide becomes calcium carbonate by chemical reaction with calcium hydroxide, and thereby, is collected.
  • the screw portion 7a of the liquid-side two-way valve 7 is slightly loosened, the refrigerant gas in the outdoor unit A is introduced, thereby bringing the pressure in the connecting pipes 9 and 10 and the pipes in the indoor units B into positive pressure (about 0.2 kgf/cm 2 ).
  • the volume of the pipe of the indoor unit B including the indoor unit heat exchanger 6 and the connecting pipes 9 and 10 was 1.5 liters.
  • the honeycomb structure body coated with zeolite the third embodiment, reached the sufficient negative pressure fastest.
  • a trap apparatus body container required for accommodating 100g of zeolite is adversely increased in size as compared with those of the first and second embodiments.
  • the trap apparatus directly accommodating the spherical zeolite particles as in the first embodiment was most compact. Therefore, it is preferable to select a suitable trap apparatus while taking time required for installing operation and a size of tool required for the operation into consideration.
  • the pressure in the trap apparatus 13 can be set to negative pressure (e.g., 1 mmHg or lower) so that the convection of gas from the connecting pipes 9, 10 and the pipe of the indoor unit B to the trap apparatus 13 can be obtained.
  • the shape of the zeolite particles may be oval spherical shape, and if the zeolite particles are formed with bumps and dips so as to increase its surface area, higher effect can be obtained.
  • the spherical zeolite particles having different size were used in the first embodiment, zeolite particles having different shape may be used. In this case, it is preferable to dispose zeolite particles having greater surface area at the place closer to the inlet.
  • a honeycomb structure body was used.
  • the same effect can be obtained if a corrugated structure body is used.
  • a structure body which can be used for the present invention should not be limited to the above embodiments, such structure body is appropriate if it has sufficient communication holes from the inlet to the bottom of the trap apparatus and zeolite can be supported on the surface or inside of such structure body so as to have sufficiently great contact area. Further, by employing the structure body such as honeycomb structure body or corrugated structure body, the trap apparatus can be conveniently transported because even if an impact is applied to the trap apparatus, the zeolite attached to the structure body is less prone to be crushed into powder.
  • a honeycomb structure body was used.
  • a structure body which can be used for the present invention should not be limited to the above embodiments, such structure body is appropriate if it has sufficient communication holes from the inlet to the bottom of the trap apparatus and calcium hydroxide can be supported on the surface or inside of such structure body so as to have sufficiently great contact area for effective chemical reactions.
  • the structure body useable in this embodiment should have such structure which does not cause gas passage impairment even when the volume of the structure body is expanded due to the chemical reaction.
  • the radiation fins 19 are provided to the trap apparatus 13D. However, it is also effective if the inside heat generation is suppressed by cooling from the outside. Affirmative cooling, for example, dipping the trap apparatus partially in a water tank and blowing the air against the radiation fins 19, is effective.
  • the weight of zeolite with which the effect of these embodiments was achieved was 60g or greater per one liter of the total volume of the pipe of the indoor unit B and the connecting pipes 9 and 10. With this weight of zeolite, carbon dioxide was trapped in two to five minutes and the negative pressure state of 10 to 30 mmHg was obtained. Although there is no problem even if the amount of zeolite exceeds the above value, if the zeolite is excessively increased, it is not preferable because the container for accommodating the trap material becomes bulk. If the amount of zeolite is less than 60g, the speed with which a pressure reaches the sufficient negative pressure becomes slow, and one of the objects of the present invention may be sacrificed.
  • Fig.11 is a graph showing the relation between the weight of zeolite charged in the trap apparatus and the pressure reached after ten minutes.
  • the pressure was measured when the volume of the pipe of the indoor unit B and the connecting pipes 9 and 10 was 1.5 liters. Therefore, if the volume is 1 liter, sufficient effect should be obtained even with 60g or less of zeolite, but since collection of carbon dioxide is hindered if water is absorbed, it is conceived that 60 to 100g of zeolite per liter is practically preferable.
  • the weight of calcium hydroxide which could obtain the sufficient effect of the embodiment was 6.6 to 16.5g.
  • Stoichiometry weight necessary for calcium hydroxide to trap 1.5 liters of carbon dioxide is 4.95g at 25C. Therefore, the weight of calcium hydroxide per 1 liter of the volume of the pipe of the indoor unit B and the connecting pipes 9 and 10 is 3.30g.
  • two to five times of calcium hydroxide is necessary to collect the carbon dioxide swiftly. By using two to five times of calcium hydroxide, the carbon dioxide was able to be collected in two to five minutes and the negative pressure state of 10 to 50 mmHg level was obtained.
  • the amount of water with respect to the calcium hydroxide was 1 wt%, but the amount of water applicable to the present invention was 0.1 to 10 wt%. If the amount was less than 0.1 wt%, the amount of water is too small to effectuate catalytic reaction trigger, and it took time to collect carbon dioxide. Further, if the amount of water exceeds 10 wt%, water vapor was generated by chemical reaction; and the vapor entered the connecting pipes, and it was not preferable in terms of reliability.
  • zeolite was used in the present embodiment.
  • activated alumina, silica gel and the like was found applicable. As a factor of the applicable materials, specific surface of 100m 2 /g was preferable.
  • the present invention can also be applied to an outdoor unit having a three-way valve and another three-way valve.
  • the connecting device may have T-bifurcation shape; and carbon dioxide may be supplied from one of the connecting portions, and the carbon dioxide can be collected from the other connecting portion. It is preferable to commonly use the same connecting device.
  • a dryer 5 is disposed in the outdoor unit A.
  • water existing in the indoor unit A and the connecting pipes 9 and 10 can also be eliminated by increasing the operation time of the vacuum pump, but it is difficult to sufficiently eliminate the water by a purge method using refrigerant gas as in the present invention. Therefore, by providing the dryer 5 in the refrigeration cycle, it is possible to ensure the long term reliability of the air conditioner.
  • the inside pressure is held positive after air has been replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the positive pressure state of the inside becomes a trigger of convection of gas so that the carbon dioxide is swiftly absorbed by the zeolite (or collected as a result of calcium chemical reaction from calcium hydroxide to calcium carbonate) in the trap apparatus.
  • the inside pressure is held at higher pressure than that of the trap apparatus after air has been replaced by carbon dioxide. Therefore, when the inside pressure is brought into communication with the trap apparatus next, the higher pressure state of the inside becomes a trigger of convection of gas so that the carbon dioxide is swiftly absorbed by the zeolite (or collected as a result of calcium chemical reaction from calcium hydroxide to calcium carbonate) in the trap apparatus.
  • the structure body when the structure body is utilized, since zeolite exists on the surface of the structure body, it is possible to increase the contact area with the carbon dioxide, and to swiftly collect the carbon dioxide.
  • the trap apparatus having 60g or more zeolite per one liter of volume of the pipe of the indoor unit and the connection pipes is used. Therefore, if the weight of zeolite is set while taking the volume of the pipe of the indoor unit and the connection pipes into consideration, it is possible to collect the carbon dioxide with sufficient speed.
  • the structure body comprising carriers with the coated layer mainly made of zeolite is included inside.
  • zeolite exists on the surface of the structure body, it is possible to increase the contact area with the carbon dioxide.
  • the honeycomb structure body or the corrugated structure body by employing the honeycomb structure body or the corrugated structure body, it is possible to increase the contact area with the carbon dioxide, and to speed up the collection of the carbon dioxide.
  • the present invention by forming the flow path space which is greater on the side of the inlet than the bottom side, it is possible to smoothly diffuse the carbon dioxide in the trap apparatus.
  • the flow path necessary for diffusing carbon dioxide can sufficiently be ensured, and it is possible to speed up the trap of carbon dioxide.
  • zeolite particles having greater surface area is charged in the trap apparatus closer to its inlet than its bottom, it is possible to smoothly diffuse the carbon dioxide in the trap apparatus.
  • zeolite particles by using the spherical or columnar zeolite particles, a flow path necessary for diffusing the carbon dioxide can sufficiently be secured, and by charging zeolite particles having greater surface area into the trap apparatus closer to its inlet than its bottom, it is possible to smoothly diffuse the carbon dioxide in the trap apparatus.
  • the trap apparatus since in the trap apparatus, a trap material exists on the structure body having communication ports, it is possible to increase the contact area for the diffusion reaction between the trap material and carbon dioxide, and to prevent the flow path from being closed by volume expansion at the time of the chemical reaction.
  • a heat radiating portion or a cooling portion is provided outside the trap apparatus, reaction heat generated by the abrupt chemical reaction can efficiently be transmitted and diffused outside, and a pressure in the connecting pipes and the indoor unit can be brought into a negative state, i.e., 50 mmHg or less.
  • a pressure in the connecting pipes and the indoor unit can be brought into a negative state, i.e., 50 mmHg or less at a sufficient speed.
  • the carbon dioxide can swiftly be collected, and the installation operation can conveniently be carried out.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Other Air-Conditioning Systems (AREA)
  • Treating Waste Gases (AREA)
EP00106823A 1999-03-31 2000-03-30 Piège pour l'installation d'un dispositif de conditionnement d'air Expired - Lifetime EP1041348B1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP09180699A JP3154986B2 (ja) 1999-03-31 1999-03-31 空気調和装置の施工方法及び空気調和装置の施工用トラップ装置
JP9180699 1999-03-31
JP9457599 1999-04-01
JP09457599A JP3154989B2 (ja) 1999-04-01 1999-04-01 空気調和装置の施工方法及び空気調和装置の施工用トラップ装置

Publications (3)

Publication Number Publication Date
EP1041348A2 true EP1041348A2 (fr) 2000-10-04
EP1041348A3 EP1041348A3 (fr) 2001-07-04
EP1041348B1 EP1041348B1 (fr) 2005-12-21

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EP00106823A Expired - Lifetime EP1041348B1 (fr) 1999-03-31 2000-03-30 Piège pour l'installation d'un dispositif de conditionnement d'air

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Country Link
EP (1) EP1041348B1 (fr)
DE (1) DE60024909T2 (fr)
ES (1) ES2254063T3 (fr)
MY (1) MY133229A (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
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EP1067340A3 (fr) * 1999-07-05 2001-07-04 Matsushita Electric Industrial Co., Ltd. Piège pour recueillir le gaz de remplacement dans un dispositif de conditionnement d'air
EP1041349A3 (fr) * 1999-04-01 2001-10-17 Matsushita Electric Industrial Co., Ltd. Dispositif pour le remplacement de gaz dans un dispositif de conditionnement d'air

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1041347A3 (fr) * 1999-04-01 2001-07-04 Matsushita Electric Industrial Co., Ltd. Elément de connection pour l'installation d'un dispositif de conditionnement d'air
EP1041349A3 (fr) * 1999-04-01 2001-10-17 Matsushita Electric Industrial Co., Ltd. Dispositif pour le remplacement de gaz dans un dispositif de conditionnement d'air
EP1067340A3 (fr) * 1999-07-05 2001-07-04 Matsushita Electric Industrial Co., Ltd. Piège pour recueillir le gaz de remplacement dans un dispositif de conditionnement d'air

Also Published As

Publication number Publication date
EP1041348A3 (fr) 2001-07-04
DE60024909T2 (de) 2006-06-29
DE60024909D1 (de) 2006-01-26
ES2254063T3 (es) 2006-06-16
EP1041348B1 (fr) 2005-12-21
MY133229A (en) 2007-10-31

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