WO2020007866A1 - Apparatus for removing non-condensable gases from a refrigerant - Google Patents

Apparatus for removing non-condensable gases from a refrigerant Download PDF

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Publication number
WO2020007866A1
WO2020007866A1 PCT/EP2019/067750 EP2019067750W WO2020007866A1 WO 2020007866 A1 WO2020007866 A1 WO 2020007866A1 EP 2019067750 W EP2019067750 W EP 2019067750W WO 2020007866 A1 WO2020007866 A1 WO 2020007866A1
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WO
WIPO (PCT)
Prior art keywords
section
pipe
refrigerant
connection geometry
condensable gases
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.)
Ceased
Application number
PCT/EP2019/067750
Other languages
French (fr)
Inventor
Thomas Lund
Johan Van Beek
Niels P. VESTERGAARD
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.)
Danfoss AS
Original Assignee
Danfoss AS
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 Danfoss AS filed Critical Danfoss AS
Priority to US17/044,395 priority Critical patent/US11365919B2/en
Priority to CN201980036074.1A priority patent/CN112204323B/en
Publication of WO2020007866A1 publication Critical patent/WO2020007866A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • 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
    • F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/04—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases
    • F25B43/043—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for withdrawing non-condensible gases for compression type systems

Definitions

  • the present invention relates to an apparatus for removing non-condensable gases from a refrigerant, said apparatus comprising a pipe arrangement having a pipe, cooling means for the pipe, and venting means, wherein the pipe comprises a connection geometry for a connection to a refrigerant system.
  • Such an apparatus is known, for example, from EP 0 256 602 A1.
  • the pipe is straight and oriented along the direction of gravity.
  • the lower end of the pipe is connected to a vessel of a refrigerant system and is provided with a shut off valve between the vessel and the pipe.
  • the other end of the pipe is provided with venting means through which gas can be blown up into the air.
  • Such an apparatus can also be named "air purger”. It is used to remove air and other non-condensable gases from an ammonia-refrigerant. Air is hindering a transfer of heat from the refrigerant to the cooling or heating surfaces, resulting in lower efficiency of the system.
  • the cooling means acting on the pipe have the effect that the refrigerant contained in the pipe condenses and changes its form into a liquid.
  • the liquid can be fed back to the vessel by means of the shut-off valve.
  • the air which is heavier than the ammonia gas enters again the vessel and has again to be purged which leads to a low efficiency of the air purger.
  • the object underlying the invention is to have an air purger with a good efficiency.
  • the pipe comprises at least a first section and a second section which are directed in different directions.
  • the pipe can still directly be connected to the refrigerant system so that gas consisting of condensable and non-condensable gases can directly enter the interior of the pipe from the refrigerant system.
  • the cooling means acting on the pipe can condense the condensable gases.
  • the liquid produced by this condensation process can be fed back to the connection geometry to enter the refrigeration system.
  • the sections of the pipe are directed in different directions, they cannot all be directed in vertical direction.
  • a direction of a section is defined as the relation between an inlet of a section, i.e.
  • connection geometry a first end close to the connection geometry, and an outlet of the section, i.e. a second end remote from the connection geometry.
  • two sections can have different directions.
  • the non-condensable gas in this section cannot flow back to the connection geometry or it flows back to the connection geometry with a smaller velocity since only a part of the gravity acts on the gas.
  • the interior of the pipe can be subjected to higher pressures, i.e. by the pressure of the refrigerant system, without having the need to fulfil the requirements of a high risk welding class which is expensive and time consuming for checking.
  • the first section comprises a first end close to the connection geometry and a second end remote from the connection geometry, wherein the first end is arranged at a lower height in direction of gravity than the second end
  • the second section comprises a first end close to the connection geometry and a second end remote from the connection geometry, wherein the second end is arranged at a lower height in direction of gravity than the first end
  • the second end of the first section and the first end of the second section are connected by a third section which is inclined upwardly. Condensable gas which condenses in the third section can flow back to the connection geometry.
  • the pipe comprises a fourth section which is inclined downwardly and connects the second section and a liquid outlet. Condensable gas which condenses in the second and fourth section can flow directly to the liquid outlet.
  • liquid outlet is connected to the first section by means of a liquid trap.
  • a liquid trap allows only liquid to escape but prevents the escape of any gases.
  • the liquid trap comprises a duct from the liquid outlet to an inlet opening in the first section, wherein the liquid outlet is arranged higher than a lower end of the inlet opening and lower than an upper end of the inlet opening. In this way it can be achieved that liquid entering the liquid outlet displaces liquid in the liquid trap without forming a larger liquid volume within the pipe.
  • the pipe comprises a fifth section connecting the fourth section to the venting means. The venting means can be arranged at a position higher in direction of gravity.
  • the fifth section is at least partly inclined upwardly. Accordingly, condensable gases condensing inside the fifth section can flow back to the liquid outlet.
  • the cooling means act on the fourth section and the fifth section.
  • the fourth section and the fifth section can be made straight and can be made longer than the other sections, so that in these sections the condensing efficiency is the greatest.
  • a filler element is arranged in the fifth section. It is assumed that most of the condensable gases are already condensed in the fifth section and most part of the gas consists of non condensable gases. Accordingly, the volume needed is smaller.
  • the fourth section comprises a first cooling jacket and the fifth section comprises a second cooling jacket, wherein the first cooling jacket comprises an inlet at one end and a connection to the second jacket at another end. Accordingly, the coolant which is used to remove heat from the pipe can flow through the first jacket, the connection, and the second jacket in a circulation.
  • the pipe has an inner diameter of 25 mm or less.
  • a small diameter facilitates the low welding risk classification.
  • no certified welders and X-ray scanning of the weldings are necessary. It is sufficient to rely solely on pressure testing of the weldings.
  • Fig. 1 shows schematically an apparatus for removing non
  • Fig. 2 shows the pipe arrangement in more detail.
  • Fig. 1 shows an apparatus 1 for removing non-condensable gases from a refrigerant.
  • the apparatus 1 can also be named "air purger”.
  • the apparatus 1 comprises a pipe arrangement 2.
  • the pipe arrangement 2 comprises a pipe 3, cooling means 4 for the pipe and a connection geometry 5 for a connection to a refrigerant system (not shown in the drawing).
  • the apparatus 1 can directly be connected to the refrigerant system.
  • the refrigerant system is operated with an ammonia-refrigerant.
  • the refrigerant can have a pressure in a range from 6 to 25 bar, depending on where in the refrigeration system the air purger is arranged.
  • the pipe 3 has in inner diameter of 25 mm or less to facilitate the low welding risk classification.
  • the inner diameter does not exceed the 25 mm a certified welder is not required and X-ray testing of the weldings is not necessary. It is sufficient to rely solely on pressure testing of the weldings.
  • the pipe arrangement 2 is shown in more detail in Fig. 2. Same reference numerals are used for the same elements.
  • the pipe 3 comprises a first section 6 which is oriented vertically, i.e. parallel to the direction of gravity.
  • the first section 6 is connected to the connection geometry 5.
  • the first section 6 is connected to a second section 7 via a third section 8.
  • the second section 7 is connected to a fourth section 9 which connects the second section 7 to a liquid outlet 10.
  • the fourth section 9 is connected to a fifth section 1 1.
  • the fifth section 1 1 comprises at an end 12 venting means 13 in a position remote from the liquid outlet 10.
  • the first section 6 comprises a first end 14 close to the connection geometry 5 and a second end 15 remote from the connection geometry 5.
  • the second section 7 comprises a first end 16 closer to the connection geometry 5 and a second end 17 remote from the connection geometry 5.
  • close and remote relate to a distance through which a gas has to flow from the connection geometry 5 to the respective ends.
  • the first end 14 of the first section 6 is arranged at a lower height in direction of gravity than the second end 15.
  • the second end 17 of the second section 7 is arranged at a lower height in gravity direction than the first end 16.
  • the third section 8 is slightly inclined upwardly with the effect that refrigerant or condensable gases which condense in the third section 8 can directly flow back to the connection geometry 5. However, since the gravity works only with a rather small component on the non-condensable gas in the third section 8 this non-condensable gas is not driven back to the connection geometry 5.
  • the fourth section 9 is slightly inclined downwardly and the fifth section 11 is slightly inclined upwardly over a large part of its length.
  • a U-shaped part 18 of the fifth section 1 1 connects to the fourth section 9.
  • the fourth section 9 is surrounded by a first cooling jacket 19 and the fifth section 1 1 is surrounded by a second cooling jacket 20 at least over its straight part.
  • the first cooling jacket 19 is supplied with a cooling medium from the cooling means 4 via an inlet pipe 21.
  • the first cooling jacket 19 is connected to the second cooling jacket 20 by means of a connecting pipe 22 and the other end of the second cooling jacket 20 is connected to the cooling means by means of an outlet pipe 23.
  • the liquid outlet is connected to an inlet opening 24 in the first section 6, more precisely in a lower part of the first section 6 of the pipe 3. This connection is made by means of a liquid trap 25.
  • the liquid trap 25 comprises a duct 26 which is arranged in a position lower than the fourth section 9.
  • the liquid outlet 10 is arranged higher than a lower end of the inlet opening 24 and lower than an upper end of the inlet opening 24. Accordingly, in the duct 26 there is permanently a volume of liquid 27 which prevents a flow of gas through the duct 26.
  • connection geometry 5 When the connection geometry 5 is connected to the refrigerant system, a gas containing condensable gases and non-condensable gases enters the pipe 3 via the connection geometry 5. This gas fills the interior of the pipe 3.
  • the fourth section 9 and the fifth section 1 1 cool down to a temperature at which the condensable gases can condense.
  • the liquid forming in this condensing process flows under the action of gravity to the liquid outlet 10 and from there through the liquid trap 25 back to the first section 6, however, without any gas.
  • Non-condensable gases are trapped within pipe 3 once they have reached the second section 7.
  • the non-condensable gases can escape only via venting means 13 at the end of the fifth section 1 1.
  • the venting means 13 can comprise, for example, a controlled venting valve.
  • the fifth section 1 1 comprises a filler element 28 reducing the free volume within the fifth section 1 1. In the fifth section 1 1 a large part of the

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

An apparatus (1) for removing non-condensable gases from a refrigerant is described, said apparatus (1) comprising a pipe arrangement (2) having a pipe (3), cooling means (4) for the pipe (3), and venting means, wherein the pipe (3) comprises a connection geometry (5) for a connection to a refrigerant system. Such an apparatus should be operated with good efficiency. To this end the pipe comprises at least a first section (6) and a second section (7) which are directed in different directions.

Description

Apparatus for removing non-condensable gases from a refrigerant
The present invention relates to an apparatus for removing non-condensable gases from a refrigerant, said apparatus comprising a pipe arrangement having a pipe, cooling means for the pipe, and venting means, wherein the pipe comprises a connection geometry for a connection to a refrigerant system.
Such an apparatus is known, for example, from EP 0 256 602 A1. The pipe is straight and oriented along the direction of gravity. The lower end of the pipe is connected to a vessel of a refrigerant system and is provided with a shut off valve between the vessel and the pipe. The other end of the pipe is provided with venting means through which gas can be blown up into the air.
Such an apparatus can also be named "air purger". It is used to remove air and other non-condensable gases from an ammonia-refrigerant. Air is hindering a transfer of heat from the refrigerant to the cooling or heating surfaces, resulting in lower efficiency of the system.
The cooling means acting on the pipe have the effect that the refrigerant contained in the pipe condenses and changes its form into a liquid. The liquid can be fed back to the vessel by means of the shut-off valve. However, when opening the valve, the air which is heavier than the ammonia gas, enters again the vessel and has again to be purged which leads to a low efficiency of the air purger.
The object underlying the invention is to have an air purger with a good efficiency.
This object is solved with an apparatus for removing non-condensable gases from a refrigerant as described at the outset in that the pipe comprises at least a first section and a second section which are directed in different directions. The pipe can still directly be connected to the refrigerant system so that gas consisting of condensable and non-condensable gases can directly enter the interior of the pipe from the refrigerant system. The cooling means acting on the pipe can condense the condensable gases. The liquid produced by this condensation process can be fed back to the connection geometry to enter the refrigeration system. However, when the sections of the pipe are directed in different directions, they cannot all be directed in vertical direction. A direction of a section is defined as the relation between an inlet of a section, i.e. a first end close to the connection geometry, and an outlet of the section, i.e. a second end remote from the connection geometry. Even if two sections are arranged vertically, they can have different directions. When a section is not directed in vertical direction, i.e. parallel to the direction of gravity, the non-condensable gas in this section cannot flow back to the connection geometry or it flows back to the connection geometry with a smaller velocity since only a part of the gravity acts on the gas. The more of the non condensable gas can be kept in the pipe and is blown out via the venting means, the better the efficiency.
Since only a pipe is used for the removal of the non-condensable gases, the interior of the pipe can be subjected to higher pressures, i.e. by the pressure of the refrigerant system, without having the need to fulfil the requirements of a high risk welding class which is expensive and time consuming for checking.
In an embodiment of the invention the first section comprises a first end close to the connection geometry and a second end remote from the connection geometry, wherein the first end is arranged at a lower height in direction of gravity than the second end, and the second section comprises a first end close to the connection geometry and a second end remote from the connection geometry, wherein the second end is arranged at a lower height in direction of gravity than the first end. With this construction the air entering the second section can no longer escape from the pipe via the connection geometry, since the air, which is heavier than the refrigerant, cannot flow back against the force of gravity from the second end of the second section remote from the connection geometry to the first end close to the connection geometry. Accordingly, the non-condensable gases are trapped in the pipe with the venting means as only exit. Non-condensable gas from the refrigerant system once purged is not again subjected to a purging process.
In an embodiment of the invention the second end of the first section and the first end of the second section are connected by a third section which is inclined upwardly. Condensable gas which condenses in the third section can flow back to the connection geometry.
In an embodiment of the invention the pipe comprises a fourth section which is inclined downwardly and connects the second section and a liquid outlet. Condensable gas which condenses in the second and fourth section can flow directly to the liquid outlet.
In an embodiment of the invention the liquid outlet is connected to the first section by means of a liquid trap. A liquid trap allows only liquid to escape but prevents the escape of any gases.
In an embodiment of the invention the liquid trap comprises a duct from the liquid outlet to an inlet opening in the first section, wherein the liquid outlet is arranged higher than a lower end of the inlet opening and lower than an upper end of the inlet opening. In this way it can be achieved that liquid entering the liquid outlet displaces liquid in the liquid trap without forming a larger liquid volume within the pipe. ln an embodiment of the invention the pipe comprises a fifth section connecting the fourth section to the venting means. The venting means can be arranged at a position higher in direction of gravity.
In an embodiment of the invention the fifth section is at least partly inclined upwardly. Accordingly, condensable gases condensing inside the fifth section can flow back to the liquid outlet.
In an embodiment of the invention the cooling means act on the fourth section and the fifth section. The fourth section and the fifth section can be made straight and can be made longer than the other sections, so that in these sections the condensing efficiency is the greatest.
In an embodiment of the invention a filler element is arranged in the fifth section. It is assumed that most of the condensable gases are already condensed in the fifth section and most part of the gas consists of non condensable gases. Accordingly, the volume needed is smaller.
In an embodiment of the invention the fourth section comprises a first cooling jacket and the fifth section comprises a second cooling jacket, wherein the first cooling jacket comprises an inlet at one end and a connection to the second jacket at another end. Accordingly, the coolant which is used to remove heat from the pipe can flow through the first jacket, the connection, and the second jacket in a circulation.
In an embodiment of the invention the pipe has an inner diameter of 25 mm or less. A small diameter facilitates the low welding risk classification. When having such a small inner diameter, no certified welders and X-ray scanning of the weldings are necessary. It is sufficient to rely solely on pressure testing of the weldings. A preferred embodiment will now be described in more detail with reference to the drawing, wherein:
Fig. 1 shows schematically an apparatus for removing non
condensable gases from a refrigerant, and
Fig. 2 shows the pipe arrangement in more detail.
Fig. 1 shows an apparatus 1 for removing non-condensable gases from a refrigerant. The apparatus 1 can also be named "air purger".
The apparatus 1 comprises a pipe arrangement 2. The pipe arrangement 2 comprises a pipe 3, cooling means 4 for the pipe and a connection geometry 5 for a connection to a refrigerant system (not shown in the drawing). The apparatus 1 can directly be connected to the refrigerant system. The refrigerant system is operated with an ammonia-refrigerant. The refrigerant can have a pressure in a range from 6 to 25 bar, depending on where in the refrigeration system the air purger is arranged.
The pipe 3 has in inner diameter of 25 mm or less to facilitate the low welding risk classification. When the inner diameter does not exceed the 25 mm a certified welder is not required and X-ray testing of the weldings is not necessary. It is sufficient to rely solely on pressure testing of the weldings.
The pipe arrangement 2 is shown in more detail in Fig. 2. Same reference numerals are used for the same elements.
The pipe 3 comprises a first section 6 which is oriented vertically, i.e. parallel to the direction of gravity. The first section 6 is connected to the connection geometry 5. The first section 6 is connected to a second section 7 via a third section 8. The second section 7 is connected to a fourth section 9 which connects the second section 7 to a liquid outlet 10. The fourth section 9 is connected to a fifth section 1 1. The fifth section 1 1 comprises at an end 12 venting means 13 in a position remote from the liquid outlet 10.
The first section 6 comprises a first end 14 close to the connection geometry 5 and a second end 15 remote from the connection geometry 5. The second section 7 comprises a first end 16 closer to the connection geometry 5 and a second end 17 remote from the connection geometry 5. The terms "close" and "remote" relate to a distance through which a gas has to flow from the connection geometry 5 to the respective ends.
As it comes out from Fig. 2, the first end 14 of the first section 6 is arranged at a lower height in direction of gravity than the second end 15. Likewise, the second end 17 of the second section 7 is arranged at a lower height in gravity direction than the first end 16.
Since air and other non-condensable gases are heavier than the refrigerant vapour, the non-condensable gases cannot escape from the pipe 3 once they have entered the second section 7.
The third section 8 is slightly inclined upwardly with the effect that refrigerant or condensable gases which condense in the third section 8 can directly flow back to the connection geometry 5. However, since the gravity works only with a rather small component on the non-condensable gas in the third section 8 this non-condensable gas is not driven back to the connection geometry 5. The fourth section 9 is slightly inclined downwardly and the fifth section 11 is slightly inclined upwardly over a large part of its length. A U-shaped part 18 of the fifth section 1 1 connects to the fourth section 9.
The fourth section 9 is surrounded by a first cooling jacket 19 and the fifth section 1 1 is surrounded by a second cooling jacket 20 at least over its straight part. The first cooling jacket 19 is supplied with a cooling medium from the cooling means 4 via an inlet pipe 21. The first cooling jacket 19 is connected to the second cooling jacket 20 by means of a connecting pipe 22 and the other end of the second cooling jacket 20 is connected to the cooling means by means of an outlet pipe 23.
The liquid outlet is connected to an inlet opening 24 in the first section 6, more precisely in a lower part of the first section 6 of the pipe 3. This connection is made by means of a liquid trap 25. The liquid trap 25 comprises a duct 26 which is arranged in a position lower than the fourth section 9.
As can be seen in Fig. 2, the liquid outlet 10 is arranged higher than a lower end of the inlet opening 24 and lower than an upper end of the inlet opening 24. Accordingly, in the duct 26 there is permanently a volume of liquid 27 which prevents a flow of gas through the duct 26.
As soon as the level of the liquid 27 in duct 26 rises, the liquid flows over into the first section 6 and from there to the connection geometry 5. On the other hand, it is hardly possible that a larger volume of liquid collects within the fourth section 9.
The operation of the air purger can be described as follows: When the connection geometry 5 is connected to the refrigerant system, a gas containing condensable gases and non-condensable gases enters the pipe 3 via the connection geometry 5. This gas fills the interior of the pipe 3. The fourth section 9 and the fifth section 1 1 cool down to a temperature at which the condensable gases can condense. The liquid forming in this condensing process flows under the action of gravity to the liquid outlet 10 and from there through the liquid trap 25 back to the first section 6, however, without any gas. Non-condensable gases are trapped within pipe 3 once they have reached the second section 7. The non-condensable gases can escape only via venting means 13 at the end of the fifth section 1 1. The venting means 13 can comprise, for example, a controlled venting valve. The fifth section 1 1 comprises a filler element 28 reducing the free volume within the fifth section 1 1. In the fifth section 1 1 a large part of the
condensable gases has already been condensed and the filler element 28 is used to increase the heat transfer from the gas within the fifth section 1 1 to cooling medium within the second cooling jacket 20.

Claims

1. Apparatus (1 ) for removing non-condensable gases from a
refrigerant, said apparatus (1 ) comprising a pipe arrangement (2) having a pipe (3), cooling means (4) for the pipe (3), and venting means (13), wherein the pipe (3) comprises a connection geometry (5) for a connection to a refrigerant system, characterized in that the pipe (3) comprises at least a first section (6) and a second section (7) which are directed in different directions.
2. Apparatus according to claim 1 , characterized in that the first section (6) comprises a first end (14) close to the connection geometry and a second end (15) remote from the connection geometry (5), wherein the first end (14) is arranged at a lower height in direction of gravity than the second end (15), and the second section (7) comprises a first end (16) close to the connection geometry (5) and a second end (17) remote from the connection geometry (5), wherein the second end (17) is arranged at a lower height in direction of gravity than the first end (16).
3. Apparatus according to claim 2, characterized in that the second end (15) of the first section (6) and the first end (16) of the second section
(7) are connected by a third section (8) which is inclined upwardly.
4. Apparatus according to claim 2 or 3, characterized in that the pipe (3) comprises a fourth section (9) which is inclined downwardly and connects the second section (7) and a liquid outlet (10).
5. Apparatus according to claim 4, characterized in that the liquid outlet (10) is connected to the first section (6) by means of a liquid trap (25).
6. Apparatus according to claim 5, characterized in that the liquid trap (25) comprises a duct (26) from the liquid outlet (10) to an inlet opening (24) in the first section (6), wherein the liquid outlet (10) is arranged higher than a lower end of the inlet opening (24) and lower than an upper end of the inlet opening (24).
7. Apparatus according to any of claims 4 to 6, characterized in that the pipe comprises a fifth section (1 1 ) connecting the fourth section (9) to the venting means (13).
8. Apparatus according to claim 7, characterized in that the fifth section (1 1 ) is at least partly inclined upwardly.
9. Apparatus according to claim 7 or 8, characterized in that the cooling means (4) act on the fourth section (9) and the fifth section (1 1 ).
10. Apparatus according to any of claims 7 to 9, characterized in that a filler element (28) is arranged in the fifth section (1 1 ).
11. Apparatus according to any of claims 7 to 10, characterized in that the fourth section (9) comprises a first cooling jacket (19) and the fifth section (11 ) comprises a second cooling jacket (20), wherein the first cooling jacket (19) comprises an inlet (21 ) at one end and a connection (22) to the second jacket (20) at another end.
12. Apparatus according to any of claims 1 top 11 , characterized in that the pipe (3) has an inner diameter of 25 mm or less.
PCT/EP2019/067750 2018-07-06 2019-07-02 Apparatus for removing non-condensable gases from a refrigerant Ceased WO2020007866A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US17/044,395 US11365919B2 (en) 2018-07-06 2019-07-02 Apparatus for removing non-condensable gases from a refrigerant
CN201980036074.1A CN112204323B (en) 2018-07-06 2019-07-02 Apparatus for removing non-condensable gases from a refrigerant

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP18182229.7A EP3591316B1 (en) 2018-07-06 2018-07-06 Apparatus for removing non-condensable gases from a refrigerant
EP18182229.7 2018-07-06

Publications (1)

Publication Number Publication Date
WO2020007866A1 true WO2020007866A1 (en) 2020-01-09

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US (1) US11365919B2 (en)
EP (1) EP3591316B1 (en)
CN (1) CN112204323B (en)
WO (1) WO2020007866A1 (en)

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EP3587962B1 (en) 2018-06-22 2020-12-30 Danfoss A/S A method for terminating defrosting of an evaporator by use of air temperature measurements
EP3587964B1 (en) 2018-06-22 2021-07-21 Danfoss A/S A method for terminating defrosting of an evaporator
EP3591316B1 (en) 2018-07-06 2026-03-04 Danfoss A/S Apparatus for removing non-condensable gases from a refrigerant
EP3712434B1 (en) 2019-03-20 2021-12-22 Danfoss A/S Check valve damping

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