Method for filling mixed refrigerant containing 2,3,3,3-tetrafluoropropene

Patent metadata

Field	Value
Publication number	US-9528735-B2
Application number	US-201314425485-A
Country	US
Kind code	B2
Filing date	Sep 4, 2013
Priority date	Sep 4, 2012
Publication date	Dec 27, 2016
Grant date	Dec 27, 2016

Abstract

A principal object of the present invention is to provide a method for filling a refrigerant mixture. According to this method, when a non-azeotropic refrigerant mixture comprising HFC-32 and HFO-1234yf is transferred, changes in the composition that occur during the transfer can be made to fall within an acceptable range in terms of refrigerant properties.

First claim

The invention claimed is:

1. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a feeding container,
adjusting, immediately before the transfer, the proportion (initial composition) of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container to x+y 1 wt % (minimum value) to x+a wt % (maximum value), so that the proportion of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container falls within a range of ±a wt % of a target composition (x) of the difluoromethane during initiation and completion of the transfer,
wherein ±a is a set tolerance (a≧0); x is a target composition with the proviso that 10≦x≦90, excluding a range satisfying an inequality: y 1 >a; and y 1 is a lower limit of a gap between the target composition and the initial composition, and is represented by Equation (1) below:
1000 y 1 =L 1 x 3 −M 1 x 2 +N 1 x−P 1   (1),

wherein L 1 =0.0002a+0.016, M 1 =0.072a+3.4761, N 1 =7.914a+187.52, and P 1 =1194.8a−9.58.

2. The method for filling a refrigerant mixture according to claim 1 , wherein the value a satisfies 0.5≦a≦3.0.

3. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a feeding container that is filled with the refrigerant mixture in an amount equal to or less than 70 wt % of a maximum filling amount of the refrigerant mixture,
adjusting, immediately before the transfer, the proportion (initial composition) of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container to x+y 2 wt % (minimum value) to x+a wt % (maximum value), so that the proportion of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container falls within a range of ±a wt % of a target composition (x) of the difluoromethane during initiation and completion of the transfer,
wherein ±a is a set tolerance (a≧0); x is a target composition with the proviso that 10≦x≦90, excluding a range satisfying y 2 >a; and y 2 is a lower limit of a gap between the target composition and the initial composition, and is represented by Equation (6) below:
1000 y 2 =L 2 x 3 −M 2 x 2 +N 2 x−P 2   (6),

wherein L 2 =−0.0016a+0.0169, M 2 =−0.1765a+3.4316, N 2 =−1.87a+180.08, and P 2 =1119.5a+148.9.

4. The method for filling a refrigerant mixture according to claim 3 , wherein the value a satisfies 0.5≦a≦3.0.

5. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a feeding container,
adjusting, immediately before the transfer, the proportion (initial composition) of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container to x+y 3 wt % (minimum value) to x+a wt % (maximum value), so that the proportion of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container falls within a range of ±a wt % of a target composition (x) of the difluoromethane during initiation and completion of the transfer, wherein ±a is a set tolerance (a≧0); x is a target composition with the proviso that 10≦x≦90, excluding a range satisfying an inequality: y 3 >a; and y 3 is a lower limit of a gap between the target composition and the initial composition, and is represented by Equation (11) below:
1000 y 3 =L 3 x 3 −M 3 x 2 +N 3 x−P 3   (11),

wherein L 3 =0.0003a+0.0172, M 3 =0.0962a+3.6851, N 3 =9.704a+196.9, and P 3 =1241.2a−93.54.

6. The method for filling a refrigerant mixture according to claim 5 , wherein the value a satisfies 0.5≦a≦3.0.

7. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a feeding container,
adjusting, immediately before the transfer, the proportion (initial composition) of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container to x+y 4 wt % (minimum value) to x+2.0 wt % (maximum value), so that the proportion of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container falls within a range of ±2.0 wt % of a target composition (x) of the difluoromethane during initiation and completion of the transfer, wherein b is an amount (wt %) initially filled into the feeding container; x is a target composition with the proviso that 10≦x≦90, excluding a range satisfying an inequality: y 4> 2; and y 4 is a lower limit of a gap between the target composition and the initial composition, and is represented by Equation (16) below:
1000 y 4 =L 4 x 3 −M 4 x 2 +N 4 x−P 4   (16),

wherein L 4 =0.0001b+0.0081, M 4 =0.0195b+1.958, N 4 =0.9878b+118.91, and P 4 =−0.176b+2408.7.

8. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a feeding container,
adjusting, immediately before the transfer, the proportion (initial composition) of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container to x+y 5 wt % (minimum value) to x+1.5 wt % (maximum value), so that the proportion of the difluoromethane in the liquid phase of the refrigerant mixture in the feeding container falls within a range of ±1.5 wt % of a target composition (x) of the difluoromethane during initiation and completion of the transfer,
wherein b is an amount (wt %) initially filled into the feeding container; x is a target composition with the proviso that 10≦x≦90, excluding a range satisfying an inequality: y 5 >1.5; and y 6 is a lower limit of a gap between the target composition and the initial composition, and is represented by Equation (22) below:
1000 y 6 =L 6 x 3 −M 6 x 2 +N 6 x−P 5   (22),

wherein L 5 =0.00005b 0.0092, M 5 =0.0171b+2.1013, N 5 =0.8528b+125.11, and P 5 =−2.372b+1972.3.

9. A method for filling a refrigerant mixture comprising difluoromethane and 2,3,3,3-tetrafluoropropene, the difluoromethane being present in a liquid phase in an amount of 10 to 18.5 wt % or 60 to 90 wt % based on 100 wt % of the total of the difluoromethane and 2,3,3,3-tetrafluoropropene,
the method comprising, in transferring the refrigerant mixture in a liquid state to a target container or equipment from a fee

Assignees

• Daikin Ind Ltd

Inventors

• Kuroki Hitomi
• Tsuchiya Tatsumi
• Yamada Yasufu
• Shibanuma Takashi

Classifications

• F25B2345/001

  Charging refrigerant to a cycle · CPC title

• C09K5/04

  the change of state being from liquid to vapour or vice versa · CPC title

• F25B45/00 Primary

  Arrangements for charging or discharging refrigerant · CPC title

• F25B1/00

  Compression machines, plants or systems with non-reversible cycle (F25B3/00, F25B5/00, F25B6/00, F25B7/00, F25B9/00 take precedence) · CPC title

• C09K2205/126

  Unsaturated fluorinated hydrocarbons · CPC title