JP2006214611A - Refrigerating device - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To cool the inside of a refrigerator down to ultra-low temperature of -60°C or less without deteriorating lubricating oil by adopting ammonia as refrigerant. <P>SOLUTION: This refrigerating device 1 is composed of a main refrigerating device 1A provided with at least a two-stage compressor 3, a condenser 4, an expansion valve 5, and an evaporator 2 using ammonia as refrigerant and an auxiliary refrigerating device 1B provided with at least a single-stage compressor 9, a condenser 10, an expansion valve 11, and an evaporator 8 using ammonia as refrigerant. A circulation circuit 13 for condenser cooling water having a circulation pump 14 is provided between the condenser 4 of the main refrigerating device 1A and the evaporator 8 of the auxiliary refrigerating device 1B. For this reason, by supplying condenser cooling water cooled in the evaporator 8 of the auxiliary refrigerating device 1B to the condenser 4 of the main refrigerating device 1A through the circulation pump 14, condensation temperature of refrigerant gas can be reduced below the temperature obtained when it is condensed by cooling water having normal temperature. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a refrigeration apparatus, and more particularly to a refrigeration apparatus that uses ammonia as a refrigerant.

  In general, a two-stage compression refrigeration apparatus using an HCFC refrigerant such as R22 is widely used as an ultra-low temperature refrigeration apparatus exceeding -60 ° C. In particular, in deep sea fishing boats, in order to maintain the freshness of frozen fish, an ultra-low temperature of −60 ° C. in a freezer compartment and −55 to −60 ° C. in a fishhouse is realized by a two-stage compression refrigeration system using R22 as a refrigerant. Yes.

  Moreover, in the ultra-low temperature refrigerated warehouse on land, it implement | achieves with the binary freezing apparatus by the combination of R717 / R23 or R22 / R23 etc. as a refrigerant | coolant.

  However, in recent years, due to the growing interest in the global environment, such as the destruction of the ozone layer, the use of HCFC-based refrigerants and HFC-based refrigerants that are alternative refrigerants is unavoidable. Therefore, its use is a concern. Therefore, in Japan, as for HCFC-based refrigerants, it has been decided to completely abolish new properties with the goal of 2010, and an ultra-low temperature refrigeration system using refrigerants instead of this is required.

On the other hand, in the past, ammonia has been actively used as a refrigerant and has begun to be used again as a countermeasure against global warming in recent years (see, for example, Patent Document 1).
JP 2000-146327 A

  By the way, ammonia has a characteristic that the temperature rise in the compression process is larger than that of other refrigerants. For example, the current general-purpose refrigerant R22 has an evaporation temperature of −15 ° C., a condensation temperature of + 30 ° C., a suction superheat degree of 0 ° C., and a compressor discharge temperature of about + 55 ° C. (in the case of single-stage compression). Is an evaporation temperature of −15 ° C., a condensation temperature of + 30 ° C., a suction superheat degree of 0 ° C., and a compressor discharge temperature of about + 98 ° C. (in the case of single stage compression).

  On the other hand, in order to cool the inside of the refrigerator to −60 ° C. or lower, first, two-stage compression is conceivable, but in order to obtain the internal temperature of −60 ° C. or lower, the evaporation temperature needs to be −70 ° C. or lower. In the case of fishing boats, it is not uncommon to operate in the tropical region. In this case, the condensation temperature is + 40 ° C, so that the superheat degree of the intake gas in each stage of the compressor is + 5 ° C, and the low to high stage ratio. In the case of = 3: 1, the temperature of the refrigerant gas (ammonia gas) discharged from the compressor is + 192 ° C.

  That is, the condensation temperature of ammonia as a refrigerant is + 40 ° C., the evaporation temperature is −70 ° C., the superheat degree of the suction gas at each stage in the compressor is + 5 ° C., and the two-stage compression is performed under the condition of the low / high stage ratio = 3: 1. As is apparent from the Mollier diagram of FIG. 7 showing the temperature change of the compression process in the adiabatic compression when the refrigeration apparatus is operated, the discharge temperature of ammonia gas after high-stage compression is theoretically + 192 ° C. (with a compressor) It becomes about + 172 ° C. with a thermometer.

  In the refrigeration apparatus, the lubricating oil of the compressor circulates in the apparatus together with the refrigerant. However, the lubricating oil is denatured when exposed to a temperature of + 170 ° C. (about + 150 ° C. with a thermometer with a compressor). Therefore, when the ammonia two-stage compression refrigeration system is operated at a condensation temperature of + 40 ° C., the compressor discharge temperature is less than + 170 ° C. (about + 150 ° C. with a thermometer with a compressor) at which the lubricating oil is not denatured. The temperature is limited to about −60 ° C. More specifically, a two-stage compression refrigeration system with a condensing temperature of + 40 ° C., an evaporation temperature of −60 ° C., a superheat degree of intake gas at each stage of the compressor of + 5 ° C., and a low / high stage ratio = 3: 1. Is operated, the temperature of the compressed refrigerant gas is theoretically + 165 ° C. (about + 145 ° C. with a thermometer with a compressor) (see the Mollier diagram in FIG. 8).

  On the other hand, as described above, in order to obtain an ultra-low temperature for cooling the refrigerator interior temperature to -50 ° C or lower, the evaporation temperature must be lowered to -60 ° C or lower. It is clear that ultra-low temperature operation in a compression refrigeration system is impossible.

  In the case of a binary refrigeration system, a combination of ammonia / R23 is conceivable. However, R23 is an HFC-based refrigerant, and its influence on global warming is unavoidable and is not preferred for use.

  The present invention has been made in view of such problems, and employs ammonia as a refrigerant so that the refrigerator can be cooled to an ultralow temperature of −60 ° C. or lower without causing deterioration of the lubricating oil. A device is provided.

  The present invention includes at least one or a plurality of two-stage compressors, one condenser, one or a plurality of expansion valves and evaporators corresponding to each of the two-stage compressors using ammonia as a refrigerant. A main refrigeration apparatus, a sub refrigeration apparatus including at least one single-stage compressor, a condenser, an expansion valve, and an evaporator using ammonia as a refrigerant; and a condenser of the main refrigeration apparatus and an evaporator of the sub refrigeration apparatus A condenser cooling water circulation circuit having a circulation pump, and circulating the refrigerant of the sub refrigeration unit in the order of the single stage compressor of the sub refrigeration unit, the condenser, the expansion valve, and the evaporator. The condenser cooling water cooled by the evaporator of the refrigeration apparatus is supplied to the condenser of the main refrigeration apparatus via a circulation pump.

  According to the present invention, by operating each of the main refrigeration apparatus and the sub refrigeration apparatus, ammonia as a refrigerant of the main refrigeration apparatus is circulated in the order of the two-stage compressor, the condenser, the expansion valve, and the evaporator. Ammonia as a refrigerant of the refrigeration apparatus can be circulated in the order of a single-stage compressor, a condenser, an expansion valve, and an evaporator. Then, by driving the circulation pump of the circulation circuit, the condenser cooling water circulates between the evaporator of the sub refrigeration apparatus and the condenser of the main refrigeration apparatus, and is cooled by the evaporator of the sub refrigeration apparatus. Cooling water can be supplied to the condenser of the main refrigeration unit. By using this cooled condenser cooling water, the condensing temperature of the refrigerant gas in the main refrigeration apparatus can be lowered as compared with the case of condensing with normal temperature cooling water. For example, when the temperature of the condenser cooling water is + 10 ° C., the condensation temperature of ammonia gas in the main refrigeration apparatus is + 15 ° C.

  As a result, when the main refrigeration system is operated under the conditions of the condensation temperature + 15 ° C., the evaporation temperature −70 ° C., the superheat degree 5 ° C. of the suction gas at each stage of the compressor, and the low / high stage ratio 3: 1, the compressor discharge gas temperature is The lubricating oil does not deteriorate and is maintained at + 143 ° C. (about 123 ° C. with a thermometer with a compressor) or lower. Therefore, ammonia can be employed as the refrigerant, and the internal temperature can be maintained at an ultra-low temperature of −60 ° C. or less without deteriorating the lubricating oil.

  The present invention uses ammonia as a refrigerant and corresponds to one or a plurality of two-stage compressors, a two-stage compressor that can be switched to one single-stage compressor, one condenser, and each two-stage compressor. A main refrigeration apparatus including at least a plurality of expansion valves and an evaporator, a sub-refrigeration apparatus using ammonia as a refrigerant and including at least one single-stage compressor, a condenser, an expansion valve, and an evaporator, and a main refrigeration A condenser cooling water circulation circuit provided with a circulation pump, a two-stage compressor and a sub-refrigeration unit that can be switched to a single-stage compressor. Connected to the low-stage suction port side and high-stage discharge port side of the two-stage compressor that can be switched to the single-stage compressor, and the single-stage compressor suction side and discharge port side. A single-stage compressor instead of the single-stage compressor of the sub-refrigeration system Using the switchable two-stage compressor as a single-stage compressor, the refrigerant of the sub-refrigeration unit is circulated through the bypass circuit in the order of the condenser of the sub-refrigeration unit, the expansion valve, and the evaporator to evaporate the sub-refrigeration unit The condenser cooling water cooled by the cooler is supplied to the condenser of the main refrigeration apparatus via a circulation pump.

  According to the present invention, by operating each of the main refrigeration apparatus and the sub refrigeration apparatus, ammonia as a refrigerant of the main refrigeration apparatus is circulated in the order of the two-stage compressor, the condenser, the expansion valve, and the evaporator. Ammonia as a refrigerant of the refrigeration apparatus can be circulated in the order of a single-stage compressor, a condenser, an expansion valve, and an evaporator. Then, by driving the circulation pump of the circulation circuit, the condenser cooling water circulates between the evaporator of the sub refrigeration apparatus and the condenser of the main refrigeration apparatus, and is cooled by the evaporator of the sub refrigeration apparatus. Cooling water can be supplied to the condenser of the main refrigeration unit.

  On the other hand, when the single-stage compressor of the sub-refrigeration system cannot be operated due to a failure or the like, the sub-refrigeration is switched by switching the two-stage compressor that can be switched to the single-stage compressor to the single-stage compressor. It can replace with the single stage compressor of an apparatus, and can be used as a single stage compressor. In this case, the ammonia as the refrigerant of the main refrigeration apparatus can be circulated in the order of the two-stage compressor, the condenser, the expansion valve, and the evaporator, and the ammonia as the refrigerant of the sub refrigeration apparatus via the bypass circuit The two-stage compressor switched to the single-stage compressor, the condenser, the expansion valve, and the evaporator can be circulated in this order. Then, by driving the circulation pump of the circulation circuit, the condenser cooling water circulates between the evaporator of the sub refrigeration apparatus and the condenser of the main refrigeration apparatus, and is cooled by the evaporator of the sub refrigeration apparatus. Cooling water can be supplied to the condenser of the main refrigeration unit.

  For this reason, even if it is a case where the single stage compressor of a sub-refrigeration apparatus fails, the condensation temperature of refrigerant gas can be made lower than the case where it condenses with normal temperature cooling water. For example, when the temperature of the condenser cooling water is + 10 ° C., the condensation temperature of ammonia gas in the main refrigeration apparatus is + 15 ° C.

  As a result, when the main refrigeration system is operated under the conditions of the condensation temperature + 15 ° C., the evaporation temperature −70 ° C., the superheat degree 5 ° C. of the suction gas at each stage of the compressor, and the low / high stage ratio 3: 1, the compressor discharge gas temperature is The lubricating oil does not deteriorate and is maintained at + 143 ° C. (about 123 ° C. with a thermometer with a compressor) or lower. Therefore, ammonia can be employed as the refrigerant, and the internal temperature can be maintained at an ultra-low temperature of −60 ° C. or less without deteriorating the lubricating oil.

  According to the present invention, ammonia can be used as the refrigerant, and the inside of the refrigerator can be cooled to an ultralow temperature of −60 ° C. or lower without causing deterioration of the lubricating oil.

  Hereinafter, embodiments of the present invention will be described with reference to the drawings.

  FIG. 1 shows an embodiment of a refrigeration apparatus 1 according to the present invention.

  The refrigeration apparatus 1 includes a main refrigeration apparatus 1A and a sub refrigeration apparatus 1B.

  The main refrigeration apparatus 1A is compressed by an evaporator 2 provided in a refrigerator (not shown), a two-stage compressor 3 that sucks and compresses refrigerant gas (ammonia gas) evaporated in the evaporator 2, and a two-stage compressor 3. The condenser 4 that condenses the refrigerant gas and the expansion valve 5 that expands the condensed refrigerant liquid (ammonia liquid). The inside is frozen by taking it away.

  Here, as shown in FIG. 2, the two-stage compressor 3 includes a low-stage suction port 3a for sucking the refrigerant gas from the evaporator 2 and a low-stage discharge port for discharging the refrigerant gas compressed in the first stage. 3b, a high stage suction port 3c for sucking the compressed refrigerant gas in the first stage, and a high stage discharge port 3d for discharging the refrigerant gas compressed in the second stage to the condenser 4, A gas cooler 6 for cooling the refrigerant gas is disposed in a pipe line connecting the discharge port 3b and the high-stage suction port 3c.

  The pipe connecting the condenser 4 and the expansion valve 5 is provided with a liquid receiver 7 for storing the refrigerant liquid condensed by the condenser 4. An oil separator that separates the lubricating oil from the compressed gas discharged from the high-stage discharge port 3 d of the compressor 3 is provided in a pipe line that connects the high-stage discharge port 3 d of the two-stage compressor 3 and the condenser 4. Yes.

  The sub-refrigeration apparatus 1B includes an evaporator 8, a single-stage compressor 9 that sucks and compresses refrigerant gas (ammonia gas) evaporated by the evaporator 8, and a condensation that condenses the refrigerant gas compressed by the single-stage compressor 9. It is mainly comprised from the container 10 and the expansion valve 11 which expands the condensed refrigerant | coolant liquid (ammonia liquid). The conduit connecting the condenser 10 and the expansion valve 11 is provided with a liquid receiver 12 for storing the refrigerant liquid condensed by the condenser 10, and although not shown in detail, An oil separator that separates the lubricating oil from the compressed gas discharged from the discharge port 9 b of the stage compressor 9 is provided in a pipe that connects the discharge port 9 b of the single-stage compressor 9 and the condenser 10.

  By the way, between the condenser 4 of the main refrigeration apparatus 1A and the evaporator 8 of the sub refrigeration apparatus 1B, a circulation circuit 13 for circulating condenser cooling water such as fresh water, seawater, and brine is provided. The condenser cooling water can be circulated between the condenser 4 of the main refrigeration apparatus 1A and the evaporator 8 of the sub refrigeration apparatus 1B through a circulation pump 14 disposed in the circulation circuit 13. For this reason, the condenser cooling water cooled by the evaporator 8 of the sub refrigeration apparatus 1B can be supplied to the condenser 4 of the main refrigeration apparatus 1A.

  In addition, normal temperature cooling water, for example, seawater, is supplied to the condenser 10 of the sub-refrigeration apparatus 1 </ b> B via the cooling water pump 15.

  Next, the operation of the refrigeration apparatus 1 configured as described above will be described.

  First, in the main refrigeration apparatus 1A, ammonia as a refrigerant is sucked into the low-stage suction port 3a of the two-stage compressor 3, compressed by the first-stage compression mechanism, and then discharged from the low-stage discharge port 3b. After being cooled by the gas cooler 6 and sucked into the high-stage suction port 3c and compressed again by the second-stage compression mechanism, it becomes high-temperature and high-pressure refrigerant gas and is discharged from the high-stage discharge port 3d.

  Next, the discharged refrigerant gas is supplied to the condenser 4 after the lubricating oil is separated by an oil separator (not shown), condensed by the condenser 4, and becomes a high-pressure refrigerant liquid. 7 flows into the expansion valve 5. Then, the refrigerant liquid becomes wet gas by the expansion valve 5 and is sent to the evaporator 2, evaporates in the evaporator 2, performs a cooling action, and then serves as a refrigerant gas as a low-stage suction port of the two-stage compressor 3. It is sucked into 3a and compressed again by the first stage compression mechanism.

  Also in the sub-refrigeration apparatus 1B, ammonia as a refrigerant is sucked into the suction port 9a of the single-stage compressor 9, compressed by the compression mechanism, and then discharged as a high-temperature and high-pressure refrigerant gas from the discharge port 9b. The The discharged refrigerant gas is supplied to the condenser 10 after the lubricating oil is separated by an oil separator (not shown), condensed by the condenser 10, and becomes a high-pressure refrigerant liquid. 12 flows into the expansion valve 11. Then, the refrigerant liquid becomes wet gas by the expansion valve 11 and is sent to the evaporator 8, evaporates in the evaporator 8, performs a cooling action, and then enters the inlet 9 a of the single-stage compressor 9 as superheated gas. Inhaled and compressed again by the compression mechanism.

  Here, when the circulation pump 14 of the circulation circuit 13 is driven, the condenser cooling water circulates between the evaporator 8 of the sub-refrigeration apparatus 1B and the condenser 4 of the main refrigeration apparatus 1A. At this time, the condenser cooling water is cooled by the evaporator 8 of the sub refrigeration apparatus 1B and supplied to the condenser 4 of the main refrigeration apparatus 1A, and the refrigerant gas of the condenser 4 in the main refrigeration apparatus 1A is cooled to perform the sub refrigeration. It will return to the evaporator 8 of the apparatus 1B. That is, the refrigerant gas of the main refrigeration apparatus 1A is cooled by the condenser cooling water, and condenses at a lower temperature than when normal temperature cooling water is used. Specifically, when the temperature of the condenser cooling water is + 10 ° C., the condensing temperature of the refrigerant gas in the main refrigeration apparatus 1A is about + 15 ° C.

  In such a refrigeration apparatus 1, the condensation temperature is + 15 ° C., the evaporation temperature is −70 ° C., the superheat degree of the suction gas in each stage in the two-stage compressor 3 is + 5 ° C., and the low / high stage ratio = 3: 1. The temperature change in the compression process in adiabatic compression is shown in the Mollier diagram of FIG. As is apparent from the Mollier diagram of FIG. 3, the temperature of the refrigerant gas after compression is + 143 ° C. (about 123 ° C. with a thermometer with a compressor).

  As a result, the temperature of the compressed refrigerant gas becomes + 170 ° C. or lower, so that the lubricating oil circulating in the apparatus together with the refrigerant is not denatured, and ammonia is used as the refrigerant, leading to deterioration of the lubricating oil. And an ultra-low temperature of −60 ° C. or lower can be obtained.

  That is, when installing a refrigeration facility for a pelagic fishing boat, instead of the HCFC or HFC two-stage compression refrigeration equipment, the main refrigeration equipment of the ammonia two-stage compression refrigeration equipment is installed, the sub-refrigeration equipment having an ammonia single-stage compressor, and the circulation By adding a circuit, an ultra-low temperature of −60 ° C. or lower can be obtained. This can be handled regardless of new equipment or existing equipment.

  In the above-described embodiment, the refrigeration apparatus for a pelagic fishing boat has been described as an example. However, it is needless to say that the invention can be applied to a refrigeration apparatus for land as well as a fishing boat.

  FIG. 4 shows a modification of the embodiment of the refrigeration apparatus 1 described above.

Also in this embodiment, the refrigeration apparatus 1 includes a main refrigeration apparatus 1A and a sub refrigeration apparatus 1B. In the main refrigeration apparatus 1A of this embodiment, a plurality of two-stage compressors 3 ₁ and 3 ₂ are used. In addition, a plurality of evaporators 2 ₁ and 2 ₂ and expansion valves 5 ₁ and 5 ₂ are used corresponding to the two-stage compressors 3 ₁ and 3 ₂ , respectively.

  Also in this embodiment, the main refrigeration apparatus 1A and the sub refrigeration apparatus 1B are operated, and when the circulation pump 14 is driven, the space between the evaporator 8 of the sub refrigeration apparatus 1B and the condenser 4 of the main refrigeration apparatus 1A. The condenser cooling water circulates, and the condenser cooling water cooled by the evaporator 8 of the sub-refrigeration apparatus 1B can be supplied to the condenser 4 of the main refrigeration apparatus 1A. Therefore, the refrigerant gas of the condenser 4 in the main refrigeration apparatus 1A is cooled by the condenser cooling water and condensed at a lower temperature than when the normal temperature cooling water is used. For example, when the temperature of the condenser cooling water is + 10 ° C., the condensing temperature of the refrigerant gas in the main refrigeration apparatus 1A is about + 15 ° C.

Also in this refrigeration apparatus 1, the condensation temperature is + 15 ° C., the evaporation temperature is −70 ° C., the superheat degree of the suction gas in each stage in the two-stage compressors 3 ₁ and 3 ₂ is + 5 ° C., and the low / high stage ratio = 3: 1. As is apparent from the Mollier diagram of FIG. 3 showing the temperature change in the compression process in the case of adiabatic compression, the temperature of the refrigerant gas after compression only rises to + 143 ° C.

  As a result, the temperature of the compressed refrigerant gas becomes + 170 ° C. or lower, so that the lubricating oil circulating in the apparatus together with the refrigerant is not denatured, and ammonia is used as the refrigerant, leading to deterioration of the lubricating oil. And an ultra-low temperature of −60 ° C. or lower can be obtained.

In this embodiment of the refrigeration apparatus, a plurality of two-stage compressors 3 ₁ , 3 ₂ are employed in the main refrigeration apparatus, so that the plurality of two-stage compressors 3 ₁ , 3 ₂ are driven simultaneously. The inside of the refrigerator can be quickly cooled, and if the inside of the refrigerator is frozen to a set temperature, it can be controlled to drive only one two-stage compressor.

  In the embodiment shown in FIG. 4, two two-stage compressors are exemplified as the plurality of two-stage compressors, but it is needless to say that three or more may be used.

By the way, in embodiment mentioned above, when the single stage compressor 9 of the sub-refrigeration apparatus 1B should be out of order, the condenser cooling water cannot be cooled. For this reason, the cooled condenser cooling water cannot be supplied to the condenser 4 of the main refrigeration apparatus 1A, and the condensation temperature of the refrigerant gas (ammonia gas) cannot be lowered to room temperature or lower. As a result, as described above, the temperature of the refrigerant gas discharged from the two-stage compressors 3, 3 ₁ , 3 ₂ is theoretically + 192 ° C. (about + 172 ° C. with a thermometer with a compressor). There is a risk of denaturing and degrading, leading to seizure of the two-stage compressors 3, 3 ₁ , 3 ₂ .

  In order to prepare for such a situation, FIGS. 5 and 6 show another embodiment of the refrigeration apparatus 1 of the present invention.

  The refrigeration apparatus 1 of this embodiment is also composed of a main refrigeration apparatus 1A and a sub refrigeration apparatus 1B.

  5 and 6, the same reference numerals are used for the same configurations as those in the above-described embodiment, and detailed description thereof will be omitted, and only different points will be described.

In the main refrigeration system 1A, of the plurality of two-stage compressors 3 ₁ and 3 ₃ , one of the two-stage compressors 3 ₃ employs a two-stage compressor that can be switched to a single-stage compressor. The two-stage compressor 3 _3, as shown in FIG. 6, except that valve 16 ₁ in the pipe between the low-stage discharge port 3b and the gas cooler 6 is disposed, the evaporator 2 ₂ and two-stage compression a conduit connecting the low-stage suction port 3a of the machine 3 _3, between the conduit that connects the gas cooler 6 and the two-stage compressor 3 ₃ of the high-stage suction port 3c, two-stage compression from the evaporator 2 ₂ machine 3 ₃ branch pipe which is disposed a check valve 17 ₁ which permits the flow of the refrigerant gas high-stage suction port 3c direction only are connected. Further, a conduit which connects the low-stage discharge port 3b of the stop valve 16 ₁ and two-stage compressor 3 ₃ described above, a conduit connecting the high-stage discharge port 3d and the condenser 4 of the two-stage compressor 3 ₃ between the branch pipe which is disposed a check valve 17 ₂ that allows the flow of the condenser 4 direction only refrigerant gas from the low-stage discharge port 3b of the two-stage compressor 3 ₃ are connected.

Thus when using switchable two-stage compressor 3 ₃ as a two-stage compressor in a single-stage compressor is operated in the open state of the check valve 16 _1. In this case, the refrigerant gas from the evaporator 2 ₂ is sucked into the low-stage suction port 3a, after being compressed by the first-stage compression mechanism is discharged from the low-stage discharge port 3b. Thereafter, the compressed refrigerant gas is sucked through the opened the stop valve 16 ₁ and the gas cooler 6 to the high-stage suction port 3c, after being compressed again by the second stage of the compression mechanism, the high-temperature high-pressure refrigerant gas And discharged from the high-stage discharge port 3d.

At this time, the pressure of the refrigerant gas before and after the check valve 17 ₁ is higher in the high-stage intake port 3c side than in the low-stage intake port 3a side because the first-stage compression is performed. Does not flow through the check valve 17 ₁ toward the high stage suction port 3c. The pressure before and after the refrigerant gas of the check valve 17 ₂ is, since the compression of the second stage being carried out, has a higher high-stage discharge port 3d side of the low-stage discharge port 3b side, the refrigerant gas It does not flow to the high-stage discharge port 3d side through the check valve 17 ₂ .

On the other hand, when using a switchable two-stage compressor 3 ₃ as single stage compressor single-stage compressor is operated in the closed state of the check valve 16 _1. When closing the stop valve 16 _1, refrigerant gas from the evaporator 2 ₂ is sucked into the low-stage suction port 3a, after being compressed by the first-stage compression mechanism is discharged from the low-stage discharge port 3b. Here, by stop valve 16 ₁ it is closed, the supply of the high-stage suction port 3c of the compressed refrigerant gas is shut off, the pressure of the high-stage suction port 3c side is reduced. For this reason, the refrigerant gas from the evaporator 2 ₂ is simultaneously sucked into the high stage suction port 3c via the check valve 17 ₁ , compressed by the second stage compression mechanism, and then discharged from the high stage discharge port 3d. Is done. The refrigerant gas compressed by the first-stage compression mechanism is supplied to the check valve 17 _2, the pressure in the low stage discharge port 3b side is increased. The refrigerant gas discharged from the high-stage discharge port 3d also, only one stage is compressed, the pressure of the low-stage discharge port 3b side of the check valve 17 ₂ is, even a little than the pressure of the high-stage discharge port 3d side becomes higher, it is supplied to the condenser 4 merges with the refrigerant gas discharged from the high stage discharge port 3d via the check valve 17 _2.

Further, in the main refrigeration system 1A, refrigerant gas is connected to the pipe connecting the evaporator 2 ₁ and the two-stage compressor 3 ₁ and the pipe connecting the evaporator 2 ₂ and the two-stage compressor 3 ₃ , respectively. Switching mechanisms 18 ₁ and 18 ₂ are provided, and a refrigerant gas switching mechanism 18 ₃ is also provided in the pipe line connecting the two-stage compressors 3 ₁ and 3 ₃ and the condenser 4.

Furthermore, the conduit connecting the evaporator 2 ₂ and the switching mechanism 18 _second pipe line connecting the and two-stage compressor 3 ₃ and the switching mechanism 18 _3, respectively three-way valve 19 _1, 19 ₂ are disposed In addition, a three-way valve 19 ₁ disposed in a line connecting the evaporator 2 ₂ and the switching mechanism 18 ₂ and a line connecting the evaporator 2 ₁ and the two-stage compressor 3 ₁ are disposed. A connecting pipe line is provided between the switching mechanism 18 ₁ .

Accordingly, the refrigerant gas in the evaporator 2 _2, and supplied to the three-way valve 19 ₁ and the switching mechanism 18 ₂ which can be switched by the single-stage compressor via a two-stage compressor 3 _3, or the three-way valve 19 ₁ and the switching mechanism The two-stage compressor 3 ₁ can be supplied via 18 ₁ .

Further, in the sub-refrigeration apparatus 1B, a three-way valve 19 ₃ is disposed in a pipe line connecting the evaporator 8 and the single-stage compressor 9, and the three-way valve 19 ₃ , the evaporators 2 _2, and 2 bypass line is connected between the switching mechanism 18 ₂ disposed in the conduit connecting the stage compressor 3 _3. Furthermore, the conduit connecting the condenser 10 and the single-stage compressor 9, stop valve 16 ₂ is disposed. Further, a bypass between the stop valve 16 ₂ and the pipe connecting the condenser 10, is disposed in the conduit connecting the two-stage compressor 3 ₃ and the switching mechanism 18 ₃ three-way valve 19 ₂ The pipeline is connected.

Accordingly, the stop valves 16 ₁ and 16 ₂ are closed, while the three-way valve 19 ₁ is switched so that the refrigerant gas of the evaporator 2 ₂ is supplied to the two-stage compressor 3 ₁ via the switching mechanism 18 _1. switches the three-way valve 19 ₃ to supply the two-stage compressor 3 ₃ through the bypass circuit and the switching mechanism 18 ₂ refrigerant gas of the evaporator 8 in the refrigeration apparatus 1B, a two-stage compressor 3 ₃ of the refrigerant gas By switching the three-way valve 19 ₂ to be supplied to the condenser 10 via the bypass circuit, the refrigerant gas of the evaporator 8 is switched to the three-way valve 19 ₃ , the bypass circuit, the switching mechanism 18 ₂ , and the single-stage compressor. The two-stage compressor 3 ₃ , the three-way valve 19 ₂ , the bypass circuit, the condenser 10, the liquid receiver 12 and the expansion valve 11 can be circulated in this order and supplied to the evaporator 8 again.

At this time, the refrigerant gas of the evaporator 2 ₂ in the main refrigeration apparatus 1A can be supplied to the two-stage compressor 3 ₁ via the three-way valve 19 ₁ and the switching mechanism 18 ₁ .

The condenser cooling water circulation circuit 13 is provided with three-way valves 19 ₄ and 19 ₅ , respectively. These three-way valves 19 ₄ and 19 ₅ circulate the cooling water in the condenser 10 of the sub-refrigeration apparatus 1B. Connected to the circuit. Therefore, when the operation of the auxiliary refrigeration apparatus 1B can no longer be continued, the three-way valves 19 ₄ and 19 ₅ can be switched to supply room temperature cooling water to the condenser 4 of the main refrigeration apparatus 1A.

Further, the conduit connecting the evaporator 8 and a three-way valve 19 ₃ is the evaporation pressure adjusting valve 20 is disposed, steam pressure of the refrigerant in the evaporator 8 of the secondary refrigeration system 1B is reduced unnecessarily Then, the condenser cooling water supplied to the condenser 4 of the main refrigeration apparatus 1A is controlled so as not to freeze in the evaporator 8 of the sub refrigeration apparatus 1B.

  Next, the operation of the refrigeration apparatus 1 configured as described above will be described.

In the initial state, stop valve 16 ₁ is opened, switchable two-stage compressor 3 ₃ a single stage compressor is configured to operate as a two-stage compressor.

The three-way valve 19 ₁ is switched to supply the refrigerant gas of the evaporator 2 ₂ to the two-stage compressor 3 ₃ via the switching mechanism 18 ₂ , and the three-way valve 19 ₂ is switched to the two-stage compressor 3 ₃ . The refrigerant gas is switched to be supplied to the condenser 4 via the switching mechanism 18 ₃ . Further, the three-way valve 19 ₃ is other are switched so as to supply the refrigerant gas in the evaporator 8 in the secondary refrigeration system 1B in single stage compressor 9, check valve 16 ₂ is opened, a single-stage compressor The refrigerant gas compressed by 9 can be led to the condenser 10.

Further, the three-way valves 19 ₄ and 19 ₅ of the circulation circuit 13 are respectively switched so that the condenser cooling water circulates between the evaporator 8 of the sub-refrigeration apparatus 1B and the condenser 4 of the main refrigeration apparatus 1A. Yes.

In such an initial state, when operating the refrigeration system 1, ammonia as a refrigerant in the main refrigerating apparatus 1A is sucked into the low-stage suction port 3a of the two-stage compressor 3 _1, it is compressed by the first-stage compression mechanism After that, it is discharged from the low-stage discharge port 3b, cooled by the gas cooler 6, sucked into the high-stage intake port 3c, and compressed again by the second-stage compression mechanism, and then becomes a high-temperature and high-pressure refrigerant gas. It is discharged from the stage discharge port 3d.

Then, the refrigerant gas discharged is supplied to the condenser 4 through the switching mechanism 18 _3, it is condensed by the condenser 4, and flows into the expansion valve 5 ₁ via the receiver 7 is a refrigerant liquid of a high pressure. Then, the refrigerant liquid is sent to the evaporator 2 ₁ becomes humid gas by the expansion valve 5 _1, after cooling operation evaporates in the evaporator 2 _1, through the switching mechanism 18 ₁ as a refrigerant gas two is sucked into the low-stage suction port 3a of the stage compressor 3 _1, it is compressed by the first-stage compression mechanism again.

Similarly in the two-stage compressor 3 _3, ammonia as the refrigerant is sucked into the low-stage suction port 3a, after being compressed by the first-stage compression mechanism is discharged from the low-stage discharge port 3b, the gas cooler 6 After being cooled by the air and sucked into the high stage suction port 3c and compressed again by the second stage compression mechanism, it becomes a high-temperature and high-pressure refrigerant gas and is discharged from the high stage discharge port 3d.

Next, the discharged refrigerant gas is supplied to the condenser 4 through the _three- way valve 19 ₂ and the switching mechanism 18 ₃ , is condensed by the condenser 4, becomes high-pressure refrigerant liquid, passes through the liquid receiver 7, and the expansion valve 5. Flows into ₂ . Then, the refrigerant liquid is sent to the evaporator 2 ₂ becomes humid gas by the expansion valve 5 _2, after the cooling operation evaporates in the evaporator 2 _2, three-way valve 19 ₁ and the switching mechanism as the refrigerant gas 18 ₂ is sucked into the low-stage suction port 3a of the two-stage compressor 3 ₃ through, is compressed by the first-stage compression mechanism again.

Also in the sub-refrigeration apparatus 1B, ammonia as a refrigerant is sucked into the suction port 9a of the single-stage compressor 9, compressed by the compression mechanism, and then discharged as a high-temperature and high-pressure refrigerant gas from the discharge port 9b. The The compressed refrigerant gas is supplied to the condenser 10 via the check valve 16 _2, is condensed by the condenser 10 flows into the expansion valve 11 via the liquid receiver 12 by a refrigerant liquid of a high pressure. Then, the refrigerant liquid is sent to the evaporator 8 as a wet gas by the expansion valve 11, evaporates in the evaporator 8, performs a cooling action, and then passes through the _three- way valve 193 as a refrigerant gas to provide a single-stage compressor. 9 is sucked into the suction port 9a and compressed again by the compression mechanism.

  Here, when the circulation pump 14 of the circulation circuit 13 is operated, the condenser cooling water circulates between the evaporator 8 of the sub-refrigeration apparatus 1B and the condenser 4 of the main refrigeration apparatus 1A. At this time, the condenser cooling water is cooled by the evaporator 8 of the sub refrigeration apparatus 1B and supplied to the condenser 4 of the main refrigeration apparatus 1A, and the refrigerant gas of the condenser 4 in the main refrigeration apparatus 1A is cooled to perform the sub refrigeration. It will return to the evaporator 8 of the apparatus 1B. That is, the refrigerant gas of the main refrigeration apparatus 1A is cooled by the condenser cooling water, and condenses at a lower temperature than when normal temperature cooling water is used. Specifically, when the temperature of the condenser cooling water is + 10 ° C., the condensing temperature of the refrigerant gas in the main refrigeration apparatus 1A is about + 15 ° C.

  For this reason, the temperature of the compression process in adiabatic compression when the condensation temperature is + 15 ° C., the evaporation temperature is −70 ° C., the superheat degree of the suction gas at each stage in the compressor 2 is + 5 ° C., and the low / high stage ratio = 3: 1. As is apparent from the Mollier diagram of FIG. 3 described above, the temperature of the refrigerant gas after compression is + 143 ° C.

  As a result, the temperature of the refrigerant gas after compression becomes + 170 ° C. (about + 150 ° C. with a thermometer with a compressor) or less, so that the lubricating oil circulating in the apparatus together with the refrigerant is not denatured, and ammonia is added to the refrigerant. It is possible to obtain an ultra-low temperature of −60 ° C. or less without causing deterioration of the lubricating oil.

On the other hand, as when a single-stage compressor 9 of the secondary refrigeration system 1B has any chance failure, it closes the stop valve 16 _1, operates a single-stage compressor switchable two-stage compressor 3 ₃ as single stage compressor Switch.

Further, the three-way valve 19 ₁ is switched so that the refrigerant gas of the evaporator 2 ₂ is supplied to the two-stage compressor 3 ₁ via the switching mechanism 18 ₁ , and the three-way valve 19 ₂ is switched to the two-stage compressor 3 ₃ . It switches so that refrigerant gas may be supplied to the condenser 10 of the sub-refrigeration apparatus 1B. Further, the three-way valve 19 ₃ is switched so as to supply the refrigerant gas of the evaporator 8 in the auxiliary refrigeration apparatus 1B to the switching mechanism 18 ₂ , and the stop valve 16 ₂ is closed.

In such a state, when operating the refrigeration system 1, the main refrigeration system 1A, the ammonia as the refrigerant is sucked into the low-stage suction port 3a of the two-stage compressor 3 _1, it is compressed by the first-stage compression mechanism After that, it is discharged from the low-stage discharge port 3b, cooled by the gas cooler 6, sucked into the high-stage intake port 3c, and compressed again by the second-stage compression mechanism, and then becomes a high-temperature and high-pressure refrigerant gas. It is discharged from the stage discharge port 3d. The refrigerant gas discharged is supplied to the condenser 4 through the switching mechanism 18 _3, it is condensed by the condenser 4, and flows into the expansion valve 5 ₁ via the receiver 7 is a refrigerant liquid of a high pressure. Then, the refrigerant liquid is sent to the evaporator 2 ₁ becomes humid gas by the expansion valve 5 _1, after cooling operation evaporates in the evaporator 2 _1, through the switching mechanism 18 ₁ as a refrigerant gas two is sucked into the low-stage suction port 3a of the stage compressor 3 _1, it is compressed by the first-stage compression mechanism again.

Incidentally, the refrigerant liquid that flows through the expansion valve 5 ₂ from the receiver 7 is sent to the evaporator 2 ₂ becomes humid gas by the expansion valve 5 _2, was cooled action evaporated in the evaporator 2 ₂ Thereafter, the refrigerant gas is sucked into the low-stage suction port 3a of the two-stage compressor 3 ₁ through the three-way valve 19 ₁ and the switching mechanism 18 ₁ .

The refrigerant gas flowing into the two-stage compressor 3 _3, as described above, is sucked into the low-stage suction port 3a and the high-stage suction port 3c, respectively, by the first-stage compression mechanism and the second-stage compression mechanism After being compressed by one stage, they are discharged from the low-stage discharge port 3b and the high-stage discharge port 3d, respectively, and merge. The refrigerant gas discharged is supplied through the three-way valve 19 ₂ and the bypass circuit to the condenser 10 of the secondary refrigeration system 1B, is condensed by the condenser 10, via the receiver 12 becomes a refrigerant liquid of a high pressure It flows into the expansion valve 11. Then, the refrigerant liquid becomes wet gas by the expansion valve 11 and is sent to the evaporator 8, evaporates in the evaporator 8, performs a cooling action, and then serves as a refrigerant gas as an evaporation pressure adjusting valve 20 and a three-way valve 19 _3. , it is drawn into the bypass circuit and the switching mechanism 18 of the ₂ via switched to single-stage compressor two-stage compressor 3 ₃ low-stage suction port 3a and the high-stage suction port 3c is compressed by the first-stage compression mechanism again The

In the sub-refrigeration apparatus 1B, the intake of the refrigerant gas into the intake port 9a of the single stage compressor 9 is blocked by the _three- way valve 193, and the discharge of the refrigerant gas from the discharge port 9b is stopped by the stop valve 16 ₂ . It is blocked.

  Here, when the circulation pump 14 of the circulation circuit 13 is operated, the condenser cooling water circulates between the evaporator 8 of the sub-refrigeration apparatus 1B and the condenser 4 of the main refrigeration apparatus 1A. At this time, the condenser cooling water is cooled by the evaporator 8 of the sub refrigeration apparatus 1B and supplied to the condenser 4 of the main refrigeration apparatus 1A, and the refrigerant gas of the condenser 4 in the main refrigeration apparatus 1A is cooled to perform the sub refrigeration. It will return to the evaporator 8 of the apparatus 1B. That is, the refrigerant gas of the main refrigeration apparatus 1A is cooled by the condenser cooling water, and condenses at a lower temperature than when normal temperature cooling water is used. Specifically, when the temperature of the condenser cooling water is + 10 ° C., the condensing temperature of the refrigerant gas in the main refrigeration apparatus 1A is about + 15 ° C.

For this reason, in the adiabatic compression when the condensation temperature is + 15 ° C., the evaporation temperature is −70 ° C., the superheat degree of the suction gas in each stage in the compressors 3 ₁ and 3 ₃ is + 5 ° C., and the low / high stage ratio is 3: 1. As apparent from the Mollier diagram of FIG. 3 described above, the temperature change of the compressed refrigerant gas is + 143 ° C.

  As a result, the temperature of the refrigerant gas after compression becomes + 170 ° C. (about + 150 ° C. with a thermometer with a compressor) or less, so that the lubricating oil circulating in the apparatus together with the refrigerant is not denatured, and ammonia is added to the refrigerant. It is possible to obtain an ultra-low temperature of −60 ° C. or less without causing deterioration of the lubricating oil. Moreover, even if the single-stage compressor 9 of the sub-refrigeration apparatus 1B becomes inoperable due to a failure or the like, one two-stage compressor of the two-stage compressor of the main refrigeration apparatus 1A is used as the single-stage compressor. Therefore, it is possible to reliably prevent a situation in which freezing cannot be performed in the ocean.

Further, when the condenser 10 or the evaporator 8 of the sub refrigeration apparatus 1B breaks down and the operation of the sub refrigeration apparatus 1B cannot be continued, the condenser cooling water is cooled and supplied to the condenser 4 of the main refrigeration apparatus 1A. I can't do that. In this case, the three-way valves 19 ₄ and 19 ₅ are switched, and the normal temperature cooling water is supplied to the condenser 4 of the main refrigeration apparatus 1A to condense the refrigerant gas in the condenser 4 at normal temperature. As described above, when the refrigerant gas in the condenser 4 is condensed at room temperature, the number of operating units is adjusted, and the evaporative temperature of the refrigerant gas is increased more than before so that the lubricating oil is not denatured. You can continue driving.

  In this embodiment as well, a plurality of two-stage compressors can be used according to the required refrigeration capacity. When a plurality of two-stage compressors are used, a plurality of expansion valves and evaporators corresponding to the respective two-stage compressors may be provided.

  As described above, according to the present invention, ammonia is used as the refrigerant, and the inside of the refrigerator can be cooled to an ultralow temperature of −60 ° C. or less without causing deterioration of the lubricating oil, which contributes to protection of the global environment. be able to.

It is a circuit diagram which shows one Embodiment of the freezing apparatus of this invention. It is explanatory drawing which shows the two-stage compressor of the freezing apparatus of FIG. It is a Mollier diagram which shows the temperature change of the compression process in the freezing apparatus of FIG. It is a circuit diagram which shows the modification of the freezing apparatus of FIG. It is a circuit diagram which shows other embodiment of the freezing apparatus of this invention. It is explanatory drawing which shows the two-stage compressor which can be switched to the single stage of the freezing apparatus of FIG. It is a Mollier diagram which shows the temperature change of the compression process in the conventional two-stage compression refrigeration apparatus. It is a Mollier diagram which shows the temperature change of the compression process in the conventional two-stage compression refrigeration apparatus.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Refrigeration equipment 1A Main refrigeration equipment 1B Sub refrigeration equipment 2, 2 ₁ , 2 ₂ Evaporator 3, 3 ₁ , 3 ₂ Two-stage compressor 3 ₃ Two-stage compressor switchable to single-stage compressor 4, 10 Condenser 5, 5 ₁ , 5 ₂ , 11 Expansion valve 6 Gas cooler 7, 12 Receiver 9 Single stage compressor 13 Circulation circuit 14 Circulation pump 15 Cooling water pump 16 ₁ , 16 ₂ Stop valve 17 ₁ , 17 ₂ Check valve 18 _1, 18 _2, 18 ₃ switching mechanism 19 _1, 19 _2, 19 _3, 19 _4, 19 ₅ three-way valve 20 evaporation pressure regulating valve

Claims (2)

A main refrigeration system comprising at least one or a plurality of two-stage compressors, one condenser, one or a plurality of expansion valves and an evaporator respectively corresponding to each of the two-stage compressors using ammonia as a refrigerant; The refrigerant is provided between a sub-refrigeration apparatus including at least one single-stage compressor, a condenser, an expansion valve, and an evaporator, and a condenser of the main refrigeration apparatus and an evaporator of the sub-refrigeration apparatus. And a circulation circuit of the condenser cooling water having a circulation pump, and the refrigerant of the sub refrigeration apparatus is circulated in the order of the single stage compressor of the sub refrigeration apparatus, the condenser, the expansion valve, and the evaporator to evaporate the sub refrigeration apparatus. And supplying the condenser cooling water cooled by the condenser to the condenser of the main refrigeration apparatus through a circulation pump. Using ammonia as a refrigerant, one or a plurality of two-stage compressors, a two-stage compressor that can be switched to one single-stage compressor, a condenser, and a plurality of compressors corresponding to each of the two-stage compressors. A main refrigeration apparatus having at least an expansion valve and an evaporator, a sub-refrigeration apparatus having at least one single-stage compressor, a condenser, an expansion valve, and an evaporator using ammonia as a refrigerant, and a condenser of the main refrigeration apparatus A condenser cooling water circulation circuit having a circulation pump, a two-stage compressor switchable to a single-stage compressor, and a single-stage compressor of the sub-refrigeration apparatus And a bypass circuit for connecting the low-stage inlet side and the high-stage outlet side of the two-stage compressor that can be switched to the single-stage compressor and the inlet side and outlet side of the single-stage compressor, respectively. Can be switched to a single-stage compressor instead of a single-stage compressor of the sub-refrigeration system Using the two-stage compressor as a single-stage compressor, the refrigerant of the sub-refrigeration unit is circulated in the order of the condenser of the sub-refrigeration unit, the expansion valve, and the evaporator through the bypass circuit, and cooled by the evaporator of the sub-refrigeration unit A refrigeration apparatus, wherein the condenser cooling water is supplied to a condenser of a main refrigeration apparatus via a circulation pump.

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