EP1422487A2

EP1422487A2 - Hot gas defrosting of refrigeration plants

Info

Publication number: EP1422487A2
Application number: EP03026471A
Authority: EP
Inventors: Per Skaerbaek Nielsen
Original assignee: Johnson Controls Denmark ApS; York Refrigeration ApS
Current assignee: Johnson Controls Denmark ApS
Priority date: 2002-11-21
Filing date: 2003-11-20
Publication date: 2004-05-26
Also published as: EP1422487A3

Abstract

In refrigeration systems using CO₂ as effective refrigerant there are severe problems with respect to defrosting in freezer equipments calling for operative defrosting, e.g. in plate freezer units in fishing vessels. The invention provides for a refrigeration plant comprising at least one compressor unit (12), which compressor unit (12) is delivering compressed refrigerant to at least one condenser (14), from which condenser liquid refrigerant is led to at least one evaporator (8) through at least one restriction element, where the compressor is connected to the evaporator, and where a defroster circuit (56) is arranged for selectively supplying hot refrigerant to said evaporator equipment (8) for defrosting purposes, whereby at least one compressor unit (12) comprises at least a first compressor section (52) and a second compressor section (54), which first and second compressor sections (52,54) are operating in serial connection during defrost, where the first and second compressor sections (52,54) are operating in parallel during normal operation, where the pressure outlet of the second compressor section (54) during defrost is connected to a gas pipe connection (56) which is connected to a refrigerant channel system of said evaporator equipment (8).

Description

A refrigeration plant comprising at least one compressor, which compressor is delivering compressed refrigerant to at least one condenser, from which condenser liquid refrigerant is led to at least one evaporator through at least one restriction element, where the compressor is connected to the evaporator, and where a defroster circuit is arranged for selectively supplying hot refrigerant to said evaporator equipment for defrosting purposes.
Defrosting is necessary to remove ice built up on a freezer or a cooler. In most cases it is a question of proper and efficient function of the equipment, but in some cases it is a vital part of the function. One of the latter cases is a plate freezer, where the product is frozen between two metal plates wherein refrigerant is circulated. To be able to remove the product it is necessary to defrost the plates.
Defrosting can be done in several ways, with the most common being:

Spraying with hot water, which is very common but not very practical due to hygienic considerations.
Electrical defrosting by means of electrical heating rods placed near the cooling surface. The main disadvantage is that when compared to the hot gas defrost, the power consumption is much higher. Because of the defrost compressors COP (cooling capacity kW per power consumption kW) the power fed to the defrost system is 4-5 times higher with electrical defrost for the same defrost capacity. Another disadvantage is that, when using electrical defrosting, the ice is melted from the outside, which means that more ice has to be melted before the remaining ice falls from the cooler and that the power consumption is to high.
Circulation of a hot liquid (usually a glycol/water mix) in a separate circuit within the cooler/freezer. When defrosting from the inside the ice on the surface melts first enabling the ice to fall off as soon as possible.
Hot gas defrosting where gas is condensed in the cooler/freezer at a temperature above the freezing point. Condensing takes place in the same circuit that is used for cooling/freezing. In some types of evaporators e.g. plate freezers hot gas defrost is the only possible solution for defrosting

Where ever possible hot gas defrosting is used. Hot gas defrosting is very efficient as heat is delivered where the ice has built up and it is very economical since the heat used is present in the system. Electrical and hot liquid defrosting requires an external power source which hot gas defrosting does not. During hot gas defrosting the cooler/freezer acts as a secondary condenser dispersing the heat otherwise dispersed in the cooling media (usually water or air).
With the reintroduction of CO₂, cascade systems are becoming more frequent. Due to the high saturation pressure of CO₂, it is not possible to keep the pressure within the range normally encountered in refrigeration plants while still condensing it against air or water at ambient temperatures. Thus a cascade system is used, wherein a secondary refrigeration plant cools the CO₂ condenser. The secondary refrigeration plant condenses against the available cooling media. The condensing temperature of the CO₂ is usually in the range of-20°C to -5°C.
If a traditional approach for hot gas defrosting was to be used, the gas, otherwise to be condensed in the cascade cooler, would be led to the evaporator. But in the case of CO₂ the condensing temperature is, as mentioned above, in the range of -20°C to -5°C, which is not sufficiently hot to remove ice from the evaporator. When defrosting a cooler it is, of cause, necessary to get the temperature of the cooler (well) above 0°C.
One solution to this problem could be to raise the temperature in the cascade cooler (e.g. refrigeration compressor outlet) to a level above the freezing point. This is possible, but several disadvantages arise from this solution. The overall energy efficiency of the system drops, and more important, components to handle the increased pressure are, at best, expensive or not available. Also a very large part of the plant would be subjected to very high pressures.
Often a valve in the outlet controls the defrosting pressure in the evaporator. This valve will close when the pressure is lower than the desired pressure. However, this restricts the liquid condensed during the defrosting from leaving the evaporator, thus resulting in a build up of liquid in the evaporator. The build up of liquid reduces the surface inside the evaporator available for condensing and as such reduces the overall effect of the defrosting.
As a refrigerant CO₂ gives some general advantages:

Highly efficient system, both with regard to component sizing and energy consumption.
Efficient to low evaporating temperatures. Other refrigerants become inefficient below -40°C, but CO₂ is efficient down to -55°C, limited only by the triple point (-56,6°C)
A CO₂ leak will not destroy the product in the processing area affecting not only the yield but also the insurance costs.
CO₂ is considered a safe refrigerant. It is non-flammable, non-explosive and it is considerably safer to the crew than other refrigerants.
The low evaporating temperature yields a higher capacity of the production equipment, usually resulting in a faster freezing. The faster freezing has a positive effect on product quality.
CO₂ is a natural refrigerant with none of the environmental problems associated with older refrigerants such as CFC's and HCFC'S. CO₂ is not harmful to the environment ensuring unrestricted use in the future from the environmental point of view.

The patent application DK 2001 00310 describes a plant and a process using CO₂ for defrost. This system is a unit that delivers both defrosting and standstill cooling, e.g. keeping system pressure down during standstill. In a combined system like in DK 2001 00310, failure of the defrost system would mean that no standstill cooling is available and it is from some classification societies a demand that the standstill cooling is performed by a separate unit as a part of the safety system.
The above-mentioned system is connected to the "distribution system", defined as a vessel with gas/liquid equilibrium along with the piping to the consumers e.g. the evaporators. From the application and its definitions it appears that the possible connection points are: A pump separator, a high-pressure receiver, and the piping to the consumers.
Connecting the defrosting compressor to the refrigeration cycle's low-pressure side results in a very large pressure difference, which most industrial refrigeration compressors cannot handle. Furthermore a defrosting compressor connected to the low pressure side needs to be about 4 times bigger (by swept volume) than one connected to the high pressure side to deliver the same defrosting capacity. Standard refrigeration equipment can be used when connecting to the high-pressure side, while this is not the case when connecting to the low-pressure side.
If connecting the defrosting compressor to the high-pressure receiver it is very doubtful if sufficient gas is available in the receiver. The receiver essentially collects liquid from the condenser and will normally not contain the large amounts of gas necessary for defrosting.
In the DK 2001 00310 system the suction gas for the compressor is saturated, necessitating a liquid separation. Ensuring that the suction gas contains no liquid is essential for safe compressor operation - especially when using reciprocating compressors.
US 4,962,647 comprises a refrigerating circuit apparatus includes a two stage compressor having an upper stage compressing cylinder and a lower stage compressing cylinder, a heat storage tank, an upper stage side variable opening expansion valve and a lower stage side variable opening expansion valve. The upper stage side variable opening expansion valve is controlled towards its closed position for executing a heat storing operation in which heat is discharged from refrigerant to the heat storage tank. The upper stage side variable opening expansion valve is opened and the lower stage side variable opening expansion valve is closed for carrying out a defrosting operation. Heat stored in the heat storage tank is used in the defrosting operation for removing frost accumulated on an external heat-exchanger during the heating operation.
In this way only a restricted part of the refrigerant leaving the upper stage of the compressor is used for defrost, part of the refrigerant is sent to a condensing unit and liquefied before it is lead to a separator. From the separator gaseous refrigerant is drawn through a heat storage tank to the inlet to the upper compressor stage. The refrigerant is at fist cooled and liquefied in the condenser and later heated and evaporated in the heat storage tank. At the inlet the refrigerant flow is combined with the outlet from the lower compressor stage. The two compressor stages are never operating in parallel. An increase in the total compressor capacity by parallel operation is not possible.
It is the purpose of the invention to define a system that can perform a hot gas defrosting a refrigeration plants, where the system can deliver efficient defrosting while offering noticeable benefits in terms of lower overall power consumption of the plant and a high degree of use of standard refrigeration components.
The present invention comprises a refrigeration plant as the one described in the opening paragraph, operating with at least one compressor which comprises at least a first compressor section and a second compressor section, which first and second compressor sections can be operating in serial connection during defrost, where the first and second compressor sections can be operating in parallel during normal operation, where the pressure outlet of the second compressor section during defrost is connected to a gas pipe connection which is connected to a refrigerant channel system of said evaporator equipment.
In this way a compressor build in sections, maybe with a common motor, can operate very flexibly because defrost of evaporators is only necessary in a few minutes with an interval of several hours. The compressor section can operate in parallel in periods with no defrost. If the refrigeration plant operates as a heat pump, defrost may only be necessary in the coldest winter.
The second compressor section is being operable to supply defrost gas at elevated pressure and temperature governed by preset or presetable discharge pressure/temperature requirements. In this way special requirements for the cooling plant can bee fulfilled. Defrost can take place in a form depending on the use of the cooling plant. In one situation rapid defrost with a high temperature is the best solution, but in other situations the defrost temperature needs to bee low in order not to damage the food, but the defrost period can bee longer.
This invention also relates to a refrigeration system of the cascade type where said defroster circuit comprises a defrost compressor section arranged in a gas pipe connection from the discharge side of said one or more refrigeration compressors or compressor sections to the refrigerant channel system of said evaporator equipment, said defrost compressor being operable to supply defrost gas at elevated pressure and temperature governed by preset or preset able discharge pressure/temperature requirements. At +10°C the CO₂ pressure is 45 bar, which calls for a separate dedicated defrost system.
The system according to the invention limits the high pressure to an absolute minimum number of components while employing as many standard components as possible. Using a dedicated defrosting compressor section another pressure level is created with the sole purpose of defrosting. In this way the high pressure can be limited to the defrosting compressor section, the defrost pipe, the evaporator to be defrosted and a few valves at the evaporator. The cascade cooler, refrigeration compressor and associated equipment can be held at the temperature/pressure yielding the most overall efficient plant and still be standard refrigeration components. The defrosting compressor section is connected to the refrigeration compressor outlet.
A system according to the invention has an especially dedicated compressor section for defrosting. This defroster compressor section suction gas is the refrigeration compressor discharge gas. The gas has been desuperheated before entering the defrost compressor to avoid too high discharge temperature that could create a problem with lubrication of the defrost compressor. Furthermore the COP (cooling capacity kW per power consumption kW) of the defrost compressor would be lower and oil cooling would be necessary.
Desuperheating (cooling) of the suction gas to the defrosting compressor section has an effect on the overall power consumption of the plant. Two methods of cooling are the most likely; the first one being cooling with the same media used in the secondary systems condenser (air or water) and the other method is using the cascade cooler.
Normally a cascade cooler would desuperheat the gas before condensing, so introducing a nozzle in the appropriate place in the cascade cooler would yield a supply of cooled gas. In the cascade cooler the cooling is performed by the secondary system so power will be required by the secondary system. Also it is of very high importance that the gas supplied to the defrosting compressor does not contain liquid. A positive superheat is required to avoid liquid hammer (attempting to compress liquid) in the compressor.
The other option, the air/water cooled cooler, offers some advantages. As mentioned earlier, it is not practically possible to condense the CO₂ against air/water at a normal ambient temperature, but it is possible to use it to cool the gas before entry into the cascade cooler and defrosting compressor. The benefit is that every kW cooled by the cooler does not have to be removed in the cascade cooler. This results in a reduction of both the size, and power consumption of the secondary system. In such a cooler the gas can be cooled to a temperature very close to the ambient temperature, but since the saturation (condensing) temperature is much lower, the gas is still sufficiently superheated to avoid liquid hammer. The selection of one of these two systems will be a question of installation costs versus the savings in running costs.
The defrost compressor section can comprise capacity regulation. The condensing temperature determines the suction pressure in the cooling cycle. This pressure is kept constant by the "hot" refrigeration cycle.
To avoid excessive changing of the compressor capacity steps and an unintended pressure rise at the end of the defrost period when defrost capacity demand is low, a controllable bypass valve is used to bypass hot gas back to the cascade cooler. The bypass valve is arranged in a connection from the discharge side of the defrost compressor section and the discharge side of the one or more refrigerating compressors. A precise control of the defrost pressure and temperature is thereby enabled and the bypass valve will smoothen the capacity steps and secure that the pressure does not exceed the maximum design pressure. This control method makes it unnecessary to mount control valves on each cooler to control the pressure during defrost. All defrost control is done by the compressor section and the bypass valve.
The defrost pressure/temperature can be set individually for each evaporator by changing the defrost compressor section. In this way the defrost can be optimised for the individual type of evaporator. Some applications can benefit from a more gradual defrost while some need a fast defrost. Considerations when selecting defrosts temperature will include heat loss into the surroundings, water/steam contents in the room air and product quality.
On a system according to the invention the refrigerant outlet from the evaporator equipment can be connected to the suction side of the one or more refrigeration compressors through a liquid operated liquid draining device.
Draining the cooler during defrost is a very important issue. When the cooler fills with liquid the surface available for condensing (defrost) becomes smaller and consequently the possible capacity drops meaning a slower defrost. The system according to the invention has for this purpose employed a thermodynamic liquid drain designed for steam and compressed air application. This device allows liquid to pass and stops gas in much the same way as a float valve mechanism. Float valve mechanisms employ a floating ball but these have been difficult or expensive to get for the high pressure needed. The liquid drain used is simple and can accept the pressures. The benefit is that when the compressor controls the pressure completely, the liquid drain only needs to drain the liquid in the freezer and not concern itself with regulating the pressure. The result is an extremely simple system with an efficient operation.
A system as described, wherein the entire gas conductor system from the defrost compressor section through the evaporator equipment and to the drain pipe of the evaporator can generally be without pressure regulating means and will preferably be laid out for operating at pressures not exceeding 50 bar.
It can, however, not be excluded that a higher pressure, for instance 55 bar, will be more suitable in a alternative embodiment of the invention.
All together the installation is considerably simpler, less expensive and more secure compared to known solutions.
The system according to the invention described herein has a plurality of benefits compared to the alternative systems:

Except for the defrost compressors' oil separator there are no vessels in the high-pressure system. The oil separator has a very low volume. Large volumes under high pressure present a safety hazard due to the high energy content.
The defrost pressure/temperature is controlled by the compressor section. The compressor section can regulate its discharge pressure rather than the traditional suction pressure regulation. It is possible to regulate the compressor section either by the normal compressor capacity step supplemented by a bypass valve to achieve a finer regulation or by using a frequency converter on the compressor motor to regulate the compressor RPM. This can be necessary because of the high capacity of a single capacity step on reciprocating compressor section.
It is not necessary with regulating valves for the cooler. The compressor does all pressure/temperature regulation.
When the defrost pressure is controlled by the compressor it is only necessary to drain the cooler of liquid. When liquid is drained the maximum surface is available for condensing.
The drainage is secured by a thermodynamic liquid drain, a commonly available component for compressed air and for steam or by a high-pressure float valve.
High-pressure is only present while the compressor is running. In effect all pressure will equalize when a critical situation occurs (e.g. a power failure, wrong valve position) or when the compressor emergency stop is pressed.
By taking the discharge gas from the refrigeration compressors and not from the pump separator the COP (cooling capacity kW per power consumption kW) is greatly enhanced offering a much better economy. Furthermore the requirement for the compressor size is greatly decreased.
In systems where the need for defrosting is not continuous, but rather at discrete intervals, the defrost compressor could be used as a normal refrigeration compressor. The compressor used for defrosting can be a dedicated defrost compressor section, but can also be combined with anyone of the refrigeration compressors. A system according to the invention can be designed with the possibility to use one or more sections of a plurality of compressors in the system as defrost compressor sections. In this way an increased safety and reliability of the system is achieved. The performance of the compressor in the two running conditions is well matched. That is, when running in the defrost condition the compressor yields 3-5 times as much as when in the refrigeration condition. This ratio is deemed suitable for defrosting in a reasonable time. Thus, when a cooler is taken out of operation to be defrosted, the excess compressor capacity at cooling level matches the need for defrost capacity.
The gas for defrosting is greatly superheated which, apart from the actual gain in heating capability, secures the system against condensation in pipes and valves before entering the cooler. If liquid enters a low-pressure area from a high-pressure area it can be "shot" into the low-pressure area and considerable damage can occur from this.
The compressor is able to start the defrost "gently" while running up the pressure at the start of the defrost. This reduces the risk of pressure surges and liquid hammer.
It is possible to make individual defrost conditions for different evaporators to suit the individual needs.

Power consumption of the system is considerably affected if the system according to the invention is employed. Heat absorbed in the evaporators will, along with the CO₂ compressor motor heat, be delivered to the secondary (usually R717) refrigeration system in the cascade cooler. Even though the cascade temperatures have been fixed at the overall most efficient point, the secondary system accounts for 60-70% of the overall power consumption. But when the defrosting compressor is in action the defrost compressor suction gas need not be condensed by the secondary system resulting in a drop in required cooling capacity of the secondary system.
The gas will, after compression in the defrosting compressor, be condensed in the evaporator to be defrosted. However, the COP (cooling capacity kW per power consumption kW) is much higher in the defrosting compressor than in the secondary systems compressor. The difference is naturally dependent on the type (refrigerant etc) of the secondary system and running conditions, but in general terms a factor of two is realistic. This means that for every 100 kW used by the defrosting compressor, the power consumption of the secondary system drops with 200 kW with a resulting overall drop of 100 kW.
With 100 kW power consumption, the defrost compressor employed in this system will deliver approximately 600 kW heating. If electrical defrosting is to be used, all 600 kW is needed in electricity, so the comparison is really an increase of 600 kW compared to a drop of 100 kW. If hot glycol is to be used the heating could be extracted in the system (most likely the secondary system's hot side) so the power consumption only increases with the pump power. However, no gain similar to the one described above is achieved.
On a plant according to the invention it has been discovered that there is a large over all efficiency benefit during defrosting, as mentioned above. For the understanding of the invention it has to be mentioned that the compressors used are mainly large industrial compressors for industrial cooling purposes, but that the invention can also be used in connection with plants comprising commercial compressors capable of handling the given pressure and temperature. As an example cooling and freezing plants in butcher shops, in supermarkets or in other retail shops can be mentioned as places to use the system.
To save even more energy using the system according to the invention it is possible to use the defrost compressor capacity to supply hot gas to other elements than to a traditional evaporator e.g. to elements consisting of heating/evaporator pipes placed in areas where ice otherwise will built up. As an alternative the hot gas could also be used for heating.
Freezers that need defrosting are often used onboard fishing vessels, and in such plants heating/evaporator pipes can be installed in the floor in the freezing area. In this area there will typically be ice formations, which today is removed or controlled by electrical heating elements. By replacing these elements with heating/evaporator pipes less electrical power is needed and the defrost compressor is used more efficiently whereby energy is saved in the second condensing unit.
CO₂ hot gas from the defrost compressor can be used for traditional defrosting, for heating and for defrosing in all places where the temperature is below 10 °C.
In the following the invention will be described with reference to the drawing where:
Fig. 1 shows a system according to the invention,
Fig. 2 shows a system comprising more compressors, and
Fig. 3 shows a log(P)-H diagram of defrost according to the invention in cascade systems.
Referring to fig. 1, which shows a system according to the invention, the system's function will be described. Please note that the figure is simplified to ease the understanding.
The freezing system 2 is executed in the traditional manner. The pump separator 4 contains liquid refrigerant at the evaporating temperature. The pumps 6 pump refrigerant liquid to at least one evaporator 8 through the valve station 10.
In the evaporator 8 the refrigerant liquid is partially or completely evaporated and returned through a line 26 to the pump separator 4. The gas generated in the evaporator 8 is removed by at least one refrigeration compressor 12, which compresses the gas to the condensing pressure. From the refrigeration compressor 12 the gas is primarily led to the cascade cooler 14 where the gas is condensed before being led back to the pump separator 4. A secondary condensing unit 16 provides cooling for the cascade cooler 14. The freezing system 2, as described here, is prior art technology and is as such not interesting, but the defrosting system is the essence of the invention described here.
The compressor 12 is a two section compressor, comprising a common motor 50 connected to a primary compression section 52 and to a defrosting section 54. The defrost compressor section 54 takes suction from the discharge of the refrigeration compressor section 52 (e.g. at condensing pressure) and compresses it to the desired defrost pressure. Please note that the gas from the refrigeration compressor section 52 is significantly superheated. To avoid too high discharge temperature (oil problems) from the defrost compressor section 52, it could be necessary to desuperheat (cool) the gas before entry into the defrost compressor section 54. This cooler has not been included on the sketch, because the function is not vital to the principal function of the defrost system. The gas cooling could take place in an external heat exchanger or it could take place in the cascade cooler 14. As mentioned this gas cooling is not essential for the principal function of the system 2, but since some energy efficiency issues arise from this, it will be discussed later in detail.
From the defrost compressor section 54 the gas is led to the evaporator 8. In fig. 1 the gas is led through a conduit 56 comprising a magnetic valve 58 to the liquid/gas "outlet" 22 of the evaporator 8, resulting in a defrosting flow backward in the evaporator 8. Considerable differences of opinion exist about defrosting forward or backward, but in this case backward defrosting is considered most efficient and thus it is outlined here. Furthermore backward defrosting is safer since the risk of liquid bullets being shot through the system is reduced. In the evaporator 8 the defrost gas condenses and it is led out through the liquid "inlet" 24 of the evaporator 8. Returning this (for now high-pressure) liquid is done in the normal return line 26 to the pump separator 4, however, the pressure needs to be reduced to the evaporating pressure before entering the return line 26. This is done in a high-pressure float valve 28 or a component with the same characteristics. The purpose of this component 28 is both to reduce the pressure, but also to allow all liquid to drain from the evaporator 8, but not allowing any gas to pass during defrosting. With the use of this float valve 28 (or like) the evaporator 8 will always be completely drained during defrosting resulting in an efficient defrost. Furthermore, since the evaporator 8 will be full of liquid from the freezing cycle at the beginning of the defrosting, a fast and efficient drainage is secured with the float valve system 28.
One small thing needs to be observed with this arrangement. During the freezing cycle the float valve 28 could act as a short circuit and bypass all the liquid pumped to the evaporator 8 back to the return line 26. This is avoided by adding a valve 30 in series with the float valve 28. This valve 30 has an opening pressure that is larger than the pressure loss in the evaporator 8 and will thus remain closed during the freezing cycle.
Regulation of the pressure during defrosting is performed by the compressor section 54 capacity regulation. The compressor section 54 capacity regulation will regulate according to the discharge pressure as opposed to the "normal" suction pressure regulation. This method of regulation is common in heat pumps. The suction pressure for the defrosting compressor section 54 (e.g. the condensing pressure in the CO₂ circuit) is kept constant by the secondary condensing unit 16. Regulating the pressure with the compressor section 54 while the float valve 28 drains the evaporator 8 (regardless of the pressure) has some benefits:

Rather than using a regulating valve for each evaporator 8, the control is at one point only resulting in a more simple control. Furthermore pressure regulators for 50 bars pressure are not standard refrigeration equipment.
Changing the compressor discharge pressure set point makes it possible to adapt the defrosting to the component to be defrosted. For instance in a plate freezer 8 the defrosting time is very important and thus the maximum temperature would be specified to the compressors control system, while in an air cooler in a freezing storage room it could be desirable to minimize the heat ingress into the room. This could be done with a defrosting at a lower temperature for a longer time.
The evaporator 8 is, as mentioned, completely drained and thus offering the maximum surface area for condensing. Once the gas has condensed, e.g. given off its latent heat, it is of little use in the defrosting process. Removing the liquid enables the maximum defrosting capacity to be achieved.
The defrosting compressor section 54 can bee coupled in a parallel mode by opening and closing of magnetic valves 58, 60, 62, 64 when no defrost is required, thus reducing wear from excessive start-stop situations. In defrost mode magnetic valves 58 and 60 are open. The valves 62 and 64 are closed. Regulation of the compressor section 54 can take place by valve 64, which valve 64 can bee opened partly by modulation and a controllable bypass connection 66 around the compressor section is formed to bypass hot gas back to the cascade cooler 14.

Fig. 2 shows an alternative embodiment for the invention, where the figure differs in having more compressors 70 and 72. These compressors are always operating as cooling compressors, where defrost is carried out by the compressor section 54.
Fig. 3 is showing a log (P)-H diagram of defrost according to the invention in cascade systems. The diagram shows the normal refrigeration cycle (34). From evaporating pressure (36) the refrigerant is compressed (38) up to the condensing pressure (40). From the compressor discharge (42) the gas is cooled and eventually condensed before it is flashed back to the evaporating pressure (36). The system according to the invention connects the defrosting compressor section (54) after the refrigeration compressors discharge port (42) and before condensing takes place (44) in the condenser/cascade cooler. The compressor section (54) is compressing (39) the refrigerant to the defrost pressure (45), where the refrigerant remains at a nearly constant pressure (45) during defrost of an evaporator. After end of defrost the pressure of the refrigerant is reduced (43) to the normal condensation pressure (40).
On other known systems for CO₂ defrosting the defrost compressor is connected at the refrigeration compressors suction side (46) or after the condenser/cascade cooler (48).

Claims

A refrigeration plant comprising at least one compressor unit (12), which compressor unit (12) is delivering compressed refrigerant to at least one condenser(14), from which condenser liquid refrigerant is led to at least one evaporator (8) through at least one restriction element, where the compressor is connected to the evaporator, and where a defroster circuit (56) is arranged for selectively supplying hot refrigerant to said evaporator equipment (8) for defrosting purposes, characterized in, that at least one compressor unit (12) comprises at least a first compressor section (52) and a second compressor section(54), which first and second compressor sections (52, 54) are operating in serial connection during defrost, where the first and second compressor sections (52, 54) are operating in parallel during normal operation, where the pressure outlet of the second compressor section (54) during defrost is connected to a gas pipe connection (56) which is connected to a refrigerant channel system of said evaporator equipment (8)
A refrigeration plant according to claim 1, characterized in, that the second compressor section (54) being operable to supply defrost gas at elevated pressure and temperature governed by preset or presetable discharge pressure/temperature requirements.
A refrigeration plant according to claim 1 or 2, characterized in, that the suction side of the second compressor section (54) is connected to the discharge side of the first compressor section (52) or one or more refrigerator compressors 70 through a desuperheater unit, preferably constituted by said condenser unit (14).
A refrigeration plant according to one of the claims 1-3, characterized in, that a controllable bypass valve (64) is arranged in a connection from the discharge side (56) of the second compressor section and the discharge side the first compressor section or of one or more refrigerating compressors (12).
A refrigeration plant according to one of the claims 1-4, characterized in, that the refrigerant outlet from the evaporator equipment (8) is connected to the suction side of one or more refrigeration compressor units (12) through a liquid operated liquid draining device (28).
A refrigeration plant according to one of the claims 1-5, characterized in, that the entire gas conductor system between the second compressor section (54) through the evaporator equipment (8) and to the drain pipe (24) of the evaporator (8) is generally without pressure regulating means and is laid out for operating at pressures not exceeding 50 bar.
A refrigeration plant according to one of the claims 1-6, characterized in, that the discharge side (56) of the second compressor section (54) is selectively connectable to any one or more of a number of evaporator units (8) in said evaporator equipment, while the remaining units are still operable in refrigeration mode.
A refrigeration plant according to one of the claims 1-7, characterized in, that at least one refrigeration compressor section (54) in parallel with one or more refrigeration compressor sections (52, 70) is connectable so as to temporarily operate as a defrost compressor section.