Refrigerator recycling system

Abstract

The invention relates to a refrigerator recycling system (1) and to a method (S300) for recycling refrigerators (22), wherein the refrigerator recycling system (1) comprises: a refrigerator comminuting device (10), an inert gas source (30), a dehumidifying cooling device (40), a process gas line (50), a compressor (60), a cooling device (70), a gas-liquid separating device (80), a process gas return line (100), a membrane device (90) and a pressure swing adsorption device (200). The membrane device (90) is designed in such a way that a hydrocarbon-enriched return process gas is obtained from the remaining process gas on the permeate side (92) of the membrane device (90), and a hydrocarbon-depleted transfer process gas is obtained on the retentate side (94) of the membrane device (90), the permeate side (92) of which is connected to the process gas line (50) via an HC-enriched gas return line (110) at a return point (112) upstream of the compressor (60), optionally between the dehumidifying cooling device (40) and the compressor (60), in order to return the hydrocarbon-enriched return process gas to the process gas at said return point (112) and the retentate side (94) of which is connected to an HC-depleted gas transfer line (120) in order to transfer the hydrocarbon-depleted transfer process gas.

Description

[0001] Refrigerator recycling plant

[0002] The invention relates to a refrigerator recycling system.

[0003] A challenge with refrigerator recycling is that the volatile hydrocarbons contained in refrigerators, such as CFCs and / or pentane, for example, in their insulation material, which is usually made of foamed material with a propellant / propellant gas, or in their refrigeration circuit, must be largely recovered to prevent them from entering the atmosphere. Furthermore, the corresponding recycling must also be energy- and cost-efficient.

[0004] Accordingly, the invention aims to create a refrigerator recycling system with which refrigerators can be recycled in an environmentally friendly manner as well as in an energy and cost-efficient manner.

[0005] For this purpose, the invention provides a refrigerator recycling system which comprises:

[0006] - a refrigerator shredding device having a sealed process chamber and a mechanical shredding device arranged in the process chamber for mechanically shredding a, e.g. substantially complete, refrigerator,

[0007] - an inert gas source, optionally a nitrogen gas source, which is connected to the process chamber and from which inert gas, optionally nitrogen gas, can be supplied to the process chamber,

[0008] - a dehumidification-cooling device which is connected to the process chamber (e.g. immediately downstream thereof) via a process gas line in order to receive process gas discharged from the process chamber, which contains hydrocarbon gas resulting from the mechanical comminution of the refrigerator, and which is arranged to cool the process gas to a

[0009] Dehumidification temperature, which is optionally in the range of 5 ° -20 °, to cool down so that water is separated from the process gas via condensation in order to dehumidify the process gas,

[0010] - a compressor arranged downstream of the dehumidification-cooling device in the process gas line (e.g. immediately downstream of the dehumidification-cooling device) and which is designed to compress the dehumidified process gas, optionally to a pressure in the range of 10-15 bar,

[0011] - a cooling device arranged downstream of the compressor in the process gas line (e.g. immediately downstream of the compressor) and designed to cool the compressed process gas to a separation operating temperature in the range of 5-15 °C in order to thereby separate the hydrocarbon contained in the process gas via condensation as liquid hydrocarbon,

[0012] - a gas-liquid separation device which is arranged downstream of the cooling device in the process gas line (e.g. immediately downstream of the cooling device) and which is designed to separate the liquid hydrocarbon separated from the compressed and cooled process gas (which may and / or does contain further liquid residual moisture) from the remaining process gas, a membrane device,

[0013] - which is connected to the gas-liquid separation device via a process gas return line in order to receive the remaining process gas,

[0014] - which is arranged in such a way that a hydrocarbon-enriched recycle process gas is obtained from the remaining process gas on a permeate side of the membrane device and a hydrocarbon-poor further process gas is obtained on a retentate side of the membrane device,

[0015] - the permeate side of which is connected via a hydrocarbon-enriched gas return line to the process gas line at a return point upstream of the compressor, optionally between the dehumidification-cooling device and the compressor, in order to return the hydrocarbon-enriched return process gas to the process gas at this return point in order to increase its hydrocarbon content, and

[0016] - whose retentate side is connected to a low-hydrocarbon gas feed line in order to feed the low-hydrocarbon feed process gas.

[0017] The membrane device can be designed, for example, in the manner of a gas separation membrane device as described in EP 0 329 962 A2.

[0018] By increasing the hydrocarbon content of the process gas fed to the compressor via the membrane device, the invention allows the liquefaction of the hydrocarbon in the cooling device downstream of the compressor to be achieved in temperatures well above 0 °C at pressures achievable with a compressor with acceptable energy consumption (e.g., 10-15 bar). Since cryogenic cooling / liquefaction is thus not required, the system according to the invention can be operated cost-effectively and is also less complex to construct.The inventors have further recognized that by simply cooling the process gas downstream of the comminution device and upstream of the compressor, the water content in the process gas can be reduced in a simple and cost-effective manner sufficiently for the subsequent processes (compression, cooling to separate the hydrocarbon) to not impede these subsequent processes. Due to the non-cryogenic cooling for liquefying the volatile hydrocarbons, there is little or no risk of water icing of the plant components involved in the liquefaction process due to the residual moisture still present in the process gas after dehumidification.

[0019] The refrigerator shredding device can, for example, be equipped with a heating device connected to the process chamber to heat the process chamber to a shredding process temperature, which optionally lies in a range of 70° to 80°. It has been shown that at higher temperatures, the release of gases, including volatile hydrocarbon gases, from, for example, foamed refrigerator insulation elements, is improved. An electric heater, for example, can be used as the heating device.

[0020] The mechanical comminution device comprises, for example, a rotary impact device which has one or more rotary bodies which are arranged in the process chamber, optionally on the floor of the process chamber, so as to be rotatably drivable about a rotation axis, and which is (are) each provided with at least one impact chain, e.g. with at least or with exactly two impact chains, which (e.g. each of which) is fastened with one chain end to the rotary body outside its rotation axis and which (e.g. each of which) has another, free chain end, wherein the respective impact chain optionally has a length in a range of 30-50 cm, and wherein the respective impact chain is optionally designed as a ring chain.It has been shown that by means of this mechanically relatively simple design of the mechanical comminution device, it is possible to comminute foamed refrigerator insulation material into a granulate form thereof, which has proven to be effective / supportive with regard to the release of the gases contained in the insulation material.

[0021] The cooling device can, for example, have a first cooling device heat exchanger, which is further arranged in the process gas return line between the gas-liquid separation device and the membrane device (e.g. immediately downstream of the compressor) and which is designed to allow the remaining process gas present in the process gas return line to exchange heat with the compressed process gas. By means of this first cooling device heat exchanger, a cooling of the compressed process gas (e.g. a first or first cooling process) can take place in an efficient / cost-effective manner, since the remaining process gas, for example untreated, from the gas-liquid separation device is simply used for this purpose. In this case, the first cooling device heat exchanger is connected, for example, directly between the gas-liquid separation device and the membrane device.

[0022] The cooling device has, for example, a first cooling device cooling apparatus which has a refrigeration unit, a second cooling device heat exchanger and a refrigerant line which connects the refrigeration unit and the second cooling device heat exchanger to one another and in which a refrigerant circulates which can be cooled by the refrigeration unit, wherein the second cooling device heat exchanger is arranged between the first cooling device heat exchanger and the gas-liquid separation device (e.g. immediately upstream of the gas-liquid separation device) and is designed to allow the refrigerant to exchange heat with the compressed process gas in order to thereby cool the compressed process gas to the separation operating temperature in the range of 5-15°C, for example, so that hydrocarbons contained in the process gas are separated as liquid hydrocarbons via condensation. The dehumidification cooling device is optionally e.g.designed as a dehumidification heat exchanger which is arranged downstream (e.g. immediately downstream) of the second cooling device heat exchanger in the refrigerant line and is arranged to allow the refrigerant to exchange heat with the process gas in order to cool the process gas to the dehumidification temperature.

[0023] Thanks to the non-cryogenic refrigerator recycling system, the refrigeration unit can be designed to be smaller and thus more cost-effective. The optional use of the refrigerant as a cooling medium for the dehumidification and cooling system can further increase the system's efficiency.

[0024] The cooling device has, for example, a second cooling device cooling apparatus which has an air cooler with a cooling air fan, a third cooling device heat exchanger and a coolant line which connects the air cooler and the third cooling device heat exchanger to one another and in which a coolant circulates which can be air-cooled by the air cooler by means of the cooling air fan, wherein the third cooling device heat exchanger is arranged between the first cooling device heat exchanger and the second cooling device heat exchanger and is configured to allow the coolant to exchange heat with the compressed process gas. The air cooling is cost-effective and allows the refrigeration unit of the first cooling device cooling apparatus to be dimensioned / designed to be even smaller.

[0025] In the refrigerator recycling plant described herein, for example, the low-hydrocarbon gas feed line can be connected to the process chamber so that the hydrocarbon-free feed process gas can be fed to the process chamber. Additionally or alternatively, for example, the low-hydrocarbon gas feed line can be connected to a pressure swing adsorption device (PWA device) which has two or more storage containers with activated carbon material, wherein the hydrocarbon remaining in the feed process gas can be adsorbed by the activated carbon material to thereby generate essentially hydrocarbon-free exhaust air, which can be discharged to the environment via an exhaust air line connected to the respective storage container and / or which can be fed via a regeneration line to one of the storage containers whose activated carbon material is to be regenerated.The refrigerator recycling plant can therefore be operated flexibly to supply clean exhaust air when needed or at all times, whereby the remaining volatile hydrocarbons (HC) can be fed back into the hydrocarbon separation process.

[0026] The refrigerator recycling plant may further be provided with a liquid-liquid separation device,

[0027] - which is either integrally formed with the gas-liquid separation device or which is connected to the gas-liquid separation device via a liquid discharge line in order to receive the separated liquid hydrocarbon therefrom, and

[0028] - which is designed to separate any remaining water from the separated liquid hydrocarbon. The liquid-liquid separation device operates, for example, simply via gravity, with the water, which is heavier than the liquid hydrocarbon, essentially separating automatically.

[0029] The refrigerator recycling plant may further be equipped, for example, with a small material removal device which is connected to the process chamber in order to remove the material shredded by the mechanical shredding device from the process chamber.

[0030] The inert gas source and / or the retentate side of the membrane device can further be connected, for example, via a respective additional inert gas supply line to the HC-enriched gas return line and / or between the dehumidification cooling device and the compressor to the process gas line at an associated additional inert gas supply point, so that inert gas originating from the inert gas source and / or HC-enriched gas can be supplied to the process gas via the associated additional inert gas supply point in order to reduce the oxygen content in the process gas, wherein an oxygen sensor is arranged in the process gas line downstream of the respective additional inert gas supply point in order to detect the oxygen content in the process gas, and wherein the refrigerator recycling system can further be connected, for example,is provided with an electronic system control device, which is electrically connected to the oxygen sensor and to a respective additional inert gas control valve arranged in the respectively assigned additional inert gas supply line and which is designed to control the respective additional inert gas control valve on the basis of the oxygen content received from the oxygen sensor as electrical signals, such that a predetermined oxygen content in the process gas is set at the level of the oxygen sensor, wherein the predetermined oxygen content is optionally less than or equal to an oxygen limit concentration (LCC) for the propellant, optionally in conjunction with nitrogen gas as inert gas, e.g., less than or equal to 9.3 mol%. This design of the system allows, for example,To efficiently set a desired, predetermined oxygen content in the process gas upstream of the compressor without unduly impeding the hydrocarbon separation process and minimizing potential explosion risks. The term "limiting oxygen concentration" (LOC) used herein is the maximum oxygen concentration (molar fraction) in a mixture of a combustible substance with air and an inert gas (e.g., inert gas) at which an explosion can no longer occur, regardless of the fuel content. The LOC depends on the combustible gas or vapor and the inert gas used.

[0031] The heating device of the refrigerator recycling plant comprises, for example, a heat pump device which comprises:

[0032] - a heat pump supply line, which is connected to the coolant line of the second cooling device via an inlet point and a return point,

[0033] - a heat pump connected to the heat pump supply line,

[0034] - a heat pump discharge line which is connected to the heat pump and to a heat exchanger of the heating device arranged on the process chamber, by means of which the heat can be transferred from the heat pump to the process chamber.

[0035] This can, for example, save the electric heater or reduce its energy consumption, and further increase the energy efficiency of the refrigerator recycling plant.

[0036] The invention further provides a method for recycling refrigerators, optionally by means of a refrigerator recycling plant as described in this application, e.g. as previously described, comprising the steps:

[0037] - Feeding, optionally individual feeding, of the refrigerators into a (e.g. the) process chamber,

[0038] - Supply of inert gas, optionally nitrogen gas, into the process chamber, - Mechanical crushing of the respective refrigerator in the process chamber,

[0039] - removing gas present in the process chamber as process gas from the process chamber and supplying the process gas to a (e.g. the) dehumidification cooling device,

[0040] - Cooling the process gas by means of the dehumidification cooling device to a temperature that is optionally in the range of 5-20°C in order to dehumidify the process gas by condensing and separating water contained in the process gas,

[0041] - Compression of the dehumidified process gas by means of a compressor (e.g. the compressor), optionally to a pressure in the range of 10-15 bar,

[0042] - Cooling the compressed process gas in a (e.g. the) cooling device to a (e.g. the) separation operating temperature in the range of 5-15°C in order to separate the hydrocarbon contained in the process gas via condensation as a liquid hydrocarbon,

[0043] - Separating the liquid hydrocarbon separated from the compressed and cooled process gas from the remaining process gas by means of a (e.g.) gas-liquid separation device,

[0044] - feeding the remaining process gas to a (e.g. the) membrane device, from which a hydrocarbon-enriched recycle process gas is obtained from the remaining process gas on a (e.g. the) permeate side of the membrane device and a hydrocarbon-poor further process gas is obtained on a (e.g. the) retentate side of the membrane device,

[0045] - Returning the recycle process gas to the process gas in the process gas line at a (e.g. the) return point upstream of the compressor, optionally between the dehumidification-cooling device and the compressor, in order to increase the hydrocarbon content of the process gas. The method can, for example, further comprise: -additional supply of inert gas, optionally nitrogen gas, and / or the continued process gas to the process gas at an (e.g. the) assigned additional inert gas supply point between the compressor and the dehumidification-cooling device, and / or to the return process gas at a (e.g. the) correspondingly assigned additional inert gas supply point in a return-controlled (or regulated) manner such that the oxygen content of the process gas entering the compressor is less than or equal to an oxygen limit concentration (LCC) for the propellant, optionally in conjunction with nitrogen gas as inert gas, e.g. less than or equal to 9.3 mol%.

[0046] The method may further comprise, for example: feedback-controlled (e.g. regulated) heating of the process chamber in order to set a predetermined comminution process temperature therein, which is optionally in the range of 70-80°.

[0047] The method may further comprise, for example:

[0048] Removal of refrigerator compressors and, optionally, removal of refrigerator refrigerant lines from the refrigerators prior to feeding the refrigerators into the process chamber. The refrigerators, with the exception of the removed refrigerator compressors and, optionally, the removed refrigerator refrigerant lines, are otherwise fed into the process chamber completely as received. This can, for example, reduce the mechanical load on a (e.g., the) mechanical comminution device and also improve the composition of the comminuted materials, e.g., with regard to further separation.

[0049] In this process, mechanical comminution occurs, for example, in such a way that the foamed insulation material present in refrigerators is reduced to particles with a maximum circumference of 2 mm, or optionally with a maximum circumference of 1 mm. This type of particle formation has been shown to be very effective in removing hydrocarbons from refrigerator insulation.

[0050] The invention is described below using exemplary embodiments, which, however, do not limit the invention. Where reference is made to a first, second, etc., component (or, for example, step), etc., in the above and following descriptions, this does not necessarily dictate a specific order in which these components (or, for example, steps), etc., appear; i.e., the first component (or, for example, step) could also be the second or third component (or, for example, step), and vice versa.

[0051] The drawing shows:

[0052] Figure 1 is a schematic view of a refrigerator recycling plant according to a first embodiment of the invention,

[0053] Figure 2 is a schematic view of a refrigerator recycling plant according to a second embodiment of the invention,

[0054] Figure 3 is a schematic view of a refrigerator recycling plant according to a third embodiment of the invention,

[0055] Figure 4 is a schematic view of a refrigerator shredding device with, connected thereto, a refrigerator feed device and small material removal device of the refrigerator recycling plant according to an embodiment of the invention,

[0056] Figure 5 is a sectional view of the sealed process chamber of the refrigerator recycling plant from Fig. 4 along the line A-

[0057] A,

[0058] Figure 6 is a sectional view of the sealed process chamber of the refrigerator recycling plant from Fig. 4 along the line B-

[0059] B,

[0060] Figure 7 is a flow diagram of a process for recycling refrigerators, and

[0061] Figure 8 is a flow chart of the refrigerator recycling process of Figure 7 with additional steps.

[0062] Figure 1 shows a schematic view of a refrigerator recycling plant 1 according to a first embodiment of the invention, which plant comprises a refrigerator shredding device 10 having a sealed process chamber 12 and a mechanical shredding device 20 arranged in the process chamber 12 for mechanically shredding a refrigerator 22 (see, for example, Fig. 4). The refrigerator recycling plant 1 further comprises an inert gas source 30, which is connected to the process chamber 12 via an inert gas line 32 and is arranged, for example, directly upstream of the process chamber 12. From the inert gas source 30, inert gas, optionally nitrogen gas, can be supplied to the process chamber 12 in order to inertize the gases generated during the mechanical shredding of the refrigerators 22 in the process chamber 12 and thus minimize the risk of explosion within the process chamber 12. Inert gases other than nitrogen gas, e.g., CO2, could be used, for example.when using membrane technologies (see e.g. membrane device described below) have disadvantages with regard to diffusion behavior.

[0063] Furthermore, the refrigerator recycling plant 1 has a dehumidification and cooling device 40, which is connected to the process chamber 12 via a process gas line 50. The dehumidification and cooling device 40 is designed to receive process gas discharged from the process chamber 12, which contains hydrocarbon gas resulting from the mechanical comminution of the refrigerator 22. The dehumidification and cooling device 40 is likewise designed to cool the process gas to a dehumidification temperature, which is optionally in the range of 5°-20°, so that water can be separated from the process gas via condensation via a wastewater line 42 in order to dehumidify the process gas.

[0064] The refrigerator recycling system 1 further comprises a compressor 60, which is arranged downstream of the dehumidification-cooling device 40 in the process gas line 50. The compressor 60 is configured to compress the dehumidified process gas, optionally to a pressure in the range of 10-15 bar.

[0065] In addition, the refrigerator recycling plant 1 has a cooling device 70, which is arranged in the process gas line 50 downstream of the compressor 60 and, for example, immediately after the compressor 60. The cooling device 70 is designed to cool the compressed process gas to a separation operating temperature in the range of 5-15 °C in order to thereby separate the hydrocarbon contained in the process gas as liquid hydrocarbon via condensation.

[0066] In addition, the refrigerator recycling system 1 has a gas-liquid separation device 80, which is arranged downstream of and immediately after the cooling device 70 in the process gas line 50. The gas-liquid separation device 80 is configured to separate the liquid hydrocarbon separated from the compressed and cooled process gas from the remaining process gas via a liquid discharge line 82.

[0067] The refrigerator recycling plant 1 further comprises a membrane device 90, which is connected to the gas-liquid separation device 80 via a process gas return line 100. The membrane device 90 is configured to receive the remaining process gas from the gas-liquid separation device 80 via the process gas return line 100. The membrane device 90 is also configured to obtain a hydrocarbon-enriched recycle process gas from the remaining process gas on a permeate side 92 of the membrane device 90 and a hydrocarbon-poor continuation process gas on a retentate side 94 of the membrane device 90.The permeate side 92 of the membrane device 90 is connected via a hydrocarbon-enriched gas return line 110 to the process gas line 50 at a return point 112 upstream of the compressor 60 between the dehumidification-cooling device 40 and the compressor 60 in order to return the hydrocarbon-enriched recycle process gas to the process gas at this return point 112 in order to increase its hydrocarbon content. The retentate side 94 of the membrane device 90 is connected to a hydrocarbon-lean gas forward line 120 in order to forward the hydrocarbon-lean forward process gas. According to the present embodiment, the hydrocarbon-lean gas forward line 120 is connected to the process chamber 12 in order to supply hydrocarbon-lean forward gas to the process chamber 12. In this embodiment, the refrigerator shredding device 10 of the refrigerator recycling plant 1 is also provided with a heating device 130.The heating device 130 is directly connected to the process chamber 12 in order to heat, or be able to heat, the process chamber 12 to a comminution process temperature, which optionally lies in a range of 70° to 80°, in order to improve the release of gases from, for example, the foamed refrigerator insulation elements. An electric heating device, for example, can be used as the heating device 130.

[0068] The refrigerator shredding device 10 of the refrigerator recycling plant 1 is configured such that the refrigerators 22 to be shredded can be fed from outside the process chamber 12 by means of a refrigerator feed device 140 in order to supply the mechanical shredding device 20 with refrigerators 22 to be shredded and to shred them. The refrigerator recycling plant 1 is further provided with a small material removal device 150 in order to remove material 152 (see, for example, Fig. 4) of the refrigerators 22 that has been shredded by the mechanical shredding device 20 from the process chamber 12. The small material removal device 150 is connected to the process chamber 12 and configured to separate the shredded material 152 of the refrigerators 22 depending on the material properties of the shredded material 152 in order to be able to subsequently recycle and / or reuse it.

[0069] The cooling device 70, which here is arranged directly downstream of the compressor 60 and is designed to cool the process gas heated by the compressor 60 to the separation operating temperature in the range of 5-15°C, has a first cooling device heat exchanger 160. The first cooling device heat exchanger 160 is arranged on the one hand in the process gas line 50 and on the other hand is also arranged in the process gas return line 100, specifically between the gas-liquid separation device 80 and the membrane device 90. The first cooling device heat exchanger 160 is designed to allow the remaining process gas present in the process gas return line 100 to exchange heat with the compressed process gas. By means of this first cooling device heat exchanger 160, a (e.g. a first or first occurring) cooling of the compressed process gas takes place in an ef fi cient / cost-ef fi cient manner, since for this purpose the e.g.Untreated, remaining process gas from the gas-liquid separation device 80 is used as a heat exchange medium for cooling. For this purpose, the first cooling device heat exchanger 160 is arranged, for example, directly after the compressor 60 in the process gas line 50.

[0070] The cooling device 70 further comprises a first cooling device cooling apparatus 170, which in turn comprises a refrigeration unit (e.g. an electrically operated refrigeration unit) 172, a second cooling device heat exchanger 174 and a refrigerant line 176. The refrigerant line 176 connects the refrigeration unit 172 and the second cooling device heat exchanger 174 to one another and circulates a refrigerant which can be cooled by the refrigeration unit 172. The second cooling device heat exchanger 174 is arranged between the first cooling device heat exchanger 160 and the gas-liquid separation device 80 in the process gas line 50 and is configured to allow the refrigerant to exchange heat with the compressed process gas. Accordingly, hydrocarbon contained in the process gas can be separated via condensation in the second cooling device heat exchanger 174.In this exemplary embodiment, the dehumidification cooling device 40 is designed as a dehumidification heat exchanger, which is arranged, on the one hand, in the process gas line 50 and, on the other hand, in the refrigerant line 176 between (e.g., as here, directly between) the second cooling device heat exchanger 174 and the refrigeration unit 172 in the refrigerant line 176. The dehumidification cooling device 40, designed as a dehumidification heat exchanger, is configured to allow the refrigerant to exchange heat with the process gas in order to cool the process gas to the dehumidification temperature using residual cold from the refrigerant, thereby further increasing the efficiency of the refrigerator recycling system 1.

[0071] The cooling device 70 of the refrigerator recycling plant 1 further comprises a second cooling device cooling device 180, which in turn comprises an air cooler 182 with a cooling air fan (e.g., an electrically operated cooling air fan) 186, a third cooling device heat exchanger 184, and a coolant line 188. The coolant line 188 connects the air cooler 182 and the third heat exchanger 184 to one another and circulates a coolant that can be air-cooled by the air cooler 182 by means of the cooling air fan 186. In addition, the coolant line 188 is connected, or can be selectively connected, to the refrigeration unit 172 of the first cooling device cooling device 170 in order to be able to additionally cool the coolant (e.g., optionally, selectively, in a switchable manner). The third cooling device heat exchanger 184 is arranged between (e.g.,The second cooling device heat exchanger 174 is arranged in the process gas line 50 (e.g., directly between) the first cooling device heat exchanger 160 and the second cooling device heat exchanger 174 and is configured to allow the coolant to exchange heat with the compressed process gas. The second cooling device heat exchanger 174 is further connected (e.g., directly connected) to the gas-liquid separation device 80 via the process gas line 50 in order to supply the process gas with the hydrocarbon-containing condensate to the gas-liquid separation device 80.

[0072] In this exemplary embodiment, the refrigerator recycling system 1 has a liquid-liquid separation device 190 that is separate from the gas-liquid separation device 80. The liquid-liquid separation device 190 is connected to the gas-liquid separation device 80 via a liquid discharge line 192 and is designed to essentially automatically separate the water, which is heavier than the liquid hydrocarbon, via gravity. The water separated by the liquid-liquid separation device 190 and the liquid hydrocarbon can each be discharged via a wastewater connection line 194 of the refrigerator recycling system 1 and via a propellant discharge line 196 of the refrigerator recycling system 1. The waste water connection line 194 is further connected to the waste water line 42 of the dehumidifying cooling device 40 in order to further discharge the separated water to the waste water.The propellant discharge line 196 can be used, for example, to supply the liquid hydrocarbon to a propellant filling system.

[0073] The refrigerator recycling plant 1 here also comprises, for example, a pressure swing adsorption device 200, which is connected to the low-carbon gas feed line 120 between the membrane device 90 or its retentate side 94 and the process chamber 12 of the refrigerator shredding device 10. The pressure swing adsorption device 200 comprises two or more storage containers 202 with activated carbon material, an exhaust air line 204, a regeneration line 206, and a first and a second control valve 208, 209. The pressure swing adsorption device 200 is capable of having the hydrocarbon remaining in the feed process gas adsorbed by the activated carbon material, thereby generating substantially hydrocarbon-free exhaust air.The essentially hydrocarbon-free exhaust air can be discharged to the environment by actuating the two control valves 208, 209 via an exhaust air line 204 connected to the respective storage tank 202 and / or can be fed to one of the storage tanks 202 whose activated carbon material is to be regenerated by actuating the two control valves 208, 209 via the regeneration line 206.

[0074] The refrigerator recycling system 1 optionally has an additional inert gas supply line 210. The additional inert gas supply line 210 is connected to the inert gas source 30 and / or to the retentate side 94 of the membrane device 90 and is further connected between the dehumidification cooling device 40 and the compressor 60, or, for example, between the process chamber 12 and the dehumidification cooling device 40, to the process gas line 50 at an associated additional inert gas supply point 212. By means of the associated additional inert gas supply point 212, inert gas originating from the inert gas source 30 and / or HC-enriched gas can be supplied to the process gas in order, for example, to reduce the oxygen content in the process gas as needed.

[0075] The process gas line 50 of the refrigerator recycling system 1 here has, for example, an oxygen sensor 220 downstream of the additional inert gas supply point 212 between the dehumidification-cooling device 40 and the compressor 60. The oxygen sensor 220 is configured to detect the oxygen content in the process gas, wherein the predetermined oxygen content is optionally less than or equal to a limiting oxygen concentration (LCC) for the propellant, optionally in conjunction with nitrogen gas as an inert gas, e.g., less than or equal to 9.3%.

[0076] The refrigerator recycling system 1 here also has, for example, an electronic system control device 230, which is electrically connected to the oxygen sensor 200 and to a respective additional inert gas control valve 240 arranged in the respectively assigned additional inert gas supply line 210. The electronic system control device 230 is configured to control the respective additional inert gas control valve 240 based on the oxygen content received as electrical signals from the oxygen sensor 220 such that a predetermined oxygen content in the process gas is set at the level of the oxygen sensor 220.

[0077] Figure 2 shows a refrigerator recycling system 1 according to a second embodiment of the invention. The refrigerator recycling system 1 according to the second embodiment is essentially identical to that of the first embodiment, so that with regard to the similarities, reference is made to the preceding description, and the corresponding reference numerals are also shown in Figure 2. Therefore, only the differences will be discussed below.

[0078] In contrast to the embodiment of Figure 1, the embodiment of Figure 2 has a three-phase separation device 250 which replaces the gas-liquid separation device 80 and the liquid-liquid separation device 190 from the previous embodiment and which combines the functions of both the gas-liquid separation device 80 and the liquid-liquid separation device 190. This means that in the embodiment of Figure 2, the gas-liquid separation device 80 and the liquid-liquid separation device 190 are integrally formed in the form of the three-phase separation device 250, or the liquid-liquid separation device 190 is integrated into the gas-liquid separation device 80. The three-phase separation device 250 is capable of separating the liquid hydrocarbon process gas discharged from the cooling device 70 into a recycle process gas, liquid hydrocarbon and water.The recycle process gas is then fed to the membrane device 90 via the process gas return line 100, as in the first embodiment, and the water and the liquid hydrocarbon are each discharged separately via the wastewater connection line 194 and the propellant filling line 196. By means of the three-phase separation device 250, for example, the complexity of the refrigerator recycling system 1 can be reduced and the hydrocarbon recovery process can be further simplified.

[0079] Figure 3 shows a refrigerator recycling system 1 according to a third embodiment of the invention. The refrigerator recycling system 1 according to the third embodiment is essentially identical to that of the first embodiment, so that with regard to the similarities, reference is made to the preceding description, and the corresponding reference numerals are also shown in Figure 3. Therefore, only the differences will be discussed below.

[0080] In contrast to the exemplary embodiment of Figure 1, the heating device 130 in the exemplary embodiment of Figure 3 has a heat pump device 260 which has a heat pump supply line 261. The heat pump supply line 261 is connected after (in this case immediately after) the third cooling device heat exchanger 184 via an inlet point 262 to the coolant line 188 of the second cooling device device 180 and is connected again via a return point 263 before (in this case immediately before) the air cooler 182 to the coolant line 188 of the second cooling device device 180, wherein coolant from the third cooling device heat exchanger 184 is supplied to a heat pump 264 by means of the heat pump supply line 261 and the coolant is then returned from the heat pump 264 to the air cooler 182.

[0081] The heat pump device 260 further comprises the heat pump 264, which is connected to the heat pump supply line 261 between the inlet point 262 and the return point 23 of the heat pump supply line 262 and is configured to generate heat. Furthermore, the heat pump 264 can, for example, comprise a pump for conveying the coolant and / or heat pump control valves (not shown).

[0082] In addition, the heat pump device 260 has a heat pump discharge line 265, which is connected to the heat pump 264 and to a heat exchanger 266 arranged on the process chamber 12 (which is a component of the heating device 130), in order to transfer the heat generated by the heat pump 264 from the heat pump 264 to the process chamber 12. Furthermore, the heat pump device 260 has a coolant line control valve 267, which is arranged between the inlet point 262 and the return point 263 of the heat pump supply line 261 in the coolant line 188 and is configured to block or allow a coolant flow in the coolant line 188. Furthermore, the heating device 130 has an inlet control valve 268 and a return control valve 269, which are each assigned between the inlet point 262 and the

[0083] Heat pump 264 as well as the heat pump 264 and the return point

[0084] 263 and control the coolant flow in the heat pump supply line 261, wherein the coolant line control valve 267, the supply control valve 268, and the return control valve 269 are controllable / adjustable relative to one another by means of the electronic system control device 230. For example, the supply control valve 268 and the return control valve 269 can be open (e.g., in an open state) when the coolant line control valve 267 is closed (e.g., in a closed state), and vice versa.

[0085] By means of the heat pump device 260, residual cold from the coolant flowing from the third cooling device heat exchanger 184 to the air cooler 182 can be reused to feed the heat pump 264, which generates heat according to the principle of a heat engine and, in turn, supplies the heat to the process chamber 12 via the heat exchanger 266 to achieve the shredding process temperature. This further increases the energy efficiency of the refrigerator recycling plant.

[0086] Figure 4 shows a schematic view of a refrigerator shredding device 10 with, connected thereto, a refrigerator feed device 140 and small material removal device 150 of the refrigerator recycling plant 1 according to an embodiment which can be used, for example, in the embodiments of Figures 1 and 2.

[0087] The refrigerator feed device 140, e.g., a conveyor belt, is configured to feed refrigerators 22 sequentially, optionally individually, to the refrigerator shredding device 10 and consequently to the process chamber 12, and is, e.g., located directly upstream of the refrigerator shredding device 10. The material 152 of the refrigerators 22 shredded within the process chamber 12 is present, among other things, in granular form, wherein the small material removal device 150 is configured to remove the shredded material 152 of the refrigerators 22 from the process chamber 12 and to separate it according to the material properties of the shredded materials 152.

[0088] With reference to Figure 5, the mechanical comminution device 20 according to one embodiment of the present invention has, for example, exactly one rotary impact device 270. This is arranged in the process chamber 12, optionally at the bottom thereof, and has a rotating body 272. The rotating body 272 can be driven in rotation about a rotation axis A and is provided with two impact chains 274, which here are designed, for example, as ring chains. The impact chains 274 are each fastened by their chain ends 276 to the rotating body 272 outside its rotation axis A and each have a free chain end 268.The impact chains 274 with the free chain ends 268 are designed to generate a swirling material flow of the comminuted material 152 upon rotation of the rotating body 272 and thus of the impact chains 274, so that in addition to an interaction between the refrigerators 22 to be comminuted and the rotary impact device 270, an interaction is also generated within the comminuted material 152 itself. This intensifies the mechanical stress on the comminuted material 152, and in conjunction with an interaction between the comminuted material 152 and the process chamber 12 as well as the swirling material flow, the granular form of the comminuted material 152 is formed.

[0089] Figure 6 shows a sectional view of the sealed process chamber 12 of the refrigerator recycling plant 1 from Fig. 4 along the line BB. In this exemplary embodiment, four rotary impact devices 270 are arranged within the process chamber 12, which are arranged opposite one another in pairs, for example in a rectangular arrangement. For example, the rotary impact devices 270 which are horizontally opposite one another in the view in Fig. 6 are provided with the same direction of rotation, and the vertically opposite rotary impact devices 270 are provided with an opposite direction of rotation (see rotation arrows R), so that in addition to the swirling material flow of each rotary impact device 270, a translational material flow (translation arrow T) is also generated, for example through the process chamber 12 towards the small material discharge device 150, in order to feed the shredded material 152 in the direction of the small material discharge device 150.This exemplary arrangement of the rotary impact devices 270, including the respective rotation directions, can be configured in any manner to generate a directed material flow of the comminuted material 152 within the process chamber 12.

[0090] Figure 7 shows a flowchart of a method S300 for recycling refrigerators 22, which can be carried out, for example, with the refrigerator recycling system 1 according to the first embodiment of the invention. In a first step S320, refrigerators 22 are fed, optionally individually, to the process chamber 12 of the refrigerator shredding device 20 by means of the refrigerator feed device 140, e.g., the conveyor belt.

[0091] In a second step S330, inert gas, optionally nitrogen gas, is supplied to the process chamber 12, into which the refrigerators 22 were supplied by means of the refrigerator supply device 140, in order to inertize the process chamber 12. The supply S330 of inert gas can, for example, be carried out continuously during the process in order to maintain a consistently high inert gas content in the process chamber 12.

[0092] In a third step S350, the supplied refrigerators 22 are mechanically crushed by means of the at least one or more rotary impact devices 270 of the mechanical crushing device 20. The mechanical crushing S350 is carried out in such a way that the foamed insulation material present in the refrigerators 22 is crushed by the mechanical crushing device 20 into particles with a maximum circumferential diameter of 2 mm, optionally with a maximum circumferential diameter of 1 mm.

[0093] In a fourth step S360, the gas present in the process chamber 12 is removed as hydrocarbon-containing process gas from the process chamber 12 via the process gas line 50 (e.g. sucked off) and then fed to the dehumidification cooling device 40, which is located downstream of the process chamber 12.

[0094] In a fifth step S370, the process gas supplied from the process chamber 12 via the process gas line 50 is cooled by the dehumidification / cooling device 40, which is designed as a dehumidification / heat exchanger. The process gas is preferably cooled to a temperature in a range of 5-20°C in order to dehumidify the process gas via condensation and to discharge the condensate via the wastewater line 42 connected to the dehumidification / cooling device 40. The dehumidified gas is then fed to the compressor 60 via the process gas line 50.

[0095] In a sixth step S390, the dehumidified process gas supplied to the compressor 60 is compressed to a pressure that is optionally in the range of 10-15 bar, thereby heating the dehumidified process gas. The pressure increase serves to raise the dew point of the hydrocarbons present in the process gas, thus enabling easier, energy-efficient separation of these hydrocarbons.

[0096] In a seventh step S400, the compressed process gas is fed to the cooling device 70 via the process gas line 50, in order to be subsequently cooled to a temperature in the range of 5-15 °C by means of the heat exchangers 160, 174, 184. Due to the increased dew point, the cooling of the process gas causes hydrocarbon to be separated again via condensation, and the process gas with liquid hydrocarbon is fed to the gas-liquid separation device 80 via the process gas line 50.

[0097] In an eighth step S410, the hydrocarbon, which is now largely liquid in the process gas, is separated from the remaining process gas in the gas-liquid separation device 80 by discharging the liquid hydrocarbon through the liquid discharge line 82 and passing the remaining process gas further via the process gas return line 100.

[0098] In a ninth step S420, the remaining process gas in the process gas return line 100 is fed to the membrane device 90. From the membrane device 90, the hydrocarbon-enriched return process gas is obtained from the remaining process gas on the permeate side 92 of the membrane device 90, and the hydrocarbon-free further process gas is obtained on the retentate side 94 of the membrane device 90.

[0099] In a tenth step S430, the recycle process gas is returned to the process gas. For this purpose, the recycle process gas is fed to the process gas in the process gas line 50 via the hydrocarbon-enriched gas return line 110 at the return point 112 upstream of the compressor 60, optionally between the dehumidification-cooling device 40 and the compressor 60, in order to increase the hydrocarbon content of the process gas in the process gas line 50.

[0100] Figure 8 shows a flow chart of the method S300 for recycling refrigerators 22 according to Figure 7 with additional steps. In an additional step S340, the process chamber 12 is additionally heated in a feedback-controlled manner (this control can be carried out, for example, by means of the system control device 230 of the refrigerator recycling system 1) in order to set the predetermined shredding process temperature, which optionally lies in the range of 70-80 °C. The feedback-controlled heating S340 can, for example, take place in parallel to the previous steps S310-S330 and, for example, permanently throughout the entire method S300 in order to keep the temperature of the process chamber 12 at a constant level.

[0101] In a further additional step S310, refrigerator compressors of the refrigerators 22 (to be recycled) and optionally refrigerator refrigerant lines of the refrigerators 22 (to be recycled) are removed from the refrigerators 22 before the refrigerators 22 are fed S320 into the process chamber 12. In this case, the refrigerators 22, with the exception of the refrigerator compressors and optionally with the exception of the removed refrigerator refrigerant lines, are otherwise fed completely, as received by the refrigerator feed device 140, to the process chamber 12 for mechanical comminution S350. This serves, for example, to prevent high wear on the impact chains 274 of the rotary impact device 22 due to metal parts of the refrigerator compressors and / or refrigerator refrigerant lines striking them.In a further additional step S380, additional inert gas, optionally nitrogen gas, and / or continued process gas is supplied to the process gas at the assigned additional inert gas supply point 212 between the compressor 60 and the dehumidification-cooling device 40. Furthermore, inert gas, optionally nitrogen gas, and / or continued process gas can also be additionally supplied in parallel or independently to the return process gas at the correspondingly assigned additional inert gas supply point 212. The additional supply S380 takes place, for example, in a return-controlled manner such that the oxygen content of the process gas entering the compressor 60 is less than or equal to the limiting oxygen concentration (LCC) for the propellant, optionally in conjunction with nitrogen gas as an inert gas, for example, less than or equal to 9.3 mol%, thus enabling efficient operation of the membrane device 90.

[0102] List of reference symbols:

[0103] 1 Kühls ehr ankrecyclmganl age

[0104] 10 Refrigerator shredding device

[0105] 12 trial chamber

[0106] 20 mechanical crushing device

[0107] 22 Refrigerator

[0108] 30 Inert gas source

[0109] 32 Inert gas line

[0110] 40 Dehumidification and cooling device

[0111] 42 sewer line

[0112] 50 Process gas line

[0113] 60 compressors

[0114] 70 cooling equipment

[0115] 80 Gas-liquid separator

[0116] 82 Liquid drainage line

[0117] 90 Membrane device

[0118] 92 Permeate side

[0119] 94 Retentate side

[0120] 100 Process gas return line

[0121] 110 KW enriched gas return line

[0122] 112 return parts

[0123] 120 KW low-gas pipeline

[0124] 130 Heating device refrigerator feed device

[0125] Small material removal device shredded material first cooling device heats up rather first cooling device cooling device refrigeration unit second cooling device heats up rather refrigerant line second cooling device

[0126] Air cooler third cooling device - heats from rather

[0127] Cooling air fan

[0128] coolant line

[0129] Liquid-liquid separator

[0130] Liquid drainage line

[0131] Wastewater connection line

[0132] Propellant discharge line

[0133] Pressure swing adsorption device storage tank

[0134] Exhaust air duct

[0135] Regeneration line first control valve second control valve

[0136] Additional inert gas supply line

[0137] Additional inert gas supply parts

[0138] oxygen sensor

[0139] System control device

[0140] Additional inert gas control valve

[0141] Three-phase separation device

[0142] Heat pump device

[0143] Heat pump supply line

[0144] Inlet point

[0145] Return point

[0146] heat pump

[0147] Heat pump discharge line

[0148] heat exchanger

[0149] Heat pump control valve

[0150] Inlet control valve

[0151] Return control valve

[0152] Rot at ions impact device

[0153] Rotational body

[0154] Impact chain

[0155] Chain end

Claims

Claims 1. Refrigerator recycling plant (1) with - a refrigerator crushing device (10) having a sealed process chamber (12) and a mechanical crushing device (20) arranged in the process chamber (12) for mechanically crushing a refrigerator (22), - an inert gas source (30), optionally a nitrogen gas source, which is connected to the process chamber (12) and from which inert gas, optionally nitrogen gas, can be supplied to the process chamber (12), - a dehumidification-cooling device (40) which is connected to the process chamber (12) via a process gas line (50) in order to receive process gas discharged from the process chamber (12) which contains hydrocarbon gas resulting from the mechanical comminution of the refrigerator (22), and which is designed to cool the process gas to a Dehumidification temperature, which is optionally in the range of 5°-20°, to cool down so that water is separated from the process gas via condensation in order to dehumidify the process gas, - a compressor (60) arranged downstream of the dehumidification-cooling device (40) in the process gas line (50) and arranged to compress the dehumidified process gas, optionally to a pressure in the range of 10-15 bar, - a cooling device (70) which is arranged downstream of the compressor (60) in the process gas line (50) and which is designed to cool the compressed process gas to a separation operating temperature in the range of 5-15°C in order to thereby separate hydrocarbon contained in the process gas via condensation as a liquid hydrocarbon, - a gas-liquid separator (80) arranged downstream of the cooling device (70) in the Process gas line (50) is arranged and which is designed to separate the liquid hydrocarbon separated from the compressed and cooled process gas from the remaining process gas, a membrane device (90), - which is connected to the gas-liquid separation device (80) via a process gas return line (100) in order to receive the remaining process gas, - which is arranged in such a way that a hydrocarbon-enriched recycle process gas is obtained from the remaining process gas on a permeate side (92) of the membrane device (90) and a hydrocarbon-poor further process gas is obtained on a retentate side (94) of the membrane device (90), - the permeate side (92) of which is connected via a hydrocarbon-enriched gas return line (110) to the process gas line (50) at a return point (112) upstream of the compressor (60), optionally between the dehumidifying cooling device (40) and the compressor (60), in order to return the hydrocarbon-enriched return process gas to the process gas at this return point (112) in order to increase its hydrocarbon content, and - the retentate side (94) of which is connected to a hydrocarbon-poor gas forwarding line (120) in order to forward the hydrocarbon-poor forwarding process gas.

2. Refrigerator recycling plant (1) according to claim 1, wherein the refrigerator crushing device (10) is provided with a heating device (130) connected to the process chamber (12) for heating the process chamber (12) to a crushing process temperature, which is optionally in a range of 70° to 80°.

3. Refrigerator recycling plant (1) according to claim 1 or 2, wherein the mechanical shredding device (20) has a rotary impact device (270) which has one or more rotary bodies (272) which are arranged in the process chamber (12), optionally on the floor of the process chamber (12), so as to be rotatably driven about a rotation axis (A), and which are each provided with at least one impact chain (274) which is fastened with one chain end to the rotary body (276) outside its rotation axis (A) and which has another, free chain end (268), wherein the respective impact chain (272) optionally has a length in a range of 30-50 cm, and wherein the respective impact chain (272) is optionally designed as a ring chain.

4. Refrigerator recycling plant (1) according to one of claims 1-3, wherein the cooling device (70) has a first cooling device heat exchanger (160) which is further arranged in the process gas return line (100) between the gas-liquid separation device (80) and the membrane device (90) and which is configured to allow the remaining process gas present in the process gas return line (100) to exchange heat with the compressed process gas.

5. Refrigerator recycling plant (1) according to claim 4, wherein the cooling device (70) comprises a first cooling device cooling device (170) which comprises a refrigeration unit (172), a second cooling device heat exchanger (174) and a refrigerant line (176) which connects the refrigeration unit (172) and the second cooling device heat exchanger (174) to one another and in which a refrigerant circulates which can be cooled by the refrigeration unit (172), wherein the second cooling device heat exchanger (174) is arranged between the first cooling device heat exchanger (160) and the gas-liquid separation device (80) and is arranged to allow the refrigerant to exchange heat with the compressed process gas, wherein optionally the dehumidification cooling device (40) is designed as a dehumidification heat exchanger which is arranged downstream of the second cooling device heat exchanger (174) in the refrigerant line (176) and is arranged to allow the refrigerant to exchange heat with the process gas in order to cool the process gas to the dehumidification temperature.

6. Refrigerator recycling plant (1) according to claim 5, wherein the cooling device (70) has a second cooling device cooling device (180) which has an air cooler (182) with a cooling air fan (186), a third cooling device heat exchanger (184) and a coolant line (188) which connects the air cooler (182) and the third cooling device heat exchanger (184) to one another and in which a coolant circulates which can be air-cooled by the air cooler (182) by means of the cooling air fan (186), wherein the third cooling device heat exchanger (184) is arranged between the first cooling device heat exchanger (184) and the second cooling device heat exchanger (174) and is configured to allow the coolant to exchange heat with the compressed process gas.

7. Refrigerator recycling plant (1) according to one of claims 1-6, - wherein the low-hydrocarbon gas feed line (120) is connected to the process chamber (12) so that the low-hydrocarbon feed process gas can be fed to the process chamber (12), and / or - wherein the low-carbon gas forwarding line (120) is connected to a pressure swing adsorption device (200) (PWA device) which comprises two or more storage containers (202) with activated carbon material, wherein the hydrocarbon remaining in the forward process gas can be adsorbed by the activated carbon material in order to thereby generate substantially hydrocarbon-free exhaust air, which can be discharged to the environment via an exhaust air line (204) connected to the respective storage container (202) and / or which can be fed via a regeneration line (206) to one of the storage containers (202) whose activated carbon material is to be regenerated.

8. Refrigerator recycling plant (1) according to one of claims 1- 7, further comprising a liquid-liquid separator (190), - which is either formed integrally with the gas-liquid separation device (80, 82) or which is connected to the gas-liquid separation device (80) via a liquid discharge line (192) in order to receive the separated liquid hydrocarbon therefrom, and - which is designed to separate remaining water from the separated liquid hydrocarbon.

9. Refrigerator recycling plant (1) according to one of claims 1- 8, further comprising a small material removal device (150) which is connected to the process chamber (12) in order to remove the material (152) comminuted by the mechanical comminution device (20) from the process chamber (12).

10. Refrigerator recycling plant (1) according to one of claims 1-9, wherein the inert gas source (30) and / or the retentate side (94) of the membrane device (90) are further connected via a respective additional inert gas supply line (210) - with the HC-enriched gas return line (110) and / or - between the dehumidification cooling device (40) and the Compressor (60) is / are connected to the process gas line (50) at an associated additional inert gas supply point (212), so that inert gas originating from the inert gas source (30) and / or HC-enriched gas can be supplied to the process gas via the associated additional inert gas supply point (212) in order to reduce the oxygen content in the process gas, wherein an oxygen sensor (220) is arranged in the process gas line (50) downstream of the respective additional inert gas supply point (212) in order to detect the oxygen content in the process gas, and wherein the refrigerator recycling system (1) is further provided with an electronic system control device (230) which is electrically connected to the oxygen sensor (220) and to a respective additional inert gas control valve (240) arranged in the respectively associated additional inert gas supply line (210), and which is set up,to control the respective additional inert gas control valve (240) on the basis of the oxygen contents received from the oxygen sensor (220) as electrical signals so that a predetermined oxygen content in the process gas is set at the level of the oxygen sensor (220).

11. Refrigerator recycling plant (1) according to one of claims 7-10 when in combination with claims 2 and 6, wherein the heating device (130) comprises a heat pump device (260) comprising: - a heat pump supply line (261) which is connected to the coolant line (188) of the second cooling device (180) via an inlet point (262) and a return point (263), - a heat pump (264) connected to the heat pump supply line (261), - a heat pump discharge line (265) which is connected to the heat pump (264) and to a heat exchanger (266) of the heating device (130) arranged on the process chamber (12) is connected, by means of which the heat from the heat pump (264) can be transferred to the process chamber (12).

12. A method (S300) for recycling refrigerators (22), optionally by means of a refrigerator recycling plant (1) according to one of claims 1-10, comprising the steps: - feeding (S320), optionally individual feeding, of the refrigerators (22) into a process chamber (12), - Supplying (S330) inert gas, optionally nitrogen gas, into the process chamber (12), - mechanical crushing (S350) of the respective refrigerator (22) in the process chamber (12), - discharging (S360) gas present in the process chamber (12) as process gas from the process chamber (12) and supplying the process gas to a dehumidification cooling device (40), - Cooling (S370) the process gas by means of the dehumidification cooling device (40) to a temperature which is optionally in the range of 5-20°C in order to dehumidify the process gas by condensing and separating water contained in the process gas, - compression (S390) of the dehumidified process gas by means of a compressor (60), optionally to a pressure in the range of 10-15 bar, - cooling (S400) the compressed process gas in a cooling device (70) to a separation operating temperature in the range of 5-15°C in order to separate hydrocarbon contained in the process gas via condensation as a liquid hydrocarbon, - separating (S410) the liquid hydrocarbon separated from the compressed and cooled process gas from the remaining process gas by means of a gas-liquid separation device (80), - feeding (S420) the remaining process gas to a membrane device (90), from which the remaining process gas is discharged on a permeate side (92) of the membrane device (90) a hydrocarbon-enriched recycle process gas and on a retentate side (94) of the membrane device (90) a hydrocarbon-poor further process gas is obtained, - Returning (S430) the return process gas to the process gas in the process gas line (50) at a return point (112) upstream of the compressor (60), optionally between the dehumidification-cooling device (40) and the compressor (60), in order to increase the hydrocarbon content of the process gas.

13. The method (S300) according to claim 12, further comprising - Additional supply (S380) of inert gas, optionally of Nitrogen gas, and / or the continuation process gas to the process gas at an associated additional inert gas supply point (212) between the compressor (60) and the dehumidification-cooling device (40), and / or to the return process gas at a correspondingly associated additional inert gas supply point (212) in a return-controlled manner such that the oxygen content of the process gas entering the compressor (60) is less than or equal to an oxygen limit concentration (SGK) for the propellant, and optionally - feedback-controlled heating (S340) of the process chamber (12) in order to set a predetermined comminution process temperature therein, which is optionally in the range of 70-80°.

14. The method (S300) according to claim 12 or 13, further comprising Removing (S310) refrigerator compressors and optionally removing refrigerator refrigerant lines from the refrigerators (22) before feeding (S320) the refrigerators (22) into the process chamber (12), wherein the refrigerators (22) are fed to the process chamber (12) completely as received, with the exception of the removed refrigerator compressors and optionally with the exception of the removed refrigerator refrigerant lines.

15. Method (S300) according to one of claims 12-14, wherein the mechanical comminution is carried out in such a way that foamed insulation material present in the refrigerators (22) is comminuted into particles having a size of maximum 2 mm circumferential diameter, optionally of maximum 1 mm circumferential diameter.

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