Centrifuge having a compressor cooling device, and method for controlling a compressor cooling device of a centrifuge

1. A laboratory centrifuge with a centrifuge bowl and a compressor cooling device, comprising:

a refrigeration cycle;

an evaporator;

a condenser; and

a compressor,

wherein the refrigeration cycle includes at least one continuously variable controllable throttle device upstream of the evaporator,

wherein the at least one continuously variable controllable throttle device acts as an expansion element for regulating a refrigerant flow,

wherein devices for determining an actual temperature of the centrifuge bowl of the centrifuge are provided,

wherein the compressor is configured controllable with respect to its feed volume,

wherein a nominal temperature of the centrifuge bowl is predetermined,

wherein a tolerance range of +/−5K about the nominal temperature of the centrifuge bowl is predetermined,

wherein the laboratory centrifuge is configured to adjust the at least one continuously variable controllable throttle device to a predetermined refrigerant flow upon startup of the compressor cooling device, and

wherein the laboratory centrifuge is configured to lower the actual temperature in the centrifuge bowl into the tolerance range through the controllable compressor and to keep compressor power constant thereafter as on as the actual temperature of the centrifuge bowl is in the tolerance range,

wherein the actual temperature of the centrifuge bowl is regulated exclusively by the at least one continuously variable controllable throttle device as long as the actual temperature of the centrifuge bowl is in the tolerance range, and

wherein the controllable compressor and the at least one continuously variable controllable throttle device are controlled by at least one regulation device.

2. The laboratory centrifuge according to claim 1 ,

wherein at least one device is provided for detecting a first temperature of the refrigerant upstream of the evaporator and a second temperature of the refrigerant downstream of the evaporator or the actual temperature of the centrifuge bowl.

3. The laboratory centrifuge according to claim 1 ,

wherein the compressor is power controllable with respect to its feed volume or frequency controllable, or

wherein a bypass is configured in the refrigeration cycle for bridging the evaporator, and

wherein the bypass is configured regulatable through a second controllable throttle device.

4. The laboratory centrifuge according to claim 1 ,

wherein regulation devices are provided which use at least one detected temperature from the group consisting of: the first temperature of the refrigerant upstream of the evaporator, the second temperature of the refrigerant downstream of the evaporator, and the actual temperature of the centrifuge bowl as an input value, and

wherein the regulation devices control and regulate at least one of the elements from the group consisting of the at least one continuously variable Controllable throttle device, controllable bypass and the controllable compressor.

5. The laboratory centrifuge according to claim 1 ,

wherein devices for determining a tendency of the actual temperature of the centrifuge bowl in a predetermined tendency period are provided, and

wherein the laboratory centrifuge is configured to regulate the at least one continuously variable controllable throttle device up or down when the tendency of the of the actual temperature of the centrifuge bowl in the tendency period increases or decreases.

6. The laboratory centrifuge according to claim 1 , wherein the at least one continuously variable controllable throttle device is configured as an electronic injection valve.

7. The laboratory centrifuge according to claim 1 ,

wherein the laboratory centrifuge includes regulation capable of coarse regulation and fine regulation,

wherein the regulation controls the compressor and the at least one continuously variable controllable throttle device, or only the compressor in a first coarse regulating step, and

wherein a regulation through the at least one continuously variable controllable throttle device without regulating the compressor is performed in a second fine regulating step.

8. The centrifuge according to claim 1 ,

wherein the regulation is configured so that the nominal temperature of the centrifuge bowl of the centrifuge is predeterminable and the actual temperature of the centrifuge bowl of the centrifuge is determinable,

wherein the tolerance range about the nominal temperature is predeterminable which tolerance range is +/−5 K at the most,

wherein the actual temperature of the centrifuge bowl is reducible through the compressor into the tolerance range upon start up of the compressor cooling device, and

wherein the compressor power is maintained to be constant as long as the actual temperature of the centrifuge bowl is in the tolerance range and the actual temperature of the centrifuge bowl is regulatable through the at least one continuously variable controllable throttle device.

9. The centrifuge according to claim 8 ,

wherein the regulation is configured to consider a tendency of the actual temperature of the centrifuge bowl, and

wherein a tendency period of at least 10 s is adjustable.

10. A method for controlling and regulating the compressor cooling device of the laboratory centrifuge with the centrifuge bowl according to claim 1 , comprising the steps:

using the at least one continuously variable controllable throttle device upstream of the evaporator for regulating the refrigerant flow in the refrigeration cycle of the compressor cooling device;

controlling the compressor with respect to its feed volume;

predetermining the nominal temperature of the centrifuge bowl;

determining the actual temperature of the centrifuge bowl of the centrifuge;

predetermining a tolerance range of +/−5K at the most about the nominal temperature of the centrifuge bowl;

adjusting the at least one continuously variable controllable throttle device to the predetermined refrigerant flow upon startup of the compressor cooling device;

lowering the actual temperature of the centrifuge bowl into the tolerance range through the controllable compressor; and thereafter

keeping the compressor power constant as long as the actual temperature of the centrifuge bowl is in the tolerance range and the actual temperature of the centrifuge bowl is regulated by the controllable throttle device.

11. The method according to claim 10 ,

wherein a tendency of the actual temperature of the centrifuge bowl is determined in a predetermined tendency period,

wherein the tendency period is at least 10 s, or

wherein the at least one continuously variable controllable throttle device is regulated up or down when the tendency of the actual temperature of the centrifuge bowl increases or decreases during the tendency period.

12. The method according to claim 11 ,

wherein the tolerance range about the nominal temperature of the centrifuge bowl is +/−3 K at the most, and

wherein the actual temperature of the centrifuge bowl is regulated by the at least one continuously variable controllable throttle device when the actual temperature of the centrifuge bowl is within the tolerance range, and

wherein the controllable compressor is used and the compressor is controlled when the actual temperature of the centrifuge bowl exceeds or undercuts the tolerance range so that the actual temperature of the centrifuge bowl returns into the tolerance range.

13. The method according to claim 11 ,

wherein the compressor is regulated over a first time period until the actual temperature of the centrifuge bowl is within the tolerance range for a second time period, which is 60 times the tendency period at the most, and

wherein the compressor power is kept constant thereafter as long as the actual temperature of the centrifuge bowl is in the tolerance range and the actual temperature of the centrifuge bowl is controlled by the at least one continuously variable controllable throttle device.

14. The method according to claim 10 ,

wherein a temperature of the refrigerant in the refrigeration cycle is determined

a) upstream of the evaporator,

b) downstream of the evaporator, and

wherein the at least one continuously variable controllable throttle device is regulated so that a difference of the temperature of the refrigerant in the refrigeration cycle upstream of the evaporator and the temperature of the refrigerant in the refrigeration cycle downstream of the evaporator is between 0 K and 5 K.

15. The method according to claim 10 ,

wherein the temperature of the refrigerant in the refrigeration cycle is determined upstream of the evaporator and when undercutting a predetermined minimum temperature the predetermined minimum temperature is at least reached again through one of the subsequent measures:

lowering the feed volume of the compressor;

opening and regulating a bypass which circumvents the condenser in the refrigeration cycle; and

regulating the controllable throttle device for increasing the refrigerant flow in the refrigeration cycle of the compressor cooling device.

16. The method according to claim 10 ,

wherein an early cut off value is provided above the nominal temperature of the centrifuge bowl or above the tolerance range, and

wherein the compressor is regulated down or switched off or the at least one continuously variable controllable throttle device is actuated in a closing direction when reaching the early cutoff value with the actual temperature of the centrifuge bowl.

17. The method according to claim 10 , wherein an electronic injection valve is used for the at least one continuously variable controllable throttle device.

18. The laboratory centrifuge according to claim 1 ,

wherein at least one device is provided for detecting a first temperature of the refrigerant upstream of the evaporator and a second temperature of the refrigerant downstream of the evaporator and the actual temperature of the centrifuge bowl.

19. The laboratory centrifuge according to claim 1 , wherein the compressor is power controllable with respect to its feed volume or frequency controllable and

wherein a bypass is configured in the refrigeration cycle for bridging the evaporator, and

wherein the bypass is configured regulatable through a second controllable throttle device.

20. The method according to claim 10 ,

wherein a tendency of the actual temperature of the centrifuge bowl is determined in a predetermined tendency period,

wherein the tendency period is at least 10 s, and

wherein the at least one continuously variable controllable throttle device is regulated up or down when the tendency of the actual temperature of the centrifuge bowl increases or decreases during the tendency period.