Method for operating a liquid ring compressor
The invention relates to a method of operating a liquid ring compressor having an impeller installed eccentrically in a compressor body, with gas being supplied to the liquid ring compressor on a suction side and gas being discharged from the liquid ring compressor on a pressure side. A liquid ring is generated in the liquid ring compressor on the inside of the compressor body by rotation of the impeller. Chambers are formed between blades of the impeller and the liquid ring and gas is drawn into these. The gas is compressed in the chambers which become smaller from the suction side to the pressure side as a result of the rotation of the eccentrically mounted impeller. The compressed gas is ejected on the pressure side. An ionic liquid is used as service liquid for generation of the liquid ring.
1. A method of operating a liquid ring compressor having an impeller installed eccentrically in a compressor body, with gas being supplied to the liquid ring compressor on a suction side and gas being ejected from the liquid ring compressor on a pressure side, which comprises the following steps:
i) generating a liquid ring on the inside of the compressor body by rotation of an impeller mounted eccentrically in the body,
ii) drawing of gas into chambers formed between blades of the impeller and the liquid ring,
iii) compressing the gas in the chambers which become smaller from the suction side to the pressure side as a result of the rotation and the eccentric positioning of the impeller,
iv) ejecting the compressed gas on the pressure side and passing the gas ejected on the pressure side to a liquid precipitator,
wherein an ionic liquid is used as service liquid for generation of the liquid ring.
2. The method according to claim 1 , wherein the pressure on the suction side is less than atmospheric pressure and that on the pressure side is equal to atmospheric pressure.
3. The method according to claim 1 , wherein the pressure on the suction side is equal to atmospheric pressure and that on the pressure side is greater than atmospheric pressure.
4. The method according to claim 1 , including returning the liquid separated off in the liquid precipitator to the liquid ring compressor.
5. The method according to claim 1 , including heating or cooling apparatuses through which the ionic liquid flows to maintain the apparatuses at the operating temperature.
6. The method according to claim 1 , wherein the ionic liquid has a viscosity in the range from 10 to 200 mPas at the operating temperature of the liquid ring compressor.
7. The method according to claim 1 , wherein the ionic liquid is chemically inert and thermally stable at the operating temperature of the liquid ring compressor.
8. The method according to claim 1 , wherein the ionic liquid is not corrosive.
9. The method according to claim 1 , wherein the ionic liquid has a melting point below 100° C.
10. The method according to claim 1 , wherein the operating temperature of the liquid ring compressor is in the range from 25 to 100° C.
11. The method according to claim 1 , wherein the ionic liquid contains sulfate, hydrogensulfate, alkylsulfate, thiocyanate, phosphate, borate, tetrakis-hydrogensulfatoborate or silicate ions.