GAS HEATING APPARATUS FOR DISPOSABLE BIOREACTOR

1 . A bioreactor comprising:

a single-use circular bag with a top and a bottom, sealed edge, and capable of holding a nutrient media;

at least one gas/liquid inlet connected at the top surface;

at least one liquid outlet connected to the bottom surface;

a heating and cooling element connected to gas/liquid inlet;

at least one tubular porous pouch connected to the gas/liquid inlet and disposed inside the bag;

at least one temperature sensor disposed inside or outside of the bag; and

a controller to adjust the temperature of an inlet gas.

2 . The bioreactor of claim 1 , wherein the bag further comprises additional sensors.

3 . The bioreactor of claim 2 , wherein the sensors are selected from pH, pO2 or pCO2 measurement.

4 . The bioreactor of claim 1 , wherein the gas/liquid inlet is further comprises a mass flow controller to mix a plurality of gases.

5 . The bioreactor of claim 1 , wherein the tubular porous pouch is tufted.

6 . The bioreactor of claim 1 , further comprising a plurality of tubular porous pouches connected to the gas/liquid inlet.

7 . The bioreactor of claim 1 , wherein the tubular porous pouch is secured to the bottom inner surface of the bag.

8 . The bioreactor of claim 1 , wherein the pore size of porous pouch is 5-300 microns.

9 . The bioreactor of claim 1 , wherein the bag is lined with a layer of a polytetrafluoroethylene membrane.

10 . The bioreactor of claim 1 , wherein the sealed edge of the bag includes holes, grommets or other devices for holding the bag on a supporting base.

11 . The bioreactor of claim 10 , wherein the supporting base is a metal mesh, a perforated plastic sheet, or perforated glass.

12 . The bioreactor of claim 11 , further comprising at least one source of acoustic radiation attached below the perforated surface of the support.

13 . The bioreactor of claim 12 , wherein the acoustic radiation source is capable of producing acoustic waves from 2-300 Hz.

14 . The bioreactor of claim 1 , wherein the gas outlet is connected to a condenser to condense liquid particles.

15 . The bioreactor of claim 14 , wherein the condenser has a cooling surface capable of reaching temperatures sufficient to freeze the liquid particles.

16 . A method of cultivating and harvesting proteins comprising:

providing the bioreactor of claim 1 ;

providing a sufficient quantity of nutrient media and biological culture to produce a target protein;

heating the nutrient media and biological culture by starting flow of heated gas;

starting the acoustic radiation;

adjusting reaction conditions as needed for optimal growth and expression of proteins;

closing the gas/liquid inlet to stop flow of gas and opening the gas/liquid inlet to introduce a binding resin after the cycle of upstream expression is complete;

closing the gas/liquid port liquid inlet and opening the gal/liquid port gas inlet;

adjusting the temperature of inlet gas to a suitable temperature optimal for binding of protein to the resin.

draining the nutrient media and biological culture upon completion of binding of proteins to resin through liquid outlet;

washing the resin in the tubular porous pouch with a washing liquid entered through the gas/liquid inlet;

eluting the protein by washing with an eluting medium and collecting the protein solution through liquid outlet.

17 . The method of claim 16 , wherein the temperature of gas is programmed to change during the cultivation of biological entities.

18 . The method of claim 17 , wherein the gas is a mixture of nutrient gases such as oxygen (O2) or carbon dioxide (CO2) and inert gases such as nitrogen (N2), helium (He), neon (Ne), argon (Ar), krypton (Kr), xenon (Xe), or radon (Rn), or a mixture thereof.

19 . The method of claim 17 , wherein the composition of the mixture of gas is altered during the cultivation of biological entities.

20 . The method of claim 14 , wherein the frequency of the acoustic waves is altered during the cultivation, washing and elution stages.