container ( 1 ) ( fig1 ) contains the load , for example , in the form of packaged fruits ( 2 ). transfer and stirring of gas medium inside the container is ensured by the charger ( 3 ). the device for control of the gas medium inside the container ( 1 ) is embodied in the form of a chamber ( 4 ) with an inner space ( 5 ) ( see fig2 ) and a gas - permeable membrane ( 6 ). the membrane separates the inner space ( 5 ) of chamber ( 4 ) from the external ambient air . a connecting pipe ( 7 ) of the container ( 1 ) and the hose ( 8 ) form a channel for uptake of the gas medium from the container ( 1 ) and for feeding it into the chamber ( 4 ). the connecting pipe ( 9 ) and the hose ( 10 ) form a channel for return of the modified gas medium from the chamber ( 4 ) to the container ( 1 ). valves ( 11 and 12 ) are installed on connecting pipes ( 7 and 9 ). these valves are connected to the corresponding control system ( not shown in fig1 ), containing sensors and devices controlling the operation of the valves ( 11 , 12 ) and the charger ( 3 ). the device for controlling the gas medium composition in the container ( 2 ), in the above - described design alternative , operates as follows : to modify the gas medium , the chamber ( 4 ) is connected to connecting pipes ( 7 and 9 ) using hoses ( 8 and 10 ). valves ( 11 and 12 ) are opened by the control system and if the charger ( 3 ) has not yet been turned on by the time , it is switched on . the gas medium from the container ( 1 ) begins to enter the inner space ( 5 ) of the chamber ( 4 ) through the connecting pipe ( 7 ) and hose ( 8 ). the gas exchange between the gas remaining in the inner space ( 5 ) of the chamber ( 4 ) and external atmospheric air occurs via the gas - permeable membrane ( 6 ). the direction of the gas exchange is determined by the difference in concentration of gas medium components of the container ( 1 ) and external ambient air . the circulation of the gas medium of the container ( 1 ) through the chamber ( 4 ) is accompanied by its gradual modification . valves ( 11 and 12 ) are closed when the required composition of the gas medium in the container ( 1 ) is achieved . after that , the chamber ( 4 ) can be disconnected from the container ( 1 ), or it can remain connected for further atmospheric modification , as needed . as an example , let us consider the device as applied to shipping green bananas in the container . in this case , to prevent early ripening and spoilage of bananas , in addition to a reduced temperature ( about 14 ° c . ), it is necessary to maintain the gas medium in the container with reduced oxygen content ( relative to ambient air )— about 2 - 4 %, and increased carbon dioxide content ( relative to ambient air )— about 4 - 7 %. however , during storage , the bananas absorb oxygen and release carbon dioxide , which leads to the reduction of the oxygen content ( which gets lower than the normal value ) and to the increase of the carbon dioxide concentration ( which gets higher than the normal value ) in the container . to maintain the required composition of the gas medium in the container , the gas - permeable membrane ( 6 ) of the chamber ( 4 ) is characterized by a ratio of permeability values of carbon dioxide and oxygen of about “ 4 ”, which means that v ( co 2 )/ v ( o 2 )≈ 4 , taking into account the ratio of concentrations of carbon dioxide in the container and in ambient air ( which , in the latter case , constitutes approximately 0 . 03 % for carbon dioxide and approximately 21 % for oxygen ) based upon the above - described gas exchange in the chamber , the concentration of carbon dioxide needs to be reduced , while the oxygen concentration needs to be increased . furthermore , gas of modified composition from the chamber ( 4 ) passes from the chamber to the container ( 1 ). this preconditions the compensation of modification of the gas medium composition in the container that is caused by banana respiration . the absolute permeability value of the membrane ( 6 ) material can be , for example , about 1 . 12 * 10 6 cc / 100 sq . ins . atm - 24 hrs for carbon dioxide . for oxygen , this value can be about 2 . 8 * 10 5 cc / 100 sq . ins . atm - 24 hrs . the indicated characteristics of the membrane ( 6 ) material allow the system to quickly achieve the required concentrations of oxygen and carbon dioxide in the container ( 1 ). it is possible to use other materials for the membrane , with the same ratio of permeability values , but with smaller absolute values of this parameter , which should be compensated for by an increase of the operating surface area of the membrane . the device described above can serve several containers concurrently . for this purpose , the chamber ( 4 ) should be equipped with the appropriate number of input and output channels . additionally , to enhance the entire gas exchange process , chargers ( 14 and 15 ) can be introduced into the chamber ( 4 ) ( see fig3 ), or into the channels for uptake and return ( not shown in fig1 ). these chargers would ensure the required velocity of the flow in the chamber . it is possible to use additional chargers if several containers are connected to the chamber ; however , they can be used only when the container is serviced . the rate of gas medium modification in the chamber depends upon the volume of the chamber , surface area and permeability of the membrane ( 6 ), and the flow rate into and out of the container . velocity of flow through the chamber is regulated depending upon the velocity of the gas exchange and upon the required rate for substitution of the gas medium in the container ( 1 ). control of the gas composition of the atmosphere inside the container ( 1 ) can require an additional gas , for example , ethylene . in this case ( see fig3 ), an additional input with a connecting pipe ( 26 ) is executed , intended for feeding in gas from an external gas storage device or from a gas generator . in another example of the device ( see fig4 ), the gas exchange chamber is a section ( 16 ) that is connected to the container ( 1 ) from the side of the connecting pipes ( 7 and 9 ). the gas - permeable membrane ( 6 ) is installed in the section ( 16 ), and is protected by the wall ( 17 ). the membrane has orifices ( 18 ) intended for ensuring contact of the membrane &# 39 ; s surface with ambient air . channels for uptake of the gas medium from the container and for the return of the modified gas medium are executed as connection pipes ( 19 and 20 ) of the section ( 16 ), correspondingly . the section ( 16 ) is connected to the container to ensure a hermetically sealed connection of pipes of the container , to the connecting pipes ( 19 and 20 ) of the section . the device functions in a manner similar to that of the device presented in fig1 , and described above . also , the device described here can be a separate section ( 21 ) of the container ( 1 ), as shown in fig5 . in this case , the section ( 21 ), constituting a gas exchange chamber , appears , for example , in the form of an enclosure constituting a separate part of the container . the section ( 21 ) is connected with the cargo part of the container via channels in the form of orifices ( 22 and 23 ), blocked by controlled shutters or valves ( 24 and 25 ), correspondingly .
a device for controlling the composition inside a shipping / storage container for produce , such as bananas , is disclosed . such atmospheric control is particularly important when dealing with the ripening of respiring fruit . the device comprises a chamber surrounded by an outer wall , at least a portion of that wall made up of a selectively gas - permeable membrane which is in communication with the outside atmosphere . the chamber also includes at least two channels which are connected to the container : one which transmits gas form the chamber to the container , and one which transmits gas from the container to the chamber .