Process and plant for supplying carbon dioxide under high pressure

Claim 2

A process for supplying carbon dioxide under a high pressure which is above the liquid-vapor equilibrium pressure of carbon dioxide at ambient temperature, by means of a high pressure pump from a tank storing liquid carbon dioxide under a medium pressure and at a first temperature lower than 0° C., the process comprising: completely filling an intermediate vessel with liquid carbon dioxide from the storage tank, said filling being achieved merely under the effect of gravity; isolating said intermediate vessel from said tank; bringing the liquid in the intermediate vessel to a second temperature which is about ambient temperature; and while maintaining the intermediate vessel at said second temperature: withdrawing liquid from said intermediate vessel; subcooling the withdrawn liquid while maintaining it above 0° C.; and conveying the subcooled liquid to the inlet of the pump.

Claim 3

A process according to claim 1, comprising putting, before withdrawing the liquid from the intermediate vessel, said vessel in communication with an auxiliary source of gaseous carbon dioxide at a liquid-vapour equilibrium pressure of the carbon dioxide at said second temperature.

Claim 4

A process according to claim 2, comprising employing as the auxiliary source of gaseous carbon dioxide a cylinder containing liquid carbon dioxide and maintained at said second temperature.

Claim 5

A process according to claim 1, comprising continuously regulating the output of the high pressure pump by comparing the delivery pressure thereof with a set pressure and modifying the output of the pump in the sense which tends to eliminate the difference between said delivery and set pressures.

Claim 6

A process according to claim 1, comprising subcooling the withdrawn liquid by increasing its pressure by means of an auxiliary pump.

Claim 7

A process according to claim 1, comprising using a cooling fluid maintained at a temperature lower than said second temperature for subcooling the liquid withdrawn from the intermediate vessel and subcooling the liquid delivered by the high pressure pump.

Claim 8

A process according to claim 6, wherein said cooling fluid is water.

Claim 9

A process according to claim 1, comprising employing two said intermediate vessels, one said vessel being filled while liquid is being withdrawn from the other vessel.

Claim 10

A plant for supplying carbon dioxide under a high pressure which is above the liquid-vapor equilibrium pressure of carbon dioxide at ambient temperature, the plant comprising a tank for storing liquid carbon dioxide under a medium pressure and at a first temperature lower than 0° C., a high pressure pump having an inlet and a discharge outlet, and means for supplying liquid carbon dioxide to said pump from the tank, said plant further comprising: an intermediate vessel entirely located below a minimum level of the liquid in the tank and connected to lower and upper parts of said tank; means for heating said intermediate vessel, and means for regulating said heating means at a second temperature which is about ambient temperature; and a conduit connecting the intermediate vessel to the inlet of the pump and provided with means for subcooling the liquid conveyed in said conduit while maintaining it above 0° C.

Claim 11

A plant for supplying carbon dioxide under a high pressure which is above the liquid-vapor equilibrium pressure of carbon dioxide at ambient temperature, the plant comprising a tank for storing liquid carbon dioxide under a medium pressure and at a first temperature lower than 0° C., a high pressure pump having an inlet and a discharge outlet, and means for supplying liquid carbon dioxide to said pump from the tank, said plant further comprising: an intermediate vessel entirely located below a minimum level of the liquid in the tank and connected to lower and upper parts of said tank; means for heating said intermediate vessel, and means for regulating said heating means at a second temperature which is about ambient temperature; and a conduit connecting the intermediate vessel to the inlet of the pump and provided with means for subcooling the liquid conveyed in said conduit while maintaining it above 0° C.

Claim 12

A plant according to claim 9, comprising an auxiliary source of gaseous carbon dioxide under a liquid-vapour equilibrium pressure of the carbon dioxide at said second temperature, connected to the intermediate vessel.

Claim 13

A plant according to claim 9, comprising a source of auxiliary gas under said high pressure, a differential pressure sensor measuring the difference between the pressure of said gas and the pressure of the liquid delivered by the high pressure pump, and a frequency converter receiving from said sensor a signal representing the difference between the two pressures and regulating the output of the pump as a function of said signal.

Claim 14

A plant according to claim 11, wherein the subcooling means comprise an auxiliary pump in said conduit.

Claim 15

A plant according to claim 9, comprising a water circuit maintained at a temperature lower than said second temperature, in thermal exchange relation to the liquid withdrawn from the intermediate vessel and to a conduit delivering liquid carbon dioxide under high pressure.

Claim 16

A plant according to claim 9, comprising two said intermediate vessels operating alternately and interposed in parallel between the storage tank and the high pressure pump whereby, in use, one said vessel is filled while liquid is being withdrawn from the other vessel.