Liquid cryogen delivery system

Claim 2

Apparatus capable of delivering small controlled quantities of a liquid cryogen to a use point in an intermittent manner comprising an on-period during which a predetermined amount of liquid cryogen is delivered to said use point continuously during said on-period, followed by an off-period during which no liquid cryogen is desired at said use point, said apparatus comprising in combination: (a) insulated conduit means for transferring cryogen from a liquid cryogen supply source to said use point; (b) subcooling means adjacent said use point and upstream thereof, adapted to condense vaporized cryogen in said conduit means and to subcool said cryogen; and (c) flow control means located downstream of said subcooling means, adapted to cause a low flow of cryogen downstream of said subcooling means during said off-period, said low flow being sufficient upon vaporization to offset heat leaks in, as well as purge cryogen vapor from, said conduit means downstream of said subcooler, said flow control means also being adapted to cause a high flow of said cryogen during said on-period so that said predetermined amount of liquid cryogen is delivered to said use point essentially free of vapor.

Claim 3

The apparatus of claim 1 wherein said subcooling means is adapted to receive a second quantity of liquid cryogen to be employed as a coolant at essentially ambient pressure.

Claim 4

The apparatus of claim 2 wherein said flow control means comprises at least one low-flow valve to be employed during off-periods and at least one high flow valve to be used during on-periods connected in parallel with said low flow valve.

Claim 5

The apparatus of claim 2 wherein said flow control means comprises a pneumatically activated valve operating at two signal pressures: (a) a low flow signal pressure during said off-period, and (b) a high flow signal pressure during said on-period.

Claim 6

A process for delivering small controlled quantities of liquid cryogen to a use point in an intermittent manner comprising an off-period during which no liquid cryogen is desired at said use point followed by an on-period during which a predetermined amount of said liquid cryogen is delivered to said use point continuously for the duration of said on-period, said method comprising: (a) transferring said cryogen through a conduit from a liquid cryogen supply source to said use point; (b) in the course of said transfer and adjacent said use point, cooling said cryogen so as to condense all vapor formed therein and to further subcool said liquid to a temperature at which the vapor pressure of said liquid is higher than its equilibrium vapor pressure at said temperature; and (c) controlling the flow of said cryogen in said conduit downstream of the point at which said subcooling takes place by (i) adjusting said flow to a low value during said off-period sufficient to completely absorb the heat added through heat leak downstream of said cooling point, thereby vaporizing said cryogen so that essentially no liquid cryogen reaches said use point and compensating for said heat leak, and (ii) adjusting said flow to a higher value during said on-period so that said predetermined amount of said cryogen is delivered to said use point essentially free of vapor.

Claim 7

A process for delivering small controlled quantities of liquid cryogen to a use point in an intermittent manner comprising an off-period during which no liquid cryogen is desired at said use point followed by an on-period during which a predetermined amount of said liquid cryogen is delivered to said use point continuously for the duration of said on-period, said method comprising: (a) transferring said cryogen through a conduit from a liquid cryogen supply source to said use point; (b) in the course of said transfer and adjacent said use point, cooling said cryogen so as to condense all vapor formed therein and to further subcool said liquid to a temperature at which the vapor pressure of said liquid is higher than its equilibrium vapor pressure at said temperature; and (c) controlling the flow of said cryogen in said conduit downstream of the point at which said subcooling takes place by (i) adjusting said flow to a low value during said off-period sufficient to completely absorb the heat added through heat leak downstream of said cooling point, thereby vaporizing said cryogen so that essentially no liquid cryogen reaches said use point and compensating for said heat leak, and (ii) adjusting said flow to a higher value during said on-period so that said predetermined amount of said cryogen is delivered to said use point essentially free of vapor.

Claim 8

The process of claim 5, wherein during said on-period the desired quantity of liquid cryogen at the use point ranges between about 10 and 400 lbs/hr.

Claim 9

The process of claim 5 wherein said cryogen is liquid nitrogen.