Compact Configuration for Cryogenic Pumps and Turbines
A single cryogenic liquid vessel in which two cryogenic machines are disposed, supported and operable in tandem. In one embodiment the two cryogenic machines are operable in series or individually, and in another embodiment the two cryogenic machines are operable in parallel or individually. Preferably the machines are supported intermediately relative to the vessel, or at a top of the vessel. In various embodiments the machines are pumps or turbines or expanders.
1 . A compact configuration for two cryogenic liquid expanders mounted within a single cryogenic liquid pressure vessel within which the expanders are disposed vertically and supported and operable in tandem, in series or individually, the two expanders supported intermediately relative to the vessel, the two cryogenic liquid expanders comprising a lower expander and an independently operated upper expander, the lower expander and the upper expander each having its own center rotational shaft and both connected to an intermediary support plate, the lower expander having a fixed rotational speed, the lower expander further comprising a high pressure inlet and an outlet, the upper expander having a variable rotational speed, the upper expander further comprising an inlet and a low pressure discharge, the inlet of the upper expander in communication with the outlet of the lower expander, whereby the wall thickness and overall diameter of the pressure vessel are minimized.
2 . The compact configuration for two cryogenic liquid expanders of claim 1 in which the pressure vessel further comprises an intermediate pressure discharge.
3 . The compact configuration for two cryogenic liquid expanders of claim 2 , in which the intermediate pressure discharge is single-phase.
4 . The compact configuration for two cryogenic liquid expanders of claim 2 , in which the intermediate pressure discharge is two-phase.
5 . The compact configuration for two cryogenic liquid expanders of claim 1 , wherein the low-pressure discharge is two-phase.
6 . A method for minimizing the overall diameter of a cryogenic pressure vessel containing cryogenic liquid expanders in order to minimize wall thickness and overall weight of the cryogenic pressure vessel, the method comprising the following steps:
A. Obtaining an elongated cryogenic liquid pressure vessel;
B. Placing a lower expander and an independently operated upper expander vertically inside the pressure vessel supported and operable in tandem, the two cryogenic liquid expanders each having its own central rotational shaft and operable in series or individually, and the two expanders supported intermediately relative to the pressure vessel;
C. Operating the lower expander at a fixed rotational speed and operating the upper expander at a variable rotational speed;
D. Introducing cryogenic liquid into a high-pressure inlet associated with the lower expander;
E. Communicating the cryogenic fluid from the lower expander to the upper expander; and
F. Discharging expanded cryogenic liquid from a low-pressure discharge associated with the upper expander at low pressure, whereby the overall diameter of the pressure vessel is minimized, thus minimizing the wall thickness and overall weight of the pressure vessel.
7 . The method of claim 6 , in which the cryogenic liquid vessel further comprises a medium-pressure discharge, further comprising the following step:
G. Discharging expanded cryogenic liquid from the medium-pressure discharge.
8 . The method of claim 6 , further comprising the following step:
G. Discharging expanded cryogenic liquid and vapor from a low-pressure discharge associated with the upper expander at low pressure.
9 . The method of claim 8 , further comprising the following step:
H. Discharging expanded cryogenic liquid and vapor from the medium-pressure discharge.