Patent GB-469948-A (GB)
Title: Method of and apparatus for transferring a liquefied gas from a region of relatively low pressure to a region of relatively high pressure
IPC: F17C9/00
Filed: 1936-02-05
Abstract: 469,948. Transferring and revaporizing liquefied gases. LINDE AIR PRODUCTS CO. Feb. 5, 1936, Nos. 3414 and 3415. Convention dates, March 1, 1935 and June 18, 1935. [Class 8 (ii)] Liquefied gas is withdrawn periodically from a heat-insulated storage vessel 11, Fig. 1, to a transfer vessel 12 also insulated ; the connection between the vessels is then cut, and valves are opened to connect vessel 12 with a vaporizer 35 both at the top and bottom of the vessel, the vapour being delivered to a receiver 36 in communication with a consumer's pipe line 37 with a reducing valve 38. To assist delivery from the vessel 11, a coil 27 communicates with it at top and bottom and may be heated as described in Specification 307,070, [Class 8 (ii)], the liquid being transferred through conduits 31 and 18 and a removable conduit 31<1>. Residual gas from a previous discharge is first delivered from vessel 12 through valve 17<11> to raise the pressure in vessel 11, and a valve 21 is opened to release vapour during the filling of vessel 12. During transportation, vapour evolved in vessel 11 passes off through a coil 29 and a valve 30 to atmosphere, while gas remaining in the vessel 12 is gradually cooled by circulation through a conduit 17 in contact with the wall of vessel 11. In a modification, two transfer vessels are provided, one being filled from the storage vessel while the other is discharging to receivers ; the vapour from the discharging vessel flows to the receivers through an ejector which entrains and compresses vapour remaining in the vessel being filled. In a further modification, residual gas is drawn from a transfer vessel being filled, by a gas pump through a conduit immersed in heating fluid which also heats the evaporator coil, and is delivered through lubricant removal and chemical purifying traps to the receivers. The pressure in the main vessel may be increased by admitting gas from the transfer vessel when the gas pump is not operating. Fig. 4 shows apparatus comprising two transfer vessels. Liquefied gas is transferred from vessel A to a transfer vessel 81 by pressure of vapour ; the pressure in vessel 81 is increased in stages by inflow of gas from the storage vessels 150 through an exchanger R<1>. For discharge of liquid from vessel 81, a heater C rapidly vaporizes liquefied gas therefrom ; the liquefied gas is forced through a passage 225 of the exchanger R<1> to a vaporizing coil 45 and the gas supply main 65. Meanwhile vessel 82 is being filled with liquid. Residual gas in vessel 81 is stored at successively lower pressures in vessels 150, and the pressures in vessels 81, 82 may be equalized, after which the pressure in vessel 82 is raised by inflow of stored gas from the vessels 150. The exchanger R<1> may comprise a pressureresistant chamber with multi-tubular liquid outflow to the vaporizer, residual gas being stored in the baffied space around the tubes partly in liquid form. Fig. 6 shows a further modification, in which the liquefied gas is discharged through conduits 176, 164 into a pressure-resistant vessel 166. Valve 164<1> is then closed and the residual gas flows through conduit 168, coil 167, and expansion valve 170 into a container 180. When the vessel B is again refilled and discharged, the liquid in vessel 166 is forced through a heater 46<1> to the receiving devices. The liquid in vessel 180 is transferred to the vessel B after filling to raise the pressure.