NON-VENTING TRANSFER SYSTEM AND METHOD
The present invention provides non-venting transfer systems and methods related to transferring cryogenic liquid between two vessels without venting evaporated cryogenic liquid into the atmosphere. The stations, systems, and methods utilize a feed line and a return line connecting a source tank and a pump system to allow for flow of a cryogenic liquid to the pump and return of evaporated cryogenic liquid to the source tank, thereby avoiding release of the evaporated cryogenic liquid into the atmosphere.
1 . A non-venting transfer system, comprising:
a station cryogenic liquid tank;
a pump with a pump suction line, a vapor return line, and a cryogenic liquid outflow line, wherein the cryogenic liquid outflow line is connected to the station cryogenic liquid tank;
a feed line comprising a cryogenic hose with two ends, the first end connected to the pump suction line of the pump, the second end terminating at a self-sealing nozzle;
a return line comprising a cryogenic hose with two ends, the first end connected to the vapor return line of the pump, the second end terminating at a self-sealing nozzle;
wherein the feed line self-sealing nozzle and the return line self-sealing nozzle are adapted to connect to a source cryogenic liquid tank, and the pump is used to transfer cryogenic liquid from the source cryogenic liquid tank to the station cryogenic liquid tank.
2 . The system of claim 1 , wherein the pump comprises a cryogenic pump.
3 . The system of claim 1 , wherein the pump suction line comprises at least one valve capable of restricting liquid or gas flow through the pump suction line in at least one direction.
4 . The system of claim 1 , wherein the pump suction line comprises at least one valve capable of restricting liquid or gas flow through the pump suction line.
5 . The system of claim 1 , wherein the pump suction line comprises at least one valve capable of restricting liquid or gas flow through the pump suction line in one direction.
6 . The system of claim 1 , wherein the pump suction line comprises at least two valves arranged in parallel, wherein one valve is capable of restricting liquid or gas flow through the pump suction line, and one valve is capable of restricting liquid or gas flow through the pump suction line in one direction.
7 . The system of claim 1 , wherein the vapor return line comprises at least one valve capable of restricting liquid or gas flow through the vapor return line in at least one direction.
8 . The system of claim 1 , wherein the vapor return line comprises at least one valve capable of restricting liquid or gas flow through the vapor return line.
9 . The system of claim 1 , wherein the vapor return line comprises at least one valve capable of restricting liquid or gas flow through the vapor return line in one direction.
10 . The system of claim 1 , wherein the vapor return line comprises at least two valves arranged in parallel, wherein one valve is capable of restricting liquid or gas flow through the vapor return line, and one valve is capable of restricting liquid or gas flow through the vapor return line in one direction.
11 . The system of claim 1 , wherein the cryogenic liquid dispensing station is a liquid natural gas (LNG) dispensing station.
12 . A method of transferring a cryogenic liquid from a source tank to a receiving tank without venting, the method comprising:
connecting a receiving tank to a source tank via a pump system, the pump system comprising:
a pump,
an outflow line connected to the receiving tank, the outflow line comprising at least one valve capable of preventing flow of cryogenic liquid from the pump to the receiving tank,
a pump suction line connected to a first cryogenic hose terminating with a self-sealing nozzle, and
a vapor return line connected to a second cryogenic hose terminating with a self-sealing nozzle, the vapor return line comprising at least one valve capable of preventing flow through the vapor return line to the second cryogenic hose;
wherein connecting the receiving tank to the source tank comprises connecting the self-sealing nozzles of the first and second cryogenic hoses to the source tank, and wherein the pump system is initially at a first temperature above the boiling temperature of the cryogenic liquid;
flowing cryogenic liquid from the source tank to the pump system via the first cryogenic hose and flowing gas produced by evaporation of the cryogenic liquid at the pump system back to the source tank via the second cryogenic hose until the pump system is cooled to a second temperature at or below the boiling temperature of the cryogenic liquid;
configuring the vapor return line valve to prevent flow from the pump system to the source tank through the second cryogenic hose;
configuring the outflow line valve to allow flow from the pump system to the source tank; and
using the pump to transfer cryogenic liquid from the source tank to the receiving tank.
13 . The method of claim 12 , wherein the pump comprises a submersible cryogenic pump.
14 . The method of claim 12 , wherein the pump suction line comprises at least one valve capable of preventing liquid or gas flow through the pump suction line in at least one direction.
15 . The method of claim 12 , wherein the pump suction line comprises at least one valve capable of preventing liquid or gas flow through the pump suction line.
16 . The method of claim 12 , wherein the pump suction line comprises at least one valve capable of preventing liquid or gas flow through the pump suction line in one direction.
17 . The method of claim 12 , wherein the pump suction line comprises at least two valves arranged in parallel, wherein one valve is capable of preventing liquid or gas flow through the pump suction line, and one valve is capable of preventing liquid or gas flow through the pump suction line in one direction.
18 . The method of claim 12 , wherein the vapor return line valve is capable of preventing liquid or gas flow through the vapor return line.
19 . The method of claim 12 , wherein the vapor return line further comprises a valve capable of preventing liquid or gas flow through the vapor return line.
20 . The method of claim 12 , wherein the vapor return line comprises at least two valves arranged in parallel, wherein one valve is capable of preventing liquid or gas flow through the vapor return line, and one valve is capable of preventing liquid or gas flow through the vapor return line in one direction.
21 . The method of claim 12 , wherein the cryogenic liquid dispensing station is a liquid natural gas (LNG) dispensing station.