1 |
用于以温度受控制的方式进行气体分配的方法和系统 |
CN201410161706.6 |
2014-04-22 |
CN104110578B |
2017-04-12 |
J.P.科亨 |
本发明涉及用于以温度受控制的方式进行气体分配的方法和系统。一种用于将压缩气体分配到接收容器中的系统和方法,其中,提供接收容器在分配期间的目标温度分布,并且控制进入到接收容器中的压缩气体的流率,以使接收容器在分配期间的温度分布符合目标温度分布。 |
2 |
用于以温度受控制的方式进行气体分配的方法和系统 |
CN201410161706.6 |
2014-04-22 |
CN104110578A |
2014-10-22 |
J.P.科亨 |
本发明涉及用于以温度受控制的方式进行气体分配的方法和系统。一种用于将压缩气体分配到接收容器中的系统和方法,其中,提供接收容器在分配期间的目标温度分布,并且控制进入到接收容器中的压缩气体的流率,以使接收容器在分配期间的温度分布符合目标温度分布。 |
3 |
JPH0511403B2 - |
JP10462586 |
1986-05-09 |
JPH0511403B2 |
1993-02-15 |
SAEKI MITSURU; TAKAHASHI TSUYOSHI |
PURPOSE:To reduce a quantity of evaporated liquid helium by reducing a quantity of invading heat by providing a thermal anchor nearly in parallel to a horizontal axis of a container. CONSTITUTION:A port 6 for injection of liquid helium is inclined in circumferential direction (by nearly 45 deg.to a vertical direction of a superconducting device.) A thermal anchor 8 from a gas helium 20K shielding of an inner cylinder 7 of the liquid helium injection port, and a thermal anchor 9 from a a liquid nitrogen about 80K shielding are arranged in nearly vertical (horizontal) direction to a gravity vertical direction. By convection of a gas helium and heat exchange in the inner cylinder 7, a direct heat invasion into a helium container 1 part is prevented. Accordingly, a quantity of evaporated liquid helium is reduced. |
4 |
JPS4822892B1 - |
JP3363366 |
1966-05-27 |
JPS4822892B1 |
1973-07-10 |
|
|
5 |
温度制御式の気体を分配する方法及びシステム |
JP2014087073 |
2014-04-21 |
JP5947330B2 |
2016-07-06 |
ジョセフ ペリー コーエン |
|
6 |
Preventive device of roll over in low temperature liquid storage tank |
JP7220981 |
1981-05-15 |
JPS57190199A |
1982-11-22 |
TAKAGISHI YASUHIRO; TASHIMO MAKOTO; NAKANO MOTOHIRO |
PURPOSE:To prevent a roll over in a low temperature liquid storage tank, by opening both upper and lower ends of a heat exchanger, forming cross sectional area of the heat exchanger smaller in its lower part while larger in its upper part and arranging said heat exchanger in the storage tank. CONSTITUTION:A horn shaped heat exchanger 10, in which a lower end opening is narrowed and cross sectional area is spread increasing gradually toward an upper end opening, is arranged in a cylindrical low temperature liquid storage tank T. If high temperature liquid, slightly at higher temperature than of liquid in a low temperature liquid tank 2 further with larger specific gravity than said liquid, is injected through a pipe line P, a high temperature liquid layer 3 is formed to a lower layer in the storage tank T, and a low temperature liquid layer 2 is overlapped on the layer 3, fianlly only a low temperature liquid layer 2' in the heat exchanger 10 is lifted by the high temperature liquid layer 3, thus thickness of the liquid layer is gradually reduced. As a result, heat exchanging area, separately contacted with an external wall of the heat exchanger 10, between the high temperature liquid layer 3 and low temperature liquid layer 2, is particularly increased, and a thermally stable neutral condition can be generated in the storage tank T. |
7 |
JPS4823565B1 - |
JP2460467 |
1967-04-19 |
JPS4823565B1 |
1973-07-14 |
|
|
8 |
Space Conserving Integrated Cryogenic Fluid Delivery System |
US15924779 |
2018-03-19 |
US20180266629A1 |
2018-09-20 |
Peter Murray; Brian Poag; Michael Sable; Luis Serentill |
An integrated cryogenic fluid delivery system includes a tank adapted to hold a supply of cryogenic liquid and having an end wall. A shroud is positioned on the end wall and contains a shell and tube heat exchanger. The heat exchanger includes a shell defining a warming fluid chamber and having a shell inlet and a shell outlet in fluid communication with the warming fluid chamber. A number of cryogenic fluid coils are positioned within the warming fluid chamber and are in fluid communication with a cryogenic fluid inlet port and a cryogenic fluid outlet port. A fuel shutoff valve has an inlet in fluid communication with a liquid side of the tank and an outlet in fluid communication with the cryogenic fluid inlet port of the heat exchanger. A manual vent valve has an inlet in fluid communication with a headspace of the tank and an outlet. The fuel shutoff valve and the manual vent valve each have a control knob that is accessible from the first or second side of the shroud. |
9 |
Purity monitor |
US15291712 |
2016-10-12 |
US10054357B2 |
2018-08-21 |
Paul L. Buelow |
A purity monitor is provided. The purity monitor includes a cryo-cooler and a piezo-electric crystal microbalance that may have a matte finish. The cryo-cooler includes a nozzle and plumbing components disposed to supply a fluid having a working pressure of up to 10,000 psig to the nozzle. The nozzle provides for locating substantially all of a pressure drop of the cryo-cooler near an exit thereof. The nozzle sprays fluid onto the piezo-electric crystal microbalance and the piezo-electric crystal microbalance measures a mass of non-volatile residue (NVR) left thereon by the spraying. Respective temperatures of the fluid and the piezo-electric crystal microbalance are controllable based on a type of the NVR. |
10 |
PURITY MONITOR |
US15291712 |
2016-10-12 |
US20180142937A1 |
2018-05-24 |
Paul L. Buelow |
A purity monitor is provided. The purity monitor includes a cryo-cooler and a piezo-electric crystal microbalance that may have a matte finish. The cryo-cooler includes a nozzle and plumbing components disposed to supply a fluid having a working pressure of up to 10,000 psig to the nozzle. The nozzle provides for locating substantially all of a pressure drop of the cryo-cooler near an exit thereof. The nozzle sprays fluid onto the piezo-electric crystal microbalance and the piezo-electric crystal microbalance measures a mass of non-volatile residue (NVR) left thereon by the spraying. Respective temperatures of the fluid and the piezo-electric crystal microbalance are controllable based on a type of the NVR. |
11 |
Method and system for temperature-controlled gas dispensing |
US13867208 |
2013-04-22 |
US09279541B2 |
2016-03-08 |
Joseph Perry Cohen |
A system and method for dispensing a compressed gas into a receiving vessel wherein a target temperature profile for the receiving vessel during dispensing is provided, and the flow rate of compressed gas into the receiving vessel is controlled to conform the temperature profile for the receiving vessel during dispensing to the target temperature profile. |
12 |
Method and Apparatus for Dampening Flow Variations and Pressurizing Carbon Dioxide |
US13950350 |
2013-07-25 |
US20150027682A1 |
2015-01-29 |
Peter D. Guerra |
An apparatus is provided for maintaining a steady flow rate and pressure of a carbon dioxide stream at high pressure when a low-pressure source of the carbon dioxide varies with time. Liquid level in an accumulator that is sized to accommodate variations in supply rate is controlled by sub-cooling of liquid entering the accumulator and heating in the accumulator, the sub-cooling and heating being controlled by a pressure controller operable in the accumulator. |
13 |
Cryogenic Liquid Conditioning and Delivery System |
US13735691 |
2013-01-07 |
US20140190187A1 |
2014-07-10 |
Kenneth Leo Snyder; Robert Francis Desjardins; Nathaniel Eaton Allen; James Joseph Donovan; Mark Ray Nuernberger; Peter Maurice Coleman |
A cryogenic liquid conditioning system with flow driven by head pressure of liquid contained in a cryogenic storage tank, and a cryogenic liquid delivery system with flow driven by pressure in the vapor space of said cryogenic storage tank. A heat exchanger, coupled to the cryogenic storage tank located below the liquid level of said tank, operates as a portion of both the conditioning system and delivery system. A piping system moves cryogenic liquid to the heat exchanger where it is vaporized, and then moves vaporized liquid to the vapor space of the cryogenic tank and an application. The piping system includes a means for controlling flow through the system. A means for measuring the saturated pressure of cryogenic liquid is coupled to the storage tank or piping system, and is in communication with the means for controlling flow. |
14 |
Motor vehicle having a unit operated by a cryogenically stored fuel |
US12199559 |
2008-08-27 |
US07992670B2 |
2011-08-09 |
Rainer Richter; Carsten Schwarz; Michael Schreiner; Johann Tonhauser |
A motor vehicle having a unit, particularly a drive assembly, which is operated by a fuel that is cryogenically stored in a vehicle tank, is provided, in which fuel is heated by a heat exchange with a warmer medium. The fuel taken from the vehicle tank comes in contact with the cold side of a thermoelectric generator, particularly in the form of a Seebeck element, in order to generate electric current for the electric power supply of the vehicle. The warm side of the thermoelectric generator is preferably acted upon by the warmer medium also used for the heat exchange with the cold fuel, in which case the thermoelectric generator may be integrated in a heat exchanger for the heat exchange between the fuel taken and the warmer medium. |
15 |
Seamless fluid storage and transport module |
US12288530 |
2008-10-21 |
US20100096030A1 |
2010-04-22 |
David A. Hinkley |
A fluid storage and transport module includes complex plumbing features such as fluid reservoirs, filters, heat exchangers, three-dimensionally routed tubing, valves, mixing chambers, and exit apertures formed in and on a monolithic common bulk material using an additive rapid prototyping process of depositing multiple layers of rapid prototyping materials without welds, adhesives or compression fittings, being made by a method that minimizes leaks, maximizes packing density of the functional components, and increases the plumbing robustness to leaks. |
16 |
SYSTEM FOR RECLAIMING LIQUEFIED PETROLEUM GAS |
US15769638 |
2017-04-07 |
US20180312763A1 |
2018-11-01 |
MICHAEL JOSEPH GOESSL; ISAAC RAY AINSWORTH; JEREMIAH HURST; JAY ALAN HADDOCK; JAMES NORMAN RETTLER; JODY ALAN MCKINLEY |
An LPG reclaim system for withdrawing and reclaiming liquefied petroleum gas (LPG) from an unspent LPG cylinder. The reclaim system has a reclaim station for reclaiming unspent LPG from LPG bottle containers, a compressor for applying a vacuum on the reclaim station and pressurizing LPG vapor from the reclaimed LPG fluid, and a receiving tanlc for receiving a stream of pressurized liquid LPG. The reclaim system has a pair of shell-and-tube heat exchangers include cold-side tubes and a hot side shell. The reclaimed LPG fluid is passed through the cold-side tubes, while the pressurizing LPG vapor is passed through the hot-side shell of the heat exchanger. The heat applied to the cold-side reclaimed LPG fluid promotes evaporation of the LPG fluid to LPG vapor for pressurizing, and the cooling applied to the hot-side pressurized LPG vapor promotes condensation of the LPG vapor to LPG liquid for the refill containers. |
17 |
System and method for unloading compressed natural gas |
US14677725 |
2015-04-02 |
US09784411B2 |
2017-10-10 |
David A. Diggins |
A system and method for unloading highly pressurized compressed natural gas from transport vessels by depressurizing the gas through flow lines linking a series of automated flow control valves that lower the gas pressure to a predetermined level, the valves being linked in series with and separated by heat exchangers in which the lower pressure gas flowing through the system is also reheated to a predetermined temperature by a heat exchange medium recirculation system in which the heat exchange medium is reheated by a heat source that can be internal to the system. The use of a minor portion of the depressurized and reheated gas as fuel gas to reheat the heat exchange medium is also disclosed. The subject system can be skid-mounted if desired. |
18 |
Method and System for Temperature-Controlled Gas Dispensing |
US13867208 |
2013-04-22 |
US20140311622A1 |
2014-10-23 |
Joseph Perry Cohen |
A system and method for dispensing a compressed gas into a receiving vessel wherein a target temperature profile for the receiving vessel during dispensing is provided, and the flow rate of compressed gas into the receiving vessel is controlled to conform the temperature profile for the receiving vessel during dispensing to the target temperature profile. |
19 |
Seamless fluid storage and transport module |
US12288530 |
2008-10-21 |
US08820359B2 |
2014-09-02 |
David A. Hinkley |
A fluid storage and transport module includes complex plumbing features such as fluid reservoirs, filters, heat exchangers, three-dimensionally routed tubing, valves, mixing chambers, and exit apertures formed in and on a monolithic common bulk material using an additive rapid prototyping process of depositing multiple layers of rapid prototyping materials without welds, adhesives or compression fittings, being made by a method that minimizes leaks, maximizes packing density of the functional components, and increases the plumbing robustness to leaks. |
20 |
Monitoring of Ultra-high purity product storage tanks during transportation |
US10680267 |
2003-10-06 |
US20040065382A1 |
2004-04-08 |
Vladimir
Yliy
Gershtein; Robert
William
Ford; John
Frederick
Cirucci |
System for the transportation and storage of a product which comprises a tank including cylindrical wall section and two ends, wherein the cylindrical wall section and two ends define a cylindrical tank periphery, and wherein the tank periphery has an interior and an exterior. The system utilizes a valve box that includes one or more side walls, a bottom wall, and a removable, sealable top cover which can be attached to the one or more side walls to seal the valve box, wherein the valve box side walls are sealably joined to the cylindrical wall. One or more process valves are disposed in the valve box, wherein each valve has a first and a second end, wherein each first end is connected to a pipe which passes through a wall of the valve box for introducing product into the tank or withdrawing product from the tank. A purge valve and pressure measurement means are installed in fluid communication with the valve box. The product in the tank is isolated from the atmosphere surrounding the tank when the valve box is sealed. |