Pressure Building Cryogenic Fluid Delivery System
US-2018306383-A1 · Oct 25, 2018 · US
US10495257B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10495257-B2 |
| Application number | US-201715588752-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 8, 2017 |
| Priority date | May 8, 2017 |
| Publication date | Dec 3, 2019 |
| Grant date | Dec 3, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
According to one or more aspects, a hydrogen fueling station is provided and includes one or more hydrogen fuel storage tanks, a pressure control device positioned downstream from the hydrogen fuel storage tanks, a dispenser positioned downstream from the pressure control device, and a heat load reduction line which forms a circulation loops from a first point downstream of the pressure control device to one or more of the hydrogen fuel storage tanks.
Opening claim text (preview).
The invention claimed is: 1. A hydrogen fueling station, comprising: a hydrogen fuel storage tank; a pressure control device including one or more control valves positioned downstream from the hydrogen fuel storage tank and connected to the hydrogen fuel storage tank by a first fuel line; a dispenser positioned downstream from the pressure control device and connected to the pressure control device by a second fuel line; a heat load reduction line which forms a circulation loop from a first point downstream of the pressure control device to the hydrogen fuel storage tank and back to a second point downstream of the pressure control device; a compressor positioned upstream from the hydrogen fuel storage tank and connected to the hydrogen fuel storage tank; a second hydrogen fuel storage tank; a first temperature sensor monitoring a first temperature of the hydrogen fuel stored in the hydrogen fuel storage tank; a second temperature sensor monitoring a second temperature of the hydrogen fuel stored in the second hydrogen fuel storage tank; a valve configured to control flow of hydrogen fuel through the circulation loop and a second circulation loop; and a controller controlling operation of the valve based on the first temperature and the second temperature; wherein the pressure control device is positioned downstream from the second hydrogen fuel storage tank and connected to the second hydrogen fuel storage tank, wherein the heat load reduction line includes the second circulation loop from the first point downstream of the pressure control device to the second hydrogen fuel storage tank and back to the second point downstream of the pressure control device, and wherein the controller operates the valve to flow hydrogen fuel through the circulation loop of the heat load reduction line based on the first temperature being less than the second temperature. 2. The hydrogen fueling station of claim 1 , comprising a heat exchanger positioned downstream from the pressure control device and connected to the pressure control device. 3. A hydrogen fueling station, comprising: a first hydrogen fuel storage tank; a pressure control device including one or more control valves positioned downstream from the first hydrogen fuel storage tank and connected to the first hydrogen fuel storage tank; a dispenser positioned downstream from the pressure control device and connected to the pressure control device; a heat load reduction line which includes a first circulation loop from a first point downstream of the pressure control device to the first hydrogen fuel storage tank and back to a second point downstream of the pressure control device; a compressor positioned upstream from the first hydrogen fuel storage tank and connected to the first hydrogen fuel storage tank; a second hydrogen fuel storage tank; a first temperature sensor monitoring a first temperature of the hydrogen fuel stored in the first hydrogen fuel storage tank; a second temperature sensor monitoring a second temperature of the hydrogen fuel stored in the second hydrogen fuel storage tank; a valve configured to control flow of hydrogen fuel through the first circulation loop and a second circulation loop; and a controller controlling operation of the valve based on the first temperature and the second temperature; wherein the pressure control device is positioned downstream from the second hydrogen fuel storage tank and connected to the second hydrogen fuel storage tank, wherein the heat load reduction line includes the second circulation loop from the first point downstream of the pressure control device to the second hydrogen fuel storage tank and back to the second point downstream of the pressure control device, and wherein the controller operates the valve to flow hydrogen fuel through the first circulation loop of the heat load reduction line based on the first temperature being less than the second temperature. 4. The hydrogen fueling station of claim 3 , wherein the second hydrogen fuel storage tank is cascaded with the first hydrogen fuel storage tank. 5. The hydrogen fueling station of claim 3 , wherein the controller operates the valve to bypass both the first and second circulation loops of the heat load reduction line based on a temperature of the first point downstream of the pressure control device being less than or equal to both the first temperature and the second temperature. 6. The hydrogen fueling station of claim 3 , wherein the controller operates the valve to flow hydrogen fuel through the second circulation loop of the heat load reduction line based on the second temperature being less than the first temperature. 7. The hydrogen fueling station of claim 3 , wherein the heat load reduction line includes one or more protrusions. 8. The hydrogen fueling station of claim 7 , wherein one or more of the protrusions are fins. 9. The hydrogen fueling station of claim 3 , wherein a path of the heat load reduction line through the first hydrogen fuel storage tank has a shape of a loop, an ‘S’, or a zig-zag. 10. The hydrogen fueling station of claim 3 , comprising a heat exchanger positioned downstream from the pressure control device and connected to the pressure control device. 11. A hydrogen fueling station, comprising: a hydrogen fuel storage tank; a pressure control device including one or more control valves positioned downstream from the hydrogen fuel storage tank; a dispenser positioned downstream from the pressure control device; a heat load reduction line which forms a circulation loop from a first point downstream of the pressure control device to the hydrogen fuel storage tank, wherein hydrogen fuel within the heat load reduction line does not mix with the hydrogen fuel within the hydrogen fuel storage tank; a compressor positioned upstream from the hydrogen fuel storage tank and connected to the hydrogen fuel storage tank; a second hydrogen fuel storage tank; a first temperature sensor monitoring a first temperature of the hydrogen fuel stored in the hydrogen fuel storage tank; a second temperature sensor monitoring a second temperature of the hydrogen fuel stored in the second hydrogen fuel storage tank; a valve configured to control flow of hydrogen fuel through the circulation loop and a second circulation loop; and a controller controlling operation of the valve based on the first temperature and the second temperature; wherein the pressure control device is positioned downstream from the second hydrogen fuel storage tank and connected to the second hydrogen fuel storage tank, wherein the heat load reduction line includes the second circulation loop from the first point downstream of the pressure control device to the second hydrogen fuel storage tank and back to the second point downstream of the pressure control device, and wherein the controller operates the valve to flow hydrogen fuel through the circulation loop of the heat load reduction line based on the first temperature being less than the second temperature.
Very high pressure (>80 bar) · CPC title
for refuelling vehicle fuel tanks · CPC title
using the same fluid · CPC title
Fuel stations · CPC title
Pressure · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.