Methods utilizing active quantum chemistry
US-2024317612-A1 · Sep 26, 2024 · US
US2025354272A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025354272-A1 |
| Application number | US-202418897068-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 26, 2024 |
| Priority date | May 14, 2024 |
| Publication date | Nov 20, 2025 |
| Grant date | — |
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.
Provided is an electrochemical system comprising a water electrolysis stack with an anode and a cathode. The system includes a reaction fluid supply line that supplies a reaction fluid to the anode, a first gas-liquid separator located in the reaction fluid supply line to separate the reaction fluid into gaseous and liquid components, and a first filter part positioned upstream of the first gas-liquid separator to filter the reaction fluid. The system further includes a first circulation line that circulates the liquid reaction fluid from the anode back to the first gas-liquid separator. Additionally, a second gas-liquid separator in a discharged fluid discharge line is connected to the cathode, with a second circulation line configured to maintain the ionic purity of the discharged fluid. The system also includes a mechanism to monitor ionic conductivity and selectively control the operation of the water electrolysis stack based on detected ionic levels.
Opening claim text (preview).
What is claimed is: 1 . An electrochemical system comprising: a water electrolysis stack comprising an anode and a cathode; a reaction fluid supply line configured to supply a reaction fluid to the anode; a first gas-liquid separator located in the reaction fluid supply line and configured to separate the reaction fluid into a gaseous reaction fluid and a liquid reaction fluid; a first filter part located in the reaction fluid supply line, located at an upstream side of the first gas-liquid separator, and configured to filter the reaction fluid; a first circulation line configured to connect the first gas-liquid separator and the anode and circulate the liquid reaction fluid, which has passed through the anode, to the first gas-liquid separator; and a first bypass line having one end located between the first gas-liquid separator and the water electrolysis stack and connected to the reaction fluid supply line, and the other end located at an upstream side of the first filter part and connected to the reaction fluid supply line. 2 . The electrochemical system of claim 1 , comprising: a first ion sensor located in the reaction fluid supply line, disposed at the upstream side of the first gas-liquid separator, and configured to sense ionic conductivity of the reaction fluid, wherein an operation of the water electrolysis stack is configured to be selectively controlled based on a detection by the first ion sensor. 3 . The electrochemical system of claim 1 , comprising: a first three-way valve located in the reaction fluid supply line and connected to one end of the first bypass line. 4 . The electrochemical system of claim 3 , comprising: a second ion sensor located in at least any one of the reaction fluid supply line and the first circulation line and configured to sense ionic conductivity of the liquid reaction fluid, wherein the first three-way valve is configured to selectively switch a flow of the liquid reaction fluid from a downstream side of the first gas-liquid separator to the upstream side of the first gas-liquid separator based on a detection by the second ion sensor. 5 . The electrochemical system of claim 4 , wherein the first filter part is replaced when the ionic conductivity of the liquid reaction fluid detected by the second ion sensor is equal to or higher than preset reference ionic conductivity when a preset reference time elapses after the flow of the liquid reaction fluid is switched from the downstream side of the first gas-liquid separator to the upstream side of the first gas-liquid separator. 6 . The electrochemical system of claim 1 , comprising: a discharged fluid discharge line connected to the cathode and configured to discharge a discharged fluid from the cathode; a second gas-liquid separator located in the discharged fluid discharge line and configured to separate the discharged fluid into a gaseous discharged fluid and a liquid discharged fluid; and a second circulation line configured to connect the second gas-liquid separator and the reaction fluid supply line and circulate the liquid discharged fluid to the reaction fluid supply line. 7 . The electrochemical system of claim 6 , comprising: a reaction fluid storage part located in the reaction fluid supply line, disposed at the upstream side of the first filter part, and configured to store the reaction fluid; and a pre-processing filter part located in the reaction fluid supply line, disposed at an upstream side of the reaction fluid storage part, and configured to filter the reaction fluid, wherein the second circulation line is connected to the reaction fluid storage part. 8 . The electrochemical system of claim 6 , comprising: a second filter part located in the second circulation line and configured to filter the liquid discharged fluid. 9 . The electrochemical system of claim 8 , comprising: a second bypass line having one end located at a downstream side of the second filter part and connected to the second circulation line, and the other end connected to the cathode. 10 . The electrochemical system of claim 9 , comprising: a second three-way valve located in the second circulation line and connected to one end of the second bypass line. 11 . The electrochemical system of claim 10 , comprising: a third ion sensor located in at least any one of the discharged fluid discharge line and the second circulation line and configured to sense ionic conductivity of the liquid discharged fluid, wherein the second three-way valve selectively switches a flow of the liquid discharged fluid from the downstream side of the second filter part to the cathode based on a detection by the third ion sensor. 12 . The electrochemical system of claim 11 , wherein the second filter part is replaced when the ionic conductivity of the liquid discharged fluid detected by the third ion sensor is equal to or higher than preset reference ionic conductivity when a preset reference time elapses after the flow of the liquid discharged fluid is switched from the downstream side of the second filter part to the cathode. 13 . The electrochemical system of claim 8 , comprising: a discharged fluid storage part located in the second circulation line, disposed at a downstream side of the second filter part, and configured to store the liquid discharged fluid. 14 . An electrochemical system comprising: a water electrolysis stack comprising an anode and a cathode; a reaction fluid supply line configured to supply a reaction fluid to the anode; a first gas-liquid separator located in the reaction fluid supply line and configured to separate the reaction fluid into a gaseous reaction fluid and a liquid reaction fluid; a first filter part located in the reaction fluid supply line, positioned at an upstream side of the first gas-liquid separator, and configured to filter the reaction fluid; a first circulation line configured to connect the first gas-liquid separator and the anode and circulate the liquid reaction fluid, which has passed through the anode, to the first gas-liquid separator; a reaction fluid storage part located in the reaction fluid supply line, disposed at an upstream side of the first filter part, and configured to store the reaction fluid; a first ion sensor located in the reaction fluid supply line upstream of the first gas-liquid separator and configured to detect the ionic conductivity of the reaction fluid; a second ion sensor located in at least one of the reaction fluid supply line and the first circulation line, and configured to detect the ionic conductivity of the liquid reaction fluid; wherein the electrochemical system further comprises a system configured to selectively stop the operation of the water electrolysis stack based on the ionic conductivity detected by the first and second ion sensors. 15 . The electrochemical system of claim 14 , further comprising: a sensor configured to monitor the ionic conductivity of the reaction fluid, wherein the system is configured to replace the first filter part when the ionic conductivity exceeds a predetermined threshold. 16 . The electrochemical system of claim 14 , wherein the control system is configured to selectively stop the operation of the water electrolysis stack when a specific ionic conductivity threshold is detected. 17 . The electrochemical system of claim 14 , wherein the reaction fluid storage part is configured to store the reaction fluid before it is supplied to the first filter part. 18 . An electrochemical system comprising: a water elec
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
by electrolysis of water · CPC title
Conductivity · CPC title
Assemblies comprising two or more cells · CPC title
Removing impurities · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.