Process for the preparation of glycols
US-2018362424-A1 · Dec 20, 2018 · US
US9289741B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9289741-B2 |
| Application number | US-201313753714-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 30, 2013 |
| Priority date | Feb 1, 2012 |
| Publication date | Mar 22, 2016 |
| Grant date | Mar 22, 2016 |
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.
An apparatus for generating a large volume of gas from a liquid stream is disclosed. The apparatus includes a first channel through which the liquid stream passes. The apparatus also includes a layer of catalyst particles suspended in a solid slurry for generating gas from the liquid stream. The apparatus further includes a second channel through which a mixture of converted liquid and generated gas passes. A heat exchange channel heats the liquid stream. A wicking structure located in the second channel separates the gas generated from the converted liquid.
Opening claim text (preview).
We claim: 1. An apparatus for generating a large volume of gas from a liquid stream, comprising: a. a first channel through which the liquid stream passes; b. a layer of catalyst particles suspended in a solid slurry, through which the liquid stream passes from one side of the catalyst layer to the other, for generating gas from the liquid stream; and c. a second channel through which a mixture of converted liquid and generated gas passes, wherein the first and second channels are located on opposite sides of the catalyst layer. 2. The apparatus of claim 1 further comprising a heat exchange channel for heating the liquid stream. 3. The apparatus of claim 1 further comprising a wicking structure located in the second channel for separating the gas generated from the converted liquid. 4. The apparatus of claim 1 wherein the liquid stream is a liquid organic hydrogen carrier and the generated gas is hydrogen. 5. The apparatus of claim 1 wherein the catalyst particles comprise at least one of the following: Pt/Al 2 O 3 and Pd/Al 2 O 3 . 6. The apparatus of claim 1 wherein the catalyst particles are approximately 2 μm or less. 7. The apparatus of claim 1 wherein the solid slurry consists of catalyst particles held together in a solid-like matrix with a polymer. 8. The apparatus of claim 7 wherein the polymer is Teflon. 9. The apparatus of claim 7 wherein the catalyst particles comprise at least 90% by mass of the solid slurry. 10. The apparatus of claim 7 wherein greater than 50% of the catalyst is accessible relative to 100% catalyst particles. 11. The apparatus of claim 2 further comprising a structural element in the first channel to support the suspended slurry and to improve heat transfer. 12. The apparatus of claim 1 wherein the suspended slurry is less than about 0.5 mm thick. 13. The apparatus of claim 1 wherein the suspended slurry is less than about 0.15 mm thick. 14. The apparatus of claim 1 wherein the suspended slurry is in a sheet with an area to thickness ratio of at least 10 mm. 15. The apparatus of claim 1 wherein the suspended slurry is in a sheet with an area to thickness ratio of at least 1000 mm. 16. The apparatus of claim 1 wherein the suspended slurry is in a sheet with an area to thickness ratio of at least 10,000 mm. 17. An apparatus for generating a large volume of gas from a liquid stream, comprising: a. a first channel through which the liquid stream passes; b. a layer of catalyst particles suspended in a solid slurry, through which the liquid stream passes from one side of the catalyst layer to the other, for generating gas from the liquid stream; c. a second channel through which a mixture of converted liquid and generated gas passes, wherein the first and second channels are located on opposite sides of the catalyst layer; d. a heat exchange channel for heating the liquid stream; and e. a wicking structure located in the second channel for separating the gas generated from the converted liquid; wherein the liquid stream is a liquid organic hydrogen carrier and the generated gas is hydrogen, and the solid slurry contains catalyst particles held together in a solid-like matrix with a polymer.
Thickness of the active catalytic layer · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Plate-type reactors · CPC title
Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon · CPC title
Composition of support materials · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.