Urea synthesis method
US-2016075642-A1 · Mar 17, 2016 · US
US11338221B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11338221-B2 |
| Application number | US-202017114317-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 7, 2020 |
| Priority date | Oct 27, 2017 |
| Publication date | May 24, 2022 |
| Grant date | May 24, 2022 |
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.
Disclosed is a shell-and-tube heat exchanger type with a tube bundle and has a redistribution chamber connected to tubes of the tube bundle and to a duct. The duct extends between the redistribution chamber and the shell.
Opening claim text (preview).
The invention claimed is: 1. A shell-and-tube heat exchanger which comprises a vessel which comprises a shell and at least one tube bundle, wherein the shell encloses a vessel space, wherein the tube bundle comprises tubes having ends, and wherein a shell space is provided between the tubes and the shell, wherein the heat exchanger further comprises a redistribution chamber located in said vessel space, wherein said redistribution chamber comprises a wall for separating a first fluid in the shell space from a second fluid inside the redistribution chamber, wherein the wall of the redistribution chamber comprises a flat plate comprising a plurality of bore holes, wherein a plurality of said tubes are connected to a single redistribution chamber at said bore holes such that said second fluid can flow between said tubes and said redistribution chamber, wherein the heat exchanger further comprises a duct extending from an opening for the second fluid in said shell through said vessel space to said redistribution chamber such that the second fluid can flow between a tube end and said opening for the second fluid in said shell through said redistribution chamber and said duct. 2. The heat exchanger according to claim 1 , wherein the duct has a first duct end connected with a wall of the redistribution chamber and a second end connected with the shell. 3. The heat exchanger according to claim 2 , wherein the first duct end is aligned with an opening in the wall and the second duct end is aligned with an opening in the shell, such that fluid can flow from outside the shell to the redistribution chamber through the duct; wherein the duct is at least in part located in the vessel; wherein the first duct end is located in the vessel; wherein the duct extends through the vessel space; and wherein the outer surface of the duct is exposed to the shell space. 4. The heat exchanger according to claim 2 , wherein the first duct end is connected to said redistribution chamber. 5. The heat exchanger according to claim 4 , wherein the first duct end is connected to said redistribution chamber with a weld. 6. The heat exchanger according to claim 4 , wherein the first duct end is placed radially outwardly of the tube ends connected to that redistribution chamber. 7. The heat exchanger according to claim 1 , wherein the duct has an outer surface exposed to the shell space. 8. The heat exchanger according to claim 1 configured for condensation of a compound. 9. The heat exchanger according to claim 8 , wherein the compound is carbamate. 10. The heat exchanger according to claim 1 configured for operation at pressures below 100 bar. 11. The heat exchanger according to claim 1 , wherein the flat plate has a thickness that is 0.5 to 2 times the thickness of any other part of the wall of the redistribution chamber. 12. The heat exchanger according to claim 1 , wherein the redistribution chamber comprises an internal load bearing structure. 13. The heat exchanger according to claim 1 , wherein the internal load bearing structure is a spacer.
Horizontal tubes · CPC title
Recirculating of the cooling medium · CPC title
Removing and treatment of non condensable gases · CPC title
Feeding the steam or the vapours · CPC title
Condensation of vapours; Recovering volatile solvents by condensation (B01D8/00 takes precedence; condensers F28B) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.