Process scheme to improve divalent metal salts removal from mono ethylene glycol (MEG)
US-9790153-B2 · Oct 17, 2017 · US
US10456707B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10456707-B2 |
| Application number | US-201615762468-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2016 |
| Priority date | Nov 30, 2015 |
| Publication date | Oct 29, 2019 |
| Grant date | Oct 29, 2019 |
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The present invention relates to a reactor, and according to one aspect of the present invention, there is provided a reactor comprising a housing provided with a reaction space, a tube disposed inside the housing, an impeller provided inside the housing to allow reactants in the reaction space to flow into and out of the tube and a nozzle provided to spray a liquid from the reaction space toward the housing wall surface side.
Opening claim text (preview).
The invention claimed is: 1. A reactor comprising: a housing provided with a reaction space; a tube disposed inside said housing; an impeller provided inside the housing to allow reactants in the reaction space to flow into and out of the tube; and a nozzle provided to spray a liquid from the reaction space toward the housing wall surface side, wherein the nozzle is provided such that a jetting port is located at 5% or less of the distance between the housing wall surface and the tube, and wherein the nozzle is provided along the circumferential direction of the tube. 2. The reactor according to claim 1 , wherein the nozzle is provided to spray the liquid toward the housing wall surface side after being extended from the housing wall surface toward the tube side. 3. The reactor according to claim 2 , wherein the nozzle is provided to have a bent part. 4. The reactor according to claim 1 , wherein the reactor is provided such that in the reaction space, a crystallization reaction takes place, and the nozzle sprays the liquid for eliminating crystallization heat. 5. The reactor according to claim 4 , wherein the nozzle is provided so that vapor generated by vaporization of the liquid sprayed from the nozzle during the crystallization reaction rises adjacent to the wall surface of the housing. 6. The reactor according to claim 1 , wherein the tube has a hollow opening along the height direction of the housing. 7. The reactor according to claim 6 , wherein the impeller is disposed inside the tube. 8. The reactor according to claim 6 , wherein the tube is provided such that the diameter increases or decreases at any one of the upper end and the lower end.
Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title
Stationary reactors having moving elements inside (B01J19/08, B01J19/26 take precedence) · CPC title
Crystallisation (crystallisation directly from the vapour phase B01D7/02; making single crystals C30B {; crystallisation as part of the Bayer process also classified in C01F7/14}) · CPC title
General arrangements of crystallisation plant, e.g. flow sheets · CPC title
Processes or apparatus therefor · CPC title
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