Fluid distribution device for multibed reactors
US-9211516-B2 · Dec 15, 2015 · US
US11319505B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11319505-B2 |
| Application number | US-201716305780-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 19, 2017 |
| Priority date | May 30, 2016 |
| Publication date | May 3, 2022 |
| Grant date | May 3, 2022 |
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The invention relates to a device for the upflow of a single-phase fluid comprising at least two beds of solid particles and at least one bypass means for a portion of said fluid, and also to the use thereof.
Opening claim text (preview).
The invention claimed is: 1. A system comprising a device purifying a fouling single-phase fluid upstream of a catalytic reactor, said device comprising: a source of fouling single-phase fluid comprising an oil containing triglycerides and/or fatty adds and/or fatty add esters, fluidly connected to said device, which device is capable of upflow of the fouling single-phase fluid, at least two beds of solid particles retained on a lower surface of each bed by a distributor of said fouling single-phase fluid and on an upper surface of each bed by a retainer of said particles, each bed comprising at least one bypass of a portion of said fouling single-phase fluid, attached to said distributor and to said retainer, each bypass comprising a pipe, a lower end of which opens below a lower surface of said distributor and an upper end of which opens above said retainer, said pipe comprising a restrictor restricting the passage actuated by differential pressure across said bed, and a fluid connection of purified single-phase fluid to the catalytic reactor. 2. The device system according to claim 1 , comprising at least two bypasses per bed, the restrictor restricting the passage of said bypass being actuated by different differential pressures across each of said beds. 3. The system according to claim 1 , in which said restrictor comprises: a flared tubular portion, an orifice of which that has the smallest cross section is oriented towards the upstream of the pipe of the bypass, a movable part, mounted in said flared tubular portion so as to allow a displacement between a closure position and a maximum opening position, the positioning of the movable part being a function of the flow rate of fluid in said flared tubular portion, and a return that acts on the movable part in order to displace it towards the closure position in which the movable part blocks the orifice of the flared tubular portion that has the smallest cross section. 4. The system according to claim 1 , in which said restrictor comprises: at least one plate movably mounted about an axis on the upper end of the pipe of the bypass so as to allow a displacement between a closure position and a maximum opening position, the positioning of said at least one plate being a function of the flow rate of fluid in the bypass, and a return that acts on the at least one plate in order to displace it (them) towards the closure position during which the at least one plate blocks the end of the pipe. 5. The system according to claim 1 , in which a small space is made between an upper surface of at least one bed and a corresponding retainer retaining the particles. 6. A process for treating an oil containing triglycerides and/or free fatty acids and/or esters in the system according to claim 1 , said process comprising: operating said device at a temperature of 50° C. to 320° C., at a pressure of 0.1 to 7 MPa, and with a residence time of said oil on said at least two beds of solid particles of 0.1 to 1.8 hours; wherein said solid particles are an adsorbent formed by porous refractory oxides, clays, zeolites, activated carbons, silicon carbide, or mixtures thereof. 7. The process according to claim 6 , in which at least two of said device are used in parallel in said system. 8. The process according to claim 6 , in which said adsorbent is a porous refractory oxide that has a macroporosity. 9. The process according to claim 6 , in which said adsorbent is free of catalytic metals from groups 6 and 8 to 12. 10. The process according to claim 6 , in which a process for hydrotreating said oil is conducted in said catalytic reactor, and said device is used for pretreatment of said oil upstream of said catalytic reactor.
Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title
including a sorption process as the refining step in the absence of hydrogen · CPC title
the beds being superimposed one above the other · CPC title
Means for supporting the bed of particles, e.g. grids, bars, perforated plates · CPC title
the beds being placed in separate reactors · CPC title
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