Rate/kinetic selective multiple bed adsorption process cycle
US-11883775-B2 · Jan 30, 2024 · US
US10357737B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10357737-B2 |
| Application number | US-201916257971-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 25, 2019 |
| Priority date | Apr 12, 2017 |
| Publication date | Jul 23, 2019 |
| Grant date | Jul 23, 2019 |
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A sulfur removal system including a first reactor and a second reactor that are located in series to one another each having an adsorbent that includes cobalt and copper on an activated carbon support, a method of desulfurizing a sulfur-containing hydrocarbon stream via the sulfur removal system, and a method of making the adsorbent. Various embodiments of the sulfur removal system, the desulfurizing method, and the method of making the adsorbent is also provided.
Opening claim text (preview).
The invention claimed is: 1. A sulfur removal system with a cylindrical adsorbent vessel, comprising: a first reactor comprising a first vessel having a first internal cavity with a first adsorbent bed that contains a first adsorbent, a first inlet located proximal to a bottom of the first vessel, and a first outlet located proximal to a top of the first vessel, wherein the first vessel is in the form of a cylinder mounted vertically along the axis of the cylinder; wherein the first reactor is a fluidized-bed reactor; and a second reactor comprising a second vessel having a second inlet, a second outlet, and a second internal cavity with a second adsorbent bed that contains a second adsorbent, wherein the first and the second adsorbents comprise cobalt and copper on an activated carbon support, wherein the first adsorbent bed has a cross-sectional area that is substantially the same as a cross-sectional area of the first vessel, and wherein the second inlet is fluidly connected to the first outlet via a connecting line. 2. The system of claim 1 , further comprising a lower mesh structure located in the first internal cavity and proximal to the bottom of the first vessel and an upper mesh structure located in the first internal cavity and proximal to the top of the first vessel, defining the first adsorbent bed. 3. The system of claim 2 , wherein the first adsorbent has a particle size in the range of 0.5 to 10 mm, and wherein the lower and the upper mesh structures have a mesh size of less than 0.5 mm. 4. The system of claim 1 , wherein the second reactor is a fixed-bed reactor. 5. The system of claim 4 , wherein the second inlet is located proximal to a top of the second vessel and the second outlet is located proximal to a bottom of the second vessel. 6. The system of claim 4 , wherein the second inlet is located proximal to a bottom of the second vessel and the second outlet is located proximal to a top of the second vessel. 7. The system of claim 1 , further comprising: a liquid reservoir located upstream of and fluidly connected to the first inlet via a solvent line, wherein the liquid reservoir is configured to deliver a solvent to the first and the second internal cavities to regenerate the first and the second adsorbents.
Carbon · CPC title
according to the "fluidised technique" · CPC title
according to the "fluidised bed" technique · CPC title
Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106 · CPC title
using two beds · CPC title
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