A method for decreasing feed impurities
US-2024350942-A1 · Oct 24, 2024 · US
US9868910B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9868910-B2 |
| Application number | US-201615137471-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 25, 2016 |
| Priority date | Jun 4, 2015 |
| Publication date | Jan 16, 2018 |
| Grant date | Jan 16, 2018 |
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A process for managing hydrates and hydrocarbon-based solids in a hydrocarbon stream. The process includes: introducing the hydrocarbon stream into an inlet of a system comprising at least a first cold flow reactor and a second cold flow reactor, each cold flow reactor comprising a heat exchanger and at least one static mixer; directing at least a portion of the hydrocarbon stream to the first cold flow reactor; cooling the portion of the hydrocarbon stream directed to the first cold flow reactor to a temperature less than the hydrate formation temperature, the temperature effective to substantially complete hydrate formation upon exiting the system to form a hydrate and hydrocarbon-based solids managed hydrocarbon stream; directing a lesser portion of the hydrocarbon stream to the second cold flow reactor; and remediating the second cold flow reactor by removing hydrate or hydrocarbon-based solids formed on internal surfaces of the second cold flow reactor. A remediable system for managing hydrates and hydrocarbon-based solids in a hydrocarbon stream is also described.
Opening claim text (preview).
What is claimed is: 1. A process for managing hydrates and hydrocarbon-based solids in a hydrocarbon stream, the process comprising: (a) introducing the hydrocarbon stream into an inlet of a system comprising at least a first cold flow reactor and a second cold flow reactor, each cold flow reactor comprising a heat exchanger and at least one static mixer; (b) directing at least a portion of the hydrocarbon stream to the first cold flow reactor; (c) cooling the portion of the hydrocarbon stream directed to the first cold flow reactor to a temperature less than the hydrate formation temperature to form a hydrate and hydrocarbon-based solids managed hydrocarbon slurry stream; (d) directing a lesser portion of the hydrocarbon stream to the second cold flow reactor; (e) remediating the second cold flow reactor by removing hydrate or hydrocarbon-based solids formed on internal surfaces of the second cold flow reactor; (f) forming a remediation slipstream comprising removed hydrate or hydrocarbon-based solids from the second cold flow reactor; and (g) returning the remediation slipstream from the second cold flow reactor to the inlet of the system. 2. The process of claim 1 , wherein hydrate or hydrocarbon-based solids are removed by introducing methanol into the lesser portion of the hydrocarbon stream. 3. The process of claim 2 , wherein hydrate or hydrocarbon-based solids are removed by heating the external surfaces of the second cold flow reactor. 4. The process of claim 1 , wherein hydrate or hydrocarbon-based solids are removed by heating the external surfaces of the second cold flow reactor. 5. The process of claim 1 , further comprising: (h) after the remediating (e), directing at least a subsequent portion of the hydrocarbon stream to the second cold flow reactor; (i) cooling the subsequent portion of the hydrocarbon stream directed to the second cold flow reactor to a temperature less than the hydrate formation temperature to form a hydrate and hydrocarbon-based solids managed hydrocarbon slurry stream; (j) directing a subsequent lesser portion of the hydrocarbon stream to the first cold flow reactor; and (k) remediating the first cold flow reactor by removing hydrate or hydrocarbon-based solids formed on internal surfaces of the first cold flow reactor. 6. The process of claim 5 , further comprising (l) forming a subsequent remediation slipstream comprising removed hydrate or hydrocarbon-based solids from the first cold flow reactor. 7. The process of claim 6 , further comprising (m) returning the subsequent remediation slipstream from the first cold flow reactor to the inlet of the system.
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