Treatment of interface rag produced during heavy crude oil processing
US-9023213-B2 · May 5, 2015 · US
US9284496B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9284496-B2 |
| Application number | US-201314087758-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 22, 2013 |
| Priority date | Jul 27, 2010 |
| Publication date | Mar 15, 2016 |
| Grant date | Mar 15, 2016 |
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.
The improved system relates to desalting hydrocarbon feeds using a separator with a stacked disk centrifuge to separate an emulsified oil and water rag layer. This system is effective for desalting heavy, high ionic, and non-traditional crude oils.
Opening claim text (preview).
The invention claimed is: 1. A crude oil desalter system comprising: a) a feed for a crude oil and water mixture; b) a separator connected to said feed wherein said separator comprises three or more outlets including an outgoing crude oil stream outlet, an outgoing wastewater stream outlet and an outgoing rag layer stream outlet, wherein the rag layer is an emulsion formed between the crude oil and water; and c) a disk stack centrifuge connected to said outgoing rag layer stream outlet wherein said disk stack centrifuge comprises three or more separate outgoing streams including an outgoing crude oil stream for desalted crude oil, an outgoing wastewater stream for waste water and an outgoing solids rich stream. 2. The desalter of claim 1 , wherein said separator is selected from the group consisting of one or more low pressure separators, high pressure separators, 2 phase separators, electrostatic coalescence separators, AC deep-field electrostatic separators, dual frequency separators, dual polarity combination AC/DC electrostatic separators, 3 phase separators, high velocity electrostatic coalescing separators, vessel internal electrostatic coalescers, and combinations thereof. 3. The desalter of claim 1 , wherein said disk stack centrifuge is selected from the group consisting of nozzle separators, self-cleaning disk separators, solid-wall separators, and the like which contain a stack of conical disks either with or without chambers to collect a variety of materials separated using centrifugal forces. 4. The desalter of claim 1 , further including a heater to heat the crude oil emulsion to a temperature of between approximately 140° F. and 300° F. prior to separation or centrifugation in the stacked disk centrifuge.
by centrifugal force · CPC title
with the aid of centrifugal force · CPC title
by using a centrifuge · CPC title
Dewatering · CPC title
Water · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.