Method of reducing corrosion and corrosion byproduct deposition in a crude unit
US-9150793-B2 · Oct 6, 2015 · US
US9611431B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9611431-B2 |
| Application number | US-201514874675-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 5, 2015 |
| Priority date | Nov 3, 2008 |
| Publication date | Apr 4, 2017 |
| Grant date | Apr 4, 2017 |
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.
A method of optimizing system parameters in a crude unit to reduce corrosion and corrosion byproduct deposition in the crude unit is disclosed and claimed. The method includes measuring or predicting properties associated with the system parameters and using an automated controller to analyze the properties to cause adjustments in the chemical program to optimize the system parameters. Adjusting the system parameters effectively controls corrosion in the crude unit by reducing the corrosiveness of a fluid in the process stream and/or by protecting the system from a potentially corrosive substance. System parameter sensing probes are arranged at one or more locations in the process stream to allow accurate monitoring of the system parameters in the crude unit.
Opening claim text (preview).
The claimed invention is: 1. A method of optimizing a system parameter in a process stream of a crude unit, the method comprising: (a) introducing a challenging crude oil into a crude unit that previously contained a different kind of crude oil, the properties of the challenging crude differing such from the previous crude oil that it disrupts the steady state of the unit including causing a corrosion inducing spike in chloride concentration, (b) measuring and/or predicting a property associated with the system parameter at one or more points in the crude unit; (c) determining an optimum range associated with the measured and/or predicted property; (d) if the measured and/or predicted property is outside of the optimum range associated with that property, causing a change in an influx of a composition into the process stream, the composition capable of adjusting the property associated with the system parameter in a manner to bring the measured and/or predicted property within said optimum range; provided that adjustments are limited to no more than one per 30 minutes and if there are either four overall adjustments or the adjustment results in a change of at least 50% of added composition then further influx of composition is suspended for 4 hours; and (e) optionally repeating steps (b) to (d) for a plurality of different system parameters, each different system parameter having a unique associated property wherein the measuring/or predicting property comprises: collecting a sample of fluid from a process stream to form a sample stream; adding a sulfide scavenger obtained by reacting morpholine with formaldehyde to the sample stream; passing the sample stream through a membrane that prevents a reaction product of the sulfide scavenger and sulfide from flowing therethrough; and allowing the sample stream that flows through the membrane to contact a chloride specific electrode of a measurement cell to measure chloride content. 2. The method of claim 1 , including: (i) converting the measured property into an input electrical signal capable of being transmitted to a controller and (ii) transmitting the input electrical signal to the controller. 3. The method of claim 2 , including transmitting the input electrical signal via a wireless interface. 4. The method of claim 2 , wherein the controller is operable to: (i) receive the transmitted input electrical signal; (ii) convert the received electrical signal into an input numerical value; (iii) analyze the input numerical value: (iv) generate an output numerical value; (v) convert the. output numerical value into an output electrical signal; and (vi) transmit the output electrical signal. 5. The method of claim 4 , including transmitting the output electrical signal via a wireless interface. 6. The method of claim 4 , wherein the controller is operable to: (i) analyze the input numerical value and (ii) determine if the input numerical value corresponds to the optimum range associated with the measured property. 7. The method of claim 6 , wherein if the input numerical value does not correspond to the optimum range, the transmitted output electrical signal causing the change in the influx of the composition into the process stream, the composition capable of adjusting the property associated with the system parameter in a manner to cause the input numerical value to correspond to the optimum input range. 8. The method of claim 1 , including continuously or intermittently measuring and/or predicting the system parameter. 9. The method of claim 1 , including monitoring the system parameter in real time. 10. The method of claim 1 , including a plurality of different compositions, wherein an influx of one or more of the different compositions into the process stream are collectively and/or individually capable of adjusting the property associated with the system parameter. 11. The method of claim 1 , wherein the plurality of different system parameters is selected from the group consisting of: pH, chloride ion concentration; iron ion concentration; non-iron Metal ion concentration; corrosion rate; and combinations thereof. 12. The method of claim 11 , wherein the crude unit has a plurality of components including an atmospheric tower with at least one heat exchanger, and wherein the pH and chloride ion concentration are derived from a dew point water sample and/or an accumulator boot water sample in the crude unit and the iron ion concentration or the non-iron metal ion concentration is derived from the accumulator hoot water sample in the crude unit. 13. The method of claim 12 , including obtaining the dew point water sample and/or the boot water sample with an online, optionally automated, sampling device. 14. The method of claim 1 , wherein the optimum range is user-defined. 15. The method of claim 1 , including operating the method continuously, automatically, and online or on a batch basis. 16. The method of claim 1 , including operating the method either simultaneously or sequentially for at least two of the different system parameters. 17. The method of claim 1 , including operating the method over a network. 18. The method of claim 1 , further comprising selecting the system parameter to reduce corrosion and/or corrosion byproduct deposition in the crude unit. 19. The method of claim 1 , further comprising selecting the system parameter to optimize preheating operations to keep product and/or effluent water within specifications. 20. The method of claim 1 , further comprising selecting the system parameter to optimize desalting operations to keep product and/or effluent water within specifications. 21. The method of claim 1 , farther comprising selecting the system parameter to optimize distilling operations to keep product and/or effluent water within specifications.
Limiting deterioration of equipment · CPC title
by treating with water · CPC title
by addition of corrosion inhibitors · CPC title
of metals · CPC title
Corrosion probes · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.