METHOD OF REDUCING CORROSION AND CORROSION BYPRODUCT DEPOSITION IN A CRUDE UNIT

Abstract

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.

Claims

1-18. (canceled)

19. A system for controlling chloride ion concentrations in a process stream of a crude unit to reduce corrosion and/or corrosion byproduct deposition in the crude unit, the system comprising: (a) a sensing device operable to sense and/or predict the chloride ion concentrations over time and convert the sensed or predicted chloride ion concentrations into input electrical signals capable of being transmitted, wherein the sensed and/or predicted chloride ion concentrations over time include a variation comprising chloride ion concentration spikes, and wherein the sensing device is operable to sense and/or predict the chloride ion concentrations at a frequency that shows the chloride ion concentration spikes over time; (b) a transmitter operable to transmit the input electrical signals; (c) a controller operable to receive the transmitted input electrical signals, convert the received input electrical signals into input numerical values, analyze the input numerical values, determine if the analyzed input numerical values are within an optimum range, generate output numerical values based upon the analyzed values, convert the output numerical values into output electrical signals, and transmit the output electrical signals; and (d) a receiver operable to receive the output electrical signals and cause changes in an influx rate of a composition into the process stream if the output numerical signal is not within the optimum range, wherein the composition is capable of adjusting the chloride ion concentration of the process stream, and wherein controlling the influx of the composition occurs to smooth the variation associated with the chloride ion concentration spikes.

20. The system of claim 19, further comprising a wireless interface by which the transmitter transmits the input electrical signals to the controller.

21. The system of claim 19, wherein the sensing device is operable to continuously or intermittently measure and/or predict the chloride ion concentration.

22. The system of claim 19, wherein the sensing device is operable to measure and/or predict the chloride ion concentration in real time.

23. A method of reducing corrosion and/or corrosion byproduct deposition in a crude unit, the method comprising: (a) providing a process stream flowing through the crude unit, wherein a process stream portion comprises process stream water, and wherein the process stream comprises a chloride ion concentration that comprises a variation including chloride ion concentration spikes that occur over time; (b) introducing an influx of a chloride ion controlling composition into the process stream, wherein the influx of the chloride ion controlling composition controls the chloride ion concentration; (c) automatically measuring and/or predicting the chloride ion concentration, wherein said measuring and/or predicting occurs at a frequency that shows the chloride ion concentration spikes in the chloride ion concentration over time; and (d) controlling the influx of the chloride ion controlling composition responsive to the measured and/or predicted chloride ion concentration in a manner effective to reduce crude unit corrosion and/or corrosion byproduct deposition and to smooth the variation associated with the chloride ion concentration spikes.

24. The method of claim 23, wherein step (d) comprises (i) analyzing the input numerical values, and (ii) determining if the input numerical values correspond to a corresponding optimum range associated with the chloride ion concentration.

25. The method of claim 24, wherein if an input numerical value does not correspond to the corresponding optimum range, step (d) comprises causing the transmitted output electrical signal to change the influx of the composition into the process stream.

26. The method of claim 23, wherein step (c) comprises continuously or intermittently measuring and/or predicting the chloride ion concentration.

27. The method of claim 23, wherein step (c) comprises monitoring the chloride ion concentration in real time.

28. The method of claim 23, further comprising the step of controlling the influx of one or more compositions to adjust at least one additional measured and/or predicted property of the process stream, wherein the at least one additional property is selected from the group consisting of: pH; iron ion concentration; non-iron metal ion concentration; corrosion rate; and combinations thereof.

29. The method of claim 28, further comprising a step of using a hierarchy logic to prioritize the influxes of one or more compositions used to adjust the chloride ion concentration and the at least one additional property.

30. The method of claim 23, further comprising the step of controlling an influx of a filming inhibitor composition into the process stream to adjust a measured and/or predicted Fe ion property of the process stream.

31. The method of claim 23, further comprising the step of controlling an influx of a neutralizer composition into the process stream to adjust a measured and/or predicted pH property of the process stream.

32. The method of claim 31, wherein the influx of the neutralizer composition is controlled using pH properties obtained at two sample points in the process stream.

33. The method of claim 23, wherein the influx of the chloride ion controlling composition is controlled using chloride ion measurements obtained at two sample points in the process stream.

34. The method of claim 31, wherein the neutralizer composition is selected from the group consisting of 3-methoxypropylamine, monoethanolamine, N,N-dimethylaminoethanol, or methoxyisopropylamine.

35. The method of claim 23, wherein the chloride ion controlling composition comprises a caustic agent.

36. The method of claim 35, wherein the caustic agent comprises NaOH.

37. The method of claim 30, wherein the filming inhibitor composition comprises an oil soluble blend comprising an amide and an imidazoline.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0021] FIG. 1 is a diagrammatic view of an embodiment of the invention showing various crude unit components and exemplary points at which system parameters are measured.

[0022] FIG. 2 shows a flowchart of a preferred embodiment of controlling the introduction of neutralizer(s) into the system based upon measured pH.

[0023] FIG. 3 illustrates an embodiment of the invention for controlling the introduction of caustic agent(s) into the system driven by the chloride ion concentration signal.

[0024] FIG. 4 illustrates an embodiment of the invention for controlling the introduction of filming inhibitors into the system driven by the iron ion concentration signal.

[0025] FIG. 5 depicts an embodiment of the invention for controlling the override of the introduction of neutralizer(s), caustic agent(s), and filming inhibitors into the system driven by the corrosion rates derived from one or more corrosion probes or other corrosion monitoring devices at any point in the system.

[0026] FIG. 6 shows a number of spikes of chloride concentration above the upper control limit from actual data from a crude unit and demonstrates how the method of the invention will be used to stabilize chloride ion concentration when tied to corrective action.

[0027] FIG. 7 shows pH and chloride ion concentration values tracked over time in an actual crude unit and demonstrates how the method of the invention will be used to stabilize these values.

DETAILED DESCRIPTION

[0028] As one of the main components of a crude unit process, corrosion control plays a vital role in maintaining system integrity. This invention provides a way to optimize the corrosion control component of the crude unit through optimizing one or more system parameters in a process stream of the crude unit. This optimization includes measuring properties associated with those parameters in the process stream.

[0029] The corrosion control program of the invention is designed to reduce corrosion of refinery processing equipment and subsequent fouling due to deposition of corrosion byproducts. A typical corrosion control program includes components such as a neutralizing amine, a filming inhibitor, a caustic solution, etc. Such corrosion control chemicals are traditionally injected into the system based upon measurements derived from grab samples and analyzed in the lab or some flow indication on the unit. This invention provides an automated method of adjusting chemical injection into the system.

[0030] In a preferred embodiment, the method of the invention includes a controller operable to receive and process information and provide instructions to various components (e.g., chemical injection pumps). The term controller refers to a manual operator or an electronic device having components such as a processor, memory device, digital storage medium, cathode ray tube, liquid crystal display, plasma display, touch screen, or other monitor, and/or other components. The controller is preferably operable for integration with one or more application-specific integrated circuits, programs, computer-executable instructions or algorithms, one or more hard-wired devices, wireless devices, and/or one or more mechanical devices. Moreover, the controller is operable to integrate the feedback, feed-forward, or predictive loop(s) of the invention. Some or all of the controller system functions may be at a central location, such as a network server, for communication over a local area network, wide area network, wireless network, internet connection, microwave link, infrared link, and the like. In addition, other components such as a signal conditioner or system monitor may be included to facilitate signal transmission and signal-processing algorithms.

[0031] Preferably, the controller includes hierarchy logic to prioritize any measured or predicted properties associated with system parameters. For example, the controller may be programmed to prioritize system pH over chloride ion concentration or vice versa. It should be appreciated that the object of such hierarchy logic is to allow improved control over the system parameters and to avoid circular control loops.

[0032] In one embodiment, the method includes an automated controller. In another embodiment, the controller is manual or semi-manual. For example, where the crude refining process includes one or more datasets received from a various sensors in the system, the controller may either automatically determine which data points/datasets to further process or an operator may partially or fully make such a determination. A dataset from a crude unit, for instance, may include variables or system parameters such as oxidation-reduction potential, pH, levels of certain chemicals or ions (e.g., determined empirically, automatically, fluorescently, electrochemically, colorimetrically, measured directly, calculated), temperature, pressure, process stream flow rate, dissolved or suspended solids, etc. Such system parameters are typically measured with any type of suitable data capturing equipment, such as pH sensors, ion analyzers, temperature sensors, thermocouples, pressure sensors, corrosion probes, and/or any other suitable device or method. Data capturing equipment is preferably in communication with the controller and, according to alternative embodiments, may have advanced functions (including any part of the control algorithms described herein) imparted by the controller.

[0033] Data transmission of measured parameters or signals to chemical pumps, alarms, or other system components is accomplished using any suitable device, such as a wired or wireless network, cable, digital subscriber line, internet, etc. Any suitable interface standard(s), such as an ethernet interface, wireless interface (e.g., IEEE 802.11a/b/g/x, 802.16, Bluetooth, optical, infrared, radiofrequency, etc.), universal serial bus, telephone network, the like, and combinations of such interfaces/connections may be used. As used herein, the term network encompasses all of these data transmission methods. Any of the described devices (e.g., plant archiving system, data analysis station, data capture device, process station, etc.) may be connected to one another using the above-described or other suitable interface or connection.

[0034] In an embodiment, system parameter information is received from the system and archived. In another embodiment, system parameter information is processed according to a timetable or schedule. In a further embodiment, system parameter information is immediately processed in real-time/substantially real-time. Such real-time reception may include, for example, streaming data over a computer network.

[0035] Referring now to the Figures, FIG. 1 depicts a diagram of a preferred embodiment of the invention. It should be appreciated that the particular configuration of the crude unit is not critical to the invention and FIG. 1 illustrates one possible configuration. FIG. 1 shows a typical atmospheric distillation tower system 100 of a crude unit that includes overhead heat exchanger bank 102, accumulator 104, distillation tower 106, and pumparound heat exchangers 108a and 108b. In this embodiment, a dew point water sample is obtained at the indicated point and a sample of accumulator boot water is obtained at the indicated points on FIG. 1. These samples are measured and analyzed for the system parameters of pH, chloride ion concentration, and iron ion concentration.

[0036] FIG. 1 shows values of 5.8 for pH and 93 ppm for chloride ion concentration at the dew point water sample point and values of 6.7 and 10, respectively, at the accumulator boot sample point. The measurement differences at these two sample points require a corresponding algorithm to adjust chemical injection. The preferred location in the crude unit for determining pH and chloride ion concentration is a dew point water sample, usually derived from the overhead heat exchangers of the distillation tower. Another advantage of determining pH from the dew point water is that the pH probe encounters lower levels of contaminants and fewer solid particles and oil droplets resulting in less frequent fouling. The term dew point refers to the point of initial condensation of steam to water or the temperature at which a phase of liquid water separates from the water vapors and liquid hydrocarbons and begins to form liquid water as the vapors cool. Though possible to use the accumulator water boot to measure pH and chloride ion level, a level of accuracy is usually sacrificed because data is diluted or masked by the full volume of steam and weak acids and bases that have condensed downstream of the water dew point.

[0037] In a preferred embodiment, dew point water is analyzed for pH and chloride. It is advantageous to analyze dew point water rather than overhead accumulator water for pH and chloride because the dew point water is typically cleaner and provides a faster response with more accurate measurement of these system parameters. Testing usually reveals a dramatic difference between water samples from these two locations. On many units, the dew point chloride concentration may be several hundred ppm, while a similar sample taken from overhead accumulator water may, at the same time, be from 10 to 50 ppm. For example, dew point water may have a pH of 5.8 and a chloride ion concentration of 93 ppm; whereas, the accumulator boot water of the same unit may have values of 6.7 and 10, respectively.

[0038] Likewise, it is possible to measure iron (or other metals, such as copper, molybdenum, nickel, zinc) ion concentration from the dew point water. The preferred location for determining iron or other metal ion concentration is at the accumulator water boot because these ions indicate corrosion has taken place and metal has been removed from an internal component in the system upstream of the sample point.

[0039] It should be appreciated that any suitable method may be used for obtaining the dew point water sample. For example, devices for obtaining the dew point water sample are disclosed in U.S. Pat. No. 4,335,072, titled Overhead Corrosion Simulator and U.S. Pat. No. 5,425,267, titled Corrosion Simulator and Method for Simulating Corrosion Activity of a Process Stream, each of which is incorporated herein by reference in its entirety.

[0040] In alternative embodiments, different fluid or system parameters or other constituents present in the system could be measured and/or analyzed. Representative measured parameters or constituents include pH; chloride ion; other strong and weak acids, such as sulfuric, sulfurous, thiosulfurous, carbon dioxide, hydrogen sulfide; organic acids; ammonia; various amines; and liquid or solid deposits. Various methods of measuring such parameters are contemplated and the invention is not limited to one particular method. Representative methods include, but are not limited to those disclosed in U.S. Pat. No. 5,326,482, titled On-Line Acid Monitor and Neutralizer Feed Control of the Overhead Water in Oil Refineries; U.S. Pat. No. 5,324,665, titled On-Line Method for Monitoring Chloride Levels in a Fluid Stream; U.S. Pat. No. 5,302,253, titled On-Line Acid Monitor and Neutralizer Feed Control of the Overhead Water in Oil Refineries, each of which is incorporated herein by reference in its entirety.

[0041] In response to the measured system parameters, FIG. 1 shows exemplary introduction points for neutralizers, filming inhibitors (sometimes referred to herein as filmers), and caustic agents. These points are labeled Neutralizer based on acid or pH, Filmer based on iron, and Caustic based on chloride. It should be appreciated that such chemicals may be added at any suitable location in the system, but are preferably added at the indicated point on FIG. 1. In this embodiment, neutralizer and filming inhibitor is added upstream of overhead heat exchanger bank 102 and caustic agent is added into the crude oil charge of atmospheric distillation tower system 100. According to a preferred embodiment, introduction of such chemicals into the system are adjusted continuously. In other embodiments, chemical introduction is adjusted intermittently or in relation to a schedule as determined for each individual system.

[0042] Neutralizer(s), caustic agent(s), and filming inhibitor(s) may be introduced to the system using any suitable type of chemical feed pump. Most commonly, positive displacement injection pumps are used powered either electrically or pneumatically. Continuous flow injection pumps are sometimes used to ensure specialty chemicals are adequately and accurately injected into the rapidly moving process stream. Though any suitable pump or delivery system may be used, exemplary pumps and pumping methods include those disclosed in U.S. Pat. No. 5,066,199, titled Method for Injecting Treatment Chemicals Using a Constant Flow Positive Displacement Pumping Apparatus and U.S. Pat. No. 5,195,879, titled Improved Method for Injecting Treatment Chemicals Using a Constant Flow Positive Displacement Pumping Apparatus, each incorporated herein by reference in its entirety.

[0043] Representative neutralizers include but are not limited to 3-methoxypropylamine (MOPA) (CAS #5332-73-0), monoethanolamine (MEA) (CAS #141-43-5), N,N-dimethylaminoethanol (DMEA) (CAS #108-01-0), and methoxyisopropylamine (MIOPA) (CAS #37143-54-7).

[0044] As a caustic agent, a dilute solution of sodium hydroxide is typically prepared in a 5 to 10% concentration (7.5 to 14 Baume) for ease of handling and to enhance distribution once injected into the crude oil, or desalter wash water, for example. Concentration may be adjusted according to ambient conditions, such as for freeze point in cold climates.

[0045] Filming inhibitors or filmers used in conjunction with this invention in a crude unit corrosion control program are typically oil soluble blends of amides and imidazolines. These compounds offer good corrosion control with minimal effects on the ability of the hydrocarbons in the system to carry water.

[0046] FIG. 2 shows a flowchart of a preferred embodiment of controlling the introduction of neutralizer(s) into the system based upon measured pH, labeled method 200. Box 202 represents the measuring device or analyzer that provides information related to the pH of the dew point (or accumulator) water. The analyzer (e.g., controller or operator) determines whether the pH is within an optimum range (5.8 to 6.0 in this example) as shown in box 204. If the pH is within the predetermined optimum range, the logic follows the Yes path and continues measuring and analyzing. If the pH is not within this range, the method includes determining whether the pH is below 5.8, as represented by box 206, or above 6.0, as represented by box 208. If the pH is below 5.8, the method includes increasing the neutralizer pump by, for example, 5% or 10%, as shown by box 210. If the pH is above 6.0, the method includes decreasing the neutralizer pump by, for example, 5% or 10%, as shown by box 212.

[0047] It should be appreciated that a suitable pH control or optimal range should be determined for each individual system. The optimum range for one system may vary considerably from that for another system. It is within the concept of the invention to cover any possible optimum pH range.

[0048] In different embodiments, changes in the neutralizer pump are limited in frequency. Preferably, adjustment limits are set at a maximum of 1 per 15 min and sequential adjustments in the same direction should not exceed 8. For example, after 8 total adjustments or a change of 50% or 100%, the pump could be suspended for an amount of time (e.g., 2 or 4 hours) and alarm could be triggered. If such a situation is encountered, it is advantageous to trigger an alarm to alert an operator. Other limits, such as maximum pump output may also be implemented. It should be appreciated that it is within the scope of the invention to cause any number of adjustments in any direction without limitation. Such limits are applied as determined by the operator.

[0049] FIG. 3 illustrates an embodiment of the invention as method 300 for controlling the introduction of caustic agent(s) into the system driven by the chloride ion concentration signal. Box 302 represents the measuring device or analyzer that provides information related to the chloride ion concentration of the dew point water. The analyzer (e.g., controller or operator) determines whether the chloride ion concentration is within an optimum range (50 to 100 ppm in this example) as shown in box 304. If the chloride ion concentration is within the predetermined optimum range, the logic follows the Yes path and continues measuring and analyzing. If the chloride ion concentration is not within this range, the method includes determining whether the chloride ion concentration is below 50 ppm, as represented by box 306, or above 100 ppm, as represented by box 308. If the chloride ion concentration is below 50 ppm, the method includes decreasing the caustic pump by, for example, 20%, as shown by box 310. If the chloride ion concentration is above 100 ppm, the method includes increasing the caustic pump by, for example, 20%, as shown by box 312.

[0050] It should be appreciated that a suitable or optimal chloride ion concentration range should be determined for each individual system. The optimum range for one system may vary considerably from that for another system. It is within the concept of the invention to cover any possible optimum chloride ion concentration range.

[0051] In different embodiments, changes in the caustic pump are limited in frequency. Preferably, adjustment limits are set at a maximum of 1 per 30 min and sequential adjustments in the same direction should not exceed 4. For example, after 4 total adjustments or a change of 50% or 100%, the pump could be suspended for an amount of time (e.g., 2 or 4 hours) and alarm could be triggered. If such a situation is encountered, it is advantageous to trigger an alarm to alert an operator. Other limits, such as maximum pump output or maximum sodium contribution to the system may also be implemented. It should be appreciated that it is within the scope of the invention to cause any number of adjustments in any direction without limitation. Such limits are applied as determined by the operator.

[0052] FIG. 4 illustrates an embodiment of the invention as method 400 for controlling the introduction of filming inhibitors into the system driven by the iron ion concentration signal. Other metallurgy, such as monel, titanium, brass, etc. may be used in some systems. In these cases, rather than an iron ion concentration signal, the appropriate metal ion (e.g., copper, nickel, zinc, etc.) concentration signal would be detected and analyzed. Box 402 represents the measuring device or analyzer that provides information related to the iron ion concentration of the accumulator boot water. The analyzer (e.g., controller or operator) determines whether the iron ion concentration is within an optimum range (0.05 to 1.0 ppm in this example) as shown in box 404. If the iron ion concentration is within the predetermined optimum range, the logic follows the Yes path and continues measuring and analyzing. If the iron ion concentration is not within this range, the method includes determining whether the iron ion concentration is below 0.05 ppm, as represented by box 406, or above 1.0 ppm, as represented by box 408. If the iron ion concentration is below 0.05 ppm, the method includes decreasing the filming inhibitor (i.e., filmer) pump by, for example, 5%, as shown by box 410. If the iron ion concentration is above 1.0 ppm, the method includes increasing the filmer pump by, for example, 5%, as shown by box 412.

[0053] Metal ions commonly exist in two or more oxidation states. For example, iron exists in Fe.sup.2+ and Fe.sup.3+ as well being present in soluble states (ionic and fine particulate), insoluble states (i.e., filterable), etc. Analysis and control of metal ions includes measurement or prediction of any combination (or all) of such permutations present in the system.

[0054] In different embodiments, changes in the filming inhibitor pump are limited in frequency. Preferably, adjustment limits are set at a maximum of 1 per 30 min and sequential adjustments in the same direction should not exceed 4. For example, after 4 total adjustments or a change of 50% or 100%, the pump could be suspended for an amount of time (e.g., 2 or 4 hours) and alarm could be triggered. If such a situation is encountered, it is advantageous to trigger an alarm to alert an operator. Other limits, such as maximum pump output may also be implemented. It should be appreciated that it is within the scope of the invention to cause any number of adjustments in any direction without limitation. Such limits are applied as determined by the operator.

[0055] FIG. 5 depicts an embodiment of the invention as method 500 for controlling the override of the introduction of neutralizer(s), caustic agent(s), and filmers into the system driven by the corrosion rates derived from one or more corrosion probes or other corrosion rate sensing device at any point in the system. Most crude units use electrical resistance-type corrosion probes located at the inlet and/or the outlet of the overhead heat exchangers. Although any type of corrosion-sensing device is contemplated, the above-mentioned type is preferred.

[0056] Box 502 represents the one or more corrosion probes that provide information related to the corrosion rates in the system. The analyzer (e.g., controller or operator) determines whether the corrosion rate is greater than a predetermined rate (25 mpy in this example) as shown in box 504. The actionable corrosion rate is typically determined on a case-by-case basis by a skilled artisan and is dependent on a multitude of system factors. If the corrosion rate is less than a predetermined acceptable rate, the logic follows the No path and continues measuring and analyzing. If the corrosion rate is above the predetermined acceptable rate, the method includes overriding all other programming and triggering an alarm, as shown by box 506. In alternative embodiments, rather than an override other programming could be modified as determined by an operator or controller. In this example, the override includes increasing the neutralizer, caustic agent, and filmer pump rates by, for example 20%, as shown by box 508. In other embodiments, the pump rates are changed individually as determined by an operator or controller.

[0057] Although the corrosion probes (e.g., electrical resistance corrosion probes, linear polarization probes, and/or any other suitable method for determining metal loss) may be placed at any convenient location in the system, preferably they are placed in historically reliable locations in the system. In addition, if, for example, 2 overrides are activated over a 12 hr period, a reliability check is typically initiated to ensure that the corrosion probes are operating properly. If such a situation is encountered, it is advantageous to trigger an alarm to alert an operator. Other limits, such as maximum pump output may also be implemented. It should be appreciated that it is within the scope of the invention to cause any number of adjustments in any direction without limitation. Such limits are applied as determined by the operator.

[0058] The foregoing may be better understood by reference to the following examples, which are intended for illustrative purposes and are not intended to limit the scope of the invention.

Example 1

[0059] An exemplary embodiment of the invention would consist of a cluster of on-line analyzers in an explosion-proof box receiving a sample of water from a dew point water-sampling device. Data generated by these analyzers would be appropriately conditioned to send a control signal to various process chemical injection pumps. A Programmable Logic Controller (PLC) programmed by a skilled artisan would convert the raw data into pump control signals. A typical system would include one or more of the following components: chloride analyzer; iron analyzer; corrosion rate monitoring device; conductivity; pH meter; dew point water sample device; Class I, Div II explosion proof enclosure; PLC capable of multiple inputs/outputs; logic programming to convert chloride, pH, and iron data into pump speed control; and wireless or hard-wired connections from PLC to pumps.

Example 2

[0060] This instant invention would provide improvement in control for each of three test parameters of chloride ion concentration, pH, and iron ion concentration. Of these three, chloride is usually the most damaging if not properly controlled. The graph in FIG. 6 demonstrates how the invention would be capable of improving the control of chloride ion concentration (the dotted line indicates optimum concentration). A similar concept of better control through the method of the invention will apply to pH, iron ion concentration, and other system parameters ultimately resulting in corrosion rates reduced from previous levels and extending equipment run length.

[0061] FIG. 6 shows a number of spikes of chloride concentration above the upper control limit from actual data from a crude unit. Chloride spikes are damaging to equipment and an ex post facto examination of the data will reveal increased corrosion and fouling during these episodes. Such spikes are more frequent and damaging when the crude slate is switched to a challenging or opportunity crude. Increased chloride ion concentration usually occurs with a concomitant increase in corrosion of the processing equipment and subsequent fouling due to deposition of corrosion byproducts. The section of the graph in FIG. 6 labeled Implement Control demonstrates how the method of the invention would be used to stabilize chloride ion concentration when more frequent data is available to minimize (or eliminate) disruptions.

Example 3

[0062] The graph of FIG. 7 illustrates pH and chloride ion concentration values tracked over time for an actual crude unit (the dotted lines indicate optimum concentrations). It can be seen that a drop in the pH value usually accompanies upward spikes for chloride ion concentration. Such drops in pH typically result in increased corrosion and subsequent fouling (due to corrosion byproducts) of the heat exchanging equipment. The section of the graph labeled Implement Control demonstrates how the method of the invention would be used stabilize chloride ion concentration and pH, thus reducing corrosion and fouling in the system. Smoothing variation of the incoming chloride values allows for tighter pH control and more stable and predictable chemical usage.

[0063] It should be understood that various changes and modifications to the presently preferred embodiments described herein will be apparent to those skilled in the art. Such changes and modifications can be made without departing from the spirit and scope of the invention and without diminishing its intended advantages. It is therefore intended that such changes and modifications be covered by the appended claims.