JPH0794665B2 - Apparatus and method for automatically injecting neutralizing agent into overhead system of atmospheric distillation column - Google Patents

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for automatically injecting a neutralizing agent to be injected for corrosion prevention in the overhead system of an atmospheric distillation column used for oil refining in an oil refinery and an automatic injection method thereof. Regarding

[0002]

2. Description of the Related Art Oil refining in an oil refining plant is carried out by first distilling crude oil in an atmospheric distillation column to obtain each fraction having an appropriate boiling range, that is, LPG, light naphtha, heavy naphtha, kerosene, light oil, and residue. Divided into oil, and then treated in processes such as catalytic reforming, catalytic cracking, hydrodesulfurization, distillation under reduced pressure, and gas recovery equipment to produce various petroleum products.

Distillates having a relatively low boiling point (generally LPG, light naphtha, and heavy naphtha) and water (accumulator water) flow in the top of the atmospheric distillation column or in the overhead piping. ing. At this time, hydrogen chloride generated by partial decomposition of salts and the like contained in crude oil, further hydrogen sulfide, and carbon dioxide gas are simultaneously distilled out at the top of the column and dissolved in water condensed here to make the water acidic. For this reason, it is necessary to take measures to prevent corrosion in the flow path piping of the distillation column top system, etc. In general, ammonia or amine-based neutralizers are added to neutralize the acid and prevent film-forming corrosion. This is achieved by injecting the agent.

In particular, the injection of the neutralizing agent depends on the pH of the overhead fluid.
Is important to protect the metal of the equipment from acid corrosion and to facilitate and stabilize the formation of the iron sulfide coating and the anticorrosion coating with the coating anticorrosive agent. However, excessive injection of such a neutralizing agent, on the contrary, destabilizes the iron sulfide coating, the anticorrosive coating of the film-forming anticorrosive, and deteriorates the subsequent separation of hydrocarbon and water, resulting in a hydrocarbon product. This will cause an adverse effect of deteriorating the quality.

In order to inject such a neutralizing agent, conventionally, an operator generally measures the pH of accumulator water and carries out the injection operation with reference to the measured value.
By the way, in the neutralization curve of the acid component in the accumulator water and the neutralizing agent, the pH greatly changes at the equivalence point, and a slight excess or deficiency of the neutralizing agent causes a shift to acid or alkali. The appropriate range of injection volume is extremely narrow. Therefore, in the conventional injection of the neutralizing agent based on the pH measurement by the operator, it was extremely difficult to stably maintain the pH in the overhead system of the distillation column within an appropriate range.

[0006]

However, in the atmospheric distillation tower overhead system of the above-mentioned oil refining plant, the conventional neutralizing agent injection method is often incomplete in neutralization, which may prevent corrosion. It contained many problems.

That is, the crude oil that enters the atmospheric distillation column has certain properties such as different properties depending on the type of crude oil, salt handling in the crude oil, and the salt content in the oil depending on the degree of desalting in the previous stage. Is virtually impossible to keep. As a result, the amounts of hydrogen chloride, hydrogen sulfide, and carbon dioxide gas that emerge in the overhead system of the distillation column change, and the required amount of the neutralizing agent also changes accordingly. However, in the case of a fixed amount of injection that was simply set as in the past, an injection based on measurement by an operator, and an injection that only relied on experience, the pH in the distillation column overhead system was stabilized in an appropriate range. It was difficult to maintain.

Further, when the operator determines and operates the injection amount from the pH measurement of the accumulator water as in the conventional case, there is a time lag between the pH of the fluid flowing in the overhead system and the injection of the neutralizing agent. In addition, the injection operation of the infusate is behind,
There was also the problem that the processing of the entire system was unstable.

In particular, when such an atmospheric distillation column is regarded as a control target, the control system is one with a long history, but it has reached the present without any noticeable change. In consideration of the points, it is desired to take measures in accordance with the current situation, such as automation.

The present invention has been made in view of the above circumstances, and an injection amount of a neutralizing agent injected to prevent corrosion in the overhead system of an atmospheric distillation column used in an oil refining plant. Neutralizer for the overhead system of the atmospheric distillation column, which can be controlled appropriately and automatically in the required conditions according to the type and properties of crude oil, and various conditions in each plant part. It is intended to obtain an automatic injection device and an automatic injection method.

[0011]

In order to meet such a demand, the apparatus for automatically injecting a neutralizing agent into the atmospheric distillation column overhead system according to the present invention is an overhead system for an atmospheric distillation column in a petroleum refining process. Neutralizing agent for automatically injecting the neutralizing agent into the overhead system of the atmospheric distillation column in order to adjust and maintain the pH of the overhead system within a desired range in order to prevent corrosion in An injection line, a controller for controlling the injection of the neutralizing agent that controls the automatic injection amount of the neutralizing agent through this injection line, and p in the overhead system of the atmospheric distillation column.
PH detecting means for measuring and detecting the H value and sending the measured value to the controller, raw material information inputting means for sending the raw material information fed to the atmospheric distillation column to the controller, and the overhead system of the atmospheric distillation column The flow rate detection means for measuring and detecting the amount of product withdrawal and the amount of reflux obtained from the device and sending the measured values to the controller, the controller having the neutralization titration curve and pH selected by the information from the raw material information input means. The automatic injection amount of the neutralizing agent is calculated and determined according to the information from the detecting means and the flow rate detecting means, and the neutralizing agent injection amount is controlled.

The method for automatically injecting a neutralizing agent into the atmospheric distillation column overhead system according to the present invention is designed to prevent corrosion of the atmospheric pressure distillation column overhead system in a petroleum refining process. In order to adjust and maintain the pH within the desired range, it is equipped with a neutralizer injection line to the overhead system of the atmospheric distillation column and a controller for controlling the neutralizer injection that controls the automatic injection amount. PH value in the atmospheric distillation column overhead system by means, raw material information fed to the atmospheric distillation column by raw material information input means, product withdrawal amount from the atmospheric distillation column overhead system by flow rate detection means, The amount of reflux is sent to each controller, and the neutralization titration curve in the controller is selected by the information from the raw material information input means, and according to the neutralization titration curve and the information from the pH detection means and the flow rate detection means. Calculate and determine the automatic injection amount of the neutralizing agent And performs a neutralizing agent injection amount control.

Further, the apparatus for automatically injecting the neutralizing agent into the overhead system of the atmospheric distillation column according to the present invention is drained from a receiver for gas-liquid separating the fluid from the overhead system of the atmospheric distillation column in the petroleum refining process. The accumulator water flow rate detecting means for detecting the flow rate of accumulator water and sending the accumulator water flow rate information to the controller, and the receiver liquid level detecting means for detecting the liquid level of the receiver and sending the liquid level to the controller. The controller is configured to perform dead time compensation based on the receiver liquid level information obtained by the receiver liquid level detecting means.

Further, the method for automatically injecting a neutralizing agent into the atmospheric distillation column overhead system according to the present invention measures the flow rate of accumulator water discharged from the atmospheric pressure distillation column overhead system receiver in the oil refining process, From the accumulator water flow rate information detected by the flow rate detection means, the flow rate in the overhead system of the distillation column is ascertained, and the controller uses the receiver liquid level information detected by the receiver liquid level detection means to compensate for dead time. In consideration of time, the automatic injection amount of the neutralizing agent is calculated and determined, and the neutralizing agent injection amount is controlled.

[0015]

According to the present invention, the controller for automatically controlling the injection amount of the neutralizing agent into the overhead system of the atmospheric distillation column is automatically selected from the data table by the information from the raw material information input means. Neutralization titration curve against the neutralization titration curve according to the pH measurement value in the distillation column overhead system or accumulator water by the pH detection means and the flow rate information in the distillation column overhead system or accumulator water from the flow rate detection means The amount of neutralizer injection is controlled so that the pH within the appropriate range can be obtained by determining the gain in the controller that corresponds to the pH change rate in the controller and calculating and determining the automatic amount of neutralizer injection. Is performed. In addition, such an appropriate range is generally 5.5 to 6.5.

Further, according to the present invention, the flow rate detecting means detects flow rate information of the accumulator water discharged from the receiver of the overhead distillation column overhead system to grasp the flow rate at the distillation column overhead system, and The controller compensates the dead time based on the receiver liquid level information detected by the receiver liquid level detecting means, and the neutralizer is automatically injected in consideration of the dead time.

[0017]

1 and 2 show one embodiment of the apparatus for automatically injecting a neutralizing agent into the overhead system of an atmospheric distillation column and the method for automatically injecting a neutralizing agent according to the present invention. In the present embodiment, a case is described in which a crude oil is used as a liquid to be treated (raw material), and an oil refining plant is constituted by an atmospheric distillation column for separating naphtha, LPG, gasoline and the like, and equipment and devices associated therewith. To do.

First, in the petroleum refining plant generally designated by reference numeral 1 in FIG. 1, a crude oil supply line 2 for crude oil as a liquid to be treated (raw material) is at the bottom of an atmospheric distillation column 10. In addition,
In the figure, 3 is a heating furnace for heating the crude oil supplied into the atmospheric distillation column 10. Here, in the atmospheric distillation column 10, the distillate with the lowest boiling point is at the top of the column, the highest distillate is at the bottom of the column, and liquids with different boiling points are present in each intermediate stage, and these are withdrawn. As a result, a plurality of products can be obtained.

In the figure, numeral 4 designates a stripper arranged from the bottom of the distillation column 10 to the top of the distillation column 10 so as to be connected to each other through a circulation path from a plurality of stages, and the boiling points of the respective stages in the distillation column 10 are different. It is configured to extract a distillate and deliver heavy gas oil, light gas oil, and kerosene as products. In addition, although some of the products taken out as such are commercially available as they are, most of them are modified by appropriate accessory equipment,
It is marketed as a product through secondary processing such as decomposition, desulfurization, addition of additives, and compounding.

Further, in the figure, 5 is a circulation path attached to the middle part of the distillation column 10 and provided with a side reflux 6, and 7 is an overhead circulation system line attached to the top of the distillation column 10 and having a heat exchanger 7a. Is. Further, reference numeral 8 in the figure denotes a recovery system passage for discharging atmospheric residual oil from the bottom of the distillation column 10.

Numeral 11 indicates naphtha and L from the top of the distillation column 10.
In order to distill a low boiling point distillate containing PG and the like, it is an overhead line piping that is an overhead line extraction line, and this piping 11 is connected to a naphtha receiving tank receiver 13 via a heat exchanger 12, and is described above. It is configured to be fed with naphtha and the like.

In the receiver 13, the distillate from the top of the distillation tower 10 is gas-liquid separated, and the gas fraction is taken out as fuel gas or LPG through the upper extraction pipe 14 and at the same time as the liquid distillate. Minutes are the lower extraction pipe 1
After 5 years, it is taken out as naphtha. Further, the water accumulated at the bottom of the receiver 13 is configured to be drained through the drainage pipe 16 for accumulator water.

On the other hand, a part of the overhead pipe 11 is provided with an introduction line 17 for introducing a film-forming anticorrosive agent and a neutralizing agent on the downstream side thereof in order to prevent corrosion in the pipe 11. A neutralizer injection line 20 for injecting is attached. Here, in the figure, 21 is a neutralizing agent storage tank, and 22 is a fixed quantity injection pump for quantitatively feeding the neutralizing agent through the neutralizing agent injection line 20.

Reference numeral 30 denotes an atmospheric distillation column 10 having the above-mentioned structure.
And a signal system 30a that includes a controller that receives signals from various detectors attached to its auxiliary equipment and monitors the state thereof, and outputs the rotation speed output signal of the neutralizer dosing pump 22 and the like. The controller also functions as a control unit for the automatic injection of the neutralizing agent that is sent via

In the figure, 31 is a host computer which is a raw material information input means. The computer 31 detects and measures the characteristics (type, property) of crude oil attached to the crude oil supply line 2 to the atmospheric distillation column 10 and the like. The signal from the crude oil detector 32 for the purpose of inputting is supplied by the signal system 32a, and the raw material characteristic switching signal obtained thereby is sent to the controller 30 via the signal system 31a.

Reference numeral 33 denotes a pH detector as a pH detecting means attached to a part of the drainage pipe 16 for accumulator water from the receiver 13 to measure pH of the accumulator water flowing therein. The pH measurement value is also sent to the controller 30 via the signal system 33a.

Further, reference numeral 34 in the figure denotes an accumulator water flow meter (flow rate detecting means) which is provided in a part of the drainage pipe 16 of the accumulator water and measures the flow rate flowing in the pipe 16. Further, 35 is a flow meter for fuel gas (or LPG) (flow rate detecting means) provided in the upper extraction pipe 14 of the receiver 13 for measuring the flow rate flowing in the pipe 14, and 36 is provided in the lower extraction pipe 15 and the inside Flow meter for naphtha that measures the flow rate (flow rate detection means)
Is. The measured values of these flowmeters 34, 35, 36 are also sent to the controller 30 via the signal systems 34a, 35a, 36a.

Reference numeral 37 in the drawing is a liquid level gauge (receiver liquid level detecting means) provided on the side wall of the receiver 13 for measuring the receiver liquid level in the receiver 13, and the receiver liquid level based on this is also a signal system 37a. Is sent to the controller 30.

According to the present invention, the top of the atmospheric distillation column 10, the top pipe 11 and the corrosion prevention in the top system by the receiver 13 and the like connected to the pipe 11 for gas-liquid separation. In order to adjust the pH within an appropriate range and maintain that state, the controller 30 that also functions as a controller automatically injects the neutralizing agent while injecting the neutralizing agent automatically. The device has the following configuration.

This will be described in detail. In this automatic neutralizing agent injection device, as is clear from FIGS. 1 and 2, a state in which the injection amount of the neutralizing agent can be adjusted into the top pipe 11 of the distillation column 10 can be adjusted. 1. A neutralizer injection line 20 having a metering injection pump 22 for automatically injecting the solution, and a controller / combined controller 30 for controlling the automatic injection amount of the neutralizer by the neutralizer injection line 20 are provided. ing.

A controller 30 for controlling the injection of the neutralizing agent
Is a pH detection unit for measuring the pH of the fluid flowing through the overhead pipe 11 of the atmospheric distillation column 10 (in this embodiment, a gas-liquid separation capable of obtaining a value close to the pH value of the overhead system). PH value obtained by the pH detection unit 33) that measures the pH of the accumulator water discharged from the receiver 13 which is a container,
A column which is a product information obtained by measuring a raw material characteristic switching signal by a crude oil detector 32 and the like based on raw material information (crude oil type and property information), a withdrawal amount of the overhead product from the receiver 13 and a reflux amount to the distillation column 10. The flow rate in the top system pipe 11 (a value obtained by the accumulator water flow meter 34 in proportion to the flow rate measurement value of the accumulator water) is input.

Then, in the above-mentioned structure, the controller 30 for controlling the neutralizer injection based on these input information.
The pH value in the distillation column overhead system is maintained within a proper range (pH 5.5 to 6.5) by controlling the rotation of the fixed quantity injection pump 21 in the neutralizing agent injection line 20 by the above. You can

That is, the controller 30 controls this pH.
Based on pH information from the detection unit 33 and raw material information (crude oil type, property variation information) supplied to the atmospheric distillation column 10, and product information (product withdrawal amount and reflux amount or accumulator water flow rate), the neutralizing agent The automatic injection amount of is automatically controlled by a non-linear neutralization titration curve determined in advance by a desk test or the like. As a result, it is possible to stably maintain and manage the pH range effective for preventing corrosion in the overhead pipe 11 of the atmospheric distillation column 10 and separating accumulator water and naphtha.

Therefore, the iron sulfide coating can be stably formed in the overhead piping 11, and when a film-forming anticorrosive is also used, it is possible to maintain the anticorrosion effect in the pH range which maximizes the anticorrosion effect. It becomes an effective anticorrosion measure in the atmospheric distillation column overhead system. Furthermore, the pH of the above-mentioned overhead system
Since the area is an area where the separation of the accumulator water and naphtha is good, the quality of the overhead product can also be kept good.

Here, the controller 30 described above is configured to perform variable gain calculation, pH control, and injection amount control, as is apparent from FIGS. 2 and 3, based on the various measurement information described above. Has been done.

That is, (a) and (b) of FIG. 3 show the controller 3 according to the raw material information, that is, the type and properties of crude oil.
It is for explaining the variable gain calculation process of the operation output at 0. (A) of the same figure shows a non-linear neutralization titration curve represented by the relationship between pH and the neutralizing agent addition rate. As is clear from this figure, when the type and properties of the raw materials differ, the raw material A And raw material B have different characteristics. As described above, such a neutralization titration curve may be determined in advance by a desk test or the like, stored in a data table provided in the controller 30, and used appropriately according to the raw material characteristic switching signal.

By the way, as is clear from FIG. 3 (a) described above, the raw materials A and B have different required neutralizing agent addition rates and are neutralized, as is clear from the respective neutralization titration curves. The rate of pH change per agent addition is also different, and each may be selected as needed.

In such a neutralization titration curve characteristic shown in FIG. 3 (a), depending on where the pH measured value at the present time is compared with the target value, as shown in FIG. 3 (b). In addition, it is preferable to change the gain of the operation output in the controller 30 (variable gain). In other words, the gain characteristic of the controller 30 may be switched according to the type and property of the raw material.

Here, the operation output is obtained by the following equation. Operation output = K (gain) x {pH measurement value (current value) -p
H target value} The above-mentioned "{pH measured value-pH target value}" corresponds to the deviation.

The variable gain means that, for example, in the vicinity of the neutralization point (C2 or C4 region in the case of the raw material A in FIG. 3 (a), C2 or C4 region), the rate of change in pH per neutralizing agent is large, so the gain is small. It is equivalent to doing. In addition, in the region away from the neutralization point (C1, C3 or C5 region in the case of raw material A in (a) of FIG. 3), the rate of pH change per neutralizing agent addition is small, which is equivalent to increasing the gain To do. In addition, in FIG. 3B, the gain characteristic is approximated to a broken line (linearized).

When the gain is changed and the injection amount of the neutralizing agent is appropriately controlled by the controller 30 to a desired state in this way, the pH in the overhead pipe 11 of the atmospheric distillation column 10 is controlled within a proper range. It is possible to manage.

As described above, in this embodiment, the liquid level at the receiver 13 is measured, and the measured value signal is also sent to the controller 30. Based on this receiver liquid level, the so-called Smith method is used. By compensating for the dead time, the pH in the overhead system of the distillation column and the receiver 13
It is configured to correct the time delay with respect to the pH in the accumulator water via the.

That is, the residence time of the overhead fluid in the receiver 13 is obtained by measuring the receiver liquid level as described above, and the time difference is calculated by the dead time compensation. It becomes possible to appropriately and surely control pH in a required state by eliminating a time difference. Therefore, in this way, it is possible to avoid the conventional injection of the neutralizer as a follow-up operation, and there is an advantage that the process is stable.

The present invention is not limited to the structure of the above-described embodiment, and the shape, structure, etc. of each part including the automatic neutralizer injection device to the overhead system of the atmospheric distillation column 10 are appropriately modified. It goes without saying that it can be changed.

For example, the injection amount of the neutralizing agent in the neutralizing agent injecting line 20 is appropriately controlled by using the constant amount injecting pump 22 and changing the rotation speed of the controller 30. An electromagnetic flowmeter or the like is attached to the neutralizer injection line 20 to be supplied, and the measured value is fed back to the controller 30 as a feedback signal as exemplified by reference numeral 40 in FIG. 2 to perform feedback control. You may

By doing so, compared to the above-mentioned embodiment, the injection control of the neutralizing agent can be automatically performed with higher accuracy, the pH in the distillation column overhead system can be optimized, and the column overhead can be optimized. It can be effective in preventing corrosion in the system.

In the above-mentioned embodiment, the case where the present invention is applied to the system for injecting the neutralizing agent into the overhead system of the atmospheric distillation column 10 used in the petroleum refining process 1 has been described, but the present invention is not limited to this. Needless to say, it can be used as one of the measures for preventing corrosion in the distillation column overhead system used in various chemical plants. Furthermore, the atmospheric distillation column 1 in the above-mentioned embodiment
The auxiliary equipment to 0, the piping system, and the like are not limited to these, and appropriate modified examples can be considered.

[0048]

As described above, according to the apparatus and method for automatically injecting a neutralizing agent into the atmospheric distillation column overhead system according to the present invention, the neutralizing agent is automatically injected into the atmospheric distillation column overhead system. Neutralizer injection line for effective injection, a controller for controlling the neutralizer injection control that controls the automatic injection amount of the neutralizer by this injection line, and the pH value in the overhead system of the atmospheric distillation column. PH detecting means for measuring and detecting and sending the measured value to the controller,
Raw material information input means for sending raw material information sent to the atmospheric distillation column to the controller, and measuring and detecting the amount of product withdrawn and the amount of reflux obtained from the overhead system of the atmospheric distillation column and detecting the measured value And a flow rate detecting means for sending out the neutralizing agent according to the neutralization titration curve selected by the information from the raw material information inputting means and the information from the pH detecting means and the flow rate detecting means. Calculate quantity,
Since it was determined and configured to control the injection amount of the neutralizing agent, the pH of the overhead system should be adjusted appropriately in order to prevent corrosion in the overhead system of the distillation column, despite the simple and inexpensive configuration. It can be stably adjusted and maintained within the range.

Therefore, the iron sulfide coating on the overhead piping,
The film-forming anticorrosive film can always be kept stable, which is an effective anticorrosion means in the overhead distillation column overhead system.

As a result of being able to automate the injection of the neutralizing agent in this way, it is possible to respond swiftly even if there is a change in the type of crude oil or a change in process conditions, and the labor therefor can be greatly omitted. Furthermore, since the pH of the overhead system can be kept stable, there is an advantage that the quality of the overhead product can be maintained in good condition.

According to the apparatus and method for automatically injecting a neutralizing agent into the overhead system of the atmospheric distillation column according to the present invention, the fluid from the overhead system of the atmospheric distillation column is discharged from the receiver for gas-liquid separation. The accumulator water flow rate detecting means for detecting the flow rate of the accumulator water and sending the accumulator water flow rate information to the controller, and the receiver liquid level detecting means for detecting the liquid level of the receiver and sending the liquid level to the controller. Since the controller is configured to compensate the dead time by the receiver liquid level information obtained by the receiver liquid level detecting means, the pH is measured by accumulator water.
The pH control in the overhead system of the distillation column can be appropriately and reliably performed while compensating for the time delay.

[Brief description of drawings]

FIG. 1 is a schematic configuration diagram in a petroleum refining plant showing one embodiment of an apparatus for automatically injecting a neutralizing agent and a method for automatically injecting a neutralizing agent into the overhead system of an atmospheric distillation column according to the present invention.

FIG. 2 is a schematic diagram for explaining a schematic configuration of a controller used in the neutralizer automatic injection device that characterizes the present invention.

FIG. 3 is a characteristic diagram for explaining a calculation process of a variable gain of a controller operation output according to a raw material characteristic by the device of the present invention, (a) showing a relationship between pH and a neutralizing agent addition rate. A characteristic diagram, (b) is a characteristic diagram showing the relationship between pH and gain.

[Explanation of symbols]

1 Oil Refining Plant 2 Crude Oil Supply Line 3 Heating Furnace 4 Stripper 10 Atmospheric Pressure Distillation Tower 11 Overhead System Piping as Overhead System Extraction Line 12 Heat Exchanger 13 Receiver (Naphtha Receiving Tank) 14 Upper Extraction Piping 15 Lower Extraction Piping 16 Accumulator Piping for water drainage 17 Introducing line of film-forming anticorrosive agent 20 Neutralizing agent injection line 21 Neutralizing agent storage tank 22 Metering injection pump 30 Controller 31 High-end computer (raw material information input means) 32 for sending crude oil characteristic switching signal 32 Crude oil detection Container 33 pH detector for accumulator water (pH detecting means) 34 Flow meter for accumulator water (flow rate detecting means) 35 Flow meter for fuel gas (LPG) (flow rate detecting means) 36 Flow meter for naphtha (flow rate detecting means) 37 Receiver Liquid level meter (receiver liquid level detection means)

Claims (4)

[Claims] 1. An automatic injection device of a neutralizing agent for adjusting and maintaining the pH of the overhead system within a desired range in order to prevent corrosion in the overhead system of an atmospheric distillation column in a petroleum refining process. The neutralizer injection line for automatically injecting the neutralizer into the overhead system of the atmospheric distillation column, and controlling the automatic injection amount of the neutralizer by the neutralizer injection line A controller for controlling the injection of the neutralizing agent, a pH detecting means for measuring and detecting the pH value in the overhead system of the atmospheric distillation column, and sending the measured value to the controller, and a feed to the atmospheric distillation column. Raw material information input means for sending raw material information to the controller, flow rate detection for measuring and detecting product withdrawal amount and reflux amount obtained from the overhead system of the atmospheric distillation column, and sending the measured value to the controller Means for controlling the raw material information. The neutralizing agent automatic injection amount is automatically calculated and determined according to the neutralization titration curve selected by the information from the input means and the information from the pH detecting means and the flow rate detecting means. An automatic neutralizer injection device to the overhead system of an atmospheric distillation column, which is configured to control the injection amount of the neutralizer by an injection line. 2. A method for automatically injecting a neutralizing agent for adjusting and maintaining the pH of the overhead system in a desired range in order to prevent corrosion in the overhead system of an atmospheric distillation column in a petroleum refining process. A neutralizer injection line for automatically injecting a neutralizer into the overhead system of the atmospheric distillation column, and a neutralizer injection for controlling the automatic injection amount of the neutralizer by this injector injection line And a controller for controlling, for measuring and detecting the pH value in the overhead system of the atmospheric distillation column p
Measurement value by H detection means, raw material information fed to the atmospheric distillation column obtained by the raw material information input means, and product withdrawal amount and reflux amount obtained from the overhead system of the atmospheric distillation column are measured, The measured value by the flow rate detecting means to detect,
The neutralization titration curve is selected in the controller based on the information from the raw material information inputting means, and the neutralization titration curve and the information from the pH detecting means and the flow rate detecting means are sent according to the neutralizing titration curve. Automatic injection of a neutralizer into the atmospheric distillation column overhead system characterized by automatically calculating and determining the automatic injection amount of the neutralizer and controlling the injection amount of the neutralizer by the neutralizer injection line Method. 3. An automatic neutralizer injection device for adjusting and maintaining the pH of the overhead system in a desired range in order to prevent corrosion in the overhead system of an atmospheric distillation column in a petroleum refining process. The neutralizer injection line for automatically injecting the neutralizer into the overhead system of the atmospheric distillation column, and controlling the automatic injection amount of the neutralizer by the neutralizer injection line A controller for controlling the injection of the neutralizing agent, a pH detecting means for measuring and detecting the pH value in the overhead system of the atmospheric distillation column, and sending the measured value to the controller, and a feed to the atmospheric distillation column. The raw material information input means for sending the raw material information to the controller, and the flow rate information of the accumulator water discharged from the receiver for separating the fluid from the overhead system of the atmospheric distillation column into a gas-liquid separator are detected. Accumulator to send to the controller Water flow rate detection means and receiver liquid level detection means for detecting the liquid level of the receiver and sending the receiver liquid level to the controller, wherein the controller is the receiver liquid level by the receiver liquid level detection means. The dead time is compensated by the information, and the neutralizing agent automatic injection amount is determined according to the neutralization titration curve selected by the information from the raw material information input means and the information from the pH detection means and the flow rate detection means. Calculated automatically,
An apparatus for automatically injecting a neutralizing agent to the atmospheric distillation column overhead system, which is configured to determine and control the amount of the neutralizing agent injected by the neutralizing agent injecting line. 4. A method for automatically injecting a neutralizing agent for adjusting and maintaining the pH of the overhead system within a desired range in order to prevent corrosion in the overhead system of an atmospheric distillation column in a petroleum refining process. A neutralizer injection line for automatically injecting a neutralizer into the overhead system of the atmospheric distillation column, and a neutralizer injection for controlling the automatic injection amount of the neutralizer by this injector injection line And a controller for controlling, for measuring and detecting the pH value in the overhead system of the atmospheric distillation column p
Measured value by H detection means, raw material information to be fed to the atmospheric distillation column obtained by the raw material information input means, and measuring the flow rate of accumulator water drained from the receiver of the atmospheric distillation column overhead system, Accumulator water flow rate information by the flow rate detecting means for detecting, and the receiver liquid level detected by the receiver liquid level detecting means are respectively sent to the controller, and while performing dead time compensation in the controller by this receiver liquid level, A neutralization titration curve is selected in the controller based on the information from the raw material information input means, and an automatic injection amount of the neutralizing agent is determined according to the neutralization titration curve and the information from the pH detection means and the flow rate detection means. An atmospheric distillation column characterized by automatically calculating and determining and controlling the injection amount of the neutralizing agent by the neutralizing agent injection line. A method for automatically injecting a neutralizing agent into the overhead system.