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Evaluation method of oil-soluble scale inhibitor and tester

An evaluation method and test device technology, applied in the direction of measuring devices, instruments, scientific instruments, etc., can solve the problems of less dirt generation, less effective medium circulation, and difficulty in maintaining stable system pressure, so as to increase the area and reduce fouling The effect of reducing the amount of dirt, simplifying the way of generating dirt, and increasing the amount of dirt generated

Inactive Publication Date: 2011-08-17
洛阳康润石油化工科技开发有限公司
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AI Technical Summary

Problems solved by technology

This method can better simulate the flow state of materials under actual working conditions, but it has two obvious defects: one is that the evaluation process is under normal pressure, which is only suitable for high boiling point media such as catalytic oil slurry, and has poor adaptability; The second is that the beginning and end of the test are the stages with the largest temperature fluctuations. Taking the temperature difference between the inlet and outlet of the fouling test tube as the evaluation standard at this time, it is difficult to guarantee the accuracy of the test data.
Its shortcomings: first, the dirt is distributed in the dirt generation pipe and the dirt collection pipe, which makes the test process complicated; second, the screen is set in the dirt generation pipe, which is easy to cause system blockage, so it is not suitable for testing asphaltenes and Medium with high colloid content (such as atmospheric residue, vacuum residue, etc.), and the dirt obtained by filtering through the screen is very different from the scale deposited on the wall of industrial equipment; the third is the test process The medium circulating between the dirt generation pipe and the dirt collection pipe is only the part stored between the two, and it is impossible to replenish new medium from the raw material tank. The effective circulation of the medium is small, and for some media with low boiling point or low coking tendency , the amount of dirt generated is too small, which affects the accuracy of the results; fourth, the invention does not have special pressure regulating facilities, and it is difficult to maintain a stable system pressure; The test temperature has a greater influence
However, this method uses the capillary as the main body of the flow and fouling of the sample, which has great disadvantages.
The adsorption effect of the capillary is very strong. If the sample is an organic medium, the organic matter adsorbed on the capillary wall is difficult to desorb, and will quickly polymerize and scale in the high-temperature test environment, blocking the capillary; is also very difficult; therefore, the method is not suitable for testing the fouling tendency of highly viscous media and organic media at high temperatures

Method used

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  • Evaluation method of oil-soluble scale inhibitor and tester
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  • Evaluation method of oil-soluble scale inhibitor and tester

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] The performance of the two slurry scale inhibitors was evaluated by simulating the operating conditions of the catalytic oil slurry at the bottom of the catalytic fractionation tower.

[0036] The test raw material is catalytic cracking oil slurry, which is a heavy test raw material that is prone to coking / fouling, and its properties are shown in Figure 4 .

[0037] (a), blank test:

[0038]Select the circular cross-sectional area between the rod fouling test tube and the electric heating rod: the flow area of ​​the connecting pipeline = 5.0: 1.0, weigh the total weight of the clean and dry dirt test tube 11 and the electric heating rod 12, and then connect them properly to the evaluation device. Add 2Kg of catalytic oil slurry into raw material tank 3, heat up to 110°C, and keep this temperature constant. In the washing oil bottle 5, add about account for the sherwood oil of its volume 80%. Close valves 8, 21 and 22, open valves 7, 9, 14, 18, 19 and 20, and turn o...

Embodiment 2

[0046] Simulate the operating conditions of the diesel hydrogenation raw material heat exchanger, and evaluate the diesel hydrogenation scale inhibitor C.

[0047] The diesel oil used in the test is a mixture of straight-run diesel oil:catalyzed diesel oil=1:1, which is a medium-quality test raw material with a small coking / fouling tendency, and its properties are shown in Figure 5 .

[0048] (c), blank test:

[0049] Select the annular cross-sectional area between the fouling test tube and the electric heating rod: the flow area=5.0: 1.0 of the connecting pipeline, weigh the total weight of the clean and dry dirt test tube 11 and the electric heating rod 12, and then properly connect it to the evaluation device. In raw material tank 3, add 2Kg mixed diesel oil, the temperature of raw material tank is kept on 60 ℃. In the washing oil bottle 5, add about account for the sherwood oil of its volume 80%. Close valves 8, 21, and 22, open valves 7, 9, 14, 18, 19, and 20, and tu...

Embodiment 3

[0055] Simulate the operating conditions of the coking gasoline hydrogenation raw material heat exchanger, and evaluate the gasoline hydrogenation antiscalant D.

[0056] The coking gasoline used in the test is a light test material with high coking / fouling ability, its properties are shown in Image 6 .

[0057] (e), blank test:

[0058] Select the annular cross-sectional area between the fouling test tube and the electric heating rod: the flow area=5.0: 1.0 of the connecting pipeline, weigh the total weight of the clean and dry dirt test tube 11 and the electric heating rod 12, and then properly connect it to the evaluation device. Add 2Kg of coker gasoline in raw material tank 3, the temperature of raw material tank is kept on 30 ℃. In the washing oil bottle 5, add about account for the sherwood oil of its volume 80%. Close valves 8, 21, and 22, open valves 7, 9, 14, 18, 19, and 20, and turn on the metering pump 6. When coked gasoline flows out from the return port of t...

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Abstract

The invention provides an evaluation method of an oil-soluble scale inhibitor, comprising the steps of: firstly pre-heating a test raw material and keeping the temperature at a constant value; leading the test raw material to pass through an annular space between an electric heating bar and a scale test tube at a relatively low flow speed, heating up and scaling; adjusting and stabilizing the temperature of the scale test tube by means of temperature cascade control of the electric heating bar and the scale test tube outlet; adjusting and maintaining the pressure of a scale generating part by a constant pressure valve; finally performing cycle test for the flow of returning to the original pot after being cooled, wherein the scale deposition amounts at beginning and end of blank test and agent added test are used as the evaluation standard. The method has the characteristics of easy implementation, small process parameter fluctuation, strong practicability to test raw materials, good simulation of real use working conditions of oil-soluble scale inhibitor, accurate evaluation result, and safe and reliable test procedure. Simultaneously, the flow of the tester is simplified, the volume of the tester is reduced, the constant process parameters are ensured during the evaluation procedure, and the adaptability of the tester to different raw materials is widened.

Description

technical field [0001] The invention belongs to the technical field of petrochemical industry, and mainly relates to a dynamic evaluation method and a test device for the performance of an oil-soluble scale inhibitor. Background technique [0002] Scale inhibitors, also known as antiscalants, antiscalants, and antiscorch agents, are a type of chemical additives commonly used in the petrochemical industry to inhibit and slow down the scaling tendency in processing equipment and prolong the smooth operation period of equipment. [0003] The petrochemical process is a continuous large-scale production process, and long-term operation has become one of the important indicators to measure its technical level. Due to the high temperature in the processing process, and the processing medium contains some impurities and coking precursors, these substances will gradually accumulate or deposit in parts with high temperature and low flow rate, causing scaling of equipment, affecting he...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G01N5/00
Inventor 王晓丽李昕苗伟
Owner 洛阳康润石油化工科技开发有限公司
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