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Prepn and application of alkyl aryl sulfonate

A technology of alkyl aryl sulfonate and alkyl benzene sulfonic acid, applied in the preparation of sulfonate and other directions, can solve the problems of high viscosity of raw material oil, troublesome process, complicated product composition, etc., to simplify the operation process, improve the Application performance, dynamic ultra-low interfacial tension stabilization effect

Inactive Publication Date: 2004-04-07
大庆油田有限责任公司勘探开发研究院 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the composition of petroleum sulfonate produced from crude oil distillate oil is complex, the equivalent distribution is wide, and the performance of sulfonate is not easy to control
In particular, the molecular structure of some components of sulfonate is similar to the molecular structure of certain components in the displaced oil, so it can be used for product application and related technical processing, such as mine scheme design, numerical simulation research, oil displacement process The determination and control of certain parameters (interfacial tension, adsorption capacity of different chemical agents, etc.), and the admission of relevant materials... have brought a lot of trouble
In addition, the content of sulfonated substances in crude oil fractions is low, so no matter what process is used to produce petroleum sulfonates, solvent extraction technology must be used to reduce the content of unsulfonated oil in the product and increase the content of effective active substances. Bring troubles on the process and increase the cost and power consumption to the production
[0008] 2. A large number of field tests and laboratory studies have shown that whether it is petroleum sulfonate or synthetic alkylaryl sulfonate, the process of forming an ultra-low interfacial tension between the oil displacement agent formulated with it and the displaced oil ( time) is long, so that when the residual oil in the formation contacts with the displacement agent, the ultra-low interfacial tension (10 -3 mN / m order of magnitude), is taken away by the oil-displacing agent and becomes the mobile phase, affecting the oil-displacement efficiency of the oil-displacing agent
[0009] 3. The surfactant-alkali binary system and surfactant-alkali-polymer ternary system formulated with the above-mentioned sulfonate can form ultra-low interfacial tension (10 -3 mN / m order of magnitude), but then the interfacial tension rises rapidly, so that the residual oil that becomes the mobile phase is trapped again and remains underground, which affects the oil displacement efficiency of the oil displacement agent.
[0011] Second, the process conditions
[0012] 1. At present, the production of petroleum sulfonates and many alkylaryl sulfonates (especially heavy alkylbenzene sulfonates) mostly adopts continuous membrane sulfonation. Due to the high viscosity of the raw material oil, it is often necessary to add some Organic solvents, some or all of these solvents will remain in the product, complicating the composition of the product and increasing the production cost of the product
[0013] 2. Membrane continuous sulfonation, with gas SO 3 is the sulfonating agent, SO 3 It reacts violently with alkylaromatics, and the depth of sulfonation is difficult to control
[0014] 3. Production of petroleum sulfonate and heavy alkylbenzene sulfonate by membrane sulfonation is easy to coke

Method used

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  • Prepn and application of alkyl aryl sulfonate
  • Prepn and application of alkyl aryl sulfonate
  • Prepn and application of alkyl aryl sulfonate

Examples

Experimental program
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Effect test

Embodiment 1

[0038] Mix dodecylbenzene and heavy alkylbenzene in a weight ratio of 3:7, and the spectrogram features after mixing are as follows: figure 1 shown. Sulfonation process such as figure 2 shown. The mixed alkylbenzenes are sent from the storage tank 1 to the enamel reaction kettle 5 through the feed pump 8 . Nicotinic acid enters the reaction kettle 5 from the reaction tank 2 through the nicotinic acid filter 7 . The volume of the reaction kettle is 10 tons, and the ratio of acid to hydrocarbon is 1.1:1. Since sulfonation is an exothermic reaction, the reactants are pumped into the tube-and-tube heat exchanger 6 by the circulation pump 9 to take away the heat. Control the adding speed of oleum so that the temperature in the reactor is around 50°C. Feeding finished, continue to react for half an hour. Then add 15% water of the total weight of the material into the reactor 5 from the head tank 4 through the flow meter, circulate and stir at 60°C for half an hour for hydroly...

Embodiment 2

[0040] Dodecylbenzene and heavy alkylbenzene are mixed at a weight ratio of 2:8, and the weight ratio of oleum to alkylbenzene is 1:1. The spectral characteristics of the raw oil are given by Figure 5 shown. Other conditions and operation method are identical with embodiment 1, obtain product 2#.

Embodiment 3

[0042] The cut material of heavy alkyl benzene is taken, and the spectral features are shown in Figure 6. The weight ratio of oleum to alkylbenzene is 1.2:1. Other conditions and operation method are identical with embodiment 1, obtain product 3#.

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Abstract

The preparation process of alkyl aryl sulfonate includes the following main steps: adding C8-C26 straight chain alkylbenzene in 0-50 wt% to heavy alkylbenzene of average molecular weight of 310-370; sulfonation reaction of mixed alkylbenzene and fuming sulfuric acid in the weight ratio of 1 to 0.3-3 inside a sulfonation reactor, with the adding speed of fuming sulfuric acid being controlled to result in reaction temperature of 40-55 deg.c adding water in the amount of 5-25 % of total material weight through stirring at 30-80 deg.c; for 0.2-3 hr and stagnation to balance for 0.5-5 hr; and neutralizing the ractant mixture to pH 8-9 with 10-40% concentration NaOH solution. The alkyl aryl sulfonate is applied in tertiary oil extraction to compound oil displacing agent and may form stable superlow interface tension area in relatively low and wide alkali concentration range and relatively side surfactant concentration range.

Description

technical field [0001] The invention relates to a surfactant for oil field flooding, in particular to a preparation method of alkyl aryl sulfonate. [0002] The present invention also relates to the application of the above-mentioned alkylaryl sulfonate in tertiary oil recovery. Background technique [0003] Petroleum is an important resource of energy and chemical raw materials in my country. Since oil is naturally occurring and non-renewable, the quality of oil development is critical. [0004] At present, oil field development still adopts primary oil recovery and secondary oil recovery of water flooding. Applying the above oil recovery method, only 20-40% of the original reserves of the formation can be recovered, and 60% or more of the crude oil remains underground. In order to extract the residual oil in the ground, people have studied many tertiary oil recovery methods, among which the fastest developing speed and the best application prospect should be the surfact...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C303/32
Inventor 陈惠琴廖广志常加彬韩培慧杨振宇周宇
Owner 大庆油田有限责任公司勘探开发研究院
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