Method for preparing petroleum sulfonate oil displacement agent
A technology of petroleum sulfonate and oil displacing agent, which is applied in the field of preparation of petroleum sulfonate oil displacing agent, can solve the problems of increasing equipment investment, increasing energy consumption and production cost, etc., and achieves strong adaptability and product quality control. Smooth, simple production process results
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0019] The optimized molecular weight is about 510, and the carbon number distribution is at C 22 ~C 36 The mixed raw materials are heated and stirred evenly, and then poured into a tank reactor for sulfonation reaction. The jacket temperature of the reactor is controlled to be 65-70° C., and 7% SO3 (volume) is passed through to carry out the sulfonation reaction. Stop reaction when acid value reaches 65mgNaOH / g, adopt 35% (weight) NaOH solution to carry out neutralization, control neutralization terminal pH value to be 8-11. The test results of raw materials and products are shown in Table 1 and Table 2.
[0020] Mixed raw material composition analysis Table 1
[0021] name
Saturated hydrocarbon%
Aromatics %
Non-hydrocarbon %
mixed ingredients
55.95
39.25
3.95
0.85
[0022] Interfacial tension test table 2
[0023] Daqing No. 4 Oil Production Plant Xing No. 5 Middle School Combined Station Contai...
Embodiment 2
[0027] The optimized molecular weight is about 538, and the carbon number is distributed in C 22 ~C 36 The mixed raw materials are heated and stirred evenly, and then enter the membrane reactor for sulfonation reaction. Its reaction temperature is controlled to be 55-60 DEG C, and the SO3 (volume) that feeds gas concentration 4.5% carries out sulfonation reaction, and gas volume is 2.5m3 / h. After the reaction, the acid value of the sulfonic acid is 70 mgNaOH / g, and it is neutralized with a 35% (weight) NaOH solution, and the pH value at the end point of the neutralization is controlled at 8-11. The test results of raw materials and products are shown in Table 3 and Table 4.
[0028] Mixed raw material composition analysis Table 3
[0029] name
Saturated hydrocarbon%
Aromatics %
Non-hydrocarbon %
mixed ingredients
51.52
43.7
4.43
0.35
[0030] Interfacial tension test table 4
[0031] Daqing No. 4 ...
Embodiment 3
[0035] The product of embodiment 2 is configured into a sodium carbonate weak base ternary system by adopting the crude oil and sewage of the third oil production plant in Daqing, and the detection results are as follows:
[0036] Daqing No. 3 Oil Production Plant North 2nd West Combined Station Containing Polymerized Sewage Daqing No. 3 Plant Crude Oil Daqing Refining
[0037] Chemical company salt-resistant polymer 1200ppm
[0038]
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com