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Sulfur trioxide gas jet sulfonation process and device for bisalkyl benzene

A technology of heavy alkylbenzene and gas injection, which is applied in chemical/physical/physicochemical nozzle reactors, sulfonic acid preparation, organic chemistry, etc. It can solve problems such as difficult sulfonation, long residence time, and increased production costs. Achieve the effects of convenient operation and maintenance, stable product quality, and low equipment investment

Active Publication Date: 2008-10-22
中轻化工绍兴有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] (1) The upper part of the membrane sulfonation reactor is easy to coke, which affects the uniform distribution of the liquid film on the inner wall of the membrane sulfonation reactor, thus making the quality of the sulfonation product unstable, especially in the ability to reduce the crude oil / water interfacial tension.
On the one hand, this is because the composition of heavy alkylbenzenes is relatively complex, and the sulfonation activity of different compositions is quite different, such as: dialkylbenzene, polyalkylbenzene and other substances are difficult to sulfonate, indane, tetralin and alkylnaphthalene It is very easy to sulfonate; on the other hand, because the temperature of the liquid film in the membrane sulfonation reactor reaches the peak at the upper part of the membrane sulfonation reactor, some of the easily sulfonated components in the heavy alkylbenzene have undergone side effects such as sulfonation and oxidation. reaction, even carbonization and coking
In addition, the residence time of the material in the membrane sulfonation reactor is relatively long
[0008] (2) The viscosity of heavy alkylbenzene and its sulfonated products is relatively high, and in SO 3 The liquid film in the lower half of the gas membrane sulfonation reactor is too thick, which affects the sulfonation rate and product quality
On the one hand, it affects the service life of the membrane sulfonation reactor, on the other hand, it increases the number of unqualified products and increases the production cost
[0010] Also, SO 3 The gas membrane sulfonation reactor also has disadvantages such as complex structure, high requirements for equipment processing, manufacturing precision and installation precision, high investment costs, small operating flexibility, strict process conditions, and unsuitable for frequent start-up and shutdown.

Method used

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  • Sulfur trioxide gas jet sulfonation process and device for bisalkyl benzene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Example 1: Sulfonation of heavy alkylbenzenes

[0027] SO 3 The gas jet sulfonation reactor is composed of a nozzle and a reactor body. The nozzle is composed of a gas nozzle 3, a liquid distribution chamber 4, an atomizing nozzle 5, a heavy alkylbenzene inlet 1 and a mixed gas inlet 2, and the gas nozzle 3 Connected with the mixed gas inlet 2 and fixed on the top of the liquid distribution chamber 4, the heavy alkylbenzene inlet 1 is located at the lower part of the side of the liquid distributor 4, the atomizing nozzle 5 is fixed in the liquid distribution chamber 4, and the lower part of the gas nozzle 3 enters the atomizing nozzle 5, the top of the atomizing nozzle 5 is open, the position of the top of the atomizing nozzle 5 in the liquid distribution chamber 4 is higher than the position of the heavy alkylbenzene inlet 1 in the liquid distribution chamber 4, and the nozzle is fixed on the reactor body 7 The top and the lower part of the atomizing nozzle 5 enter th...

Embodiment 2

[0029] Example 2: Sulfonation of heavy alkylbenzenes

[0030] Heavy alkylbenzene (average molar mass: 345) was continuously converted from SO at a flow rate of 10kg / h at 45°C 3 The liquid phase inlet 1 of the gas jet sulfonation reactor enters the liquid distribution chamber 4, then overflows into the atomizing nozzle 5 through the top overflow of the atomizing nozzle 5, and then flows downward along the inner wall of the atomizing nozzle 5, SO 3 / air (volume ratio 6%) mixed gas by SO at 65°C 3 The gas phase inlet 2 of the gas injection sulfonation reactor enters the gas nozzle 3 and the gas velocity ejected from the gas nozzle 3 is 238m / s, SO 3 / heavy alkylbenzene feed molar ratio 1.2:1, SO 3 / Air mixed gas contacts with heavy alkyl benzene and is sprayed into reactor still body (7) from atomizing nozzle to react together, and the reaction time in reactor still body (7) is 3 seconds, and the sulfonated reaction product obtained and unreacted SO 3 / air mixture from SO 3 A...

Embodiment 3

[0031] Example 3: Sulfonation of heavy alkylbenzenes

[0032] Heavy alkylbenzene (average molar mass: 320) was continuously converted from SO at a flow rate of 9.5kg / h at 40°C 3 The liquid phase inlet 1 of the gas jet sulfonation reactor enters the liquid distribution chamber 4, then overflows into the atomizing nozzle 5 through the top overflow of the atomizing nozzle 5, and then flows downward along the inner wall of the atomizing nozzle 5, SO 3 / air (volume ratio 4%) mixed gas by SO at 60°C 3 The gas phase inlet 2 of the gas injection sulfonation reactor enters the gas nozzle 3 and the gas velocity ejected from the gas nozzle 3 is 193m / s, SO 3 / heavy alkylbenzene feed molar ratio 1.15:1, SO 3 / Air mixed gas contacts with heavy alkyl benzene and is sprayed into reactor still body (7) from atomizing nozzle to react together, and the reaction time in reactor still body (7) is 4 seconds, and the sulfonated reaction product obtained and unreacted SO 3 / air mixture from SO 3...

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Abstract

The invention discloses a sulfur trioxide gas injecting sulfonated technique of heavy alkylate benzene, which is characterized by the following: making composite gas of SO3 / air into gas sprayer of SO3 gas injecting sulfonated reactor between 55 and 75 deg.c with spraying speed at 50-300m / s; entering heavy alkylate benzene into the SO3 gas injecting sulfonated reactor between 5 and 50 deg.c; setting the molar rate of heavy alkylate benzene and SO3 at 1.0-1.5:1; reacting heavy alkylate benzene and composite gas of SO3 / air in the SO3 gas injecting sulfonated reactor for 1-5s; separating sulfonated product from non-reacted composite gas of SO3 / air; cooling liquid phase under 40-80deg.c for 30-120min; hydrolyzing; neutralizing to obtain the product.

Description

technical field [0001] The invention relates to a process and a device for preparing anionic surfactant heavy alkylbenzene sulfonate by sulfonating heavy alkylbenzene with sulfur trioxide gas. Background technique [0002] Heavy alkylbenzene (HAB) is a by-product in the process of producing alkylbenzene, a raw material for detergents. Alkylated naphthalene, diphenyl alkanes, and a small amount of polar substances, etc. Among them, indane, tetralin and alkylnaphthalene are very easy to sulfonate, but dialkylbenzene, polyalkylbenzene and other substances are difficult to sulfonate, and the sulfonated substances account for about 70% to 90%. [0003] Heavy alkylbenzene sulfonate has excellent properties of reducing crude oil / water interfacial tension, and is cheap and simple in preparation process. It is widely used in various fields of petroleum industry, such as: drilling, oil production, crude oil demulsification, refining, And it is the main surfactant used in three recov...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C303/06C07C309/62B01J19/26
Inventor 牛金平韩亚明韩向丽
Owner 中轻化工绍兴有限公司