Butadiene polymerization inhibitor used in separation system of ethylene unit

A separation system and ethylene plant technology, applied in distillation purification/separation, hydrocarbon purification/separation, hydrocarbons, etc., can solve the problems of not fully exerting the inhibitory effect of polymerization, not taking into account the catalytic effect of metal ions, etc. Excellent aggregation effect, easy to remove, reasonable formulation effect

Inactive Publication Date: 2011-07-20
LANZHOU DAYANG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, its application in the process of butadiene extraction process cannot give full play to the ideal polymerization inhibition effect due to the lack of consideration of factors such as the catalytic effect of metal ions on the polymerization reaction of butadiene.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Example 1 Under normal temperature and pressure, 300g petroleum mixed xylene, 570g No. 200 solvent naphtha, 30g 4-hydroxyl-2,2,6,6-tetramethylpiperidine nitroxide radical, 60g N-phenyl-α-naphthylamine, Add 20g of polyisobutylene bis-succinimide and 20g of N,N'-disalicylidene propylenediamine into the container under stirring conditions, and mix well to obtain the butadiene polymerization inhibitor.

Embodiment 2

[0024] Example 2 Mix 750g of petroleum xylene, 50g of 4-hydroxy-2,2,6,6-tetramethylpiperidine nitroxide radical, 100g of N-phenyl-α-naphthylamine, 60g of polyisobutylene dibutylene under normal temperature and pressure Diimide and 40 g of N, N'-di-salicylidene propylenediamine were added to the container in turn under stirring conditions, and mixed evenly to obtain the butadiene polymerization inhibitor.

Embodiment 3

[0025] Example 3 Under normal temperature and pressure, 760g of petroleum mixed xylene, 40g of 4-hydroxy-2,2,6,6-tetramethylpiperidine nitroxide, 90g of N-phenyl-α-naphthylamine, 80g of polyisobutylene dibutyl Diimide and 30 g of N, N'-di-salicylidene propylenediamine are added to the container in turn under stirring conditions, and mixed evenly to obtain the butadiene polymerization inhibitor.

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PUM

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Abstract

The invention relates to the field of chemical additives, in particular to a butadiene polymerization inhibitor used in a separation system of an ethylene unit. The butadiene polymerization inhibitor is prepared from the following raw materials in percent by weight: 2-10 percent of radical capturing agent, 2-15 percent of antioxidant, 2-10 percent of metal passivating agent, 60-92 percent of organic solvent and 2-15 percent of clean dispersing agent. The butadiene polymerization inhibitor is prepared by the steps of: firstly adding 60-92 percent of the organic solvent in a container at normaltemperature under normal pressure, sequentially adding 2-10 percent of the radical capturing agent, 2-15 percent of the antioxidant, 2-10 percent of the metal passivating agent and 2-15 percent of the clean dispersing agent under stirring, uniformly stirring and completely dissolving to form a liquid. In the butadiene polymerization inhibitor provided by the invention, besides the efficient radical capturing agent, a synergetic effect is also specially considered with respect to components compatibility, thus, the polymerization inhibition effect is improved and the consumption of the polymerization inhibitor is decreased. The butadiene polymerization inhibitor provided by the invention is applied to a depropanizing column and a reboiler of the ethylene unit, and can effectively prevent butadiene from polymerizing and depositing on the surfaces of the devices.

Description

technical field [0001] The invention relates to the field of chemical auxiliary agents, in particular to a butadiene polymerization inhibitor used in the separation system of an ethylene plant. Background technique [0002] In ethylene production, raw materials such as light hydrocarbons and naphtha are subjected to high-temperature cracking and quenching, and the cracked gas is then compressed, alkali washed and separated, and finally polymerized grade ethylene and propylene are obtained. The material in the depropanizer of the separation system is mainly C3~C9 hydrocarbons, of which the mole fraction of butadiene is about 20~40%. Butadiene is often polymerized due to factors such as heat, oxygen, and metal ions, resulting in The fouling of the depropanizer and reboiler not only reduces the heat transfer capacity of the heat exchanger in the device, increases energy consumption, but also greatly shortens the operating cycle of the equipment, and even leads to unplanned shut...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/167C07C7/20C07C7/05
Inventor 吴长安乔德超王元平
Owner LANZHOU DAYANG CHEM
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