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Comprehensive utilization method of styrene tar

A technology of styrene and p-styrene, applied in the field of comprehensive utilization of styrene tar, can solve problems such as a large number of hazardous wastes, lack of related systems, etc., and achieve the effect of resource utilization

Active Publication Date: 2021-03-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Although the above-mentioned prior art has done relevant research on the utilization of styrene, the remaining substances after extraction have not been properly disposed of, and a large amount of hazardous waste is still generated, and for the comprehensive utilization of styrene tar, there is still a lack of relevant systematic research in the prior art

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  • Comprehensive utilization method of styrene tar
  • Comprehensive utilization method of styrene tar

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] 700g of styrene tar, 100g of sodium hydroxide, 100g of water, and 100g of carbon tetrachloride were mixed, washed with alkali, washed with water, and separated to obtain an oil phase. The oil phase was distilled at 330°C under normal pressure to obtain the gas phase. The gas phase is cooled and separated to obtain the solvent, styrene and its derivatives, and the liquid phase obtained by distillation of the oil phase is cracked and fractionated at 380°C under normal pressure to obtain the gas phase. Styrene and its derivatives are obtained after the gas phase is cooled down. The liquid phase obtained by cracking and fractional distillation is hydrotreated at 400°C under a pressure of 8.0 MPa, and the obtained hydrotreated liquid phase is distilled at a temperature of 260°C under a pressure of -0.1 MPa to obtain a gas phase. The gas phase is cooled to obtain tar resin, and the liquid phase obtained by distillation is rich in valuable components (such as stilbene).

Embodiment 2

[0055] 700g of styrene tar, 100g of potassium hydroxide, 100g of water, and 100g of carbon tetrachloride were mixed, washed with alkali, washed with water, and separated to obtain an oil phase. The oil phase was distilled at 330°C under normal pressure to obtain the gas phase. The gas phase is cooled and separated to obtain the solvent, styrene and its derivatives, and the liquid phase obtained by distillation of the oil phase is cracked and fractionated at 380°C under normal pressure to obtain the gas phase. Styrene and its derivatives are obtained after the gas phase is cooled down. The liquid phase obtained by cracking and fractional distillation is hydrotreated at 400°C under a pressure of 8.0 MPa, and the obtained hydrotreated liquid phase is distilled at a temperature of 260°C under a pressure of -0.1 MPa to obtain a gas phase. The gas phase is cooled to obtain tar resin, and the liquid phase obtained by distillation is rich in valuable components (such as stilbene).

Embodiment 3

[0057] 700g of styrene tar, 100g of calcium hydroxide, 100g of water, and 100g of carbon tetrachloride were mixed, washed with alkali, washed with water, and separated to obtain an oil phase. The oil phase was distilled at 330°C under normal pressure to obtain the gas phase. The gas phase is cooled and separated to obtain the solvent, styrene and its derivatives, and the liquid phase obtained by distillation of the oil phase is cracked and fractionated at 380°C under normal pressure to obtain the gas phase. Styrene and its derivatives are obtained after the gas phase is cooled down. The liquid phase obtained by cracking and fractional distillation is hydrotreated at 400°C under a pressure of 8.0 MPa, and the obtained hydrotreated liquid phase is distilled at a temperature of 260°C under a pressure of -0.1 MPa to obtain a gas phase. The gas phase is cooled to obtain tar resin, and the liquid phase obtained by distillation is rich in valuable components (such as stilbene).

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Abstract

The invention discloses a method for comprehensively utilizing styrene tar, and belongs to the field of petrochemical production. The technical defect that in the prior art, styrene tar cannot be comprehensively utilized is overcome. Styrene tar is produced by pyrolysis gasoline extraction or ethylbenzene dehydrogenation process, and the comprehensive utilization method comprises the following steps: firstly, pretreating the styrene tar, and collecting an oil phase; distilling the oil phase to obtain a gas phase I and a liquid phase I, and separating the gas phase I to obtain styrene and derivatives; cracking and fractionating the liquid phase I to obtain a gas phase II and a liquid phase II, and cooling the gas phase II to obtain styrene and derivatives; and finally, subjecting the liquidphase II to hydrofining to obtain a liquid phase III, distilling the liquid phase III to obtain a gas phase III and a liquid phase IV rich in valuable components, and generating tar resin after the gas phase III is cooled. The valuable components in the styrene tar are extracted in batches, so that the overall resource of the styrene tar is realized, and clean production can be realized.

Description

technical field [0001] The invention belongs to the field of petrochemical production, and in particular relates to a method for comprehensive utilization of styrene tar. Background technique [0002] The annual generation of tar hazardous waste accounts for about 20% of the total petrochemical refining industry hazardous waste. However, styrene will be produced in the ethylbenzene dehydrogenation process and pyrolysis gasoline extraction of petrochemical refining and chemical enterprises. At present, the research reports on the comprehensive utilization of styrene tar in the existing technology are as follows: [0003] Using styrene tar as fuel to burn or produce fuel, the "General Rules for Identification Standards for Solid Waste" (GB 34330-2017) stipulates that this disposal method is still managed as solid waste, and this method is strictly prohibited if you do not have the qualification for hazardous waste disposal; [0004] Styrene tar is used as some paint additives...

Claims

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Application Information

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IPC IPC(8): C10G67/10
CPCC10G67/10
Inventor 张海房师平张志远张宏哲郭磊刘政伟林笑雨
Owner CHINA PETROLEUM & CHEM CORP