Method for refining waste paperboard pyrolytic oil

A refining method and pyrolysis oil technology, which is applied in the petroleum industry, hydrocarbon oil treatment, hydrotreating process, etc., can solve the problems affecting the next start of the engine, affecting the atomization effect of the emulsion, and affecting the stability of the emulsion. Achieve the effect of low equipment requirements, stable properties, reduced acidity and corrosion

Inactive Publication Date: 2013-01-02
SOUTHEAST UNIV
View PDF4 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since crude oil contains some macromolecular polymers, these components have an adverse effect on the combustion of bio-oil
On the one hand, these components will affect the atomization effect of the emulsion, and block the nozzle in severe cases. On the other hand, after a period of combustion, more carbon deposits will be generated on the nozzle, which will affect the next start of the engine
In addition, these components have a high density, and they are easy to settle and precipitate when emulsified with diesel oil, which affects the stability of the emulsion

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for refining waste paperboard pyrolytic oil
  • Method for refining waste paperboard pyrolytic oil
  • Method for refining waste paperboard pyrolytic oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Slowly add 30ml of ether solution into 10ml of waste cardboard pyrolysis crude oil, after mixing for a period of time, let the mixture stand for 20min, and the pyrolysis crude oil component is divided into upper and lower layers. Take the upper layer mixture and carry out rotary evaporation to recover the solvent ether, and obtain the ether soluble fraction.

[0024] SiO with a mass ratio of 4:6 2 / TiO 2 Dissolved in ethanol and mixed for 1h, dried to obtain SiO 2 / TiO 2 catalyst. La with a molar ratio of 5% 2 o 3 Soluble in 0.8mol / L H 2 SO 4 solution, according to 10mL La 3+ -H 2 SO 4 Impregnate at a ratio of 5g catalyst, mix for 1h, bake at 450°C for 6h after drying, and obtain solid superacid SO after cooling 4 2- / TiO 2 -SiO 2 -La 3+ .

[0025] Add 20 g of ether solubles, 5 g of ethanol (analytically pure) and 1 g of solid acid catalyst into a three-neck round bottom flask, and react for 3 hours at a temperature of 70 ° C. After the reaction, the mi...

Embodiment 2

[0028] Slowly add 30ml of ether solution into 10ml of waste cardboard pyrolysis crude oil, after mixing for a period of time, let the mixture stand for 20min, and the pyrolysis crude oil component is divided into upper and lower layers. Take the upper layer mixture and carry out rotary evaporation to recover the solvent ether, and obtain the ether soluble fraction.

[0029] SiO with a mass ratio of 4:6 2 / TiO 2 Dissolved in ethanol and mixed for 1h, dried to obtain SiO 2 / TiO 2 catalyst. La with a molar ratio of 7% 2 o 3 Soluble in 0.8mol / L H 2 SO 4 solution, according to 10mL La 3+ -H 2 SO 4 Impregnate at a ratio of 5g catalyst, mix for 1h, bake at 450°C for 6h after drying, and obtain solid superacid SO after cooling 4 2- / TiO 2 -SiO 2 -La 3+ .

[0030] Add 20 g of ether solubles, 5 g of ethanol (analytically pure) and 1 g of solid acid catalyst into a three-neck round bottom flask, and react for 3 hours at a temperature of 70 ° C. After the reaction, the mi...

Embodiment 3

[0033] Slowly add 30ml of ether solution into 10ml of waste cardboard pyrolysis crude oil, after mixing for a period of time, let the mixture stand for 20min, and the pyrolysis crude oil component is divided into upper and lower layers. Take the upper layer mixture and carry out rotary evaporation to recover the solvent ether, and obtain the ether soluble fraction.

[0034] SiO with a mass ratio of 4:6 2 / TiO 2 Dissolved in ethanol and mixed for 1h, dried to obtain SiO 2 / TiO 2 catalyst. La with a molar ratio of 5% 2 o 3 Soluble in 0.8mol / L H 2 SO 4solution, according to 10mL La 3+ -H 2 SO 4 Impregnate at a ratio of 5g catalyst, mix for 1h, bake at 450°C for 6h after drying, and obtain solid superacid SO after cooling 4 2- / TiO 2 -SiO 2 -La 3+ .

[0035] Add 20 g of ether solubles, 5 g of ethanol (analytically pure) and 1 g of solid acid catalyst into a three-neck round bottom flask, and react for 3 hours at a temperature of 70 ° C. After the reaction, the mix...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention provides a method for refining waste paperboard pyrolytic oil (waste paperboard oil for short), which comprises the following steps: 1. carrying out component extraction separation on waste paperboard oil by using ether as an extraction solvent, thereby obtaining an ether soluble substance; 2. impregnating in a sulfuric acid solution to support La<3+> by using SiO2/TiO2 as a catalyst support, thereby obtaining a solid superstrong acid catalyst; 3. carrying out alcoholization reaction on the ether soluble substance, ethanol and solid superstrong acid catalyst in a reactor under enhanced pressure or atmospheric pressure, thereby obtaining a primary refined waste paperboard pyrolytic oil (primary refined oil for short); and 4. adding the primary refined oil and a vulcanized hydrogenation catalyst into a high-pressure reaction kettle, introducing hydrogen with a certain pressure, and heating to a certain temperature to carrying out hydrogenation reaction, thereby obtaining the refined waste paperboard pyrolytic oil (refined oil for short). The refined oil prepared by the method has high stability, and can be directly used in a diesel engine after being emulsified with diesel, thereby implementing high-quality utilization of waste paperboard pyrolytic oil.

Description

technical field [0001] The invention relates to the field of high-value utilization of solid waste, in particular to a method for refining waste cardboard pyrolysis oil. Background technique [0002] As China gradually shakes off poverty and becomes richer, people are producing more and more garbage in their daily lives. my country is one of the countries with the largest amount of garbage discharge in the world, accounting for more than 1 / 4 of the world's annual garbage output, and about 40% of the country's total garbage has not been treated centrally, forming a situation of "garbage surrounding the city". situation. Therefore, the reasonable disposal of solid waste has become an important issue that people have to face. [0003] As an effective method for treating solid waste, pyrolysis has the advantages of high product utilization value, simple pyrolysis device, and high energy conversion rate, and has wider application prospects than traditional treatment methods. Ho...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/14
Inventor 仲兆平丁宽余露露刘志超
Owner SOUTHEAST UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products