阅读说明：本技术 一种废塑料与环烷烃共催化转化制备润滑油基础油的方法 (Method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cycloparaffin ) 是由 梁长海 陈霄 杜博文 李闯 于 2020-12-21 设计创作，主要内容包括：本发明公开了一种废塑料与环烷烃共催化转化制备润滑油基础油的方法,属于石油化工领域。即以强静电吸附法制备固体酸负载的贵金属催化剂,将废塑料与环烷烃共催化转化,成功的实现了废塑料催化氢解和环烷烃烷基化反应,其中环烷烃即充当溶剂,也部分参与烷基化反应,大大的提高了润滑油基础油收率。该过程解决了传统生产过程中工艺复杂,经济效益差,污染环境等问题,并且流程简单且节省投资,适用于工业生产。(The invention discloses a method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cycloparaffins, belonging to the field of petrochemical industry. Namely, a strong electrostatic adsorption method is used for preparing a solid acid-loaded noble metal catalyst, waste plastics and cycloalkane are subjected to co-catalytic conversion, the catalytic hydrogenolysis of the waste plastics and the cycloalkane alkylation reaction are successfully realized, the cycloalkane serves as a solvent and partially participates in the alkylation reaction, and the yield of the lubricating oil base oil is greatly improved. The process solves the problems of complex process, poor economic benefit, environmental pollution and the like in the traditional production process, has simple flow and saves investment, and is suitable for industrial production.)

1. A method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cyclane is characterized by comprising the following steps:

the loading capacity prepared by adopting a strong electrostatic adsorption method is 0.5-1.5 mu mol/m²The high-dispersion solid acid-loaded noble metal catalyst is obtained by coupling catalytic hydrogenolysis and alkylation in an autoclave type reactor at the reaction temperature of 200-400 ℃ and the reaction pressure of 0.5-5 MPa, and carrying out co-catalytic conversion on waste plastics and a naphthenic hydrocarbon solvent<3 to 95 wt.% C1 to C5 low carbon alkane gas, 87 to 95 wt.% C6 to C35 long chain cycloalkane liquids and waxes, and<10 wt.% plastic residue and catalyst; separating the obtained liquid product, recycling the naphthenic hydrocarbon solvent which does not participate in the reaction, and obtaining diesel oil and lubricating oil base oil after the produced long-chain naphthenic hydrocarbon liquid and wax are cut; the catalyst is separated from the plastic residue and recycled.

2. The method of claim 1 wherein the highly dispersed solid acid supported noble metal catalyst is Rh/Nb₂O₅、Pt/Nb₂O₅Rh/HZSM-5, Pt/HZSM-5 or Ru/SiO₂-Al₂O₃。

3. The method as claimed in claim 1 or 2, wherein the solid acid supported noble metal catalyst prepared by strong electrostatic adsorption method is prepared by using noble metal chloride and ammonia complex to be adsorbed on a solid acid carrier by electrostatic adsorption to obtain monolayer metal complex precursor distribution, and obtaining the highly dispersed solid acid supported noble metal catalyst after reduction.

4. The method according to claim 1 or 2, wherein the waste plastic is one or a mixture of two or more of low density polyethylene, high density polyethylene, polypropylene and polystyrene.

5. A method according to claim 3, wherein the waste plastics is one or a mixture of two or more of low density polyethylene, high density polyethylene, polypropylene and polystyrene.

6. The method according to claim 1, 2 or 5, wherein the cycloalkane solvent is one or a mixture of two or more of cyclohexane, decalin, perhydroanthracene, perhydroindene and perhydrophenanthrene.

7. The method according to claim 3, wherein the cycloalkane solvent is one or more selected from cyclohexane, decalin, perhydroanthracene, perhydroindene, and perhydrophenanthrene.

8. The method according to claim 4, wherein the cycloalkane solvent is one or more selected from cyclohexane, decalin, perhydroanthracene, perhydroindene, and perhydrophenanthrene.

Technical Field

The invention belongs to the technical field of petrochemical industry, and relates to a method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cycloparaffin.

Background

Plastics have become an integral part of our daily lives, enhancing the safety of our food and healthcare systems, the performance of textiles, the versatility of consumer electronics, and the energy efficiency of transportation. However, plastics bring convenience to people and also have the problem of environmental pollution. Over the past decades, the production of globally synthesized petroleum-based plastics has increased dramatically, approaching 3.6 million tons in 2018, with the production expected to double again within the next 20 years. However, about 40% of plastics are currently used only for a short period and are not recycled, most of these plastic wastes are chemically stable, degrade slowly naturally, and most of them are finally landfilled or incinerated, causing severe soil hardening and pollution of river and sea environments.

Aiming at the comprehensive utilization of waste plastics, the method mainly focuses on the following aspects: 1. the waste plastic can be fully utilized in the process of incineration, the treatment is simple, but the environment is greatly polluted and damaged, and a large amount of harmful substances such as aromatic hydrocarbon compounds, sulfides and heavy metal compounds can be generated in the incineration process. 2. Recycling, namely, directly processing and molding the recycled waste plastics after classified cleaning and regrinding. However, the recycled plastic produced by this process is not comparable to the original product in terms of strength, toughness, durability, etc., and the contamination from such "degraded recycling" is more difficult to control. Creating a higher challenge to economy. 3. Biodegradation, which means that biodegradable plastics such as starch base and the like are degraded under the combined action of light, heat, water, oxygen, microorganisms, insects and the like when the biodegradable plastics are exposed to external environmental conditions, the reaction time of the degradation method is long, and the application range of the degradation method is relatively narrow, and mainly the biodegradable plastics are degradable plastics. 4. The catalytic thermal cracking is to catalytically crack the waste plastics under the action of a catalyst to obtain fuel oil and chemical products, namely, the high molecular bond is broken under the catalytic action to obtain gas, gasoline, diesel oil, heavy oil and the like, but the process has higher reaction temperature (400 ℃), lower service life and activity of the catalyst, serious coking in a reactor, complex composition of the obtained gas-liquid hydrocarbon mixture, lower value and relatively higher energy consumption. Recently, Susannah L.Scott et al, the American scientist, reported that catalysts with platinum supported on gamma-alumina convert various macromolecular chemicals such as polyethylene to low molecular weight, high value products via tandem catalytic conversion without the addition of solvents or molecular hydrogen. However, during this reaction, the catalyst is prone to coking and heavy metal poisoning. The national laboratory of attorney, department of energy, usa, reports a new catalytic hydrogenolysis process, which uses a catalyst consisting of nano platinum and strontium titanate to break polyethylene carbon-carbon chains at a milder temperature and pressure to obtain highly uniform liquid hydrocarbons, so that polyolefin waste can become a recycling economic raw material. However, in this reaction process, the noble metal loading amount is high, the catalyst amount is large, and the yield of the liquid hydrocarbon compound is desired to be further improved.

In addition, with the rapid development of the industries such as machinery, automobiles, metallurgy, electric power, national defense and the like, the demand of high-grade lubricating oil is increasing in various countries, and the quality requirement of the lubricating oil is also increasing. The improvement of the quality of the lubricating oil must depend on the improvement of the quality of the base oil to ensure the competitiveness in the high-end lubricating oil market. Therefore, it is a hot spot and a difficult point of the current research to find a catalyst which can effectively hydrogenize the waste plastics and effectively utilize the long paraffin free radicals and the cycloparaffin in the waste plastics for alkylation, and provide an effective way for preparing the lubricant base oil by effectively utilizing the waste plastics.

Disclosure of Invention

The invention provides a method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cycloparaffins, aiming at the defects of serious environmental pollution, harsh reaction conditions, poor product quality, low efficiency and the like in the comprehensive utilization of the waste plastics, the invention creatively uses a strong electrostatic adsorption method to prepare a solid acid-loaded noble metal catalyst, co-catalytic conversion of the waste plastics and the cycloparaffins is carried out, the catalytic hydrogenolysis of the waste plastics and the alkylation reaction of the cycloparaffins are successfully realized, the cycloparaffins serve as a solvent and partially participate in the alkylation reaction, the yield of the lubricating oil base oil is greatly improved, the problems of complex process, poor economic benefit, environmental pollution and the like in the traditional production process are solved, and the process is simple and the investment.

The technical scheme of the invention is as follows:

a method for preparing lubricating oil base oil by co-catalytic conversion of waste plastics and cyclane comprises the following steps:

the loading capacity prepared by adopting a strong electrostatic adsorption method is 0.5-1.5 mu mol/m²The high-dispersion solid acid-loaded noble metal catalyst is obtained by coupling catalytic hydrogenolysis and alkylation in an autoclave type reactor at the reaction temperature of 200-400 ℃ and the reaction pressure of 0.5-5 MPa, and carrying out co-catalytic conversion on waste plastics and a naphthenic hydrocarbon solvent<3 to 95 wt.% C1 to C5 low carbon alkane gas, 87 to 95 wt.% C6 to C35 long chain cycloalkane liquids and waxes, and<10 wt.% plastic residue and catalyst; separating the obtained liquid product, recycling the naphthenic hydrocarbon solvent which does not participate in the reaction, and obtaining diesel oil and lubricating oil base oil after the produced long-chain naphthenic hydrocarbon liquid and wax are cut; the catalyst is separated from the plastic residue and recycled.

The high-dispersion solid acid-supported noble metal catalyst is Rh/Nb₂O₅、Pt/Nb₂O₅Rh/HZSM-5, Pt/HZSM-5 or Ru/SiO₂-Al₂O₃。

The solid acid supported noble metal catalyst prepared by adopting the strong electrostatic adsorption method is a noble metal chloride and ammonia complex which are electrostatically adsorbed on a solid acid carrier to obtain single-layer metal complex precursor distribution, and the high-dispersion solid acid supported noble metal catalyst is obtained after reduction.

The waste plastics are one or more than two of low-density polyethylene, high-density polyethylene, polypropylene and polystyrene.

The cycloalkane solvent is one or more of cyclohexane, decalin, perhydroanthracene, perhydroindene and perhydrophenanthrene.

The invention has the beneficial effects that: the method has simple process, is green and environment-friendly, is easy for industrial production, and more importantly realizes the recycling and comprehensive utilization of the waste plastics and changes waste into valuable.

Drawings

FIG. 1 is Rh/Nb₂O₅X-ray diffraction pattern of the catalyst.

FIG. 2 is a process flow diagram for preparing lube base oil by co-catalytic conversion of waste plastics and cycloalkanes;

in the figure: 1, an autoclave reactor; 2 a solvent recovery tower; 3 a rectifying tower.

Detailed Description

The following further describes a specific embodiment of the present invention with reference to the drawings and technical solutions.

Example 1 Rh/Nb₂O₅Preparation of the catalyst

Firstly, adopting a primary wet method to measure Nb₂O₅The zero charge point of (A) was about 2.5, and 500mL of 200 mg. multidot.L was prepared^-1[ (NH) of₄)₃Rh]⁶⁺In order to achieve the highest Rh ion adsorption, the pH of the solution is adjusted to 10 with ammonia, and Nb₂O₅The precursors were mixed and shaken in a shaker for 1 h. Filtering after the end, determining the Rh ion content of the filtrate by utilizing ICP (inductively coupled plasma), and calculating the Rh content on the adsorption precursor to be 1.5 mu mol/m by combining the Rh ion content of the initial ammonium hexachlororhodate solution². The solid is dried at room temperature overnight and then reduced at 400 ℃ in hydrogen atmosphere to prepare Rh/Nb₂O₅The X-ray diffraction pattern of the catalyst is shown in figure 1.

EXAMPLE 2 preparation of Pt/HZSM-5 catalyst

Firstly, the zero charge point of HZSM-5 is measured to be about 3.0 by adopting a incipient wetness method, 500mL of 100 mg.L is prepared^-1[ (NH) of₄)₃Pt]²⁺In order to achieve the highest Pt ion adsorption, the pH of the solution was adjusted to 9.5, mixed with HZSM-5 precursor and shaken in a shaker for 1 h. Filtering after the end, measuring the Pt ion content of the filtrate by utilizing ICP (inductively coupled plasma), and calculating the Pt content on the adsorption precursor to be 1.0 mu mol/m by combining the Pt ion content of the initial ammonium chloroplatinate solution². The solid was dried at room temperature overnight and then reduced at 400 ℃ in a hydrogen atmosphere to produce a Pt/HZSM-5 catalyst.

Example 3 Rh/Nb in autoclave reactor₂O₅Catalysis from co-catalytic conversion of waste plastics and decalin derived from low density polyethylene

For prepared Rh/Nb in autoclave reactor₂O₅The catalyst was subjected to a co-catalytic conversion activity test of waste plastics derived from low-density polyethylene and decalin. Balance0.05g of catalyst, 1.0g of waste plastic and 20mL of decahydronaphthalene are continuously stirred and reacted for 36h at the temperature of 300 ℃ and the hydrogen pressure of 2.0MPa, after cooling and temperature reduction, the catalyst is separated, and 2.0% of C1-C5 low-carbon alkane gas, 95% of C6-C35 long-chain naphthenic hydrocarbon liquid and wax and 3% of plastic residues are obtained. And (3) separating the obtained liquid product, and respectively carrying out chromatography-mass spectrometer and flight time mass spectrometry to obtain the lubricating oil base oil with the yield of 90%, wherein the specific process flow is shown in figure 2.

Example 4 Rh/Nb in autoclave reactor₂O₅Catalysis from co-catalytic conversion of waste plastics and decalin from polypropylene

For prepared Rh/Nb in autoclave reactor₂O₅The catalyst was subjected to a test of co-catalytic conversion activity of waste plastic derived from polypropylene and decalin. 0.05g of catalyst, 1.0g of waste plastic and 20mL of decalin solvent are weighed, continuously stirred and reacted for 24 hours at 350 ℃ and under the hydrogen pressure of 3.0MPa, and after cooling and temperature reduction, the catalyst is separated to obtain 3.0% of C1-C5 low-carbon alkane gas, 90% of C6-C35 long-chain naphthenic hydrocarbon liquid and wax and 7% of plastic residues. And separating the obtained liquid product, and respectively carrying out chromatography-mass spectrometer and flight time mass spectrometry to obtain the lubricating oil base oil with the yield of 93%.

Example 5 Co-catalytic conversion of waste plastics derived from high density polyethylene and perhydroanthracene with Pt/HZSM-5 in an autoclave reactor

The prepared Pt/HZSM-5 catalyst was subjected to a co-catalytic conversion activity test of waste plastics derived from high density polyethylene and perhydroanthracene in an autoclave reactor. 0.5g of catalyst, 10g of waste plastic and 200mL of perhydroanthracene solvent are weighed, continuously stirred and reacted for 48 hours at 400 ℃ and under the hydrogen pressure of 1.0MPa, and after cooling and temperature reduction, the catalyst is separated to obtain 3.0 percent of C1-C5 low-carbon alkane gas, 92 percent of C6-C35 long-chain naphthenic hydrocarbon liquid and wax and 5 percent of plastic residues. Separating the obtained liquid product, recycling the unreacted solvent, and respectively carrying out chromatography-mass spectrometer and flight time mass spectrometry on the residual long-chain naphthenic hydrocarbon liquid to find that the lubricating oil base oil is obtained with the yield of 96%.

Example 6 in an autoclaveRu/SiO in a reactor₂-Al₂O₃Catalysis from co-catalytic conversion of waste plastics and perhydrophenanthrene derived from polystyrene

Subjecting the prepared Ru/SiO to reaction in an autoclave reactor₂-Al₂O₃The catalyst was subjected to a co-catalytic conversion activity test of waste plastics derived from polystyrene and perhydrophenanthrene. Weighing 1.0g of catalyst, 10g of waste plastic and 200mL of perhydrophenanthrene solvent, continuously stirring and reacting for 36h at 250 ℃ and 0.5MPa of hydrogen pressure, cooling and cooling, and separating the catalyst to obtain 1.0% of C1-C5 low-carbon alkane gas, 95% of C6-C35 long-chain naphthenic hydrocarbon liquid and wax, and 4% of plastic residues. Separating the obtained liquid product, recycling the unreacted solvent, and respectively carrying out chromatography-mass spectrometer and flight time mass spectrometry on the residual long-chain naphthenic hydrocarbon liquid to obtain the lubricating oil base oil with the yield of 95%.