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Improved regeneration technique for decolorizing and deodorizing waste tyre oil and method for preparing diesel fuel thereof

A waste tire and improved technology, applied in chemical instruments and methods, refined hydrocarbon oil, petroleum industry, etc., can solve the problems of low oil output efficiency, corrosiveness, poor power, etc., and achieve increased contact reaction area and stimulation. The effect of disappearing sexual odor and speeding up reaction time

Inactive Publication Date: 2010-03-03
刘新宇
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The poor catalytic effect leads to the incomplete interruption of the carbon-carbon long chain, and the product color can only reach maroon or light red. The long-chain structure has poor stability, and it will be oxidized to dark red after 1-2 days of storage. It has the effect of mixing with existing fossil diesel. Poor; the product has a pungent taste, is corrosive, and has poor power
Secondly, the carbon chain is not completely broken, and the distillation of macromolecules requires a higher temperature. The distillation is not complete at the same temperature, resulting in low oil extraction efficiency.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

specific Embodiment approach 1

[0030] a. Mix the following raw materials according to the weight ratio

[0031] 100 parts of waste tire oil;

[0032] 1 part of catalytic solution;

[0033] 1 core catalyst;

[0034] React for 2 hours after mixing;

[0035] Described catalytic liquid is hydrogen peroxide (H 2 o 2 ), the concentration is 20%;

[0036] The core catalyst is Fe 2 o 3 、Al 2 o 3 a mixture of the two;

[0037] b. Add the anhydrous substance in the upper layer after the mixed reaction in step a to the reactor, then add 1 part by weight of the core catalyst, heat, and collect 94.0 parts by weight of the distillate below the normal pressure of 365 °C;

[0038] c, add 1 weight part concentrated sulfuric acid (concentration 90%) to the distillate in the b step, stir for 20 minutes, add 2 weight parts of white clay to precipitate after 20 minutes, filter with less than 200 mesh filter press or filter sand, get light yellow 91.6 parts by weight of primary diesel oil;

[0039] d. Add 0.05 parts ...

specific Embodiment approach 2

[0040] a. Mix the following raw materials according to the weight ratio

[0041] 100 parts of waste tire oil;

[0042] 8 parts of catalytic solution;

[0043] 5 parts of core catalyst;

[0044] React for 5 hours after mixing;

[0045] Described catalytic liquid is hydrogen peroxide (H 2 o 2 ), concentration 30%;

[0046] The core catalyst is SiO 2 , MnO 2 a mixture of the two;

[0047] b. Add the anhydrous substance in the upper layer after the mixed reaction in step a to the reactor, then add 5 parts by weight of the core catalyst, heat, and collect 94.5 parts by weight of the distillate below 0.09MPA negative pressure at 280°C-300°C;

[0048] c. Add 6 parts by weight of vitriol oil (concentration 95%) to the distillate in the b step, stir for 30 minutes, add 6 parts by weight of white clay to precipitate for 30 minutes, filter with less than 100 mesh filter press or filter sand to obtain light yellow 92.4 parts by weight of primary diesel oil;

[0049] d. Add 0.1 par...

specific Embodiment approach 3

[0050] a. Mix the following raw materials according to the weight ratio

[0051] 100 parts of waste tire oil;

[0052] 5 parts of catalytic solution;

[0053] 3.5 parts of core catalyst;

[0054] React for 3.5 hours after mixing;

[0055] Described catalytic liquid is hydrogen peroxide (H 2 o 2 ), concentration 28%;

[0056] The core catalyst is Fe 2 o 3 , SiO 2 a mixture of the two;

[0057] b. Add the anhydrous substance in the upper layer after the mixed reaction in step a to the reactor, then add 2.6 parts by weight of the core catalyst, heat, and collect 94.7 parts by weight of distillate below 365°C under normal pressure;

[0058] c, add 2 parts by weight of concentrated sulfuric acid (concentration 97%) to the distillate in step b, stir for 25 minutes, add 4 parts by weight of white clay to precipitate for 25 minutes, filter with less than 100 mesh filter press or filter sand to get light yellow 92.8 parts by weight of primary diesel oil;

[0059] d. Add 0.08...

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PUM

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Abstract

The invention discloses an improved regeneration technique for decolorizing and deodorizing waste tyre oil and a method for preparing diesel fuel thereof, which comprise the following steps: a, mixing 100 parts of waste tire oil, 1-8 parts of hydrogen peroxide and 1-5 parts of core catalyst, and reacting for 2-5 hours after mixing, wherein the core catalyst is the mixture of at least two components selected from Fe2O3, Al2O3, SiO2 and MnO2; b, adding anhydrous materials at the upper layer after reaction in the step a to a reaction kettle, adding the core catalyst, heating, and extracting distillate at 365 DEG C under the normal pressure or at 280-300 DEG C under 0.09 MPA negative pressure; c, adding concentrated sulphuric acid to the distillate obtained in the step b, stirring, adding argil for precipitating, and filtering by a filter press or filter sands to obtain pale yellow primary diesel oil; and d, preparing the primary diesel oil obtained in the step c to a desired type of diesel oil. Compared with the prior art, the invention adopts a more improved reaction principle, and the product oil prepared by the method has the advantages of pale yellow color, stable quality, favorable evaporability and power performance, low temperature flow property, non-corrosiveness, and the like; furthermore, the product oil has the advantage of preparing the diesel oil by mixing with the traditional fossil diesel oil or other fuel diesel oils according to any proportion.

Description

1. Technical field [0001] The invention relates to a method for preparing and blending diesel oil by using waste tire oil for decolorization and deodorization. 2. Background technology [0002] As my country's dependence on foreign crude oil continues to increase, the supply gap of diesel oil in my country has also increased. Multi-channel development of existing energy, regeneration of existing resources, and increasing energy utilization have become one of the important factors affecting the development of the national economy. one. [0003] For a long time, waste tires seem to be synonymous with "black pollution". How to effectively utilize waste tires and prevent pollution has been valued by countries all over the world. Together with the United States and the European Union, my country is at the forefront of waste tire production in the world. Statistics show that the number of scrapped tires in my country has increased from 32 million in 2000 to 150 million in 2007, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G55/06C10G11/04C10G27/00C10L1/10C10L1/04B01J23/889B01J23/745B01J23/34
Inventor 刘新宇
Owner 刘新宇
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