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Step-by-step solid-phase synthesis of micro-mesoporous calcium aluminate catalysts

A micro-mesoporous calcium aluminate, solid-phase synthesis technology, applied in chemical instruments and methods, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve problems such as small surface area, large specific gravity, and lack of pore structure

Active Publication Date: 2022-02-08
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, at present, calcium aluminate catalysts are mainly synthesized by high-temperature solid-phase, lack of pore structure, small surface area, and large specificity, so it is difficult to maximize the advantages of basic catalysts in inhibiting coke formation and enhancing olefin selectivity, and become the first choice for industrial application of calcium aluminate catalysts bottleneck

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] Example 1, the nano-calcium carbonate powder and aluminum sol are ground and mixed with a ball mill according to the calcium oxide: alumina-based stoichiometry 12:7 to form a calcium-aluminum mixed powder, and a mixture of 2% modified starch and asphalt powder is used Add 15% water to make a binder melt, then add it to the mixer and mix it with the calcium-aluminum mixed powder in a semi-dry method to bond and granulate; the first step is to react in the rotary kiln reactor at an outlet temperature of 500°C 1. The conditions of residence time of 2.5 hours make the binder pyrolyze and generate coke. In the second step, the internal heating rotary kiln reactor is heated to an outlet temperature of 1200°C and the residence time of 3.5 hours is used to decompose calcium carbonate, calcium oxide and alumina. A solid-phase reaction occurs to generate calcium aluminate microsphere powder. In the third step, in the fluidized bed gasifier installed at the outlet of the rotary kil...

Embodiment 2

[0018] Example 2, limestone powder, alumina powder and superfine calcium aluminate powder are ground and mixed with a ball mill according to the calcium oxide: alumina base stoichiometry 12:6 to form a calcium-aluminum mixed powder. Add 10% water to the mixture to form a lignin adhesive melt, then add it to the mixer and mix it with calcium-aluminum mixed powder in a semi-dry method to bond and make particles; the first step is to react at the outlet of the rotary kiln reactor The temperature is 500°C and the residence time is 3.5 hours to make the binder pyrolyze and generate coke. In the second step, the internal heating rotary kiln reactor is heated to an outlet temperature of 1100°C and the residence time is 2.5 hours to decompose the limestone, calcium oxide and Alumina undergoes a solid-phase reaction to form calcium aluminate microspheres. In the third step, segmented air is used to burn the pyrolysis coke in calcium aluminate in the moving bed burner set at the outlet o...

Embodiment 3

[0020] Example 3, nano-calcium carbonate powder and aluminum sol are mixed according to calcium oxide: aluminum oxide-based stoichiometry 12:7, and 1% lignin binder is added and mixed uniformly with a colloid mill to form a calcium-aluminum mixed slurry. Atomization and granulation; the first step is to pyrolyze the binder in the calcium aluminum micropowder to generate coke in the rotary kiln reactor at an outlet reaction temperature of 450°C and a residence time of 1.5 hours; The reactor is heated to an outlet temperature of 1200°C and a residence time of 3.5 hours to decompose calcium carbonate, and a solid-phase reaction occurs between calcium oxide and alumina to form calcium aluminate microspheres. In the third step, the fluidized bed gas set at the outlet of the rotary kiln The vaporization of pyrolysis coke in the calcium aluminate in the carburetor also reduces the temperature of the calcium aluminate catalyst due to the gasification endothermic reaction, and the fluid...

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Abstract

The invention provides a step-by-step solid-phase synthesis method of a micro-mesoporous calcium aluminate catalyst. Calcium oxide-based powder and alumina-based powder are mixed evenly by grinding according to the stoichiometric ratio of 12:2-15, and then a bonding pore-enhancing agent is used. Bonding and granulation, the first step is to pyrolyze the green coke in the rotary kiln reactor at a reaction temperature of 300-500°C and the residence time of 0.2-3.5 hours, and the second step is to heat it to the outlet temperature in the internal heating rotary kiln reactor 900°C-1500°C, residence time 0.1-5 hours solid state reaction to generate calcium aluminate, the third step is to use high-temperature water vapor to vaporize pyrolysis coke in calcium aluminate to create pores to obtain micro-mesoporous calcium aluminate catalyst .

Description

1. Technical field [0001] The invention provides a step-by-step solid-phase synthesis method of a micro-mesoporous calcium aluminate catalyst, which belongs to the field of fine chemical industry. 2. Background technology [0002] Inferior heavy oil has resource characteristics such as rich polycyclic aromatic hydrocarbons, high carbon-hydrogen ratio, viscosity and density, high content of sulfur, nitrogen, oxygen, residual carbon, heavy metals and mechanical impurities, and easy condensation to generate coke. Most of the existing heavy oil processing technologies are difficult to meet the requirements of efficient and clean "chemical-type" processing. Delayed coking is currently the preferred technology for processing low-quality heavy oil, but it faces many challenges such as large output of low-quality high-sulfur coke, low yield of coking wax oil, difficult "chemical-type" processing, environmental protection pressure of a large amount of volatile emissions, and safety h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/02B01J35/10B01J37/08
CPCB01J23/02B01J37/0018B01J37/0036B01J35/615B01J35/31B01J35/40B01J35/51B01J37/105B01J37/08B01J37/04B01J37/0063
Inventor 田原宇乔英云张金弘唐瑞源车远军
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)