Catalyst for preparing heavy hydrocarbon with synthetic gas and its prepn process

A catalyst, heavy hydrocarbon technology, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of low octane number and low utilization value, and achieve increased added value and low cost. , highly selective effect

Active Publication Date: 2007-08-22
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented catalytic process uses commercial ammoniacal oxide or other materials called ZrCs instead of expensive raw material like platinum for producing synthetic gases from coal tar distillate fractions containing heavy oils such as diesel oil. By mixing small amounts of these metals together, this new type of catalyst becomes more effective at making certain types of chemical compounds through reactions between them. It also makes it easier than previous methods because they only require one metal atom per molecule compared to traditional processes involving multiple atoms.

Problems solved by technology

This patented technical problem addressed in this patents relates to improving the performance of certain types of chemical reactions called Fischer-Thrucksynthesis processes that involve mixing two reactant gases together at specific temperatures under pressure conditions. These techniques are commonly referred to as hydrocrackers because they convert light paraffin fractions into heavier ones while also producing valuable materials like diesels. To improve their effectiveness, researchers focused on developing new catalyst systems containing transition metals instead of Fe(III) which were previously found to lack durability over time due to decomposition caused by acidic components present during storage.

Method used

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  • Catalyst for preparing heavy hydrocarbon with synthetic gas and its prepn process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Catalyst A is composed of Co and SiO 2 , The weight percentage of Co element is 15%, SiO 2 The specific surface area is 380m 2 / g, the average pore diameter is 10nm, and the pore volume is 0.91ml / g. The catalyst is prepared according to the following steps:

[0020] a) Impregnate 12.75g of the above SiO with 18ml of cobalt nitrate solution containing the required cobalt content 2 ;

[0021] b) Drying the catalyst obtained in step a) at 393K for 6 hours;

[0022] c) calcining the catalyst obtained in step b) at 623K for 6 hours.

[0023] Catalyst A was activated for 2 hours under 673K ​​hydrogen atmosphere before use. The reaction conditions of catalyst A are: reaction temperature is 493K, reaction pressure is 2.0Mpa, and synthesis gas space velocity is 500h -1 , The volume ratio of hydrogen to carbon monoxide in the synthesis gas is 2.

Embodiment 2

[0025] Catalyst B is composed of Co and SiO 2 , The weight percentage of Co element is 15%, SiO 2 The specific surface area is 286m 2 / g, the average pore diameter is 13nm, and the pore volume is 0.98ml / g. The catalyst is prepared according to the following steps:

[0026] a) Impregnate 12.75g of the above SiO with 18ml of cobalt nitrate solution containing the required cobalt content 2 ;

[0027] b) Drying the catalyst obtained in step a) at 393K for 6 hours;

[0028] c) calcining the catalyst obtained in step b) at 623K for 6 hours.

[0029] The reduction conditions and reaction conditions of the catalyst B are the same as those of the catalyst A.

Embodiment 3

[0031] Catalyst C is composed of Co, Zr and SiO 2 , Co element weight percentage is 15%, Zr element weight percentage is 0.5%, SiO 2 The specific surface area is 286m 2 / g, the average pore diameter is 13nm, and the pore volume is 0.98ml / g. The catalyst is prepared according to the following steps:

[0032] a) Impregnate 12.75g of the above SiO with 18ml of zirconium nitrate solution containing the required zirconium content 2 ;

[0033] b) Drying the catalyst obtained in step a) at 393K for 6 hours;

[0034] c) calcining the catalyst obtained in step b) at 1073K for 6 hours;

[0035] d) Immerse the catalyst obtained in step c) above with 18 ml of cobalt nitrate solution containing the required cobalt content;

[0036] e) drying the catalyst obtained in step d) at 393K for 6 hours;

[0037] f) The catalyst obtained in step e) is calcined at 623K for 6 hours.

[0038] The reduction conditions and reaction conditions of the catalyst C are the same as those of the catalyst A.

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Abstract

The catalyst for preparing heavy hydrocarbon with synthetic gas has amorphous SiO2 as carrier, Co as main active component, and small amount of Zr as cocatalyst. Of the catalyst, SiO2 has specific surface area of 150-900 sq m/g, average hole size of 2-100 nm and pore volume of 0.5-1.5 ml/g; Co content is 5-35 wt%; and Zr content is 0.01-5 wt%. The preparation process of the catalyst includes the following steps: 1. soaking SiO2 in Zn containing solution, drying at 273-473 K and baking at 473-1273 K; 2. soaking SiO2 containing Zn in Co containing solution, drying at 273-423 K and baking at 423-1273 K; and 3. treating the catalyst containing H2 in 0.2-20 wt% and inert gas N2, He or Ar at 473-873 K and 0.05-2.00 MPa. The catalyst has low cost, high stability, high C20+ hydrocarbon selectivity and other advantages.

Description

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Claims

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Application Information

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Owner PETROCHINA CO LTD
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