Catalyst and a Method for Cracking Hydrocarbons

Inactive Publication Date: 2008-12-18
RES INST OF PETROLEUM PROCESSING SINOPEC +1
18 Cites 12 Cited by

AI-Extracted Technical Summary

Problems solved by technology

This method increases low-carbon olefins in a large scale, at the same time it doesn't increase the yield of aromatic extraly and lose the yield of gasoline.
Although the zeolite materials and catalysts disclosed in the prior art could effectively increas...
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Benefits of technology

[0048]The catalyst supplied by this invention by adding a proper content of the transition metal additive of Group VIIIB and the P additive, especially the samples using modified ZSM-5 zeolite as active component simultaneously, may increase the selectivity for propylene in ...
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Abstract

The invention discloses a catalyst and a method for cracking hydrocarbons. The catalyst comprises, calculated by dry basis, 10˜65 wt % ZSM-5 zeolite, 0˜60 wt % clay, 15˜60 wt % inorganic oxide binder, 0.5˜15 wt % one or more metal additives selected from the metals of Group VIIIB and 2˜25 wt % P additive, in which the metal additive is calculated by metal oxide and the P additive is calculated by P2O5. The method for cracking hydrocarbons using this catalyst increases the yield of FCC liquefied petroleum gas (LPG) and the octane number of FCC gasoline, as well as it increases the concentration of propylene in LPG dramatically.

Application Domain

Technology Topic

ChemistryZSM-5 zeolite +8

Image

  • Catalyst and a Method for Cracking Hydrocarbons
  • Catalyst and a Method for Cracking Hydrocarbons
  • Catalyst and a Method for Cracking Hydrocarbons

Examples

  • Experimental program(24)

Example

Example 1
[0064]The preparation of phosphorus-alumina sol: 1.05 kg pseudoboehmite (dry basis) and 3.35 kg deionized water was mixed together and stirred for 30 min, then 4.9 kg concentrated H3PO4 (chemical pure, 85 wt % of H3PO4) was added into the slurry under stirring. The obtained slurry was heated to 70° C. and reacted for 45 min at this temperature to form the colorless and transparent phosphorus-alumina sol with a P2O5 content of 30.6 wt % and an Al2O3 content of 10.5 wt % as well as pH=1.7.
[0065]1.75 kg A1 (dry basis), 1.4 kg kaolin (dry basis), 0.65 kg pseudoboehmite (dry basis), 6.2 kg deionized water and 2.79 kg alumina sol were mixed together and stirred for 120 min, then 1 L aqueous FeCl3.6H2O solution (having 100 g Fe2O3) was added into the slurry under stirring. The pH value of the slurry is 3.0. After stirring for another 45 min, 1.22 kg phosphorus-alumina sol was added into the slurry and stirred evenly. Microspheres with average particle size of 65 μm were obtained by the spray-drying of the slurry at input temperature of 500V and exhaust (output) temperature of 180° C. The catalyst ZJ1 with 35 wt % A1, 28 wt % kaolin, 27.5 wt % Al2O3, 2.0 wt % Fe additive (calculated by Fe2O3) and 7.5 wt % P additive (calculated by P2O5) was obtained after the calcination of the microspheres at 500° C. for 1 h.
[0066]The XRD pattern of this catalyst is shown in FIG. 1 as line a, in which the diffraction peaks at 2θ=16.35°, 2θ=26.12° and 2θ=30.94° are the characteristic diffraction peaks of FePO species.

Example

Example 2
[0067]1.84 kg A1 (dry basis), 1.33 kg kaolin (dry basis), 0.98 kg pseudoboehmite (dry basis), 7.2 kg deionized water and 2.79 kg alumina sol were mixed together and stirred for 120 min, then 1 L aqueous FeCl3.6H2O solution (having 250 g Fe2O3) was added into the slurry under stirring. The pH value of the slurry is 3.0. The slurry was stirred for another 45 min. Then microspheres with average particle size of 65 μm were obtained by the spray-drying of the slurry at input temperature of 500V and exhaust (output) temperature of 180° C. The microspheres with 36.8 wt % A1, 26.6 wt % kaolin, 31.6 wt % Al2O3 and 5.0 wt % Fe additive (calculated by Fe2O3) were obtained after calcination at 500° C. for 1 h.
[0068]1 kg microspheres obtained above (dry basis), 10 L deionized water and 100 g (NH4)2HPO4 were mixed together. The obtained slurry was heated to 60° C. under stirring and reacted for 20 min at this temperature. The slurry was vacuum-filtrated and dried. The catalyst ZJ2 with 35 wt % A1, 25.3 wt % kaolin, 30 wt % Al2O3, 4.7 wt % Fe additive (calculated by Fe2O3) and 5 wt % P additive (calculated by P2O5) was obtained after calination at 500° C. for 2 h.
[0069]The XRD pattern of this catalyst is shown in FIG. 2 as line e, in which the diffraction peaks at 2θ=16.37°, 2θ=26.22° and 2θ=30.90° are the characteristic diffraction peaks of FePO species.

Example

Example 3
[0070]1.94 kg A1 (dry basis), 1.91 kg pseudoboehmite (dry basis), 7.2 kg deionized water and 2.79 kg alumina sol were mixed together and stirred for 120 min, then 1 L aqueous FeCl3.6H2O solution (having 550 g Fe2O3) was added into the slurry under stirring. The pH value of the slurry is 3.0. The slurry was stirred for another 45 min. Then microspheres with average particle size of 65 μm were obtained by the spray-drying. Of the slurry at input temperature of 500V and exhaust temperature of 180° C. The microspheres with 38.8 wt % A1, 50.2 wt % Al2O3 and 11 wt % Fe additive (calculated by Fe2O3) were obtained after calcination at 500° C. for 1 h.
[0071]1 kg microspheres obtained above (dry basis), 10 L deionized water and 210 g (NH4)2HPO4 were mixed together. The obtained slurry was heated to 60° C. under stirring and reacted for 20 min. The slurry was vacuum-filtrated and dried. The catalyst ZJ3 with 35 wt % A1, 45.1 wt % Al2O3, 9.9 wt % Fe additive (calculated by Fe2O3) and 10 wt % P additive (calculated by P2O5) was obtained after calcination at 500° C. for 2 h.
[0072]The XRD pattern of this catalyst is shown in FIG. 2 as line f, in which the diffraction peaks at 2θ=16.25°, 2θ=26.18° and 2θ=30.87° are the characteristic diffraction peaks of FePO species.
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PUM

PropertyMeasurementUnit
Temperature420.0 ~ 600.0°C
Temperature400.0 ~ 650.0°C
Time0.5 ~ 10.0s
tensileMPa
Particle sizePa
strength10

Description & Claims & Application Information

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