Catalyst for producing BTX aromatic hydrocarbon by using organic waste, preparation method and application thereof, and method for producing BTX aromatic hydrocarbon
A technology of organic waste and BTX aromatics, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. Difficult utilization of phase products, no application market for pyrolysis solid phase products, etc.
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Embodiment 1
[0060] The preparation flow diagram of the BTX aromatic hydrocarbon of the present invention application is as figure 1 . Specifically, organic waste is pyrolyzed to obtain solid-phase product semi-coke and gas-phase product volatiles; solid-phase product semi-coke is ground to obtain carbon powder, that is, a catalyst; after carbon powder is loaded with active components, it is calcined and activated. A catalyst loaded with active components is obtained.
[0061] The volatile matter of the gas phase product produced by the pyrolysis of gasification tar and / or organic waste undergoes a catalytic reaction under the action of a catalyst and / or a catalyst loaded with active components, and the catalytic reaction product is first condensed at 150°C to 170°C to obtain The high-boiling point oil can be used as the reaction raw material after being heated to gaseous state or atomized; the catalytic reaction product is condensed at 70°C to 140°C for the second time to obtain low-boil...
Embodiment 2
[0064] In the present embodiment, the preparation method for producing BTX aromatics is as follows:
[0065] 1) In the pyrolysis reactor, the organic waste is pyrolyzed to obtain solid-phase product semi-coke and gas-phase product volatiles; among them, the organic waste is waste plastic, its calorific value is 13MJ / kg, and the moisture content is 30% , the heating rate during pyrolysis was 20°C / min, and the temperature was kept at 500°C for 60 minutes.
[0066] 2) Grinding the solid-phase product semi-coke obtained in step 1), passing through a 60-mesh sieve, and adopting gravity separation to obtain carbon powder with a carbon content of 53%, which is the catalyst.
[0067] 3) Immerse the carbon powder obtained in step 2) in a saturated solution of nickel nitrate, and dry to obtain Ni-loaded carbon powder; wherein the mass ratio of nickel nitrate to carbon powder is 1:6.5.
[0068] 4) The Ni-loaded carbon powder obtained in step 3) was calcined at 500° C. for 2 h in a nitro...
Embodiment 3
[0072] In the present embodiment, the preparation method for producing BTX aromatics is as follows:
[0073] 1) In the pyrolysis reactor, the organic waste is pyrolyzed to obtain solid-phase product semi-coke and gas-phase product volatiles; among them, the organic waste is waste plastic, its calorific value is 23MJ / kg, and the moisture content is 27% , the heating rate during pyrolysis was 28°C / min, and the temperature was kept at 550°C for 55min.
[0074] 2) Grinding the solid-phase product semi-coke obtained in step 1), passing through a 60-mesh sieve, and adopting gravity separation to obtain carbon powder with a carbon content of 65%, which is the catalyst.
[0075] 3) impregnating the charcoal powder obtained in step 2) in the mixed aqueous solution of zinc nitrate and manganese nitrate, and drying to obtain the charcoal powder loaded with Zn and Mn; wherein, the mass ratio of zinc nitrate and charcoal powder is 1:3.45, the second The mass ratio of the metal Mn to the f...
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