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A kind of environment-friendly propane direct dehydrogenation propylene production catalyst and preparation method thereof

An environment-friendly, catalyst technology is applied in the preparation of the catalyst, in the field of an environment-friendly catalyst for direct dehydrogenation of propane to propylene, and can solve the problem that the conversion rate and selectivity of the dehydrogenation catalyst cannot be coordinated, the application of fluidized bed reactors is difficult, and the The regeneration effect and other issues are not mentioned, and the effects of good industrial application prospects, high propylene selectivity and good renewable performance are achieved.

Active Publication Date: 2020-11-24
SOUTHWEST RES & DESIGN INST OF CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Chinese patents CN109289908A and CN109675548A provide molecular sieves as carriers, which require a special method to synthesize molecular sieves, and then impregnate them, and the actual volumetric space velocity of propane is relatively low, so it is difficult to apply in fluidized bed reactors; CN109939688A and CN 109926038A catalysts Although relatively new, no regenerative effects are mentioned
Chinese patent CN109382090A discloses a molybdenum vanadium double metal oxide catalyst, and the activity is very good, but the toxicity of vanadium oxide is relatively high, and it has strong carcinogenicity
However, dehydrogenation catalysts based on single or composite metal oxides have the problem of uncoordinated conversion and selectivity, and there is still room for optimization and improvement.

Method used

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  • A kind of environment-friendly propane direct dehydrogenation propylene production catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] 1) Weigh 100g of Hβ molecular sieve and measured zinc nitrate into a container, add (total mass of Hβ molecular sieve and zinc nitrate) about 10 times the mass of deionized water, seal and stir at 90°C for 6 hours, then open the cover stirring and evaporating to dryness, and then calcining at 500°C for 4 hours in a calciner to obtain Zn-doped modified Hβ molecular sieves for use;

[0049] 2) After mixing the weighed ammonium metatungstate, cobalt nitrate, nickel nitrate, lanthanum nitrate, phosphoric acid and sodium nitrate, add the measured 1mol / L oxalic acid aqueous solution and stir to dissolve at 70°C, wherein the oxalic acid solution is mixed with the modified The total weight ratio of active agent is 2.0ml / g.

[0050] 3) Mix the Zn-doped Hβ molecular sieve obtained in step 1) with the measured macroporous pseudo-boehmite, and then add 2.0 times the total weight of the solid powder in deionized water and the modifier solution prepared in step 2), Stir and mix even...

Embodiment 2

[0054] 1) Weigh 200g of Hβ molecular sieve and measured zinc nitrate into a container, add about 10 times the mass of deionized water, seal it and stir at 60°C for 24 hours, then open the cover, stir and evaporate to dryness, and then put it in a calciner at Calcined at 600°C for 2 hours to obtain Zn-doped modified Hβ molecular sieve;

[0055] 2) After mixing the weighed ammonium molybdate, manganese nitrate, zirconium nitrate, indium nitrate, cerium nitrate and strontium nitrate, add the measured 1mol / L oxalic acid aqueous solution and stir to dissolve at 90°C, wherein the volume of the oxalic acid solution is equal to Modifier total weight ratio 1.5ml / g.

[0056] 3) Mix the Zn-doped Hβ molecular sieve obtained in step 1) with the measured macroporous pseudo-boehmite, then add 3.0 times the total weight of the solid powder in deionized water and the modifier solution prepared in step 2), Stir and mix evenly; then gradually add nitric acid solution dropwise under stirring to ...

Embodiment 3

[0060] 1) Weigh 100g of Hβ molecular sieve and measured zinc nitrate into a container, add about 10 times the mass of deionized water, seal it and stir at 90°C for 4 hours, then open the lid, stir and evaporate to dryness, then put it in a calciner at Calcined at 400°C for 8 hours to obtain Zn-doped modified Hβ molecular sieve;

[0061] 2) After mixing the weighed ammonium molybdate, nickel nitrate, gallium nitrate, indium nitrate and sodium nitrate, add a measured 1mol / L citric acid aqueous solution and stir to dissolve at 50°C, wherein the volume of the oxalic acid solution is the same as that of the modified The total weight ratio of the agent is 1.8ml / g.

[0062] 3) Mix the Zn-doped Hβ molecular sieve obtained in step 1) with the measured large-pore pseudo-boehmite, then add 3.5 times the total weight of the solid powder in deionized water and the modifier solution prepared in step 2), Stir and mix evenly; then gradually add nitric acid solution dropwise under stirring to...

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Abstract

The invention belongs to the field of catalysts, and particularly relates to an environment-friendly catalyst for preparing propylene by directly dehydrogenating propane and a preparation method of the catalyst, wherein the particle size of the catalyst is 40-150 [mu] m; the catalyst comprises 30%-70% of a Zn-doped Hbeta molecular sieve, 15%-50% of Al2O3 and 3%-30% of a multi-element active modifier, wherein the modifier comprises at least one element of W, Mo, Mn, Zr, Ni, Fe and Co as a first modifier, at least one element of Ga, In, P, La and Ce as a second modifier, and any one element of Sr, Ba, Ca, Mg, Na and Li as a third modifier, and the sum of the mass percentages of oxides of all the element components is 100%. The prepared fluidized bed dehydrogenation catalyst is low in cost and good in wear resistance, and has good dehydrogenation activity and stability when used for propane dehydrogenation.

Description

technical field [0001] The invention belongs to the field of catalysts, and in particular relates to an environment-friendly catalyst for direct dehydrogenation of propane to propylene and a preparation method of the catalyst. Background technique [0002] Propylene is one of the important basic organic chemical raw materials and occupies an important position in the modern petroleum and chemical industry. Its global consumption is as high as 90 million tons, of which 58% is used for the manufacture of polypropylene, and about 10%, 8%, 7% and 6% for the manufacture of acrylonitrile, oxo alcohol, propylene oxide and cumene, respectively. . With the rapid growth of demand for polypropylene derivatives in various industries, the demand for propylene is also increasing year by year. Considering economics and maturity indicators comprehensively, propane dehydrogenation (PDH) technology is currently the most competitive propylene manufacturing process. Propane dehydrogenation t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/78C07C5/333C07C11/06
CPCB01J23/002B01J29/7815B01J2229/18B01J2523/00C07C5/3332C07C2529/78B01J2523/12B01J2523/27B01J2523/31B01J2523/3706B01J2523/51B01J2523/69B01J2523/845B01J2523/847B01J2523/24B01J2523/33B01J2523/3712B01J2523/48B01J2523/68B01J2523/72B01J2523/32B01J2523/22B01J2523/842B01J2523/11C07C11/06Y02P20/52
Inventor 韩伟梁衡潘相米陈鹏艾珍吴砚会程牧曦李博李杨王华郑敏周飞
Owner SOUTHWEST RES & DESIGN INST OF CHEM IND
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