A kind of oil hydrogenation catalyst preparation and catalyst and application

Abstract

The invention relates to a method for preparing a catalyst for hydrogenation of fats and oils to prepare liquid fuels. The specific preparation steps are as follows: first, the roasted SAPO‑11 molecular sieve and the precursor of the amorphous oxide are mixed, extruded, shaped and roasted to form a carrier precursor; the monomer molecules of the polymer are filled in the carrier precursor Then carry out temperature rise treatment to obtain a carrier in which the acid sites of the molecular sieve are partially covered and the pores are partially blocked; the metal active component is loaded on the carrier, and the target catalyst is obtained after drying and reduction. Compared with the catalyst prepared in the prior art, the catalyst prepared by the method of the invention has higher isoparaffin selectivity and yield in the process of oil hydrogenation to liquid fuel.

Description

technical field [0001] The invention belongs to the field of molecular sieve catalysts, in particular to a grease hydrogenation catalyst based on SAPO-11 molecular sieve and a preparation method thereof. Background technique [0002] With the continuous development of the economy and society, the reduction of one-time energy such as oil and coal has brought about the problem of energy shortage. The prices of crude oil and coal have been rising in recent years, which also has an impact on the price of motor fuel. In addition, since petroleum and coal are both carbon-containing resources and contain elements such as nitrogen and sulfur, carbon dioxide and toxic gases that are harmful to the environment are inevitably generated during their conversion and the use of their products. Based on this, and also due to political and economic factors, some countries have introduced relevant policies to restrict the use of fossil energy products. For example, the European Union introdu...

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Problems solved by technology

[0011] 4. Molecular sieve micropores with suitable depth: The hydroisomerization of linear alkanes is mainly carried out at the molecular sieve micropore openings. If the molecular sieve micropore channels are too deep, the probability of linear alkanes completely or mostly inserting into the micropore channels increases. The desorption is hindered, which increases the probability of cracking at the insertion end, which makes it easy to generate small molecular hydrocarbons, which reduces the selectivity and yield of the target product

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