FIELD: chemistry.
SUBSTANCE: present invention relates to a highly coordinated sulfated catalytic composition before calcination and a method for the production of a highly coordinated sulfated catalytic composition. The method includes following stages: a) dissolution of zirconium nitrate or acetate in distilled water; b) precipitation of zirconium salt hydroxide from the stage (a), using diethylamine, washing it with bidistilled water, and drying; c) loading of sulfate ions to dried zirconium hydroxide obtained at the stage (b) with sulfate ions, using ammonium sulfate or ammonium persulfate with ammonia as a competing ion; d) reduction in a particle size of zirconium hydroxide loaded with sulfate ions, obtained at the stage (c) by grinding from 310 mcm to 44 mcm; e) reduction in a particle size of acidified aluminum oxide with a large surface area by grinding from 90 mcm to 44 mcm, and then mixing with particles obtained at the stage (d) in a ball mill to obtain a total particle size of less than 37 mcm; f) addition of the mixture obtained at the stage (e) to a liquid binder containing a mixture of α-amino acids, HNO3, and H2SO4, and mixing, maintaining pH in the range from 1.5 to 3.8, where α-amino acids are a combination of α-amino acids with a non-polar side chain and a main side chain; (g) peptization followed by extrusion after settling the mixture obtained at the stage (f) for 30 minutes; (h) drying of extrudates obtained at the stage (g) at a temperature in the range of 100-200°C for 6 hours, followed by calcination; and (i) addition of a hydrogenating component. A mixture of α-amino acids has a molecular weight of ≤ 250, where α-amino acid with the non-polar side chain is selected from glycine, alanine, valine, leucine, isoleucine, methionine, proline, and phenylalanine, α-amino acid with the main side chain is selected from lysine, arginine, and histidine.
EFFECT: catalysts provide a high degree of conversion in a reaction of isomerization of hydrocarbons, while simultaneously having crushing strength in the range from 2.0 to 5.0 daN, which makes it possible to effectively use them on an industrial scale.
12 cl, 2 dwg, 6 tbl, 3 ex
Title | Year | Author | Number |
---|---|---|---|
METHOD FOR PREPARING CATALYST AND CATALYST FOR ALKYLATION OF ISOBUTANE WITH ISOBUTENE | 2014 |
|
RU2579512C1 |
CATALYST FOR ALKYLATION OF ISO-BUTANE WITH ISO-BUTENE AND METHOD FOR PRODUCING THEREOF | 2015 |
|
RU2612965C1 |
SOLID ACID CATALYST, METHOD OF PRODUCTION OF SUCH CATALYST AND ITS APPLICATION | 1999 |
|
RU2190465C2 |
SOLID ACID CATALYST AND METHOD OF USING IT | 2005 |
|
RU2338589C2 |
CATALYST FOR ISOMERISATION OF PARAFFIN HYDROCARBONS AND PREPARATION METHOD THEREOF | 2015 |
|
RU2595341C1 |
METHOD FOR OBTAINING A SPHERICAL CATALYST AND ISOBUTANE ALKYLATION CATALYST WITH ISOBUTENE | 2017 |
|
RU2671413C1 |
HIGHLY ACTIVE ISOMERISATION CATALYST AND ISOMERISATION METHOD | 2005 |
|
RU2329099C1 |
METHOD OF PREPARING CATALYST FOR ISOMERISATION OF C-C HYDROCARBONS | 2011 |
|
RU2466789C1 |
SOLID SUPERACID CATALYST FOR LIGHT HYDROCARBON ISOMERIZATION | 2020 |
|
RU2779074C2 |
HYDROCARBON CONVERSION CATALYST, CATALYST PREPARATION PROCESS, AND HYDROCARBON CONVERSION PROCESS | 2002 |
|
RU2294797C2 |
Authors
Dates
2022-09-29—Published
2021-02-17—Filed