Catalyst for oil hydrogenation to hydrocarbon fuels and its preparation and application

A technology for hydrogenation of hydrocarbon fuels and oils, which is applied in molecular sieve catalysts, preparation of liquid hydrocarbon mixtures, catalysts for physical/chemical processes, etc. It can solve the problem of reduced selectivity and yield of target products, increased probability, and probability of insertion end cracking and other problems, to achieve the effect of improving freezing point, high isomer selectivity, and increasing diesel content

Active Publication Date: 2019-11-08
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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

Method used

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  • Catalyst for oil hydrogenation to hydrocarbon fuels and its preparation and application
  • Catalyst for oil hydrogenation to hydrocarbon fuels and its preparation and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] Take 120g of the ZSM-22 molecular sieve raw powder containing the template, and roast it under an air atmosphere at 550°C for 24h to obtain 100g of the ZSM-22 molecular sieve from which the template has been completely removed; take 30g of pseudoboehmite (alumina hydrate) and Mix well, add 80g 5wt% HNO 3 solution, kneaded, molded with extruder, dried naturally, then dried at 120°C for 4h, and roasted at 550°C for 12h to obtain the carrier precursor; 100mL furfuryl alcohol and 100mL ethanol were mixed and stirred evenly at 25°C, and 1g oxalic acid was added to it , after dissolving completely, obtain monomer solution; Take 50g carrier precursor and mix with 50g monomer solution, place 6h under 25 ℃, obtain the carrier precursor of adsorption monomer solution after filtration and dry 0.5h at 120 ℃ (while drying, The polymer monomer furfuryl alcohol adsorbed by the carrier precursor undergoes spontaneous condensation reaction under heating and acidic environment), and then...

Embodiment 2

[0072] Take 120g of the ZSM-22 molecular sieve raw powder containing the template, and roast it under an air atmosphere at 550°C for 24h to obtain 100g of the ZSM-22 molecular sieve from which the template has been completely removed; take 30g of pseudoboehmite (alumina hydrate) and Mix well, add 80g 5wt% HNO 3 solution, kneaded, shaped by extruder, dried naturally, then dried at 120°C for 4h, and roasted at 550°C for 12h to obtain the carrier precursor; 100mL furfural and 100mL ethanol were mixed and stirred evenly at 25°C, and 1g oxalic acid was added to it , after dissolving completely, obtain monomer solution; Take 50g carrier precursor and mix with 50g monomer solution, place 6h under 25 ℃, obtain the carrier precursor of adsorption monomer solution after filtration and dry 0.5h at 120 ℃ (while drying, The polymer monomer furfural adsorbed by the carrier precursor undergoes spontaneous condensation reaction under heating and acidic environment), and then placed in a quart...

Embodiment 3

[0074] Take 120g of the ZSM-22 molecular sieve raw powder containing the template agent, and roast it under an air atmosphere at 550°C for 24h to obtain 100g of the ZSM-22 molecular sieve from which the template agent has been completely removed; take 20g of pseudoboehmite (alumina hydrate) and Mix well, add 80g 5wt% HNO 3 solution, kneaded, formed with extruder, dried naturally, then dried at 120°C for 4h, and roasted at 550°C for 12h to obtain the carrier precursor; 100mL furfural and 50mL ethanol were mixed and stirred at 25°C, and 5mL Hydrochloric acid, after dissolving completely, obtains monomer solution; Get 50g carrier precursor and mix with 50g monomer solution, place 6h under 25 ℃, after filtering, obtain the carrier precursor of adsorption monomer solution and dry at 120 ℃ for 0.5h (while drying , the polymer monomer furfural adsorbed by the carrier precursor undergoes spontaneous condensation reaction under heating and acidic environment), and then placed in a quar...

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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 ZSM‑22 molecular sieve is mixed with the precursor of the amorphous oxide, 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 ZSM-22 molecular sieve-based fuel catalyst for oil hydrogenation to hydrocarbons and a preparation method thereof. Background technique [0002] With the continuous development of economy and society, the reduction of primary energy such as oil and coal has brought about energy shortage. The price of crude oil and coal has been rising in recent years, which has also affected 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 will inevitably be produced during their conversion and product use. 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 launched a carbon tax coll...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/74C10G3/00
CPCB01J29/74B01J35/1038C10G3/47C10G3/50C10G2300/1018C10G2300/70C10G2400/04Y02P30/20
Inventor 王从新田志坚曲炜李鹏马怀军王琳韩健强
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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