A kind of heavy oil modified nickel-based catalyst and its preparation method and application

A nickel-based catalyst and catalyst technology, applied in the field of oilfield chemistry, can solve problems such as high cost and difficult implementation, and achieve the effects of convenient operation, short time, increased catalytic activity and stable performance

Active Publication Date: 2022-04-26
NINGBO FENGCHENG ADVANCED ENERGY MATERIALS RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above-mentioned heavy oil upgrading catalysts need to add hydrogen, methane, etc., or add hydrogen donating agent, oxygen donating agent, etc. when they catalyze the viscosity reduction of heavy oil. It is difficult to implement and the cost is also high.

Method used

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  • A kind of heavy oil modified nickel-based catalyst and its preparation method and application
  • A kind of heavy oil modified nickel-based catalyst and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0116] (1) Preparation of Zr 0.9 Ce 0.1 o2 Carrier: ZrOCl 2 ·8H 2 O and Ce(NO 3 ) 3 ·6H 2 Weigh 10 g of O according to the Zr / Ce molar ratio of 9:1 and dissolve it in 150 mL of EtOH; slowly add NH to the mixture at 30 °C 4 OH, stirred at 300rpm until the pH of the solution reached 9, then continued to stir for 4h; filtered and collected the solid precipitate; washed the solid with EtOH, and dried in an oven at 100°C for 12h; dried the solid at 550°C Calcined for 5 hours, then ground into small particles.

[0117] (2) Preparation of NiPt / Zr 0.9 Ce 0.1 o 2 Catalyst: Add nickel nitrate hexahydrate, chloroplatinic acid and hydrazine hydrate reducing agent in deionized water respectively, and prepare 0.04M nickel nitrate, 0.004M chloroplatinic acid and 0.3M reducing agent solution; / v cyclohexane, 13% v / v Triton X-100 surfactant and 47% v / v isopropanol co-surfactant oil phase mixed system are mixed in equal volume; then the three mixtures obtained are mixed at 500rpm Sti...

Embodiment 2

[0120] (1) Preparation of Zr 0.8 Ce 0.2 o 2 Carrier: ZrOCl 2 ·8H 2 O and Ce(NO 3 ) 3 ·6H 2 Weigh 10 g of O according to the Zr / Ce molar ratio of 8:1, dissolve in 200 mL of EtOH; slowly add NH to the mixture at 25 °C 4 OH, stirred at 400rpm until the pH of the solution reached 9, then continued to stir for 4h; filtered and collected the solid precipitate; washed the solid with EtOH, and dried in an oven at 100°C for 12h; dried the solid at 500°C Calcined for 6 hours, then ground into small particles.

[0121] (2) Preparation of NiPt / Zr 0.8 Ce 0.2 o 2 Catalyst: Add nickel nitrate hexahydrate, chloroplatinic acid and hydrazine hydrate reducing agent in deionized water respectively, and prepare 0.03M nickel nitrate, 0.003M chloroplatinic acid and 0.2M reducing agent solution; / v cyclohexane, 15% v / v Triton X-100 surfactant and 50% v / v isopropanol co-surfactant oil phase mixed system are mixed in equal volume; Stir at a rotating speed of 2h to form three kinds of microe...

Embodiment 3

[0124] (1) Preparation of Zr 0.7 Ce 0.3 o 2 Carrier: ZrOCl 2 ·8H 2 O and Ce(NO 3 ) 3 ·6H 2 Weigh 10 g of O according to the Zr / Ce molar ratio of 7:3, dissolve in 400 mL of EtOH; slowly add NH to the mixture at 20 °C 4 OH, stirred at 350rpm until the pH of the solution reached 8.5, then continued to stir for 5h; filtered and collected the solid precipitate; washed the solid with EtOH, and dried in an oven at 100°C for 12h; dried the solid at 6000°C Calcined for 4 hours, then ground into small particles.

[0125] (2) Preparation of NiPt / Zr 0.7 Ce 0.3 o 2 Catalyst: Add nickel nitrate hexahydrate, chloroplatinic acid and hydrazine hydrate reducing agent in deionized water respectively, and prepare 0.05M nickel nitrate, 0.005M chloroplatinic acid and 0.4M reducing agent solution; / v cyclohexane, 10% v / v Triton X-100 surfactant and 45% v / v isopropanol co-surfactant oil phase mixed system mixed in equal volume; then the three mixtures obtained were mixed at 650rpm Stir at...

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Abstract

The application discloses a nickel-based catalyst and its preparation method and application. The nickel-based catalyst includes a carrier, and the surface of the carrier is loaded with active components; the carrier is a metal oxide; the metal oxide has the general formula : A (1‑x) B x o 2 , wherein, A is selected from transition metal elements, and B is selected from lanthanide elements; the active component includes at least Ni. The nickel-based catalyst of the present application is used to reduce the viscosity of heavy oil, and the viscosity of crude oil with a kinetic viscosity of not less than 1000 mPa·s after degassing and dehydration at 50°C can be reduced by at least 65% without additional hydrogen donor or oxygen donor %, and the technical route of the present invention does not need other additives, realizes the purpose of reducing viscosity in a short time, at a lower temperature and pressure, is convenient to operate, and is suitable for large-scale industrial applications.

Description

technical field [0001] The application relates to a heavy oil modified nickel-based catalyst and its preparation method and application, belonging to the technical field of oil field chemistry. Background technique [0002] As an important unconventional crude oil resource in the world, heavy oil is an important resource to ensure my country's energy security and major engineering needs. With the continuous increase of oil demand and the gradual reduction of conventional crude oil resources, heavy oil has great development value, and the output of heavy oil in world oil exploitation is also gradually increasing. However, the high content of colloids and asphaltenes in heavy oil leads to high viscosity and freezing point, which makes the exploitation, gathering and refining of heavy oil more difficult. [0003] Due to the high viscosity of heavy oil, the fluidity of heavy oil becomes poor during production and gathering and transportation, the flow resistance increases, and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J33/00B01J35/02C09K8/58
CPCB01J23/894B01J33/00B01J35/026C09K8/58
Inventor 吴志连史建民陈斌刚崔浩业张侃王耀国
Owner NINGBO FENGCHENG ADVANCED ENERGY MATERIALS RES INST CO LTD
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