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Reformed raw oil desulfurizing agent and preparation method thereof

A technology of desulfurizer and raw oil, applied in the field of desulfurization of oil products, can solve the problems of low radial crushing strength, complex production process, short service life, etc., and achieve non-brittleness or even pulverization, low bulk density, high strength Improved effect

Active Publication Date: 2014-12-24
JINDUICHENG MOLYBDENUM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the proportion of precious metals in the existing desulfurizers is relatively high, resulting in high production costs. At the same time, there are disadvantages such as complex production processes, low radial crushing strength, and short service life.
[0005] So far, no reforming raw material oil desulfurizer with CuO, NiO and ZnO as ternary active components and aluminate cement or / and ordinary Portland cement as the carrier has been reported.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] The reformed raw oil desulfurizer in this embodiment is made of the following raw materials in mass percentage: CuO25%, NiO25%, ZnO15%, carrier 35%, and the carrier is aluminate cement or / and ordinary Portland cement. Examples The carrier is preferably CA-60 aluminate cement, and the ternary active components CuO, NiO and ZnO are preferably respectively: CuO is obtained from basic copper carbonate after roasting for 1 hour at a temperature of 500 ° C and air circulation conditions. Decomposition products; NiO comes from the roasted product obtained after roasting nickel carbonate at a temperature of 500 °C and air circulation for 2 h, and ZnO comes from the roasted product obtained after roasting zinc carbonate at a temperature of 500 °C and air circulation for 1.5 h product

[0028] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:

[0029] Step 1, taking CuO, NiO, ZnO and carrier by mass percentage ...

Embodiment 2

[0034] The reformed raw oil desulfurizer of this embodiment is made of the following raw materials in mass percentage: CuO 25%, NiO 25%, ZnO 15%, carrier 35%, and the carrier is aluminate cement or / and ordinary portland cement The carrier of this embodiment is preferably 42.5# ordinary Portland cement, and the ternary active components CuO, NiO and ZnO are preferably respectively: CuO comes from the roasted copper carbonate obtained after roasting for 2 hours under the condition of 500 ° C and air circulation. Decomposition products, NiO is obtained from the roasted product of basic nickel carbonate at a temperature of 500 °C and air circulation for 1.5 h, and ZnO is obtained from zinc carbonate after roasting at a temperature of 500 °C and air circulation for 1 h baked product.

[0035] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:

[0036] Step 1, taking CuO, NiO, ZnO and carrier by mass percentage and...

Embodiment 3

[0041] The reformed raw oil desulfurizer of this embodiment is made of the following raw materials in mass percentage: CuO 10%, NiO 30%, ZnO 5%, carrier 55%, and the carrier is aluminate cement or / and ordinary Portland cement, The carrier in this example is preferably a mixture obtained by mixing CA-50 aluminate cement and 42.5# ordinary Portland cement at a mass ratio of 1:1, and the ternary active components CuO, NiO and ZnO are respectively preferably: CuO comes from basic Copper carbonate was roasted for 2 hours at a temperature of 450°C with air circulation. NiO was obtained from basic nickel carbonate roasted for 1.5 hours at a temperature of 520°C with air circulation. ZnO It comes from the roasted product obtained after roasting basic zinc carbonate at a temperature of 520°C and air circulation for 1 hour.

[0042] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:

[0043] Step 1, taking CuO, NiO, Zn...

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Abstract

The invention provides reformed raw oil desulfurizing agent, which is prepared by following raw materials by weight percent: 10 to 40 percent of copper oxide (CuO), 15 to 30 percent of nickel oxide (NiO), 5 to 25 percent of zinc oxide (ZnO) and balance of carriers; and the carrier is aluminate cement or / and ordinary prtland cement. The invention also provides a preparation method of the reformed raw oil desulfurizing agent, and the method comprises follwing steps that A, CuO, NiO, ZnO and carriers are weighed according to the mass percent and are uniformly mixed to obtain mixture; B, after deionized water with a given quantity is placed into the mixture, the mixture is mixed and rolled and is extruded into bars; and C, and the reformed raw oil desulfurizing agent can be obtained through drying and roasting. Raw materials of the reformed raw oil desulfurizing agent is widely sourced, the preparation process is simple, and the production cost is low; and the desulfurizing efficiency of the reformed raw oil desulfurizing agent is high, the radial pressure and crush resistance is high, the service life is long, and the desulfurizing agent is suitable for the industrialized mass production.

Description

technical field [0001] The invention belongs to the technical field of desulfurization of oil products, and in particular relates to a reforming raw material oil desulfurizer and a preparation method thereof. Background technique [0002] At present, the catalytic reforming of raw oils such as straight-run naphtha is a common method for industrial production of aromatics, high-octane gasoline and hydrogen used in hydrogenation processes. [0003] Early catalytic reforming processes used single platinum catalysts, but with poor results. In order to increase the yield of aromatics, gasoline octane number, hydrogen production, and extend the operating cycle, a series of high-efficiency bimetallic reforming catalysts have been developed over the years, such as platinum-rhenium reforming catalysts with equal platinum-rhenium ratio and high platinum-rhenium ratio. However, the trace amount of hydrogen sulfide and organic sulfur contained in the reforming feed oil has a great infl...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G29/16
Inventor 卢朝阳李辉胡耕科惠三顺
Owner JINDUICHENG MOLYBDENUM CO LTD
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