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Preparation method and application of a double-functional fine desulfurizer

A fine desulfurization and dual-function technology, which is applied in the field of preparation of dual-functional fine desulfurizers, can solve the problems of limited promotion and application, and achieve the effects of overcoming long process flow, high low-temperature sulfur capacity, and reducing desulfurization costs

Active Publication Date: 2020-05-15
江苏天东新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Patent CN104941439A discloses a super-precision dual-function fine desulfurizer and its preparation method. The catalyst is composed of 50-70% zinc oxide or zinc carbonate, 1-5% copper oxide, 0-5% potassium carbonate, 0.1-0.5% Silver nitrate, 25-50% alumina and 1-10% binder, the desulfurizer shows good desulfurization accuracy in the desulfurization of chemical raw materials, but its low-temperature sulfur capacity is low, only 5wt %, the best desulfurization temperature is 200-350℃
[0006] The above-mentioned patents disclose a variety of organic sulfur conversion and absorption dual-function desulfurizers. Although the conversion efficiency of organic sulfur is relatively high, the sulfur capacity of the above-mentioned dual-functional desulfurizers, especially low-temperature sulfur capacity, limits their promotion. and application

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] (1) Configure a 0.1mol / L sodium carbonate solution, and configure a total concentration of 0.1mol / L Zn(NO 3 ) 2 and Cu(NO 3 ) 2 mixed solution, control Zn(NO 3 ) 2 and Cu(NO 3 ) 2 The molar percentages of the mixed solution are respectively 80% and 20%. Under the condition of stirring, the two solutions are added dropwise to the reactor placed in the microwave oven, and the precipitation temperature is controlled to be 60°C. Acceleration, the pH value of the control precipitation suspension is 6.5, and the first precipitation solution is obtained after the dropwise addition of the mixed solution is completed;

[0036] (2) Configure a 0.1mol / L sodium carbonate solution, prepare an aluminum nitrate solution with a total concentration of 0.1mol / L, and add the solution dropwise to a reactor placed in a microwave heating furnace under stirring conditions to control precipitation The temperature is 65° C., and the pH value of the precipitation suspension is controlled ...

Embodiment 2

[0045] (1) Configure a 0.3mol / L sodium carbonate solution, and configure a total concentration of 0.3mol / L Zn(NO 3 ) 2 and FeCl 3 -Mix solution, control Zn(NO 3 ) 2 and FeCl 3 The molar percentages of the mixed solution are respectively 85% and 15%. Under the condition of stirring, the two solutions are added dropwise to the reactor placed in the microwave oven, and the precipitation temperature is controlled to be 62°C. Acceleration, the pH value of the control precipitation suspension is 6.7, and the first precipitation solution is obtained after the dropwise addition of the mixed solution is completed;

[0046] (2) Configure 0.3mol / L sodium carbonate solution, prepare an aluminum nitrate solution with a total concentration of 0.3mol / L, add the solution dropwise to a reactor placed in a microwave heating furnace under stirring conditions, and control precipitation The temperature is 67° C., and the pH value of the precipitation suspension is controlled to be 8.1 by adju...

Embodiment 3

[0055] (1) Configure a 0.5mol / L sodium carbonate solution, and configure a total concentration of 0.5mol / L Zn(NO 3 ) 2 and MnCl 2 -CeCl 3 mixed solution, control Zn(NO 3 ) 2 , MnCl 2 and CeCl 3 The molar percentages of the mixed solution are respectively 90%, 5% and 5%. Under the condition of stirring, the two solutions are added dropwise to the reactor placed in the microwave oven, and the precipitation temperature is controlled to be 65°C. The rate of addition of the solution, the pH value of the control precipitation suspension is 7.0, and the first precipitation solution is obtained after the dropwise addition of the mixed solution is completed;

[0056] (2) Configure 0.5mol / L sodium carbonate solution, prepare an aluminum nitrate solution with a total concentration of 0.5mol / L, add the solution dropwise to a reactor placed in a microwave heating furnace under stirring conditions, and control precipitation The temperature is 69° C., and the pH value of the precipita...

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PUM

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Abstract

A preparation method of a bifunctional fine desulfurizer comprises steps as follows: a sodium carbonate solution reacts with soluble zinc salt and first active auxiliary salt under microwave, a first precipitation solution is obtained, and the sodium carbonate solution reacts with an aluminum nitrate solution under microwave, and a second precipitation solution is obtained; part of the second precipitation solution is treated, alumina powder is obtained, the other part of the second precipitation solution is mixed with the first precipitation solution, microwave radiation ageing and filtering are performed, a feed solution is prepared from a filter cake, spray drying is performed, precursor powder is obtained and retreated, zinc oxide composite oxide powder is obtained, a mixed salt solution of soluble molybdenum salt and second active auxiliary salt are subjected to equivalent-volume impregnation, drying and calcination with the alumina powder, and molybdenum oxide composite oxide powder is obtained, and the zinc oxide composite oxide powder, the molybdenum oxide composite oxide powder, a binder, a pore forming agent and water are molded, dried and calcined, and a finished product is obtained. The preparation method has the advantage of high sulfur capacity.

Description

technical field [0001] The invention belongs to the field of preparation of desulfurizers, and in particular relates to a preparation method and application of a dual-functional fine desulfurizer for hydrogenation conversion and removal of organic sulfur. [0002] technical background [0003] At present, in the conversion and utilization of coal-to-synthesis gas, natural gas, coke oven gas, refinery dry gas, liquefied petroleum gas, carbon dioxide and liquefied hydrocarbons as chemical raw materials, the sulfide in the gas must be removed, which not only avoids the Catalyst poisoning in the follow-up section also ensures the quality of the product. There are mainly two types of desulfurization technologies at home and abroad: wet desulfurization and dry desulfurization: wet desulfurization technology uses absorption liquid to absorb sulfide in the gas source, and is mainly used for low desulfurization temperature, large gas treatment capacity, high hydrogen sulfide content a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/887B01J23/34B01J23/30C10K1/34C10L3/10C10L3/12C10G70/00C10G29/16C01B3/58C01B32/50
CPCB01J23/002B01J23/30B01J23/34B01J23/8873B01J2523/00C01B3/58C01B2203/045C10G29/16C10G70/00C10G2300/202C10K1/004C10K1/34C10L3/103C10L3/12B01J2523/31B01J2523/68B01J2523/847B01J2523/27B01J2523/17B01J2523/842B01J2523/845B01J2523/72B01J2523/3712B01J2523/48B01J2523/22B01J2523/67B01J2523/69
Inventor 丁晶晶陈井凤于慧芳牛玉杰
Owner 江苏天东新材料科技有限公司