Unlock instant, AI-driven research and patent intelligence for your innovation.

In-fluid-bed reactivation method for catalyst for direct preparation of low-carbon olefins from synthesis gas

A technology for low-carbon olefins and synthesis gas, which is used in physical/chemical process catalysts, hydrocarbon production from carbon oxides, chemical instruments and methods, etc., and can solve the problems of over-temperature, recovery as before, and performance degradation of Fischer-Tropsch synthesis catalysts, etc. To achieve the effect of simple operation, avoid over temperature, good heat dissipation

Active Publication Date: 2015-11-25
CHINA PETROLEUM & CHEM CORP +1
View PDF12 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, during the regeneration process of the Fischer-Tropsch synthesis catalyst, when the reaction atmosphere and operating conditions are not adjusted properly, there will be serious over-temperature phenomena, which will lead to a decline in the performance of the Fischer-Tropsch synthesis catalyst.
So far, we have not seen any reports on in-situ regeneration of catalysts in fluidized beds to restore their activity to the original level.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • In-fluid-bed reactivation method for catalyst for direct preparation of low-carbon olefins from synthesis gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 300h -1 的nitrogen;

[0021] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 280°C, and stay in this atmosphere and this temperature and pressure for 3 hours.

[0022] (3) Adjust the temperature of the reactor to 230°C and the pressure to 0.01MPa;

[0023] (4) Switch the intake air to an airspeed of 300h -1 A mixture of nitrogen and hydrogen, stay in this atmosphere and temperature and pressure for 3 hours, where the volume ratio of nitrogen to hydrogen is N 2 : H 2 =10:1;

[0024] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 0.2MP;

[0025...

Embodiment 2

[0029] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 10000h -1 Of helium

[0030] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 520℃, and stay in this atmosphere and this temperature and pressure for 30h;

[0031] (3) Adjust the temperature of the reactor to 480°C and the pressure to 5.0MPa;

[0032] (4) Switch the intake air to an airspeed of 10000h -1 Hydrogen, stay in this atmosphere and this temperature and pressure for 60 hours;

[0033] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 10MP;

[0034] (6) Switch the activation gas to a mixed gas of helium, carbon monoxide and propylene, th...

Embodiment 3

[0038] (1) 1.5 inches, containing 100g of original iron-based catalyst (the catalyst is prepared by co-precipitation spray drying, and the composition is 100Fe / 80Mn / 5K / 80SiO in atomic ratio 2 ) And it has been reacted for about 1500 hours, and the inlet air of the fluidized bed reactor with decreased activity is switched to the space velocity of 1000h -1 的argon;

[0039] (2) Adjust the pressure of the reactor to normal pressure, adjust the temperature of the reactor to 300°C, and stay in this atmosphere and this temperature and pressure for 5 hours.

[0040] (3) Adjust the temperature of the reactor to 245°C and the pressure to 0.1MPa;

[0041] (4) Switch the intake air to an airspeed of 1000h -1 A mixture of argon and hydrogen, stay in this atmosphere and this temperature and pressure for 10 hours, where the volume ratio of argon to hydrogen is argon: H 2 =1:1;

[0042] (5) Keep the previous temperature and space velocity unchanged, and increase the reactor pressure to 0.6MPa;

[0043]...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to an in-fluid-bed reactivation method for catalyst for direct preparation of low-carbon olefins from synthesis gas. In-fluid-bed reactivation method for catalyst with reduced activity comprises following steps: removing heavy wax adsorbed at least part of catalyst surface under high temperature and normal pressure by inert gas, then regenerating for a first time the catalyst with reduced activity by mixed gas of inert gas and hydrogen gas, and reactivating for the second time the catalyst with mixture of inert gas, carbon oxide and low carbon olefin in a proper condition. The activity of the reactivated catalyst can be restored to a level before the activity declines. The reactivation in fluid bed can be easily switched from reaction state to reactivation state, and then switched to the reaction state after the reactivation. The reactivation method is suitable for but is not limited to catalyst reactivation for large-scaled fluid bed synthetic gas for direct preparation for low carbon olefin.

Description

Technical field [0001] The invention relates to a regeneration method for directly preparing a low-carbon olefin iron-based catalyst from a fluidized bed synthesis gas. Background technique [0002] The Fascher-Tropsch synthesis is the use of syngas (the main components are CO and H 2 ) The process of synthesizing hydrocarbons under the action of catalysts is an important way of indirect liquefaction of coal and natural gas. This method was invented by German scientists Frans Fischer and Hans Tropsch in 1923. It is a process in which CO undergoes a heterogeneous catalytic hydrogenation reaction on a metal catalyst to produce a mixture of linear alkanes and olefins. [0003] Germany started the research and development of Fischer-Tropsch synthesis in the 1920s, and realized industrialization in 1936. After World War II, it was closed because it could not compete with the oil industry economically; South Africa has abundant coal resources, but oil resources The lack of plaques and t...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/94B01J23/889C07C1/04C07C9/04C07C11/02
CPCY02P20/584
Inventor 庞颖聪陶跃武宋卫林李剑锋
Owner CHINA PETROLEUM & CHEM CORP