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Preparation method and application of heterogeneous catalyst for desorbing CO2 in solution

A heterogeneous catalyst, CO2 technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as large demand for low-pressure steam flow, low absorption and desorption rates, and changes in the size of regeneration towers. The effect of reducing desorption energy consumption, increasing desorption rate, and reducing desorption energy consumption

Inactive Publication Date: 2020-09-29
NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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  • Claims
  • Application Information

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Problems solved by technology

Although the chemical absorption method has the characteristics of high decarbonization efficiency, simple process, and advantages in removal cost compared with other technologies, the amine-based solution absorption method also has its inherent defects: high reaction heat leads to increased cooling costs; high regeneration energy causes low pressure Maximum steam flow demand and variable regeneration column size; large packed absorber required to provide sufficient mass transfer area for chemical reactions; high linear power loss due to overcoming pressure loss in regeneration column
The combination of the above factors led to the absorption and capture of CO by the amine-based solution. 2 Higher investment of the system, higher operating costs, among them, decarbonization and desorption of CO 2 The energy consumption of the process is large, which will increase the investment and operating costs of equipment by 70%, so reducing CO 2 The problem of high regeneration energy consumption in the capture process is conducive to the large-scale application of carbon capture process in coal-fired power plants
[0003] A large amount of existing research work is focused on the improvement of the amine-based solution absorption system, mainly for the development of new alcohol amine solutions and phase change solvents to reduce CO 2 High energy consumption and low absorption and desorption rates of the capture process
But due to the traditional CO 2 The desorption temperature is between 100°C and 150°C. In this temperature range, the large amount of gasification of water is the main energy consumption. Therefore, the CO 2 desorbs and ensures faster CO 2 Absorption and desorption rates could significantly improve current carbon capture processes

Method used

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  • Preparation method and application of heterogeneous catalyst for desorbing CO2 in solution
  • Preparation method and application of heterogeneous catalyst for desorbing CO2 in solution
  • Preparation method and application of heterogeneous catalyst for desorbing CO2 in solution

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Effect test

Embodiment 1

[0037] SO 4 2- / ZrO 2 -HZSM-5 catalyst preparation scheme: using ion exchange method, using Zr(SO 4 )2 4H 2 Ion exchange between O and HZSM-5 to synthesize SO catalysts with different zirconia contents 4 2- / ZrO 2 -HZSM-5.

[0038] 20g of Zr(SO 4 ) 2 4H 2 O was dissolved in 400mL deionized water, and after stirring evenly, 14g, 28, and 56g of HZSM-5 were added to the above solution respectively, and the resulting solution was stirred at 80-90°C for 24-48h, cooled to room temperature, and the obtained precipitate The material was centrifugally washed with deionized water for 5 times, then dried at 110-130°C for 12-24h, and finally calcined at 500-600°C for 4-6 hours at a heating rate of 5°C / min to obtain SO 4 2- / ZrO 2 -HZSM-5 white powder. Produced SO 4 2- / ZrO 2 -HZSM-5 heterogeneous catalyst material, in which ZrO is theoretically calculated 2 The mass is 7g, and the theoretically calculated ZrO 2 SO with three different zirconia contents at a mass ratio of...

Embodiment 2

[0040] Simulate the actual decarburization process and build a SO 4 2- / ZrO 2 -HZSM-5 heterogeneous catalytic desorption carbon capture process absorbs CO in liquid 2 Process plan, process flow such as Figure 8 As shown, the technological process is as follows:

[0041] The stainless steel screen plate is used as the substrate, and the heterogeneous catalyst SO is loaded on its surface 4 2- / ZrO 2 -HZSM-5, to obtain a plate-type catalyst, after treatment, the plate-type catalyst unit is assembled into a catalyst module 4, and a plurality of catalyst modules 4 are arranged at intervals along the height direction of the tower, using this structure CO 2 The absorption tower performs the decarburization process.

[0042] A plurality of catalyst modules 4 will be arranged at intervals along the tower height direction, and a plurality of non-interfering agitators 5 will be arranged below each layer of catalyst modules 4 to obtain CO 2 Desorption tower structure.

[0043] C...

Embodiment 3

[0045] The theoretically calculated ZrO prepared by embodiment 1 2 SO with three different zirconia contents at a mass ratio of 1 / 2, 1 / 4, and 1 / 8 to HZSM-5 4 2- / ZrO 2 -HZSM-5, named SZ@H-1 / 2, SZ@H-1 / 4 and SZ@H-1 / 8 respectively. Characterize it and study its structural information. ICP data (Table 1) XRD ( figure 1 ), SEM and TEM ( Figure 2a with Figure 2b ), and NH 3 -TPD and Py-IR spectra ( Figure 3a with Figure 3b ) is as follows, it can be determined that ZrO in the prepared catalyst 2 The content is 0.24-3.08wt.%, SO 4 2- / ZrO 2 Evenly dispersed on the surface of the catalyst to form uniformly dispersed active sites, in which ZrO 2 When the content is 3.08wt.%, it has the strongest acidity and the strongest active site.

[0046] Table 1 is the ICP and XRF results of three catalysts, when ZrO 2 When the mass ratio of HZSM-5 and HZSM-5 is 1 / 4, the prepared catalyst ZrO 2 and sulfate content are the most, so 1 / 4 is the best preparation ratio, and the actu...

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Abstract

The invention discloses a preparation method and application of a heterogeneous catalyst for desorbing CO2 in a solution, and belongs to the technical field of industrial boiler and power plant CO2 capture. The heterogeneous catalyst is prepared by loading SO4 < 2-> / metal oxide on an HZSM-5 carrier, and the method comprises the following specific steps: adding sulfate of a metal oxide into water,then adding an HZSM-5 carrier, heating and stirring, cooling and filtering to obtain a precipitate; and washing, drying and roasting the precipitate to obtain the SO4 < 2-> / metal oxide-HZSM-5 heterogeneous catalyst. The heterogeneous catalyst provided by the invention has the advantages that the absorption liquid can be promoted to desorb CO2, and the CO2 absorption performance of absorption liquid is improved; compared with the process of capturing the CO2 in the flue gas without adding a catalyst, the desorption rate is improved by 35-45%, the absorption efficiency is improved by 30-40%, thestability and the recycling performance are good, and the CO2 desorption energy consumption can be greatly reduced.

Description

technical field [0001] The invention belongs to industrial boiler and power plant CO 2 The technical field of capture, especially relates to a method for desorbing CO in solution 2 The preparation method and application of the heterogeneous catalyst. Background technique [0002] my country's energy structure is dominated by coal, and a large amount of CO is emitted after coal burning. 2 It will lead to the greenhouse effect and the extreme climate that comes with it. as CO 2 Largest source of emissions, CO from electricity production 2 accounted for 62.66% of the total source, therefore, from the control of CO 2 From the perspective of emissions, it is first necessary to control the CO emitted during the electricity production process. 2 . Applied to coal-fired power plant CO 2 There are three main technical routes of capture, which are divided into: post-combustion capture, pre-combustion capture and oxygen-enriched combustion. For a large number of existing power...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/40B01D53/14B01D53/18B01D53/86B01D53/62
CPCB01J29/405Y02A50/20Y02C20/40
Inventor 汪黎东邢磊魏可馨李蔷薇齐铁月
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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