Method for co-production of synthesis gas by carbonate hydrogenation refining for carbon dioxide emission reduction

A technology of carbon dioxide and carbonate, applied in the direction of carbon monoxide, calcium/strontium/barium oxide/hydroxide, silicate, etc., can solve problems such as ecological environment impact, increase production cost, and emit large carbon dioxide, and achieve reduction Decomposition temperature, improving economic benefits, and mitigating the effects of the greenhouse effect

Pending Publication Date: 2021-11-02
BEIJING UNIV OF CHEM TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this process usually involves extreme conditions such as high temperature, which not only increases production costs, but also emits a large amount of carbon dioxide, which has a serious impact on the global ecological environment.
The development of metal oxide preparation methods without carbon dioxide emissions is one of the effective ways to achieve sustainable development. It has become a key scientific and technical issue that related industries urgently need to overcome. In addition, how to reduce the preparation cost by optimizing production conditions is still a huge challenge. challenge

Method used

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  • Method for co-production of synthesis gas by carbonate hydrogenation refining for carbon dioxide emission reduction
  • Method for co-production of synthesis gas by carbonate hydrogenation refining for carbon dioxide emission reduction
  • Method for co-production of synthesis gas by carbonate hydrogenation refining for carbon dioxide emission reduction

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Effect test

Embodiment 1

[0025] like figure 1 as shown,

[0026] Carry out the concrete steps of calcium carbonate hydrogenation refining calcium oxide co-production synthesis gas with the inventive method as follows:

[0027] Using nickel-iron hydrotalcite as the anode, commercial Pt / C catalyst as the cathode, and an applied voltage of 2V, hydrogen is produced by electrolysis of water. The prepared gas is directly connected to the tube furnace after passing through the recovery system and the filtration system, and the gas flow rate of hydrogen is set to 100mL / min; 10g of calcium carbonate is placed in the tube furnace, and the pyrolysis temperature is set to 800°C, and the heating rate is The temperature is 10°C / min, and the reaction time is 60min. Calcium oxide product is obtained after roasting, and H in the syngas 2 The ratio with CO is 2:1. By adjusting the flow rate of hydrogen gas, the H in the resulting syngas can be controlled 2 The ratio range with CO is between (1:4) and (4:1).

[002...

Embodiment 2

[0030] Carry out the concrete steps of calcium carbonate / silicon dioxide hydrogenation refining calcium silicate co-production synthesis gas with the inventive method as follows:

[0031] Using cobalt-iron hydrotalcite as the anode, commercial Pt / C catalyst as the cathode, and an applied voltage of 2V, hydrogen is produced by electrolysis of water. The prepared gas is directly connected to the tube furnace after passing through the recovery system and the filtration system, and the gas flow rate of hydrogen is set to 200mL / min; 50g of calcium carbonate / silicon dioxide mixed material (molar ratio is 1 / 1) is placed in the tube In the furnace, the pyrolysis temperature is set to 850°C, the heating rate is 5°C / min, and the reaction time is 200min. Calcium silicate product is obtained after roasting, and H in the synthesis gas 2 The ratio to CO is 1 / 1. By adjusting the flow rate of hydrogen gas, the H in the resulting syngas can be controlled 2 The ratio range with CO is between ...

Embodiment 3

[0034] Carry out the concrete steps of magnesium carbonate hydrogenation refining magnesium oxide co-production synthesis gas with the inventive method as follows:

[0035] With nickel-iron hydrotalcite as the anode and commercial Pt / C catalyst as the cathode, the light intensity was 100mW cm -2 , the applied voltage is 0.6V, and the production of hydrogen is realized through photoelectric water splitting technology. The prepared gas is directly connected to the tube furnace after passing through the recovery system and the filtration system, and the gas flow rate of hydrogen is set to 100mL / min; take 20g of magnesium carbonate and place it in the tube furnace, set the pyrolysis temperature to 900°C, and the heating rate The temperature is 20°C / min, the reaction time is 100min, the magnesium oxide product is obtained after roasting, and the H in the syngas 2 The ratio to CO is 1 / 1. By adjusting the flow rate of hydrogen gas, the H in the resulting syngas can be controlled 2...

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Abstract

The invention discloses a method for co-production of synthesis gas by carbonate hydrogenation refining for carbon dioxide emission reduction. The method comprises the following steps: i) preparing hydrogen by using renewable energy source driving; and ii) taking the hydrogen obtained in the step i) as a reduction reaction gas, carrying out co-heat treatment on the reduction reaction gas and metal carbonate to obtain a metal oxide, and completing in-situ preparation of synthesis gas through carbon dioxide hydrogenation. According to the method, green hydrogen prepared from renewable energy reacts with metal carbonate to efficiently prepare metal oxide and synthesis gas, so that zero emission of carbon is realized, the greenhouse effect is relieved, the decomposition temperature of carbonate is greatly reduced, carbon emission reduction in cement, refractory and other industries is realized, and the problem of high cost of carbon dioxide hydrogenation can be solved; and meanwhile, synthesis gas with high additional value can be obtained and can be directly put into use or prepared into other high-value chemicals through a Fischer-Tropsch synthesis reaction, so that the economic benefit of oxide preparation is further improved, and the method has a wide application prospect.

Description

technical field [0001] The invention belongs to the technical field of preparing metal oxides from carbonates, and in particular relates to a method for carbon dioxide emission reduction by hydrogenation refining of carbonates for co-production of synthesis gas. Background technique [0002] Metal oxides have attracted people's attention due to their excellent thermal stability and good chemical stability, and are widely used in the production of cement, steel, refractory materials, catalysts, magnetic materials, fluorescent materials, etc. At present, the most common way to prepare metal oxides in industry is to obtain metal oxides by pyrolysis of metal carbonates. However, the process usually involves extreme conditions such as high temperature, which not only increases the production cost, but also emits a large amount of carbon dioxide, which has a serious impact on the global ecological environment. The development of metal oxide preparation methods without carbon diox...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F5/02C01F5/06C01F11/02C01F11/06C25B1/04C01B3/02C01B32/40C01B33/24
CPCC01F11/02C01F11/06C01B32/40C01B3/02C25B1/04C01B33/24C01F5/02C01F5/06C01P2002/72C01P2004/03C01P2004/62Y02E60/36Y02P20/133
Inventor 邵明飞徐明谢文富薛振李诗瑾卫敏段雪
Owner BEIJING UNIV OF CHEM TECH
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