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Production technology of catalyst for producing hydrogen by reforming methanol vapour at high temperature and application of catalyst

A technology of reforming hydrogen production and production process, which is applied in the chemical industry, can solve the problems of high requirements, uneconomical, waste of water resources, etc., and achieve the effects of saving costs and resources, small volume shrinkage, and good heat transfer effect

Active Publication Date: 2016-01-13
四川蜀泰化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The core of hydrogen production technology by steam reforming of methanol lies in the catalyst. The related catalysts have been extensively and in-depth researched, and most of them are copper-based catalysts. However, copper-based catalysts are mainly suitable for low-temperature environments of 210-300°C, and are not suitable for small High temperature environment of 300~550℃ required for mobile hydrogen production equipment and fuel cell use
In recent years, catalysts suitable for hydrogen production in high-temperature environments have mainly focused on Zn-Cr catalysts and noble metal catalysts. Although noble metal catalysts have attracted much attention due to their high activity and stability, their high prices are still difficult to adapt to the current hydrogen production market. need
Non-precious metal Zn-Cr catalysts mentioned in the Journal of Catalysis 10 (2006) by Cao Weiqiang, Chen Guangwen, etc., and non-noble metal catalysts mentioned in patent 00110041.6 with ZnO as the active component and part of Group VIII metals as active promoters , the preparation method is the co-precipitation preparation technology, this preparation method generally uses sodium carbonate as the co-precipitation agent, and the pH value is relatively high during the co-precipitation process, and a large amount of water is required to wash the precipitated filter cake ; This wastes water resources and causes a large amount of waste water to be treated, which is neither economical nor environmentally friendly. More importantly, there are still some sodium ions in the catalyst that are difficult to clean thoroughly, which affects the service life of the catalyst.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] The production process of a methanol water steam high -temperature reorganization hydrogen catalyst, which includes the following steps: the mixed water aluminum, titanium dioxide, citric acid, and graphite as raw materials, mixed to form mixed materials, The quality ratio of citric acid and graphite is: thin water aluminum 85, titanium dioxide 6, citric acid 1.5, graphite 2;The quality ratio is: mixed material 100, water 20, and the granularity of the mixed material after granules is 8 eyes. Then the mixed material after the granules is suppressed and shaped.2mm, 2mm height, and 1mm inner diameter; the hybrid material of the formation is 12h with a steam with a pressure value of 0.6MPa, and then the titanium dioxide aluminum oxide carrier is made at 700 ° C.Made of nitric acid metal salt hybrid solution in exfoliating water, the quality ratio of zinc oxide, chromium oxide, and oxide in metal salt in metal salt is: zinc oxide 75, chromium oxide 20, oxide 5;The total concent...

Embodiment 2

[0026]The production process of a methanol water steam high -temperature reorganization hydrogen catalyst, which includes the following steps: the mixed water aluminum, titanium dioxide, citric acid, and graphite as raw materials, mixed to form mixed materialsThe quality ratio of citric acid and graphite is: thin water aluminum 90, titanium dioxide 6, citric acid 1.5, graphite 2;The quality ratio is: 100 mixed materials, 30 water, the granularity of the mixed material after granules is 12 meters, and then the mixed material after the granules is suppressed and shaped.3mm, 3mm height, and 1.5mm inner diameter; the mixed material of the formation is 12h with steam with a pressure value of 0.9MPa, and then produced titanium dioxide aluminum oxide carrier at 850 ° C.Made in the deodorite water to make a nitric acid mixed solution, the quality ratio of zinc oxide, chromium oxide, and oxide in metal salts in nitrate is: zinc oxide 85, chromium oxide 10, oxide 5; mixture of metal salt mi...

Embodiment 3

[0029] The production process of a methanol water steam high -temperature reorganization hydrogen catalyst, which includes the following steps: the mixed water aluminum, titanium dioxide, citric acid, and graphite as raw materials, mixed to form mixed materialsThe quality ratio of citric acid and graphite is: thin water aluminum 88, titanium dioxide 7, citric acid 2.2, graphite 3;The quality ratio is: 100 mixed materials, 40 water, the granularity of the mixed material after granules is 10 mesh, and then the mixed material after the granules is suppressed and shaped.2.5mm, 2.5mm height, and 1.2mm inner diameter; the mixed material of the formation is 9h with a steam with a pressure value of 0.75MPa, and then the titanium dioxide aluminum oxide carrier is made at 780 ° C.The nitrate is soluble in the ionic water to make a nitrate metal salt hybrid solution. The quality ratio of zinc oxide, chromium oxide, and oxide in metal salts in nitrate is: zinc oxide 80, chromium oxide 17, oxi...

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Abstract

The invention discloses a production technology of a catalyst for producing hydrogen by reforming methanol vapour at a high temperature, and the application of the catalyst. According to the production technology disclosed by the invention, pseudo-boehmite, titanium dioxide, citric acid and graphite are used as raw materials for producing a catalyst carrier, besides, the carrier is pressed into a Raschig ring shape, and the catalyst can be suitable for a hydrogen production reaction by reforming the methanol vapour at the high temperature under the reaction condition of 300-600 DEG C; The production technology and the application of the catalyst disclosed by the invention have the beneficial effects that the catalyst does not use a noble metal catalyst, and besides, a conventional coprecipitation method is not selected for use, so that the cost and resources are greatly reduced, and the catalyst has an actual application value; the catalyst produced by the production technology disclosed by the invention uses the Raschig ring shape, so that the specific surface of the catalyst is larger, and the mass transfer effect and the heat transfer effect are better. The catalyst is simple to apply, and can be used when a reactor is directly heated to use temperature and raw gas can be used; in the process of heating, no physical water is drained, and the volume contraction of the catalyst is small.

Description

Technical field [0001] The invention involves the production process and application of hydrogen catalysts in the field of chemical industry, which specializes in a methanol water steam high -temperature reorganization hydrogen catalyst. Background technique [0002] Methanol has the advantages of low cost, high energy density, low carbon content, and convenient transportation and storage.There are three types of oxidation and reorganization. Among them, methanol water steam reorganization hydrogen is the highest response to the hydrogen content in the conversion gas. It has the advantages of low cost, mild condition, and small product composition. [0003] The core of methanol water steam reorganization hydrogen control is catalysts. The relevant catalysts have been widely and in -depth research. Most of the copper -based catalysts have been studied.The high -temperature environment required for mobile hydrogen equipment and fuel cells 300 ~ 550 ° C.In recent years, catalysts ar...

Claims

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Application Information

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IPC IPC(8): B01J23/10B01J32/00B01J21/06C01B3/32
Inventor 李华波许云波严会成李文静王灵翼
Owner 四川蜀泰化工科技有限公司
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