Deoxidizing reaction device for oxygen-containing coalbed methane

A technology of reaction device and deoxygenation reactor, which is applied in the direction of gas fuel, petroleum industry, chemical instruments and methods, etc., can solve the problems of poor catalytic reaction effect, short service life of catalyst, difficult plugging of tubes, etc., and achieve low CO generation The effect of carbon deposition amount, long catalyst life and high O2 removal rate

Inactive Publication Date: 2017-08-01
淄博赢信达知识产权咨询服务有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] 1. When high-pressure water is used as the heat exchange medium, it is limited by the steam pressure. When the reaction water temperature is above 250°C, the steam pressure of the water-cooling system is too high, which leads to the high pressure level and manufacturing cost of the reactor. It is used for coalbed methane deoxidation There are also great safety risks in the process; at the same time, the reaction temperature of coalbed methane deoxidation is high or the reaction and heat release are concentrated. When the noble metal combustion deoxidation catalyst with palladium and/or platinum as the main active component Concentrated reaction and exothermic heat, the bed temperature of the combustion deoxidation catalyst with one or more of copper, nickel, cobalt, manganese, molybdenum, and iron as the main active component is about 450-500°C, and rare earths such as cerium, lanthanum, etc. The bed temperature of

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  • Deoxidizing reaction device for oxygen-containing coalbed methane
  • Deoxidizing reaction device for oxygen-containing coalbed methane
  • Deoxidizing reaction device for oxygen-containing coalbed methane

Examples

Experimental program
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Example Embodiment

[0033] Example 1 is attached figure 2 The shown set of oxygen-containing coalbed methane deoxidation reaction test device mainly includes the main body of the catalytic reactor and the heat transfer and temperature control system;

[0034] The main body of the catalytic reactor is attached Image 6 As shown, it includes a shell 1, an axially structured catalyst reaction bed 2 and an inlet / outlet 15, a catalyst filling pipe 3, a catalyst unloading port 14, the lower part of the catalyst bed is filled with ceramic balls 11, and the reaction material in the catalyst bed The flow direction is top in and bottom out; the top is provided with a heat transfer medium distribution chamber 4 and a reflux chamber 21. The low-temperature heat transfer medium before heat absorption enters the heat transfer medium distribution chamber 4 through the heat transfer medium inlet, and distributes downward flow into the casing 10 In the inner tube 5, below the distribution chamber is the heat transf...

Example Embodiment

[0053] Example 2

[0054] After completing the above test, remove the Venturi suction mixer and high-pressure centrifugal fan in the heat transfer medium circulation pipeline, set up a molten salt circulation pump, and change it to attached figure 1 In the process, 53% potassium nitrate, 40% sodium nitrite, 7% sodium nitrate ternary eutectic mixed molten salt is used as the heat transfer medium, and the molten salt is circulated through the molten salt pump, and the by-product steam of the heat exchanger will circulate the molten salt. The heat in the medium was taken away and the temperature was reduced by about 30°C. Various process conditions were tested. Each process condition was operated for 48 hours. The temperature, pressure and flow conditions of the coalbed methane and the main composition before and after deoxidation are shown in Table 6 below. -8 listed. During the test, the molten salt pressure in the reflux chamber is controlled at about 5kPa by controlling the molt...

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Abstract

The invention discloses a deoxidizing reaction device for oxygen-containing coalbed methane. The deoxidizing reaction device for the oxygen-containing coalbed methane mainly comprises a vertical heat transfer sleeve pipe deoxidizing reactor, a heat transfer temperature control system, a heat transfer medium circulating and control assembly and a heat exchange device, wherein a heat transfer medium distribution chamber and a reflux chamber are arranged at a deoxidizing top; a vertical sleeve pipe is formed by nesting an inner pipe and an outer pipe, and extends downwards into a catalyst bed layer until the vertical sleeve pipe reaches the bottom part of the bed layer, and a heat transfer medium in the distribution chamber can flow downwards into the inner pipe, and then flow upwards into the reflux chamber via the outer pipe; the heat transfer medium circulating and control assembly and the heat exchange device are arranged in the reflux chamber and/or at the exterior of the reactor. The deoxidizing reaction device has the advantages that the circulating heat transfer temperature control is performed by the vertical heat transfer sleeve pipe deoxidizing reactor and normal-pressure or a low-temperature heat conduction oil, molten salt, nitrogen, carbon dioxide or overheated water steam heat exchange medium with temperature approximate to the temperature of the catalyst bed layer, a reaction heat point is eliminated, the reaction is stable and controllable, the running is safe, and the reaction effect is good; the service life of the catalyst is long, and the catalyst can be easily discharged out of the bottom part of the reactor in a replacing process; when the sleeve pipe with a small number of leakage is blocked off, the influence to the bed layer temperature and the reaction effect is small.

Description

technical field [0001] The invention belongs to the field of chemical reactors, in particular to a deoxidation reaction device for oxygen-containing coal bed gas. Background technique [0002] Coal bed methane, also known as gas, is the methane-containing gas extracted from coal mines before and during the mining process. The coal bed methane pumped out during the coal mining process contains more air, and is generally called oxygen-containing coal bed methane. At present, the oxygen-containing coalbed methane pumped out during the coal mining process in my country is limited by specific conditions, and only a few mining areas have utilized it, such as on-site power generation, deoxygenation and dehydration, and then entering the pipeline network to supply nearby markets or further processing to produce liquefied natural gas. Part of it is directly discharged into the atmosphere, which not only wastes energy, but also pollutes the atmosphere, because methane is a greenhouse g...

Claims

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Application Information

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IPC IPC(8): B01J8/02C10L3/10
Inventor 游夏宋睿哲游禄波
Owner 淄博赢信达知识产权咨询服务有限公司
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