Self-heating reactor for preparing methane through catalytic hydrogenation of carbon dioxide
A carbon dioxide and catalytic hydrogenation technology, which is applied in the production of hydrocarbons from carbon oxides, chemical instruments and methods, organic chemistry, etc., can solve the problems of poor heat exchange effect, low reaction heat utilization efficiency, complex design, etc. energy consumption, saving cooling energy consumption, and the effect of simple structure
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0027] A factory uses figure 1 The autothermal carbon dioxide catalytic hydrogenation to methane reactor shown: the reactors are connected in parallel; the tubular shell 1 is cylindrical, the length-diameter ratio is 20; the number of reaction tubes 2 in a single reactor is 80, The inner diameter is 20mm; the arrangement of the reaction tube 2 on the upper sealing plate 5 and the lower sealing plate 6 is an equilateral triangle, and the opening rate of the ventilation holes 11 on the upper sealing plate 5 is 20%; The shell 10 of the upper sealing section is an oval head; the shell side 4 is provided with a spiral baffle plate to strengthen the heat exchange between the tube side and the shell side.
[0028] The raw material gas first enters the shell side 4 between the tubular shell 1 and the reaction tube 2, is heated by the reaction tube 2, and then enters the upper sealing section shell 10 through the vent hole 11 Then, the methanation reaction occurs in the tube-side cata...
Embodiment 2
[0030] A factory uses figure 1 The autothermal carbon dioxide catalytic hydrogenation to methane reactor shown: a single reactor is used, the tubular shell 1 is cylindrical, the aspect ratio is 10; the number of reaction tubes 2 in the reactor is 150, and the inner diameter is 30mm The reaction tube 2 is arranged in a square staggered arrangement on the upper sealing plate 5 and the lower sealing plate 6, and the opening rate of the ventilation holes 11 on the upper sealing plate 5 is 12%; The segment shell 10 is a hemispherical head; the shell side 4 is provided with structured packing to strengthen the heat exchange between the tube side and the shell side.
[0031] The raw material gas first enters the shell side 4 between the tubular shell 1 and the reaction tube 2, is heated by the reaction tube 2, and then enters the upper sealing section shell 10 through the vent hole 11 Then, the methanation reaction occurs in the tube-side catalyst of the reaction tube 2, and the mat...
PUM
| Property | Measurement | Unit |
|---|---|---|
| porosity | aaaaa | aaaaa |
| aspect ratio | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 
