Method and apparatus for utilizing plant waste gas to prepare natural gas
A natural gas and exhaust gas technology, applied in the field of chemical engineering, can solve the problems affecting the conversion rate of synthetic methane and the decrease of methane equilibrium constant, and achieve the effects of increasing methane synthesis rate, reducing power consumption and protecting the environment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0032] use as image 3 The process flow shown is from the factory waste gas 1 (the synthetic ammonia plant contains H 2 , N 2 relaxation gas) to purify and remove ammonia, together with purified factory waste gas 2 (including CO 2 Decarburization and desorption gas), the total gas volume is 1000Kmol / h, under the pressure of 2MPa, in a vertical tube-wound water-cooled reactor equipped with a nickel-based TiO carrier methanation catalyst, at a space velocity of 3000h -1 CO 2 Hydromethanation reaction, after cooling to remove water, CH 4 About 50%, N 2 40% of the product gas is 4959Kmol / h, separated by pressure swing adsorption to obtain CH 4 88% of the product gas is compressed to 25MPa to obtain 2580Kmol / h compressed natural gas for vehicles.
Embodiment 2
[0034] Such as Figure 4 The shown device of the present invention comprises steam drum 101, water pump 102, methanation synthesis reactor 103, tower front heat exchanger 104, start-up heater 105, water cooler 106, water separator 107, methane concentration device 108, compression machine 1010 and steam turbine 109, the methanation synthesis reactor 103, tower front heat exchanger 104, water cooler 106, water separator 107, methane enrichment device 108, compressor 1010 and steam turbine 109 Connected in sequence, the methanation reactor 103 is also externally connected with a steam drum 101 , a water pump 102 and a start-up heater 105 , and the steam drum 101 is also connected with a steam turbine 109 .
[0035]The start-up heater 105 can be a steam injector, or an electric heater installed on the inlet pipeline between the pre-column heat exchanger 104 and the methanation synthesis reactor 103 .
[0036] The purified industrial waste gas advances to the pre-tower heat excha...
Embodiment 3
[0038] Figure 5 A water-cooled coiled-tube reactor is used as the methanation synthesis reactor ( Figure 5 Other equipment in the device are not shown, and the composition and connection of the rest of the equipment are the same as the schematic diagram of embodiment 2). This water-cooled coiled tube reactor is an invention patent (application number 201210033806.1, application date February 14, 2012) that the applicant has applied for ) in a reactor, including a shell 1 and a heat exchange element, the top of the shell 1 is provided with an air inlet 3 and a manhole 4, the air inlet 3 is equipped with a gas distribution plate 81, and the lower part of the shell is provided with a For headers with tube sheets: inlet header 9a and outlet header 9b. The inner and outer rings or the tops of two adjacent heat exchange tubes 2 with the same ring diameter are connected by an inverted U-shaped elbow to form an arrangement of an uplink heat exchange tube and a downlink heat exchang...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 