98/02034 Study on adsorptive removal of small amount of carbon monoxide from ammonia synthesis gas

1998 ◽  
Vol 39 (3) ◽  
pp. 185
Author(s):  
Tatyana V. Ivanova ◽  
Alexander A. Il'in ◽  
Ruslan N. Rumyantsev ◽  
Anastasia A. Kournikova ◽  
Alexander P. Ilyin

The article analyzes the work of the department for the conversion of carbon monoxide with water vapor to hydrogen as part of the ammonia synthesis unit. The effect of temperature and duration of operation of the medium-temperature conversion catalyst on the technical and technological parameters of the process is shown. The catalytic conversion of carbon monoxide is an important component of the hydrogen production process in the industrial technology of deep processing of natural gas. In modern ammonia synthesis units, the conversion process takes place in two stages: first, at a temperature of 360 – 430 °C on iron-chromium, and then at 190 – 260 °C on a copper-containing catalyst. It was found that along with the main products (H2, CO2), the presence of undesirable impurities of ammonia, amines, alcohols, acetates and formates was detected in the synthesis gas. It is shown that the main by-product at the stage of medium-temperature conversion is ammonia, the content of which in the condensate reaches 80-85%. Methanol is formed as a by-product both at the stage of medium-temperature (9-13%) and low-temperature conversion (87-91%). Most of the methanol generated during the conversion process is condensed with water in separators, while the rest goes to the CO2 removal system. In the separator, where the temperature is 160-162 °C, on average 68% of methanol remains in the gas phase, and in the separator, where deeper gas cooling is applied to 72 °C, about 81% of methanol remains in the condensate. To decrease the methanol content, it is necessary to lower the conversion temperature and increase the gas space velocity. Under the conditions of ammonia production from methanol and ammonia, a mixture of amines of varying degrees of substitution is formed, predominantly methylamine (CH3)NH2 and demytylamine (CH3)2NH2. Moreover, about 35-40% of the formed amines goes into condensate, and most of it remains in the gas phase and goes to the stage of cleaning from CO2. In the production of ammonia, solutions based on potash - K2CO3 are used to clean the converted gas from CO2, which absorb organic impurities, which are formed mainly at the stage of low-temperature conversion. Impurities impair the operation of the purification stage and cause foaming of solutions. One of the reasons for foaming is the presence of organic matter degradation products in the solution.


1961 ◽  
Vol 53 (8) ◽  
pp. 645-646 ◽  
Author(s):  
Holger C. Andersen ◽  
William J. Green

1961 ◽  
Vol 53 (10) ◽  
pp. 800-800
Author(s):  
Holger Andersen ◽  
William Green

Author(s):  
Carl D. Frohning ◽  
Christian W. Kohlpaintner ◽  
M. Gau ◽  
A. Seidel ◽  
P. Torrence ◽  
...  

2014 ◽  
Vol 875-877 ◽  
pp. 906-909
Author(s):  
Marlon José Bastidas Barranco ◽  
Orieta Ortiz Benavides ◽  
Gloria Patricia Jaramillo Álvarez ◽  
Y. Farid Chejne Janna

An important aspect in the combustion of coal for purposes of generating clean power is to achieve that this solid fuel is gasified and hereby to capture the residues across different mechanisms and to use the gas of synthesis in the production of energy. Gasification has been widely studied but the amorphous characteristics of solid fuels causes the gasification reactions do not obey a defined order, however has been made possible prosecute kinetics of these reactions and orient products of synthesis gas, according to needs. In this regard, for purposes of power generation the hydrogen production at high rates is a problem of stability of the synthesis gas combustion, therefore their generation in the gasification should be controlled by the generation of methane priority and carbon monoxide. The objective of this work is to provide guidance with a theoretical tool to establish the optimal mix of solid fuels in relation to the gasifying agents to produce a synthesis gas with appropriate levels of hydrogen, for which genetic algorithms are used due to approach a problem nonlinear and multiple variables. The variables that control the generation of products of synthesis gas, corresponds to the amount of steam and oxygen /air relative to fuel flow fed to the gasification reactor. The results show that there may be many possibilities for feeding the gasifier, but there are defined relationships that can control with some limitations the hydrogen production in convenient relationships with carbon monoxide. In the third multiobjetive runEn la tercera corrida del algoritmo multiobjetivo, se tiene la menor cantidad de cenizas y una participación muy alta de los carbones del Cesar en la mezcla. In the third run of the multiobjective algorithm, it has the least amount of ash and a very high share of coal in the mix of Cesar.


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