scholarly journals FORMATION OF IMPURITIES IN SYNTHESIS GAS AT STAGE OF CONVERSION OF CARBON MONOXIDE TO HYDROGEN IN AMMONIA PRODUCTION

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

2020 ◽  
Vol 90 (6) ◽  
pp. 1173-1177
Author(s):  
A. A. Il’in ◽  
R. N. Rumyantsev ◽  
M. A. Lapshin ◽  
A. P. Il’in ◽  
D. S. Popov ◽  
...  

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

2021 ◽  
Vol 17 ◽  
Author(s):  
Siyamak Shahab ◽  
Masoome Sheikhi ◽  
Mehrnoosh Khaleghian ◽  
Marina Murashko ◽  
Mahin Ahmadianarog ◽  
...  

: For the first time in the present study, the non-bonded interaction of the Coniine (C8H17N) with carbon monoxide (CO) was investigated by density functional theory (DFT/M062X/6-311+G*) in the gas phase and solvent water. The adsorption of the CO over C8H17N was affected on the electronic properties such as EHOMO, ELUMO, the energy gap between LUMO and HOMO, global hardness. Furthermore, chemical shift tensors and natural charge of the C8H17N and complex C8H17N/CO were determined and discussed. According to the natural bond orbital (NBO) results, the molecule C8H17N and CO play as both electron donor and acceptor at the complex C8H17N/CO in the gas phase and solvent water. On the other hand, the charge transfer is occurred between the bonding, antibonding or nonbonding orbitals in two molecules C8H17N and CO. We have also investigated the charge distribution for the complex C8H17N/CO by molecular electrostatic potential (MEP) calculations using the M062X/6-311+G* level of theory. The electronic spectra of the C8H17N and complex C8H17N/CO were calculated by time dependent DFT (TD-DFT) for investigation of the maximum wavelength value of the C8H17N before and after the non-bonded interaction with the CO in the gas phase and solvent water. Therefore, C8H17N can be used as strong absorbers for air purification and reduce environmental pollution.


Energies ◽  
2020 ◽  
Vol 13 (4) ◽  
pp. 954 ◽  
Author(s):  
Hanne Kauko ◽  
Daniel Rohde ◽  
Armin Hafner

District heating enables an economical use of energy sources that would otherwise be wasted to cover the heating demands of buildings in urban areas. For efficient utilization of local waste heat and renewable heat sources, low distribution temperatures are of crucial importance. This study evaluates a local heating network being planned for a new building area in Trondheim, Norway, with waste heat available from a nearby ice skating rink. Two alternative supply temperature levels have been evaluated with dynamic simulations: low temperature (40 °C), with direct utilization of waste heat and decentralized domestic hot water (DHW) production using heat pumps; and medium temperature (70 °C), applying a centralized heat pump to lift the temperature of the waste heat. The local network will be connected to the primary district heating network to cover the remaining heat demand. The simulation results show that with a medium temperature supply, the peak power demand is up to three times higher than with a low temperature supply. This results from the fact that the centralized heat pump lifts the temperature for the entire network, including space and DHW heating demands. With a low temperature supply, heat pumps are applied only for DHW production, which enables a low and even electricity demand. On the other hand, with a low temperature supply, the district heating demand is high in the wintertime, in particular if the waste heat temperature is low. The choice of a suitable supply temperature level for a local heating network is hence strongly dependent on the temperature of the available waste heat, but also on the costs and emissions related to the production of district heating and electricity in the different seasons.


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