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1 Nm3/h
10 Nm3/h
100 Nm3/h
500 Nm3/h
1000 Nm3/h
1500 Nm3/h
99,998%
99,998%
99,998%
99,998%
99,998%
99,998%
H2 outlet pressure
350 bar;
700 bar
(optional)
350 bar;
700 bar
(optional)
350 bar;
700 bar
(optional)
350 bar;
700 bar
(optional)
350 bar;
700 bar
(optional)
350 bar;
700 bar
(optional)
from -20°C to +40°C normal,
from -40°C to +50°C optional
from -20°C to +40°C normal,
from -40°C to +50°C optional
from -20°C to +40°C normal,
from -40°C to +50°C optional
from -20°C to +40°C normal,
from -40°C to +50°C optional
from -20°C to +40°C normal,
from -40°C to +50°C optional
from -20°C to +40°C normal,
from -40°C to +50°C optional
1,8x2x1
2,98x2,43x2,59
6x2,4x2,6
2*(6x2,4x2,6)
4*(6x2,4x2,6)
6*(6x2,4x2,6)
*6 х 2,4 х 2,6 m – 20-foot container, 100Nm3/h plant consists of one 20-foot container.
High yield and quality of hydrogen fuel, corresponding to type I – III GOST R ISO 14687-1-2012
COST PRICE CALCULATOR OF 1 Nm3 H2
0 Rub.
Steam reforming reactor
Desulphurisation
PROX reactor
Separation and purification systems
The reforming phase is combined with low-temperature and high-temperature water-shear reaction. In an adiabatic reactor with a catalyst, the initial hydrocarbon feedstock is converted into synthesis gas (a mixture of hydrogen and carbon monoxide). In the water-shear reaction CO is converted into CO2 and additional hydrogen is produced. Methane conversion is 99.3%
To provide long service life, high system efficiency, and avoid deactivation of the reforming catalyst, the hydrocarbon feedstock is desulfurized before the reforming phase
At this phase, under the influence of oxygen, full oxidation of CO into CO2 is occurred
At this stage hydrogen is separated from impurities - methane residues, CO, CO2, water vapor, oxygen. The purification stage is necessary to eliminate the risk of fuel elements poisoning by CO and CO2 impurities. According to the All-Union State Standard R 55466-2013/ISO/TS 14687-2:2008 the purity of the hydrogen fuel for fuel cells has to be more than 99,99%.
Two solutions can be integrated into the hydrogen generation unit: short-cycle adsorption or membrane separation.
Low noise and vibration level
High noise and vibration level
High noise and vibration level
High noise and vibration level
Fuel consumption is 45% lower than that of gasoline
*
Fuel consumption is 10% lower than that of gasoline
Fuel consumption is 15-20% lower than that of gasoline
~ 14 – 15 rub.
16 - 35 rub.
10 -15 rub. (CNG)
10 - 25 rub.
Maintaining its operational properties for a long time
Maintaining its operational properties for a few months
Maintaining its operational properties for a long time
Maintaining its operational properties for 6 months
Maintenance service once a year.
Equipment diagnostics every 50-70 engine hours. Maintenance service every 150-200 hours.
Equipment diagnostics every 50-70 engine hours. Maintenance service every 250-300 hours.
Equipment diagnostics every 50-70 engine hours. Maintenance service every 250-300 hours.
* Selected as a base case
Steam reforming reactor
Desulphurisation
PROX reactor
Separation and purification systems
The reforming phase is combined with low-temperature and high-temperature water-shear reaction. In an adiabatic reactor with a catalyst, the initial hydrocarbon feedstock is converted into synthesis gas (a mixture of hydrogen and carbon monoxide). In the water-shear reaction CO is converted into CO2 and additional hydrogen is produced. Methane conversion is 99.3%
To provide long service life, high system efficiency, and avoid deactivation of the reforming catalyst, the hydrocarbon feedstock is desulfurized before the reforming phase
At this phase, under the influence of oxygen, full oxidation of CO into CO2 is occurred
At this stage hydrogen is separated from impurities - methane residues, CO, CO2, water vapor, oxygen. The purification stage is necessary to eliminate the risk of fuel elements poisoning by CO and CO2 impurities. According to the All-Union State Standard R 55466-2013/ISO/TS 14687-2:2008 the purity of the hydrogen fuel for fuel cells has to be more than 99,99%.
Two solutions can be integrated into the hydrogen generation unit: short-cycle adsorption or membrane separation.
High-energy intensity: in terms of energy per unit weight hydrogen outnumbers gasoline by a ratio of 3 (143 MJ/kg vs. 47 MJ/kg)
Quick refueling time – 3-5 minutes
Car range with a fuel cell on a single refueling – 500-600 km
Car capacity with a fuel cell – 114kW
Zero harmful emissions
High flight duration
Noiseless operation
Low heat generation
Fast refueling (2-3 min)
Lightweight fuel
Eco-friendliness
Methane
Hydrogen
Hythane is a high-purity fuel type, consisting of H2 mixture and natural gas, with a hydrogen content of 5- 10% wt. (20-40% vol.).
50%
23%
16%
7%
Backup power reliability is extremely important for enterprises of the industrial sector, healthcare facilities, data collection and storage centers, etc. Fuel cell power generators are the ultimate solution for use as power backup sources.
Process gases are used in most of the manufacturing sectors and are supplied mainly by automobile transport in cylinders to the area of consumption. On-site hydrogen generation at specialized plants is a relatively reliable and profitable method compared to automobile hydrogen supply.
Thus, containerized plants with a capacity from 100Nm3 to 2000Nm3 can fully provide various petrochemical and basic organic synthesis facilities with technological gases.
Steam reforming and electrolysis are highly efficient technologies of hydrogen obtaining.