Field of invention:
This invention relates to a novel method of generating hydrogen gas from water.
Background of invention:
Hydrogen is emerging as the favorite alternative to fossil fuels. Presently, hydrogen is primarily used as a feedstock, intermediate chemical, or, on a much smaller scale, a specialty chemical. Only a small portion of the hydrogen produced today is used as an energy carrier, mostly by the Aerospace industries. Automotive industries are developing new models that run on either hydrogen based internal combustion engines (ICEs), or gasoline - fuel cell cars. However, most of the commercial hydrogen production processes are not considered as renewable as these technologies merely shift the source of pollution from a distributed one (like cars, households for example) to a more concentrated source like a hydrogen producing plants or thermal power plants. The United States hydrogen industry alone currently produces nine million tons of hydrogen per year for use in chemicals production, petroleum refining, metals treating, and electrical applications.
The technologies for the utilization of hydrogen as a fuel are at a more advanced stage today than the technologies for the efficient production of

hydrogen from renewable resources like solar energy, wind, tidal energy or geo-thermal energy. There is an immediate need to develop better, more efficient and inexpensive technology for the production of hydrogen from renewable resources and bridge this gap between the production and consumption technology of hydrogen and attain a synergy between the two segments. The National Hydrogen Energy Road map of Government of India has also given prominence on development of advanced production techniques and application of technologies based on hydrogen fuel.
The electrolytic process is used worldwide for production of hydrogen gas. Currently, this method is used to produce high purity hydrogen. The cost of hydrogen produced using this method is significantly higher and hence, it is used only in specialty applications like semiconductor manufacture. But this method can facilitate more distributed hydrogen generation using electricity made from renewable and nuclear resources and will help to cater local requirements with minimum distribution and storage requirements [I]. The primary by-product of this process is oxygen. Steam-methane reforming process is also used widely for the hydrogen production. In this catalytic process natural gas or other light hydrocarbons are reacted with steam to produce a mixture of hydrogen and carbon dioxide. The high-purity hydrogen is then separated from the product mixture. This method is the most energy-efficient commercialized technology currently available, and is most cost-effective when applied to large, constant loads. Partial oxidation of fossil fuels in large gasifiers is another method of thermal hydrogen

production. It involves the reaction of a fuel with a limited supply of oxygen to produce a hydrogen mixture, which is then purified. Partial oxidation can be applied to a wide range of hydrocarbon feedstock, including natural gas, heavy oils, solid biomass, and coal. Its primary by-product is carbon dioxide.
Emerging methods hold the promise of producing hydrogen without carbon dioxide emissions, but all of these are still in early development phases. Some of these technologies are thermo-chemical water-splitting using nuclear and solar heat, photolytic (solar) processes using solid state techniques (photo-electrochemical, electrolysis), fossil fuel hydrogen production with carbon sequestration, and biological techniques (algae and bacteria).
Objects of the invention:
An object of this invention is to propose a novel method of producing hydrogen gas from water.
Another object of this invention is to propose a novel method of producing hydrogen gas from water in presence of carbonaceous waste material and catalytic fluxes.
Further object of this invention is to propose a novel method of producing hydrogen gas from water wherein molten slag is used for the

the rmo-chemical decomposition of water.
Still further object of this invention is to propose a novel method of producing hydrogen gas from water which is simple and cost effective.
Statement of invention:
According to this invention there is provided a novel method for producing hydrogen gas from water comprising adding water to the slag and carbonaceous flux to produce hydrogen by thermo-chemical decomposition of water.
Brief description of the accompanying drawings:
The invention is explained in greater details with the accompanying drawings:
Fig la shows the Effect of water addition on the concentration of FeO and Fc203 in the slag and formation of H2gas, based on results of computation of
Water - Slag phase equilibria at 1873 K.
Fig lb relates to a plot of enthalpy of water - slag system verses water

addition, based on results of computation of Water - Slag phase equilibria at 1873 K. (b).
Fig 2 shows the effect of water addition on the concentration of FeO and Fe203 in the slag and formation of H2, CO and CO2 gases computed using FACT-sage programme.
Fig 3 shows the experimental set-up for hydrogen production.
Fig 4 shows the line diagram and schematic of the set-up for hydrogen production in the slag pit at plant level.
Detailed description of the invention:
A novel method is developed for production of hydrogen gas by water and slag reactions in presence of carbonaceous waste materials and catalytic fluxes. The overall reaction of hydrogen gas formation is:
H20+xC+2yFeO T> H2+CO+zCC2 + yFe2Oi+H20
Where A is amount of water added in the system, x is amount of C available in the flux, y is FeO in the slag and z formation of CO2 by reaction between

CO and water. In this novel process, slag not only provides sensible heat for endothermic water decomposition reaction but also arrest the reverse reactions between hydrogen and oxygen gas. The Fe and lower oxides of Fe in the slag react with oxygen gas in fee product gas mix and form Fe203 and thereby reduce the thermodynamic activity of oxygen. Different types of wastes, which can act as a deoxidizer, can be used as a flux to improve the production of hydrogen gas.
Thermal decomposition of pure water in presence of slag:
The sensible heat of molten slag can be used for the thermo-chemical decomposition of water. In this process slag acts as heat sources and some of the deoxidizing constituents (Fe, FeO) in the slag also take part in the decomposition reaction (1) by reacting with nascent oxygen via reaction (2):
H20 —T-> H2 + 1/2-02 AH 1873K = 362 kJ / mole of
water --(1)
2 FeO + 1/2 02 —T % Fe203 ΔH1873K = - 175 kJ / mole of
FeO --(2)
The exothermic oxidation reaction provides additional energy required for reaction (1) and also reduces the oxygen partial pressure of the system and thereby enhances the rate of formation of hydrogen gas. The phase equilibria

data was computed for reaction between 100 g LD slag with water at 1600 C. The amount of water varied from 0 to 100 ml to study the effect of water to slag ratio on hydrogen gas generation. The results of computation are presented in Figures la and b. The Figure la shows effect of water addition on the formation of hydrogen gas and changes in the concentration of FeO and Fe203 in the slag. The enthalpy of the system at different water addition is shown in Figure lb, which shows that enthalpy of 100 gm slag can
support reaction with op to 11.3 ml of water, any further addition of water will need additional energy input. Therefore theoretically reaction of 1 kg slag and 113 ml water will form 0.8 moles i.e. 19.2 liters of hydrogen gas without any energy input at 1873 K temperature.
Thermal decomposition of pure water in presence of slag and carbonaceous flux:
The carbonaceous and other plant wastes materials such as coal fines, coke breeze, etc. can be used as deoxidizer which will enhance formation of hydrogen by thermo-chemical decomposition of water. The reactions between water and carbon are:
H2O + c —->T H2 + CO AH in? K = 133 kJ / mole of
H2O --(3)
H2o + CO --> H2 + COi ΔH1873 K = -27 kJ / mole of
H2O -(4)

Phase equilibrium data of 100 gm slag and ml water and 10 gm carbon was computed for 1873 K temperature and results of computation are shown in Figure 2. The results computation revealed that the addition of excess water than stoichiometric requirement for carbon reaction enhances the production of hydrogen gas. The excess water reacts with CO gas in the system at high temperature and form CO2 gas. If = 5.55 mole (100 ml) and x = 0.20 mole then energy required for formation of 1.20 moles of H2, 0.46 moles of CO and 0.37 moles of C02 at 1873 K is ΔH1873 K = 740 kJ. Enthalpy of 1 kg slag at 1900 K = = ΔH1900mx = - 2120 kJ. Theoretically, reaction of 100 ml water and 10 gm carbon will generate 1.20 moles i.e. 26.9 ltrs of hydrogen gas at 1600 C and using sensible heat of 350 gm slag. (H2O : C ratio = 10:1). Therefore, theoretically reactions between 1 kg of slag can produce ~ 70 ltrs of the gas. Considering the lower efficiencies of formation reaction and heat transfer processes and other kinetic limitations, practically process can generate - 10 liters of hydrogen gas per kg of slag.
The innovative devices (laboratory and plant) have been designed and fabricated for production of hydrogen gas using the steel plant slag as a heat source. The device designed can effectively harvest the product gas with > 35% hydrogen using waste heat from slag.
The experimental set-up designed to study the reactions of molten slag and water is shown in Figure 3. Standard procedure (step-by-step) followed during conducting experiments using set-up, shown in Figure 3, is described

below:
Before starting the experiments, the condenser (6) and gas collection (11) tanks were first evacuated using vacuum pump (13), for removal of residual air and generation of negative pressure for flow of gas in the tanks. The system was isolated from surrounding by closing valves (6, 12) before experiment The granulated slag from LD steel plant was melted in the induction furnace and superheated to -1650 - 1700 C. The molten slag was poured in the pre-heated graphite crucible (1). The reaction hood (2) was then kept on the crucible. The controlled amount of water was sprayed on molten slag surface through water line (3). The product gases were formed by reactions between water, deoxidizers in the slag, and carbon from the crucible, as discussed in above sections. The product gas of the reactions was collected from the hood (2) via steel tube (4) connected to the tank. During experiment, the product gas samples were collected from the sample port (5) for chemical analysis. The product gas was passed through condenser tank (7) by opening gas valve (6). The condenser tank (7) was cooled by water stored in the outer tank (8). The products gas after removal / stripping of the steam was then collected in the gas collection tank (11) by opening the gas flow control valves (9, 10). The gas samples from condenser tank and gas collection tank were collected by connecting the gas sampler to the valves (9) and (12) respectively. The condensed water from the condenser tank (7) was removed by opening the valve (14) connected at the bottom of the condenser tank (7).

Typical analysis of the gas samples collected from sample port (5), condenser tank (7) and collection tank (ll)is given below:
(Concentration in Vol %)
Sample/
H2 CO CO2 02 CH4 CmHn N2 Constituents
Port [5] 22.8 11.2 7.0 3.0 6.2 0.6 33.4
Condenser tank [7] 23.0 1.6 1.2 1.2 2.0 1.0 70.0
Collection tank [11] 20.0 1.8 Nil 2.0 4.0 1.2 71.0
Set-up for plant tests:
The set-up designed and fabricated for conducting trials in the slag pit at LD#2 steel plant is shown in Figure 4. Standard procedure (step-by-step) followed is described below:
The experiments were carried out in slag pit in steel making unit, LD#2. The slag dumping procedure of the LD#2 steel pot is briefly described. In the plant slag from the converter vessel (batch wise) is collected in the slag pot of ~25 tonne capacity. The slag pot is then transferred to the slag dumping area by slag trolley. After arrival of the slag pot trolley in slag pit area, the pot is removed from the trolley by overhead crane and slag is then poured in the slag pit It takes about 2 days to fill the slag pit. Once pit is completely filled with slag, slag is cooled for some time and then it is quenched by spraying water jets from sides and top. It takes about a day to cool the slag in

the pit. During cooling of slag, large volume of steam is released in air. After cooling the slag is removed from the pit by dumper and is transported to slag processing area The trials were carried out in the pit which was almost full.
Before starting experiment, the entire set-up including gas collection tank (11) and condenser tank (7) were evaluated using vacuum pump (13). The pressure in the tank was monitored using the compound gauge (15) attached to condenser tank (7). Once compound gauge registered -500 mm reading, the set-up i.e. tanks were isolated by closing valves (6, 12, 17, and 18). After slag was poured in the pit by crane, the experimental set-up, as shown in Figure 2, mounted on the trolley (24) was moved close to slag pit by using tractor. When trolley with set-up reached to the marked area, first the flux containing carbonaceous material was sprayed on the molten slag surface by using polythene container bags, then the reaction hood (2) was lowered using chain-pulley block system (23) and placed on the hot slag surface. For positive isolation from surrounding atmosphere, high temperature ceramic fibre wool (25) was fixed on the edge of reaction hood (2). After placing of the hood (2) on the slag surface, the water inlet valve (20) was opened and water flow was monitor through flow indicator (21) connected to the water inlet line. The water was then sprayed uniformly on the surface of the molten slag by water nozzle (26). The product gases were formed by reactions between water-slag-flux as described earlier. Immediately after opening the water inlet valve (20), the gas blower (22) was switched ON and valve (19) was opened to remove the air and steam from the gas pipe line,

once product gas with steam started coming out from the exhaust pipe of the blower (22), the valve (19) was closed and valve (6) was opened slowly. The product gas samples were collected by opening valve (5) and by connecting gas sampler. When gas pressure in the tank reached + 800 mm (compound gauge (15) the gas valve (6) was closed and gas valve (19) was opened. After that the reaction hood (2) was moved up using pulley chain block system (23) and water inlet valve (20) was closed. Then trolley (24) was moved away from the slag pit. The gas samples were collected from condenser (7) and collection (11) tanks using samples ports connected to valves (17 and 18). After sample collection the set-up was evacuated as described before for next experiment. Explosive diaphragms were provided on both collection and condenser tanks to protect the system from any explosion as product gas contained > 30% hydrogen and < 10% CO gases which are explosive and inflammable.
Typical analysis of the gas samples collected from sample port (5) is given below:
Sample /

This invention relates to a method for producing hydrogen gas from water comprising adding water to a mixture of (a) a molten slag comprising iron and iron oxides and (b) carbonaceous flux to produce hydrogen by thermo-chemical decomposition of water.