Nuclear Production of Hydrogen, Fourth Information Exchange ...
Nuclear Production of Hydrogen, Fourth Information Exchange ... Nuclear Production of Hydrogen, Fourth Information Exchange ...
TRANSIENT MODELLING OF S-I CYCLE THERMOCHEMICAL HYDROGEN GENERATION COUPLED TO PEBBLE BED MODULAR REACTOR Introduction Hydrogen is a candidate for an all purpose energy carrier. Since the American oil crises of the 1970s, hydrogen has been regarded as an attractive supplement or replacement for fossil fuels as an energy carrier. The recent rapid development in the area of fuel cells and fuel cell powered vehicles yields additional impetus to the development of hydrogen as an energy carrier. Hydrogen has an energy density from combustion of around 120 MJ/kg, in comparison natural gas has an energy density of 43 MJ/kg, gasoline has an energy density of 44.4 MJ/kg, and ethanol has an energy density of 26.8 MJ/kg (Thomas, 2001). The waste product of hydrogen combustion is water, which is a great environmental advantage of hydrogen compared to the fossil fuels. Hydrogen is the most abundant element in the universe. Hydrogen is also very chemically reactive, and thus it is not found on Earth in its elemental form. The major challenges in shifting to a hydrogen economy involve generation, storage and transportation of hydrogen. The most common current method of hydrogen generation is hydrocarbon extraction, typically from natural gas (Rostrup-Nielsen, 2005). The fundamental problem with this method is that it retains an inherent reliance on fossil fuels and emits greenhouse gases. Thus, neither the problem of energy reserves nor the problem of carbon emission is solved. A carbon-free method of hydrogen generation that is independent of fossil fuel supplies is required for a sustainable hydrogen economy. Water covers more than two-thirds the surface of the Earth, however directly splitting water into hydrogen and oxygen requires temperatures of above 2 200 K (Kogan, 2000). There are few terrestrial heat sources capable of providing such temperatures on a large scale. In addition to direct splitting of hydrogen, there is also the option of a thermochemical cycle. A thermochemical cycle consists of a series of chemical reactions performed in parallel, of which the overall reaction is the splitting of water. Thermochemical cycles still require high temperatures, on the order of 1 100 K (Brown, 2003). There are several heat sources under consideration for driving thermochemical cycles, namely nuclear energy. Two of the primary candidates for use as thermochemical water-splitting cycles are the sulphur-iodine cycle and the Westinghouse hybrid sulphur cycle. A potential driving scheme for a thermochemical cycle is shown in Figure 1. Figure 1: Nuclear hydrogen generation scheme The sulphur-iodine (S-I) cycle consists of three chemical reaction steps expressed as sections: • Section 1 (Bunsen reaction, 393 K): I 2 + SO 2 + 2H 2 O → 2HI + H 2 SO 4 • Section 2 (sulphuric acid decomposition, 1 123 K): H 2 SO 4 → H 2 O + SO 2 + 1/2O 2 • Section 3 (hydrogen iodide decomposition, 773 K): 2HI → H 2 + I 2 364 NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010
TRANSIENT MODELLING OF S-I CYCLE THERMOCHEMICAL HYDROGEN GENERATION COUPLED TO PEBBLE BED MODULAR REACTOR Sulphuric acid (H 2 SO 4 ) and hydriodic acid (HI) are produced via the Bunsen reaction. The Bunsen reaction is exothermic. Utilising a nuclear heat source, these two acids are then decomposed into their relevant constituents. The H 2 SO 4 decomposition reaction produces oxygen, sulphur dioxide and water. The HI decomposition reaction produces hydrogen and iodine. With the exception of hydrogen and oxygen, the other products are reused in the Bunsen reaction. As the name suggests, the S-I cycle is a cyclic process. The intent of the S-I cycle is to act as a veritable “black box” where water is split into hydrogen and oxygen. In reality, a variety of reactants are involved in the process, but they are recycled continuously, so that the only inputs to the system are heat and water and the only outputs are hydrogen and oxygen. The heat input is supplied via a high temperature nuclear reactor. A simplified flow sheet for the S-I cycle is shown in Figure 2. H 2 SO 4 , SO 2 , O 2 , H 2 O Figure 2: Simplified S-I cycle schematic O 2 product H 2 SO 4 Preheater Evaporator Decomposer H 2 O Bunsen reactor H 2 SO 4 , HI, I 2 , O 2 , H 2 O 3-phase separator H 2 SO 4 , H 2 O To IHX From IHX HI, I 2 , H 2 O HI, I 2 , H 2 O HI Preheater Evaporator Decomposer H 2 product The Westinghouse sulphur cycle, also known as the HyS cycle, was developed in the United States by Westinghouse during the oil crises of the 1970s (Brecher, 1976). In the HyS process, unlike the electrolysis of water, hydrogen is actually produced at the electrolyser cathode (Brecher, 1976). Similarly, sulphuric acid is produced at the electrolyser anode (Brecher, 1976). The HyS cycle consists of a decomposition step and an electrolysis step expressed as the following equations. • Decomposition (sulphuric acid, 1 123 K): H 2 SO 4 → H 2 O + SO 2 + ½O 2 • Electrolysis: 2H 2 O + SO 2 → H 2 SO 4 + H 2 In the HyS cycle, the decomposition of sulphuric acid is the same as Section 2 of the S-I cycle. Thus, the difference between the S-I cycle and HyS cycle is the removal of the Bunsen reaction and the replacement of Section 3 with an electrolysis process. A simplified flow sheet for the HyS cycle is shown in Figure 3. Both a nuclear reactor and a thermochemical hydrogen generation plant can be subject to a variety of transient scenarios. Each plant has its own start-up and shutdown scenarios, in addition to a wide variety of other transients. For the nuclear plant, this includes minor reactivity adjustments, off-normal operation and accident scenarios. In addition, the chemical plant is also subject to a wide variety of potential transient events, including start-up, shutdown, piping system failures, tank failure, heat exchanger failure and a wide variety of other accidents (Marsh, 1987). The point of interaction between the chemical plant and the nuclear reactor is the intermediate heat exchanger. The function of the intermediate heat exchanger is to transfer energy from the nuclear reactor to the chemical plant, thereby driving the chemical reactions. Because the nuclear reactor and hydrogen generation plant are so strongly coupled via the IHX, any event that occurs on one side of the loop will by definition effect the other side of the loop. By coupling two independently validated models of a high temperature nuclear reactor and a S-I/HyS NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 365
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TRANSIENT MODELLING OF S-I CYCLE THERMOCHEMICAL HYDROGEN GENERATION COUPLED TO PEBBLE BED MODULAR REACTOR<br />
Sulphuric acid (H 2 SO 4 ) and hydriodic acid (HI) are produced via the Bunsen reaction. The Bunsen<br />
reaction is exothermic. Utilising a nuclear heat source, these two acids are then decomposed into<br />
their relevant constituents. The H 2 SO 4 decomposition reaction produces oxygen, sulphur dioxide and<br />
water. The HI decomposition reaction produces hydrogen and iodine. With the exception <strong>of</strong> hydrogen<br />
and oxygen, the other products are reused in the Bunsen reaction. As the name suggests, the S-I cycle<br />
is a cyclic process. The intent <strong>of</strong> the S-I cycle is to act as a veritable “black box” where water is split<br />
into hydrogen and oxygen. In reality, a variety <strong>of</strong> reactants are involved in the process, but they are<br />
recycled continuously, so that the only inputs to the system are heat and water and the only outputs<br />
are hydrogen and oxygen. The heat input is supplied via a high temperature nuclear reactor.<br />
A simplified flow sheet for the S-I cycle is shown in Figure 2.<br />
H 2<br />
SO 4<br />
, SO 2<br />
,<br />
O 2<br />
, H 2<br />
O<br />
Figure 2: Simplified S-I cycle schematic<br />
O 2<br />
product<br />
H 2<br />
SO 4<br />
Preheater<br />
Evaporator<br />
Decomposer<br />
H 2<br />
O<br />
Bunsen<br />
reactor<br />
H 2<br />
SO 4<br />
,<br />
HI, I 2<br />
,<br />
O 2<br />
, H 2<br />
O<br />
3-phase<br />
separator<br />
H 2<br />
SO 4<br />
,<br />
H 2<br />
O<br />
To IHX<br />
From<br />
IHX<br />
HI, I 2<br />
,<br />
H 2<br />
O<br />
HI, I 2<br />
,<br />
H 2<br />
O<br />
HI<br />
Preheater<br />
Evaporator<br />
Decomposer<br />
H 2<br />
product<br />
The Westinghouse sulphur cycle, also known as the HyS cycle, was developed in the United States<br />
by Westinghouse during the oil crises <strong>of</strong> the 1970s (Brecher, 1976). In the HyS process, unlike the<br />
electrolysis <strong>of</strong> water, hydrogen is actually produced at the electrolyser cathode (Brecher, 1976). Similarly,<br />
sulphuric acid is produced at the electrolyser anode (Brecher, 1976). The HyS cycle consists <strong>of</strong> a<br />
decomposition step and an electrolysis step expressed as the following equations.<br />
• Decomposition (sulphuric acid, 1 123 K): H 2 SO 4 → H 2 O + SO 2 + ½O 2<br />
• Electrolysis: 2H 2 O + SO 2 → H 2 SO 4 + H 2<br />
In the HyS cycle, the decomposition <strong>of</strong> sulphuric acid is the same as Section 2 <strong>of</strong> the S-I cycle.<br />
Thus, the difference between the S-I cycle and HyS cycle is the removal <strong>of</strong> the Bunsen reaction and<br />
the replacement <strong>of</strong> Section 3 with an electrolysis process. A simplified flow sheet for the HyS cycle is<br />
shown in Figure 3.<br />
Both a nuclear reactor and a thermochemical hydrogen generation plant can be subject to a<br />
variety <strong>of</strong> transient scenarios. Each plant has its own start-up and shutdown scenarios, in addition to<br />
a wide variety <strong>of</strong> other transients. For the nuclear plant, this includes minor reactivity adjustments,<br />
<strong>of</strong>f-normal operation and accident scenarios. In addition, the chemical plant is also subject to a wide<br />
variety <strong>of</strong> potential transient events, including start-up, shutdown, piping system failures, tank failure,<br />
heat exchanger failure and a wide variety <strong>of</strong> other accidents (Marsh, 1987). The point <strong>of</strong> interaction<br />
between the chemical plant and the nuclear reactor is the intermediate heat exchanger. The function<br />
<strong>of</strong> the intermediate heat exchanger is to transfer energy from the nuclear reactor to the chemical<br />
plant, thereby driving the chemical reactions.<br />
Because the nuclear reactor and hydrogen generation plant are so strongly coupled via the IHX,<br />
any event that occurs on one side <strong>of</strong> the loop will by definition effect the other side <strong>of</strong> the loop.<br />
By coupling two independently validated models <strong>of</strong> a high temperature nuclear reactor and a S-I/HyS<br />
NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 365