by EnergySpin » Sat 06 Aug 2005, 14:34:24
$this->bbcode_second_pass_quote('Devil', 'H')ow much energy is requiredd to make NH3? If used in a fuel cell, how much energy is required to split it again to feed the H2 to a fuel cell? What is the holistic EROEI? Maybe 0.1???
In an IC engine, what are you going to do with all the toxic NOxs generated?
Then consider, NH3 has a MW of 10, only 30% of which is potentially energy producing, the other 70% being ± inert. That means your fuel tank has to be so much larger to store a given amount of energy.
However, NH3 can be a precursor for some quite interesting explosives, for the benefit of AQ and Co. The ACGIH recommend a time-weighted average threshold limit value of 25 ppm, which would be very difficult to maintain for those working in a filling station. Worse, the acute toxicity is high because the pH of body fluids exposed to an accidental heavy dose can easily exceed 10, which is corrosive to human tissue. Can you imagine what could happen if an NH3-fuelled vehicle had a fuel-pipe broken or, worse, an accident ruptured the tank?
Another problem is that NH3 is extremely hygroscopic, so that any exposure to air will react with the humidity to form NH4OH. The presence of that may upset the energy-producing properties. A leak can cause damage to vegetation, nearby water courses and animals. For this reason, there are strict regulations for handling NH3, which is sometimes used as a neat fertiliser. Google
ammonia accident to see the results of accidental leaks, some of them quite small. For handling ammonia, see
http://ianrpubs.unl.edu/safety/ec738.htm. Guess we would have to wear chemical-protection goggles and other PPE when driving an NH3 car!
Then do not underestimate the toxicity of NH3.
Starting backwards a few general comments
I do not underestimate the toxicity Devil ... as I said it MIGHT be a vehicle for the hydrogen economy given its storage advantages over pure hydrogen. I was going to start another thread on methanol (the other small molecular hydrogen carrier) to see if the hydrogen research programs are (deliberately?) overlooking solutions that might be technically easier for a hydrogen economy (IF THE PUBLIC AGREES THAT SUCH A HYDROGEN ECONOMY IS NEEDED). Part of that exercise would be to compound the initial thread with realistic data on safety issues. For example the metal hydride option which people seem to be pursuing is not exactly human friendly. The majority of the heavy metals have well defined and insidious ill-effects on human health and require extensive mining (environmental destruction) but yet a holistic assessment is never made.
General Safety Issues:
To reduce toxicity for storage research will be needed in tank design (I think even that letter in Physics Today said that), but hydrogen (or methanol for that matter) are not less dangerous (factoring the dangers of flammability and exposure toxicity). Regarding the leak, I'm not sure that vegetation is going to be damaged, but animals (and humans) will through skin and respiratory tract exposure.
In addition ammonia was used in home refrigeration years ago and is still used massively in industrial refrigeration and I have not seen employees at KMarts wearing masks (granted handnling of ammonia during transportation requires such measures).
And the same arguments that you made for ammonia (i.e. it can be used in dangerous chemicals or explosives) can be made for methanol (excellent solvent, clearly defined toxicity when consumed and upon exposure), gasoline, hydrogen. For example my assessment of the dangers of methanol is that it exceeds the dangers of ammonia because it is not detectable by the human senses (ammonia is detectable at concentrations as low as 5ppm) and that people will have a huge financial incentive to use it for illicit booze distillation. When it comes to risk-benefit I suppose you know that all interventions are judged based on the relative benefits vs dangers. The fact that in the Us (and increasingly in Europe) the majority of homes are sitting on a bomb (gas distribution networks) which could potentially lead to deaths (due to explosions, asphyxiation) has not been a particularly strong deterrent to the use of natural gas even though a competitor (i.e. electric heating) might be safer by a factor of 10 or 100.
Going to energy-storage issues:
Starting from electrolysis : one needs 4KWH of electricity to produce 3 KWH of hydrogen from ammonia (this is still an energy carrier, we have to remember that) and this is the energetically expensive step (shared by ammonia and pure hydrogen) so this gives an EROEI of about 0.75
Ammonia synthesis and storage does require two extra steps (extraction of nitrogen from air and the Haber step). The DOE which did look into such matters (in the context of the OTEC program) made the following estimates (btw I cannot find the data from Norsk Hydro which did synthesisze ammonia from electricity till the 80s, so I would appreciate your input if you happen to have access to them):
- a plant with electric generating capacity of 365MW would produce 1100 metric tons a day which is equivalent to 150000 gals gasoline. One gal of gasoline gives 125000 BTU and one million BTUs are equivalent to .293 Mwh. Therefore the energy balance is
Energy In 365 x 24 = 8760 MWh
Energy Out = 150000 x 125000 x 0.293/1000000 MWh = 5493.75 MWhEROEI = 5493.75/8760 = 0.627The reason that that these figures is close is because the catalytic combination of N2 and H2 is an energetically cheap reaction. The actual figure is 0.5KWh per kgr of NH3 synthesized by the High Temperature High Pressure Haber method (figure taken from the Royal Swedish Academy of Sciences Nobel Prize Presentation speech in 1918, which can be read online at
http://nobelprize.org/chemistry/laureat ... press.html )
That's a loss of about 10% compared to hydrogen generation, but if you factor in loss of hydrogen from tanks at a rate of 1.7%/day then you can interrogate the exponential formula and see that the two fuels become roughle equivalent after 10 days of storage and after that NH3 becomes the energy winner.
2.2 gal of NH3 = 1 gal of gasoline in terms of energy (BTU/gal) when burnt in ICEs (you can verify that with the link to the PDF in my first post, as well check it against any decent chemistry book) and it can be stored under pressure temperature conditions that are more favourable for the hydrogen (and it will not leak through the tanks like hydrogen will). That means that the tank has to be less heavy than the corresponding one needed for pure hydrogen storage. So the net vehicular weight (fuel+tank) will likely be in favour of ammonia or methanol or other such carriers.The same publication I referred to, did address catalytic reduction of nitric oxides via zeolites btw.
Regarding the use of ammonia in electrolytic cells, I think I have provided more than enough links for the interested reader to follow (including the Iowa conference), but I will extract the number from page 4 of the Ali T Raissi report : 16% of the energy stored in ammonia will be needed to break the ammonia in a electrolytic cell. You can plug in this number and see why an ICE or a fuel cell are both more viable as options compared to a "pure hydrogen" future from an energy in energy out perspective (IMHO)
Vehicular safety:
Would you agree that during collisions, accidents the probability of an adverse outcome from the fuel tank itself is approximately proportional to the Probability(explosion) x Probability(leak) (technically speaking I should be using conditional probabilities of harm here since not al leaks and not all explosions will result in death or harm). Ammonia might balance the two dangers so the net result might be comparable to gasoline but I cannot provide more data to that and neither can you or anyone else till someone decides to do test this hypothesis or do the engineering.
Delivery of ammonia:
At least here in the US (cannot say about the rest of the world), the distribution network is extremely safe, but then again workers are required to go through retraining every 3 years. Accidents do happen and none of them were lethal. Regarding the limit , I do not know where you get your estimate that a limit of 25 ppm will be difficult to maintain when such limits ARE already maintained in chemical plants where ammonia is produced (and there the potential exposure is potentially in high temperature , high pressure settings). No one is full enough to go and suck NH3 for dynamite (except maybe the lunnies in Idaho) in spite of the easy access to the stuff (check the ammonia pipeline in the US)
Environmental Impacts:
The Environmental Handbook of the German Federal Ministry for Economic Cooperation and Development has an extremely detailed section on the impact of industrial scale ammonia generation using a variety of methods including water electrolysis. The relevant section can be read
here$this->bbcode_second_pass_quote('', 'I')n normal operation, the plant does not release any pollutants into the environment. The continuously formed waste gas streams are processed internally or in the synthesis gas production plant.
No problems arise with the disposal of the catalyst, consisting of iron with small quantities of Al2O3, K2O, MgO, CaO and SiO2, an operation which takes place at intervals of around 5 to 10 years (e.g. smelting, road-building).
It occurs at a concentration of around 98.5 % by volume, is used in full or in part as a raw material for urea synthesis and can be released into the atmosphere untreated as in practice the only impurities contained are H2, N2 and CH4.
If the heating medium contains too much sulphur, it may undergo a purification process to keep SO2 values in the flue gases to within admissible levels. Primary measures to reduce the NOx emission can be taken in the primary reformer. Flue gases are released into the atmosphere through a chimney so as to comply with the values of the TA-Luft [Technical Instructions on Air Quality Control] valid in Germany, for example.
All other waste gases formed in the plant contain combustible components and are fed into the plant’s heating gas system. If there is any unscheduled stoppage, process gases (H2, CH4, CO, CO2, NH3, N2, steam) have to be burnt in a flare as a temporary measure so that only flue gases are released into the atmosphere.