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PEMFCs, hydrogen production through the electrolysis of
water have been reported. In this presentation, we focused
our attentions on the fuel cell using borohydride as the fuel
directly, hydrogen generation from borohydride and fuel
recovery.
such as a number of chemical hydrides, metal hydrides,
nanotubes and carbon fibers. Protide compounds are
chemical hydrides. Early in the 1950s, Schleshinger et al.
[13] suggested using sodium borohydride to generate
hydrogen under ambient conditions. Their results showed
sodium borohydride solution released 90% of the stoichio-
metric amount of hydrogen. In our investigation, alkaline
borohydride solution in a certain concentration range (,20
wt.%) can release almost 100% of the stoichiometric
hydrogen within 15 min when using Raney Ni as the
catalyst (see Fig. 5). A prototype of the hydrogen generator
has been produced. It produced 90% of the stoichiometric
amount of hydrogen at a rate of 10 l/min at room
temperature as shown in Fig. 6.
3.1. Fuel cell using borohydride as the fuel
Our aim on fuel cell development is to develop low cost
fuel cells using borohydrides that have higher electro-
chemical reactivity than hydrogen gas. For simplicity, this
kind of fuel cell is named borohydride fuel cell (BFC). In
principle, BFC works in an alkaline environment so that
catalytic agents are not limited to noble metals. Low cost
Ni-based catalysts for anode and cathode could be ex-
pected to show good performances like alkaline fuel cells
(AFCs). The Ni-coated steels can be used to make bipolar
plates so that their manufacturing cost can be decreased
greatly by using a cold press forming technique. Because
the fuel is an aqueous solution that can act as a cooling
medium, the cooling plates that are included in the stack of
PEMFCs, are not necessary any more. Based on these
considerations, we constructed fuel cells using fluorinated
AB2 (F-AB2) as the anode catalyst, Pt–C as the cathode
catalyst and Nafion membrane as the electrolyte.
The fuel was an alkaline borohydride solution con-
taining 10 wt.% NaBH4 and 20 wt.% NaOH (containing
2.1 wt.% H2). The bipolar plates were made of stainless
steel. The flow field area of the plates was 70% of the
electrode area (20330 mm). The stack consisting of ten
cells demonstrated a good performance like PEMFCs
(shown in Fig. 4).
3.3. Fuel recovery
In the triangular hydrogen energy system, fuel recovery
is the most difficult issue. In the linear hydrogen system,
only hydrogen reacts with oxygen during energy conver-
sion. For example, hydrogen gas from metal hydrides can
be used to run a PEMFC to produce water. The hydrogen
gas can be produced by the electrolysis of water, and then
reacted with alloys to form metal hydrides. In the triangu-
lar hydrogen system, when protide compounds generate
hydrogen gas to supply PEMFCs by a thermal decomposi-
tion, the process will be the same as that in linear hydrogen
energy system. However, when protide compounds release
their hydrogen by the hydrolysis or are electrochemically
oxidized directly, the protide has not only a relation with
oxygen but also a relation with its donor. The donor will
react with oxygen when the protide is oxidized. Therefore,
the fuel recovery must include processes of not only the
hydrogen cycling but also the donor cycling. For example,
protide in borohydride (BH24 ) runs a fuel cell to produce
meta-borate and water. Protide in saline hydrides can be
formed by reacting alkali or alkali-earth metal with hydro-
3.2. Hydrogen generation
Hydrogen can been stored as a pure substance as a
liquid or compressed gas (say .300 atm.) and in materials
Fig. 4. Fuel cell using borohydride as a fuel and its performance. Anode: 200 mg/cm2 flourinated AB2 alloy, 10 wt.% NaBH4 –20 wt.%NaOH at flow-rate
of 186 ml/min. Cathode: 2 mg/cm2 Pt-black, atmosphere at flow-rate of 200 ml/min.