AU463596B2 - Hydrogen gas manufacturing process - Google Patents

Hydrogen gas manufacturing process

Info

Publication number
AU463596B2
AU463596B2 AU41103/72A AU4110372A AU463596B2 AU 463596 B2 AU463596 B2 AU 463596B2 AU 41103/72 A AU41103/72 A AU 41103/72A AU 4110372 A AU4110372 A AU 4110372A AU 463596 B2 AU463596 B2 AU 463596B2
Authority
AU
Australia
Prior art keywords
magnesium
hydrogen gas
chloride
water
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
AU41103/72A
Other versions
AU4110372A (en
Inventor
Suzuki Masahiro
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP2435371A external-priority patent/JPS4832790A/ja
Application filed by Individual filed Critical Individual
Publication of AU4110372A publication Critical patent/AU4110372A/en
Application granted granted Critical
Publication of AU463596B2 publication Critical patent/AU463596B2/en
Expired legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen; Reversible storage of hydrogen
    • C01B3/02—Production of hydrogen; Production of gaseous mixtures containing hydrogen
    • C01B3/06—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen with inorganic reducing agents
    • C01B3/08—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen with inorganic reducing agents by reaction of inorganic compounds with metals
    • C01B3/10—Production of hydrogen; Production of gaseous mixtures containing hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen with inorganic reducing agents by reaction of inorganic compounds with metals by reaction of water vapour with metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00—Making metallic powder or suspensions thereof
    • B22F9/02—Making metallic powder or suspensions thereof using physical processes
    • B22F9/04—Making metallic powder or suspensions thereof using physical processes starting from solid material, e.g. by crushing, grinding or milling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)

Description

41.103/7 This invention relates to the development of a low
cost manufacturing process of hydrogen gas used in chemical
reactions or as a fuel.
According to the present invention there is provided
a process for the preparation of hydrogen gas by the
reaction of magnesium with water including the steps of
vigorously stirring magnesium and catalyst in particle or
powder form and adding water to the resultant mixture in
the presence of potassium chloride or sodium chloride to
accelerate the reaction of magnesium with water.
The vigorous stirring of magnesium and catalyst allows
catalyst to become embedded in the magnesium and the
resultant mixture permits vigorous generation of hydrogen.
The catalyst may include a metal or a non-metal which
is silicon, aluminium, iron, zinc, tin, nickel, boron, red
phosphorus, chromium, copper, manganese, carbon, calcium,
titanium, zirconium, or one or more compounds of the above-
mentioned metals and non-metals. Many of such materials are
available nearly anywhere on earth, especially through sea or waste water, or through waste powder/solutions discarded from
metal works or smelting plants, or through industrially
polluted mud accumulated in rivers or on the bottom of the
sea.
This process yields readily large quantities of
highly pure hydrogen gas which, having a very high combustion
46.3,5 96
41,103 72 as a fuel for temperature of about 20000C, can be used ships or in homes. power generation in factories, or on and moreover the The manufacturing process is simple, and used materials serving as catalysts are regenerated cost is low. repeatedly and so the manufacturing by this Furthermore, the hydrogen gas provided components either invention does not produce polluting and a great during its manufacture or during combustion, earth can be used as number of materials available on the obtained, so that a catalysts whenever magnesium can be produced anywhere pollution-free source of energy can be
4 6 3.5 96
41,10o3/
at any time.
Since the waste solutions of metals or of chlorides which
are the source of public nuisance are employed as excellent raw
materials in this hydrogen gas manufacturing process, it contri-
butes also to the solution of the pollution problem.
So far, it is well known that hydrogen gas is produced
by the addition of water to magnesium, the amount, however, of hydrogen gas produced is extremely small in this case. It is also very small even with the use of hot water, and cannot be obtained sufficiently for practical applications.
Considering the above-mentioned fact, much research was carried out over many years in the development of this invention by which the manufacture of large quantities of highly pure
hydrogen gas, in a short time, has been made successful. Accord- ing to this invention, a metal or a non-metal such as silicon,
aluminium, iron, zinc, tin, nickel, boron, phosphorus, copper,
manganese, icarbon, calcium, titanium, zirconium, or one or more compounds of the above-mentioned metals and non-metals are added
to magnesium, and water is added to the resultant mixture in the presence of potassium chloride or sodium chloride the catalytic
action of the above-mentioned elements or compounds is used to
accelerate the formation of magnesium hydroxide from the reaction
of magnesium with water. Namely, the above-mentioned elements or compounds act as catalysts in the following reaction: Mg 2H Mg(OH) 2 H 2 producing quite readily large quantities of hydrog
gas.
When elements or compounds of good quality are
463,5 96
411 0.3/7M employed, hydrogen gas is formed and evolves vigorously
as if the mixture is boiling. It is believed that this About 930 Bm-4 energy can be used for power generation. gram of magnesium although of hydrogen gas are obtained per to the nature of the some difference exists according obtained with catalysts catalysts, and highest yields are lowest ones with silicon such as chlorides or metals while and carbon. hydrogen is pro- If iron is used as the catalyst, In this case, how- duced when iron hydroxide is formed. 4 catalysts, it- !0 ever, as well as in the case of other or potassium chloride bettcr to adr' either sodium chloride effectively the to the catalyst in opdap-to increase~kmore according to the ex- formation of hydrogen gas. Namely, the reaction occurs perimental. results of this invention, above-mentioned compounds vigorously when two kinds of the epecially7 sodium are employed, one being a chloride, or. ametal ebtlrd and chloride, or potassium chloride, The evolution of hy- the other iron, chromium or copper. By comparing the amount drogen gas is then very active. formed by 2g of hydrogen gas-obtained with the mixture and 3g of iron, with magnesium, 259 of sodium chloride, by 2g of magnesium that obtained with the mixture formed and 3g of iron, it was found that, with the same reaction not reach one third of conditions, the latter amount did a chloride increases en- the former, thus indicating that formed. ormously the amount of hydrogen with As for the compounding ratio of magnesium elements, when more other elements or compounds of these elements or compounds are than two of the above-mentioned FU 463.5-96
41,103/72
used, the amount of magnesium in the mixture is 10 50%, that of
the sodium or potassium chloride 5 70% and that of the catalyst
40%. In this case, if the amount of water added is 8 times
the amount of the above mixture, hydrogen gas is formed at a satisfactory rate.
If magnesium in lump form is used, it is introduced into
water first, before adding the catalyst or the chloride.
In this case, the temperature of the solution is increasE
by the heat of the hydrogen gas formation reaction, it is, howeve
still possible to promote the formation of hydrogen gas further I
heating the solution to a safe temperature i.e. a temperature at
which hydrogen is not so vigorously generated as to cause ad-
mixture of oxygen and the generated hydrogen.
If the hydrogen gas provided by this invention is analyzE
by gas chromatography, it is observed that even the gas obtained
from the use of ordinary water or sea water contains more than
of hydrogen. Other components are oxygen and nitrogen
coming from the amount of air dissolved in the water employed,
but it is found that the amount of impurity gas present does not
reach even 0.1 ppm. Therefore, hydrogen gas having a purity
superior to 99.9999% can be readily obtained by removing the
oxygen and nitrogen of the air component in the gas.
As for the residual reaction products remaining after th4
evolution of hydrogen, in the case of water and sea water, they
are separated, regenerated chemically and used repeatedly again.
Magnesium hydroxide is transformed into magnesium
463.5 96
41.103/72 chloride, then magnesium is regenerated by electrolysis chlorides are used or by the Pidgeion process. Iron and manufac- again. The processes involved in the continuous and in ture of hydrogen, in the steam power generation, reaction the regeneration of magnesium from the residual at a plant or at a products can be carried out either
specially constructed regeneration plant. Thus it is possible in small plants or common by a source homes to replace the conventional power source line from of energy that does not require any transmission
the exterior, by the use of a small generator. of this Hereinafter, examples of some embodiments
invention will be described.
Example 1:
of magnesium, 10g of sodium chloride, 7g of At zinc and 7g of magnesium chloride were prepared.
first, magnesium and zinc were well mixed by stirring,
then water of 8 times the amount of the above-mentioned When magnesium chlor- compounds, namely 270 2 was added. gas ide and sodium chloride were introduced, hydrogen in 7 evolved vigorously and amounted to about 2,100 m
minutes. This hydrogen gas did not contain even 0.1 ppm
of impurity gas, and had a heat capacity of about 3,000 flame when Kilocalories. It burned with a blue-white suitable as fuel supplied to a burner, and so was found small plant use. for small generators destined to home or
46 3,5 9 6
41,103/72 Example -3:
8g of magnesium, 8g of iron, and 10g of cupric ch-
loride were prepared. About 9 times the amount of these
substances of sea water was taken and cupric chloride was
added to the sea water. When the well-stirred mixture
of magnesium and iron powder was added to the solution,
hydrogen gas evolved vigorously and amounted to about
2,100-am in 12 minutes.
The purity, the heat capacity and the use of
this hydrogen gas were almost identical to those of the
gas obtained in Example 1.
Example 4:
1,000g of magnesium, 800g of iron, 500g of ferrous
chloride, 2,800g of sodium chloride and 25 liters of water
were used. Iron powder and magnesium were well mixed in
water by stirring, then sodium chloride was added while
stirring was continued. Ferrous chloride was introduced
thereafter, producing large quantities of gas which evolved
very vigorously, and even at a constant rate of 208
per second during the normal period of the reaction.
According to this experiment, the hydrogen gas
obtained did not contain even 0.1 ppm of impurity gas,
and has a heat capacity of about 3,000 Kilocalories and
was therefore found suitable as fuel for power generation
at small plants or homes.
46 3,5 96
41,103/72
agnsiull,8gof zinc and log of ferrous l~gof
chloride were prepared. About 8 times the amount of these
substances of seawater was taken, and to this, ferrous the well-stirred mixture chloride was first added. Then into the solution. of magnesium and zinc was intr~oduced in 20 minutes. -,e About 1,500H* of gasi'ere obtained sodium chloride were Exan~l.:(M~agnesium chloride, and used) and of magnesium, 200g of sodium chloride introduced into a re- of magnesium chloride powder were When water was added action flask and stirred vigorously. vigorously, giving to this mixture, hydrogen gas evolved mixture. about 300 a*g of gas per gram of added to a On the other hand, when water was and lOg of magnesium stirred mixture of 20g of magnesium over a long period. chloride, the gas evolved smoothly be used with mag- In this embodiment, brine could and the hydrogen gas nesium.!f chloride and sodium chloride, of Example 1. obtained was identical to that
4 63.5 9 6
41,103 /72 Example 19: (Ferrous chloride, ferric chloride and sodium
chloride were used)
250g of sodium chloride, 20g of magnesium and
of ferrous chloride were mixed together; to this mixture,
water was added and the gas evolved was collected. The
evolution of gas progressed well and gave a large quant-
ity of gas in 3 hours. More than 300-t of gas were ob-
tained per gram of the reacting mixture. During the
reaction, water had to be added gradually because the effect ,reaction flask.was in danger of breaking under the
of the heat of the reaction. When ferric chloride was used instead of ferrous
the gas evolved more vigorously than in the chloride,
case of ferrous chloride. In this case ferrous chloride
and ferric chloride from the waste solutions discarded chlor- by smelting plants and from the slagand the sodium
ide from sea water were used.
I
Example (Red phosphorus and sea water)
The gas evolved after 10g of magnesium and 20g of water. The red phosphorus had been added to 250 4A of sea
evolution of gas was vigorous and abundant.
10 463.596
41,103/ 72
The examples B to 4 mentioned above show that
hydrogen gas of good quality can be obtained even in the
absence of magnesium chloride, if red phosphorus or nickel
chloride are used. It has been also shown that the con-
tent of sodium chloride in the compounded mixture is
appropriate and when the particles and the size of the
solid metal components (such as iron, zinc) are well chos-
en so that no light particles can be ejected out due to
the vigorous evolution of the gas, the hydrogen gas ob-
tained burns'with a remarkably transparent flame. In summary, this invention has the advantage that
it does not present the danger of producing a polluting
gas either during the manufacturing or during the com-
bustion processes and so is free from pollution problems.
Moreover, since the combustion produces water vapor at a
temperature of 2,0000C, there is no danger of drying out
the room where combustion is carried out. Extremely large
quantities of hydrogen gas can be obtained from a very
small amount of reactants. On the other hand, as the gas
manufacturing apparatus is very simple, it can be used
very easily, producing hydrogen which can be used whenever
necessary, and so is very useful. Moreover, since the
reactants can be regenerated and used repeatedly, hydrogen
gas can be produced at low cost, and so, can be used not
11 463,596
4 1,1 03 In small.plants or only as a fuel for power generation in industry homes but is also very useful for the chemical quantities and steam power generation which require large economic and tech- of hydrogen gas, and consequently, the
nical effects of this invention are very large.
12 463.596

Claims (1)

  1. 41.103/72 THE CLAIMS DEFINING THE INVENTION ARE AS FOLLOWS:
    1. A process for the preparation of hydrogen gas by the
    reaction of magnesium with water including the steps of or vigorously stirring magnesium and catalyst in particle in the powder form and adding water to the resultant mixture to presence of potassium chloride or sodium chloride
    accelerate the reaction of magnesium with water.
    2. A process according to Claim 1, wherein the catalyst
    includes a metal or a non-metal which is silicon, aluminum,
    iron, zinc, tin, nickel, boron, red phosphorus, chromium, or copper, manganese, carbon, calcium, titanium, zirconium,
    one or mbre compounds of the above-mentioned metals or
    non-metals.
    3. A process according to Claim 1 substantially as
    hereinbefore described with reference to the foregoing
    examples.
    4. Hydrogen gas whenever produced by a process as
    claimed in-any one of the preceeding claims.
    DATED THIS 22nd Day of MAY 1975
    MASAHIRO SUZUKI
    By its Patent Attorneys:
    CLEMENT HACK CO. Fellows Institute of Patent Attorneys of Australia.
    13 463.5 96
AU41103/72A 1971-04-16 1972-04-13 Hydrogen gas manufacturing process Expired AU463596B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2435371A JPS4832790A (en) 1971-04-16 1971-04-16
JP7184364A JPS4849694A (en) 1971-04-16 1971-10-26

Publications (2)

Publication Number Publication Date
AU4110372A AU4110372A (en) 1973-10-18
AU463596B2 true AU463596B2 (en) 1975-07-31

Family

ID=26361853

Family Applications (1)

Application Number Title Priority Date Filing Date
AU41103/72A Expired AU463596B2 (en) 1971-04-16 1972-04-13 Hydrogen gas manufacturing process

Country Status (7)

Country Link
JP (1) JPS4849694A (en)
AU (1) AU463596B2 (en)
CA (1) CA978332A (en)
DE (1) DE2218470A1 (en)
FR (1) FR2133825B1 (en)
GB (1) GB1378820A (en)
IT (1) IT966890B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5823321B2 (en) * 1979-10-14 1983-05-14 鈴木 正弘 hydrogen generator
GB9115863D0 (en) * 1991-07-23 1991-09-04 Crawford Kenneth E Engine system
US6582676B2 (en) * 2000-08-14 2003-06-24 The University Of British Columbia Hydrogen generation from water split reaction
WO2002014214A1 (en) * 2000-08-18 2002-02-21 Valery Armenakovich Grigoryan Method for producing hydrogen and heat energy
RU2223221C1 (en) * 2003-02-11 2004-02-10 Закрытое акционерное общество "Фирма Риком СПб" Aluminum oxides/hydroxides and hydrogen manufacture method
RU2253606C1 (en) * 2004-02-16 2005-06-10 Терещук Валерий Сергеевич Aluminum-based alloy for generation of hydrogen, method of production of such alloy and hydrogen gas generator
JP2010110753A (en) * 2008-10-07 2010-05-20 Akira Haneda Manufacturing method of ceramic catalyst, hydrogen generation apparatus using ceramic catalyst and hydrogen using apparatus
CN102498059A (en) 2009-08-12 2012-06-13 法商Bic公司 Hydrogen generation using compositions including magnesium and silicon
JP6858371B2 (en) * 2017-04-27 2021-04-14 国立研究開発法人産業技術総合研究所 Powder and its manufacturing method
FR3085206B1 (en) * 2018-08-22 2020-11-13 Commissariat Energie Atomique METHOD FOR DETERMINING THE QUANTITY OF ALKALINE OR ALKALINO-EARTH METAL CONTAINED IN A MATERIAL

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB579246A (en) * 1943-07-08 1946-07-29 British Non Ferrous Metals Res Improvements in the production of hydrogen

Also Published As

Publication number Publication date
GB1378820A (en) 1974-12-27
FR2133825B1 (en) 1974-07-26
AU4110372A (en) 1973-10-18
IT966890B (en) 1974-02-20
CA978332A (en) 1975-11-25
FR2133825A1 (en) 1972-12-01
DE2218470A1 (en) 1972-10-26
JPS4849694A (en) 1973-07-13

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