JPS5945901A - Method and apparatus for releasing hydrogen from hydrogen-occluding substance - Google Patents

Method and apparatus for releasing hydrogen from hydrogen-occluding substance

Info

Publication number
JPS5945901A
JPS5945901A JP57152688A JP15268882A JPS5945901A JP S5945901 A JPS5945901 A JP S5945901A JP 57152688 A JP57152688 A JP 57152688A JP 15268882 A JP15268882 A JP 15268882A JP S5945901 A JPS5945901 A JP S5945901A
Authority
JP
Japan
Prior art keywords
hydrogen
sih2
silicon
aqueous solution
tank
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.)
Granted
Application number
JP57152688A
Other languages
Japanese (ja)
Other versions
JPS6232121B2 (en
Inventor
Hoki Haba
方紀 羽場
Ikuo Hayashi
郁夫 林
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
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
Application filed by Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP57152688A priority Critical patent/JPS5945901A/en
Publication of JPS5945901A publication Critical patent/JPS5945901A/en
Publication of JPS6232121B2 publication Critical patent/JPS6232121B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

PURPOSE:To release hydrogen from a silicon-containing substance for the storage of hydrogen, by utilizing the chemical reaction of said substance with an aqueous solution of an alkali. CONSTITUTION:A silicon-containing substance for the storage of hydrogen (SiH2) is prepared by carrying out the glow discharge or sputtering of silane gas at about 0.1-10Torr, thereby depositing the powdery product to the cooled face. A slurry containing abut 30wt% of the slicon-containing substance is prepared in the tank 1, and separately, an aqueous solution of NaOH is prepared in the tank 2. The pumps 5 and 6 are operated to introduce the SiH2 slurry and the NaOH solution into the reactor 7 and contact the components with each other. The generated hydrogen gas is recovered through the vapor-liquid separator 9 and the desiccating tube 11, etc. SiH2 reacts with an aqueous solution of an alkali according to the formula, and 1mol of SiH2 gives 3mol of hydrogen, which corresponds to three times the amount of hydrogen released by the simple heating of the SiH2.

Description

【発明の詳細な説明】 本発明は水素吸蔵物質からの水素放出方法および該方法
を実施するための装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for releasing hydrogen from a hydrogen storage material and an apparatus for carrying out the method.

特願昭57−13125号明細書には−(SL馬)、L
−結合鎖および四配位Si格子を含み60〜70原子チ
の水素を吸蔵している水素吸蔵物質が記載されている。
In the specification of Japanese Patent Application No. 57-13125, - (SL horse), L
- Hydrogen storage materials are described that contain bonded chains and a four-coordinated Si lattice and store 60 to 70 atoms of hydrogen.

この水素吸蔵物質はシランガスを圧力0.1〜1Q T
orrの下でグロー放電またはスパッタリングに付し、
冷却面に粉末状生成物を蒸着させることにより製造され
、多量の水素を含有しているので水素貯蔵材料として極
めて有用なものである。
This hydrogen storage material absorbs silane gas at a pressure of 0.1 to 1QT.
subjected to glow discharge or sputtering under orr;
It is produced by depositing a powdered product on a cooling surface and contains a large amount of hydrogen, making it extremely useful as a hydrogen storage material.

この水素吸蔵物質に貯蔵されている水素を利用するに当
っては、Ti、Ft等の金属の水系化合物から水素を放
出させる場合と同様に、水素吸蔵物質を例えば250C
の温度に加熱することにより水素を放出させていた。こ
のような水素放出方法によるときには、水素を放出した
後に残った物質に適当な温度および圧力下で再び水素を
吸蔵させることかできるので水素吸蔵物質を反覆使用す
ることができるという利点があるが、その反面次のよう
な欠点がある=(1)水素吸蔵物質を気密容器に収容し
て空気と接触しないような条件下で加熱しなければなら
ない。そうでない場合には水素放出のために行う加熱に
より酸化してF3i0□、H2Oを生じる。;(2)繰
返しの水素の放出および吸蔵により該物質が次第に劣化
し、水素吸蔵能力が低下し。
When utilizing the hydrogen stored in this hydrogen storage material, the hydrogen storage material must be heated to 250° C.
Hydrogen was released by heating to a temperature of . When such a hydrogen release method is used, the hydrogen storage material can be used repeatedly since the material remaining after hydrogen release can be allowed to store hydrogen again at an appropriate temperature and pressure. On the other hand, it has the following drawbacks: (1) The hydrogen storage material must be housed in an airtight container and heated under conditions that prevent it from coming into contact with air. If this is not the case, the heating performed to release hydrogen will oxidize to produce F3i0□, H2O. (2) The substance gradually deteriorates due to repeated release and storage of hydrogen, and its hydrogen storage capacity decreases.

比較的短期間に再使用串来なくなる;(3)吸蔵されて
いるすべての水素を放出させることができない。
(3) It is not possible to release all the stored hydrogen.

全ての水素を放出させると物質の劣化(酸化を含む)が
生じる;(4)約250Cの水素放出温度を得るために
多量のエネルギー消費を伴う。特に珪素よりなる水素吸
蔵物質はすべ−(の吸蔵水素を放出させるのに加熱温度
を500Cまで1煽める心安があり極めて不利である。
Releasing all the hydrogen results in material degradation (including oxidation); (4) high energy consumption is involved to obtain a hydrogen release temperature of approximately 250C; In particular, hydrogen storage materials made of silicon are extremely disadvantageous because they can safely be heated up to 500C in order to release the stored hydrogen.

本発明の目的は前記のような珪素含有水素吸蔵物質力・
ら水素を放出するに当り、上記のような欠点のない優れ
た水素放出方法および該方法を実施するための装置を提
供することである。
The purpose of the present invention is to
An object of the present invention is to provide an excellent method for releasing hydrogen without the above-mentioned drawbacks, and an apparatus for carrying out the method.

本発明による水素吸蔵物質からの水素放出方法は、珪素
含有水素1吸蔵物質をアルカリ水浴液と反応させること
を特徴とするものである。
The method for releasing hydrogen from a hydrogen storage material according to the present invention is characterized by reacting a silicon-containing hydrogen storage material with an alkaline water bath liquid.

本発明方法によれば、珪素含有水素吸蔵物質を常温でア
ルカリ水溶液に溶解するが、このときに次の化学反応が
行われる: E3iH2+ 2NaOH+H20−+ Na2F3i
03+ 3馬丁ごの反応式から明らか゛なよ5に、5L
)121モルから水素6モルが常温で得られる。また、
SiH21モルかアルカリの存在下でH2O1モルを分
解しており、このことは水の分解が化学反応により電気
分解によるよりも有利に行われていることを示している
According to the method of the present invention, a silicon-containing hydrogen storage material is dissolved in an alkaline aqueous solution at room temperature, and at this time the following chemical reaction takes place: E3iH2+ 2NaOH+H20-+ Na2F3i
03+ It is clear from the reaction equation of 3 horses that 5, 5L
) 6 moles of hydrogen are obtained at room temperature from 121 moles. Also,
21 mole of SiH or 1 mole of H2O was decomposed in the presence of an alkali, indicating that water decomposition is carried out more favorably by chemical reaction than by electrolysis.

以下に本発明により珪素含有水素1吸蔵物質から水素を
連続的に放出させる実施例を説明する。
An example in which hydrogen is continuously released from a silicon-containing hydrogen storage material according to the present invention will be described below.

実施例 第1図は本発明による水素放出フローチャートを示す。Example FIG. 1 shows a hydrogen release flowchart according to the present invention.

特JM57−13125号明細書に記載のようにして製
造された珪素含有水素吸蔵物質(StH2)の60重量
%スラリーをタンク1で調製する。−力、タンク2に苛
性ソーダおよび水を入れて10%Nc=OH水溶液を調
製する。各タンクには上部の投入口から適時5jH2お
よびNaOHを投入して常にタンク内の液盪を一定に保
つようにするのがよい。次いで弁3および4を開き、ポ
ンプ5および6を作動させてSiH2スラリーおよびN
aOH溶液を1〜2 kIA薄2に加圧し1反応器Z内
のノズル8からそれぞれ噴射し1反応器内で接触させ瞬
間的に反応を行う。ノズルの位置は上下に限らず左右に
配置しても良く、要するに2液が衝突するようにすれば
良い。反応により生成した水素ガスは気液分離器9に導
ひいてガス中の水分を除去する。発生する水素ガスの圧
力を所定の値に維持するために、気液分離器に取付けら
れている圧力計10とポンプ5および6とを電気的に連
動させてポンプの出力を制御し1反応室に送られるSi
H2およびNaOHの量を調節し1発生水素ガス量を一
定に保つ。気液分離器を通過した水素ガスは例えばCa
Cl2を充填した乾燥管11を通り、流量コントロール
弁12および流量設定制御器16により常に必要流量が
得られるように制御されて負荷に供される。反応器内で
生成するN” S t Q 3溶液は弁15により適宜
排出する。14は流量計である。このようにして放出さ
れる水素ガスの圧力および流量を自動的に制御し、原料
を順次タンク1および2に投入することにより連続的に
水素ガスを発生することができる。
A 60% by weight slurry of silicon-containing hydrogen storage material (StH2) produced as described in Japanese Patent Application No. JM57-13125 is prepared in tank 1. - Put caustic soda and water into tank 2 to prepare a 10% Nc=OH aqueous solution. It is preferable to input 5jH2 and NaOH into each tank from the upper input port at appropriate times to keep the liquid stirring in the tank constant at all times. Then valves 3 and 4 are opened and pumps 5 and 6 are activated to pump the SiH2 slurry and N
The aOH solution is pressurized to 1 to 2 kIA thin 2, injected from nozzles 8 in one reactor Z, brought into contact in one reactor, and reacted instantaneously. The position of the nozzle is not limited to the top and bottom, but may be placed on the left and right, as long as the two liquids collide with each other. The hydrogen gas generated by the reaction is led to a gas-liquid separator 9 to remove moisture from the gas. In order to maintain the pressure of the generated hydrogen gas at a predetermined value, the pressure gauge 10 attached to the gas-liquid separator and pumps 5 and 6 are electrically linked to control the output of the pumps. Si sent to
The amount of hydrogen gas generated is kept constant by adjusting the amount of H2 and NaOH. The hydrogen gas that has passed through the gas-liquid separator is, for example, Ca
It passes through a drying pipe 11 filled with Cl2, and is controlled by a flow rate control valve 12 and a flow rate setting controller 16 so that the required flow rate is always obtained, and then subjected to a load. The N" S t Q 3 solution generated in the reactor is appropriately discharged by the valve 15. 14 is a flow meter. In this way, the pressure and flow rate of the released hydrogen gas are automatically controlled, and the raw material is Hydrogen gas can be continuously generated by sequentially charging tanks 1 and 2.

本発明によれば■S t H2とアルカリ水溶液との化
学反応を利用することにより1モルの5LH2°がら水
素3モルを放出させることができて、この水素放出量は
加熱による場合(S t H2→sL+H2↑)の3倍
である;■常温で化学反応により水素の放出が行われる
ので、加熱等のためのエネルギー消費がない;■原料の
5zHzおよびアルカリ成分を適時それぞれのタンクに
投入することにより連続的に水素を発生させることがで
きる;■放出された水素の圧力および流量をポンプ出方
および流量制御弁により調節することができる;■反応
により生成するNaE3i03は無害であってそのまま
下水に放流することができる等の利益が得られる。
According to the present invention, by utilizing the chemical reaction between S t H2 and an alkaline aqueous solution, 3 moles of hydrogen can be released from 1 mole of 5LH2°, and this amount of hydrogen released is greater than when heated (S t H2 → sL+H2↑); ■Hydrogen is released by chemical reaction at room temperature, so there is no energy consumption for heating, etc.; ■Add 5 zHz raw materials and alkaline components to their respective tanks in a timely manner. can generate hydrogen continuously; ■ The pressure and flow rate of released hydrogen can be adjusted by the pump outlet and flow rate control valve; ■ NaE3i03 produced by the reaction is harmless and can be directly disposed of in sewage. Benefits such as being able to release water into the water can be obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明による水素放出フローチャートである。 図中符号=1・・・5zHzタンク、2・・・NaOH
タンク。 3.4.12.15・・・弁、6,5・・・ポンプ、7
・・・反応室。 8・・・ノズル、9・・・気液分離器、10・・・圧力
計。 11・・・乾燥管、16・・・流量設定制御器、14・
・・流量計。
FIG. 1 is a hydrogen release flowchart according to the present invention. Symbols in the figure = 1...5zHz tank, 2...NaOH
tank. 3.4.12.15...Valve, 6,5...Pump, 7
...Reaction chamber. 8... Nozzle, 9... Gas-liquid separator, 10... Pressure gauge. 11...Drying tube, 16...Flow rate setting controller, 14.
··Flowmeter.

Claims (1)

【特許請求の範囲】 り 珪素含有水素貯蔵物質(S t H2)をアルカリ
水溶液と反応させることを特徴とする珪素含有水素貯蔵
物質の水素放出方法。 2)珪素含有水素貯蔵物質のスラリーを収容したタンク
、アルカリ水浴液を収容したタンク、室内に2個のノズ
ルを設けた反応室1反応室からの放出水素が導入される
気液分離装置、乾燥管および流量設定制御器からなるこ
とを特徴とする水素放出装置。
[Claims] A method for releasing hydrogen from a silicon-containing hydrogen storage material, which comprises reacting a silicon-containing hydrogen storage material (S t H2) with an alkaline aqueous solution. 2) A tank containing a slurry of silicon-containing hydrogen storage material, a tank containing an alkaline water bath liquid, and a reaction chamber with two nozzles inside the chamber.1 Gas-liquid separation device into which hydrogen released from the reaction chamber is introduced, and drying. A hydrogen release device comprising a tube and a flow rate setting controller.
JP57152688A 1982-09-03 1982-09-03 Method and apparatus for releasing hydrogen from hydrogen-occluding substance Granted JPS5945901A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57152688A JPS5945901A (en) 1982-09-03 1982-09-03 Method and apparatus for releasing hydrogen from hydrogen-occluding substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57152688A JPS5945901A (en) 1982-09-03 1982-09-03 Method and apparatus for releasing hydrogen from hydrogen-occluding substance

Publications (2)

Publication Number Publication Date
JPS5945901A true JPS5945901A (en) 1984-03-15
JPS6232121B2 JPS6232121B2 (en) 1987-07-13

Family

ID=15545951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57152688A Granted JPS5945901A (en) 1982-09-03 1982-09-03 Method and apparatus for releasing hydrogen from hydrogen-occluding substance

Country Status (1)

Country Link
JP (1) JPS5945901A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006034885A1 (en) 2006-07-25 2008-08-07 Daimlerchrysler Ag Hydrogen and energy production by thermal conversion of silanes
FR2915742A1 (en) * 2007-05-04 2008-11-07 Centre Nat Rech Scient Use of a hydrogenated silicon to recover dihydrogen, which is useful in fuel cells
JP2009023857A (en) * 2007-07-18 2009-02-05 Toyota Central R&D Labs Inc Hydrogen generation apparatus
EP2047552A2 (en) 2006-08-03 2009-04-15 REV Renewable Energy Ventures Inc. Process for supplying a fuel cell with hydrogen by means of silanes or polysilanes
JP2013519615A (en) * 2010-02-15 2013-05-30 ユニベルシテ デ―マルセイユ Method for producing hydrogen from silylated derivative as hydrogen carrier using phosphine oxide catalyst

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8414863B2 (en) 2006-07-25 2013-04-09 Spawnt Private S.A.R.L. Hydrogen and energy generation by thermal conversion of silanes
JP2009544553A (en) * 2006-07-25 2009-12-17 アールイーヴィー・リニューアブル・エナジー・ベンチャーズ・インコーポレイテッド Acquisition of hydrogen and energy by thermal conversion of silane
DE102006034885A1 (en) 2006-07-25 2008-08-07 Daimlerchrysler Ag Hydrogen and energy production by thermal conversion of silanes
EP2047552B1 (en) * 2006-08-03 2016-10-05 Spawnt Private S.à.r.l. Process for supplying a fuel cell with hydrogen by means of silanes or polysilanes
US8435476B2 (en) * 2006-08-03 2013-05-07 Spawnt Private S.A.R.L. Process for supplying a fuel cell with hydrogen by means of silanes or polysilanes
EP2047552A2 (en) 2006-08-03 2009-04-15 REV Renewable Energy Ventures Inc. Process for supplying a fuel cell with hydrogen by means of silanes or polysilanes
WO2008148988A3 (en) * 2007-05-04 2009-03-05 Centre Nat Rech Scient Method for producing dihydrogen from hydrogenated silicon
FR2915742A1 (en) * 2007-05-04 2008-11-07 Centre Nat Rech Scient Use of a hydrogenated silicon to recover dihydrogen, which is useful in fuel cells
US20100119896A1 (en) * 2007-05-04 2010-05-13 Centre National De La Recherche Scientifique (C.N. R.S.) Method for producing dihydrogen from hydrogenated silicon
JP2010526011A (en) * 2007-05-04 2010-07-29 サントル ナシオナル ドゥ ラ ルシェルシェサイアンティフィク(セエヌエールエス) Method for generating hydrogen molecules from silicon hydride
US8802307B2 (en) 2007-05-04 2014-08-12 Centre National De La Recherche Scientifique (C.N.R.S.) Method for producing dihydrogen from hydrogenated silicon
WO2008148988A2 (en) * 2007-05-04 2008-12-11 Centre National De La Recherche Scientifique (C.N.R.S) Method for producing dihydrogen from hydrogenated silicon
JP2009023857A (en) * 2007-07-18 2009-02-05 Toyota Central R&D Labs Inc Hydrogen generation apparatus
JP2013519615A (en) * 2010-02-15 2013-05-30 ユニベルシテ デ―マルセイユ Method for producing hydrogen from silylated derivative as hydrogen carrier using phosphine oxide catalyst

Also Published As

Publication number Publication date
JPS6232121B2 (en) 1987-07-13

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