JPS6236961B2 - - Google Patents
Info
- Publication number
- JPS6236961B2 JPS6236961B2 JP57013125A JP1312582A JPS6236961B2 JP S6236961 B2 JPS6236961 B2 JP S6236961B2 JP 57013125 A JP57013125 A JP 57013125A JP 1312582 A JP1312582 A JP 1312582A JP S6236961 B2 JPS6236961 B2 JP S6236961B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- hydrogen storage
- silicon
- sih
- storage material
- 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
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Classifications
-
- 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
- Y02E60/32—Hydrogen storage
Landscapes
- Physical Vapour Deposition (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Silicon Compounds (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
本発明は新規な水素吸蔵物質およびその製造方
法に関する。
特願昭56−70200号明細書に記載されている水
素吸蔵物質は四配位Si格子とこれを取り巻くSiH2
または/およびSiH3の殻とからなつている多結
晶体である。そしてこの物質はH2によるSiの反
応性スパツタリング法またはグロー放電法などに
よつてガラス、合成樹脂、金属などの基板上に蒸
着させることにより得られ、その四配位Si格子の
空隙中に吸蔵される水素量は約50原子%であり多
量の水素を含有している。しかしながらこの水素
吸蔵物質の製造には装着上の制約(装置の寸法、
電源、反応条件などの制約)があつて多量生産が
極めて困難であり、また例えば反応性スパツタリ
ング法においてはスパツタリングにより生成され
た水素ラジカルがSi−ターゲツトと反応するいわ
ゆる化学反応が蒸着物質生成の駆動力となるに過
ぎないので、反応雰囲気に電離し易いAr等を使
用した場合と比較して蒸着量が著しく少ない。な
お、高周波電力をマグネトロンにより増大させる
ことにより蒸着量を幾分大きくすることもできる
が電力消費量の増大に相応した経済的な製造を行
うことができない。従つて現在の製品Kg当りの製
造原価は数10〜数100万円であつて経済的に極め
て不利である。
本発明者等は上記のような従来の水素吸蔵物質
の不利益を排除するために多くの研究を重ね経済
的に極めて有利な多結晶性の新規水素吸蔵物質を
製造することができた。
すなわち、本発明によれば、シランSiH4をグ
ロー放電により分解してSi−ターゲツト上に粉末
状水素含有珪素化合物を蒸着させる。前者の場合
には放電室の壁面を約0℃以下(低くければ低い
程よい)に冷却しておくと壁面上に本発明による
水素吸蔵物質が黄褐色粉末として生成する。得ら
れた生成物のIRスペクトル図を第1図に示す。
第1図からこの生成物が約2104cm-1および約2085
cm-1にピークを有することがわかる。なお破線は
水素放出後のIRスペクトル図である。また水素
ラジカルと反応しないSiH4原料も気相からの生
成粉末の冷却壁面上への析出を促進する。こうし
て得られた粉末状物質は大部分の特願昭56−
70200号と同様にSi微結晶を水素が結合したSiが
取り巻いている。しかし異なる点は−(SiH2)o−
鎖状結合と小部分の四配位Si格子とよりなり、多
量の結合水素と少量の遊離水素とを含有してい
る。すなわち、本発明は、シリコン微結晶粒子の
表面を、−(SiH2)o−結合鎖が該シリコン微結晶粒
子表面のシリコン原子と結合して覆つて成り、
100〜200℃加熱により、前記−(SiH2)o−結合鎖
より水素を40〜70原子%放出することを特徴とす
る新規水素吸蔵物質である。例えばグロー放電に
より得られた水素吸蔵物質の含有している結合水
素は壁面温度の変化に対して第2a図に示すよう
な変化を示すが、このことから粉末製品の付着す
る壁面温度はより低温度であることが好ましいこ
とがわかる。従つて本発明によれば、粉末状水素
吸蔵物質の付着すべき壁面の温度は0℃以下であ
り、このような低温に保持することにより40原子
%以上の水素を吸蔵させることができる。また、
壁面温度は低ければ低い程水素吸蔵量は増大する
が、−100℃で70原子%の水素吸蔵量のものを生産
するのが工業的に有利である。本発明によつて得
られる新規水素吸蔵物質は加熱により結合水素を
放出するが、その水素放出率と加熱温度との関係
は第4図に示す通りであり、加熱温度100〜200℃
で殆んどすべての結合水素を放出するが、第1図
のIRスペクトル図からもわかるようにこれは水
素吸蔵物質を構成している−(SiH2)o−結合鎖か
ら水素が放出されるものである。
本発明による水素吸蔵物質の製造工程を第3図
によつて説明する。1は例えば容量300Wの高周
波電源であり、マツチングボツクス2を介してガ
ラス製ベルジヤー6(径300mm)に接続されてい
る。ガスボンベ3からはシランガスが圧力計4、
流量制御器5を経てベルジヤー6の上部電極
(SUS製、径200mm)7に供給される。ベルジヤー
内は0.1〜10Torrに保持されており、上部電極と
これに対向しているSUS製コンベアー10との間
でグロー放電が行われる。コンベアー内部には液
体窒素を循環させた冷却器8が上部電極の対向位
置に配置されていて水素吸蔵粉末がコンベアー上
に沈着するのを促進するようになつている。コン
ベアーは水素吸蔵物質の生成量が或る量に達する
毎に間歇的に駆動され、粉末逆流防止堰13を経
てナイフエツジ14により掻き落されて粉末保持
容器16内に捕集される。粉末保持容器16内は
バツグフイルター15を介して減圧排気されてい
る。12はステンレス製反応室で真空計11によ
り室内の真空度が監視されている。こうして得ら
れた物質は30〜70原子%の水素を含有している。
次の実施例によつて本発明の水素吸蔵物質の製
造を説明する(第3図参照)。
実施例
純度約99%以上のシランガスを圧力約1気圧
(50Pa、ゲージ圧)、流量2〜30SCCM(標準状
態、c.c./分)で反応室に供給する。反応室内の圧
力は予め約10-2Torr以下にしてあるが、供給弁
を調節して室内の圧力を0.1〜5Torrに制御する。
反応室内のSUS製コンベアーはベルジヤー内の上
部電極(径200mm)との対向位置は所望の冷却温
度により例えばフレオン、水または液体窒素で冷
却されるが、ここでは液体窒素により−100℃以
下に冷却する。シランガスを約10分間反応室内に
流して室内雰囲気を安定化した後、上記電極に高
周波電源(13.56MHz)から電力(6W以上)を供
給する。この供給電力の多い程粉末生成量は多く
なる。こうしてグロー放電が開始すると直ちにコ
ンベアーの冷却面上に粉末が生成し始めるが、粉
末層の厚さが5〜10mmになつたときにコンベアー
を駆動させ新たな冷却面を上部電極に対向させて
停止し、新たに粉末の生成が行われる。こうして
コンベアーは間歇的に駆動され、やがてコンベア
ー上の堆積粉末は粉末保持容器の上方に達し、ナ
イフエツジでコンベアーから掻き取られ、反応後
の気体はバツグフイルターによつて粉末と分離さ
れ排気される。このようにして生成した水素吸蔵
粉末のガスクロマトグラフイーによつて測定した
水素含有量とコンベアー冷却面温度(粉末付着壁
面温度)との関係は第2a図の通りであつた。ま
たシランガス供給量を6SCCMとしたときの供給
高周波電力と水素吸蔵粉末生成量(g/時)との
関係は第2b図の通りであつた。すなわち、径
200mmの上部電極を用いたときに供給電力70Wま
では略直線的に水素吸蔵物質の生成量が増大する
ことがわかる。従つて本発明方法においては
70W/π(200mm/2)2=22×10-2W/cm2以下
の供給電力でグロー放電を行う。また高周波電源
を10Wとしたシランガス流量を15SCCMとしたと
きの反応室内圧力と水素吸蔵粉末生成量との関係
は第5a図のようであり、また高周波電源を6W
とし反応室内圧力を0.2Torrとしたときのシラン
ガス流量(SCCM)と水素吸蔵粉末生成量との関
係は第5b図のようであつた。これらの結果から
反応室内圧力、原料シランガス流量には最適値の
あることがわかる。
この実施例で得た水素吸蔵物質の生成量を従来
法(マグネトロンスパツタリング法;電源
360W、蒸着基板面積50cm2、シランガス流量
6SCCM)によるものと比較すると第1表の通り
である。
The present invention relates to a novel hydrogen storage material and a method for producing the same. The hydrogen storage material described in Japanese Patent Application No. 1987-70200 consists of a four-coordinated Si lattice and surrounding SiH 2
and/or a polycrystalline body consisting of a SiH 3 shell. This substance is obtained by vapor-depositing it onto a substrate such as glass, synthetic resin, or metal by a reactive sputtering method of Si using H 2 or a glow discharge method, and is occluded in the voids of the four-coordinate Si lattice. The amount of hydrogen released is about 50 atomic %, and it contains a large amount of hydrogen. However, the manufacturing of this hydrogen storage material has mounting limitations (device size,
For example, in the reactive sputtering method, hydrogen radicals generated by sputtering react with the Si target, a so-called chemical reaction that drives the formation of the deposited material. Since it only acts as a force, the amount of evaporation is significantly smaller than when Ar, etc., which easily ionize, is used in the reaction atmosphere. Although the amount of vapor deposition can be somewhat increased by increasing the high-frequency power using a magnetron, it is not possible to perform economical manufacturing commensurate with the increase in power consumption. Therefore, the current manufacturing cost per kg of product is several tens to several million yen, which is extremely disadvantageous economically. The present inventors have conducted extensive research in order to eliminate the disadvantages of conventional hydrogen storage materials as described above, and were able to produce a new polycrystalline hydrogen storage material that is economically extremely advantageous. That is, according to the present invention, silane SiH 4 is decomposed by glow discharge to deposit a powdered hydrogen-containing silicon compound onto a Si target. In the former case, if the wall surface of the discharge chamber is cooled to about 0.degree. C. or lower (the lower the better), the hydrogen storage material according to the present invention will be formed on the wall surface as a yellowish brown powder. The IR spectrum of the obtained product is shown in FIG.
From Figure 1, this product is about 2104 cm -1 and about 2085 cm -1
It can be seen that there is a peak at cm -1 . Note that the broken line is an IR spectrum diagram after hydrogen release. In addition, the SiH 4 raw material that does not react with hydrogen radicals also promotes the precipitation of the generated powder from the gas phase onto the cooling wall surface. The powdery substance obtained in this way is used in most of the patent applications filed in
Similar to No. 70200, Si microcrystals are surrounded by Si with hydrogen bonded to them. However, the difference is −(SiH 2 ) o −
It consists of chain bonds and a small portion of a four-coordinated Si lattice, and contains a large amount of bound hydrogen and a small amount of free hydrogen. That is, in the present invention, the surface of a silicon microcrystal particle is covered with -(SiH 2 ) o - bond chains bonded to silicon atoms on the surface of the silicon microcrystal particle,
This is a novel hydrogen storage material characterized by releasing 40 to 70 atomic % of hydrogen from the -(SiH 2 ) o - bonded chain when heated at 100 to 200°C. For example, the bound hydrogen contained in a hydrogen storage material obtained by glow discharge shows a change as shown in Figure 2a in response to a change in wall surface temperature, which suggests that the temperature of the wall surface to which the powdered product adheres will be lower. It can be seen that temperature is preferable. Therefore, according to the present invention, the temperature of the wall surface to which the powdered hydrogen storage material is to be attached is 0° C. or lower, and by maintaining the temperature at such a low temperature, it is possible to store 40 atomic percent or more of hydrogen. Also,
The lower the wall temperature, the greater the hydrogen absorption capacity, but it is industrially advantageous to produce a hydrogen absorption capacity of 70 at.% at -100°C. The new hydrogen storage material obtained by the present invention releases bound hydrogen when heated, and the relationship between the hydrogen release rate and heating temperature is as shown in Figure 4.
Almost all of the bonded hydrogen is released, but as can be seen from the IR spectrum in Figure 1, this constitutes a hydrogen storage material - (SiH 2 ) o - Hydrogen is released from the bonded chain. It is something. The manufacturing process of the hydrogen storage material according to the present invention will be explained with reference to FIG. 1 is a high frequency power source with a capacity of 300 W, for example, and is connected to a glass bell jar 6 (diameter 300 mm) via a matching box 2. Silane gas flows from gas cylinder 3 to pressure gauge 4,
It is supplied to the upper electrode (made of SUS, diameter 200 mm) 7 of the bell gear 6 through the flow rate controller 5. The inside of the bell gear is maintained at 0.1 to 10 Torr, and glow discharge occurs between the upper electrode and the SUS conveyor 10 facing thereto. Inside the conveyor, a cooler 8 that circulates liquid nitrogen is placed opposite the upper electrode to promote the deposition of the hydrogen storage powder on the conveyor. The conveyor is driven intermittently every time the amount of hydrogen storage material produced reaches a certain level, and the hydrogen storage material is scraped off by a knife edge 14 through a powder backflow prevention weir 13 and collected in a powder holding container 16. The inside of the powder holding container 16 is evacuated through a bag filter 15. Reference numeral 12 denotes a reaction chamber made of stainless steel, and the degree of vacuum in the chamber is monitored by a vacuum gauge 11. The material thus obtained contains 30-70 atomic percent hydrogen. The following example illustrates the production of the hydrogen storage material of the present invention (see Figure 3). Example Silane gas having a purity of about 99% or more is supplied to a reaction chamber at a pressure of about 1 atmosphere (50 Pa, gauge pressure) and a flow rate of 2 to 30 SCCM (standard conditions, cc/min). The pressure inside the reaction chamber is set to below about 10 -2 Torr in advance, and the pressure inside the reaction chamber is controlled to 0.1 to 5 Torr by adjusting the supply valve.
The SUS conveyor inside the reaction chamber is cooled at the position opposite the upper electrode (diameter 200 mm) in the bell jar with, for example, Freon, water, or liquid nitrogen depending on the desired cooling temperature, but here it is cooled to below -100℃ with liquid nitrogen. do. After stabilizing the chamber atmosphere by flowing silane gas into the reaction chamber for about 10 minutes, power (6 W or more) is supplied to the above electrodes from a high frequency power source (13.56 MHz). The more power is supplied, the more powder is produced. As soon as the glow discharge starts, powder begins to form on the cooling surface of the conveyor, but when the thickness of the powder layer reaches 5 to 10 mm, the conveyor is driven and the new cooling surface faces the upper electrode and then stopped. Then, new powder is generated. In this way, the conveyor is driven intermittently, and eventually the powder deposited on the conveyor reaches above the powder holding container and is scraped off from the conveyor by a knife edge, and the gas after the reaction is separated from the powder by a bag filter and exhausted. The relationship between the hydrogen content measured by gas chromatography of the hydrogen storage powder thus produced and the conveyor cooling surface temperature (powder adhesion wall surface temperature) was as shown in FIG. 2a. Furthermore, when the silane gas supply amount was 6 SCCM, the relationship between the supplied high frequency power and the amount of hydrogen storage powder produced (g/hour) was as shown in FIG. 2b. That is, the diameter
It can be seen that when a 200 mm upper electrode is used, the amount of hydrogen storage material produced increases almost linearly up to a supplied power of 70 W. Therefore, in the method of the present invention
70W/π (200mm/2) 2 = 22×10 -2 W/cm 2 Glow discharge is performed with a supplied power of less than 2. Furthermore, the relationship between the pressure in the reaction chamber and the amount of hydrogen storage powder produced when the high frequency power source is 10 W and the silane gas flow rate is 15 SCCM is as shown in Figure 5a.
The relationship between the silane gas flow rate (SCCM) and the amount of hydrogen storage powder produced when the reaction chamber pressure was 0.2 Torr was as shown in Figure 5b. From these results, it can be seen that there are optimum values for the reaction chamber pressure and the raw material silane gas flow rate. The amount of hydrogen storage material produced in this example was calculated using the conventional method (magnetron sputtering method;
360W, evaporation substrate area 50cm 2 , silane gas flow rate
6SCCM) as shown in Table 1.
【表】
第1表の結果から、本発明によれば従来法の1/
60の電力で2000倍の生産量を得ることができるこ
とが明らかであり、従つて本発明は水素吸蔵量の
大きい製品を大量生産するのに適した産業上極め
て優れた作用効果を有することがわかる。[Table] From the results in Table 1, it can be seen that according to the present invention, the conventional method
It is clear that 2,000 times the production can be obtained with 60 liters of electric power, and therefore, it can be seen that the present invention has extremely excellent industrial effects suitable for mass production of products with a large hydrogen storage capacity. .
第1図は本発明による水素吸蔵物質のIRスペ
クトル図であり、第2a図は本発明による水素吸
蔵物質の粉末壁面付着温度と結合水素量との関係
を示すグラフであり、第2b図は本発明による水
素吸蔵物質の生成量と供給電力との関係を示すグ
ラフであり、第3図は本発明による水素吸蔵物質
の製造方法を説明するための図であり、第4図は
本発明による水素吸蔵物質の加熱温度と水素放出
量との関係を示すグラフであり、第5a図および
第5b図はそれぞれ反応室圧力およびシランガス
供給量と水素吸蔵物質の生成量との関係を示すグ
ラフである。
図中符号:1……高周波電源、2……マツチン
グボツクス、3……ガスボンベ、4……圧力計、
5……流量制御器、6……ベルジヤー、7……上
部電極、8……冷却器、9……水素吸蔵物質粉
末、10……コンベアー、11……真空計、12
……反応室、13……粉末逆流防止堰、14……
ナイフエツジ、15……バツグフイルター、16
……粉末保持容器。
FIG. 1 is an IR spectrum diagram of the hydrogen storage material according to the present invention, FIG. 2a is a graph showing the relationship between the powder wall adhesion temperature and the amount of bound hydrogen of the hydrogen storage material according to the present invention, and FIG. 3 is a graph showing the relationship between the production amount of the hydrogen storage material according to the invention and the supplied power, FIG. 3 is a diagram for explaining the method for producing the hydrogen storage material according to the invention, and FIG. 5A and 5B are graphs showing the relationship between the reaction chamber pressure, the amount of silane gas supplied, and the amount of hydrogen storage material produced, respectively. FIG. Codes in the figure: 1...High frequency power supply, 2...Matching box, 3...Gas cylinder, 4...Pressure gauge,
5...Flow rate controller, 6...Belgear, 7...Upper electrode, 8...Cooler, 9...Hydrogen storage material powder, 10...Conveyor, 11...Vacuum gauge, 12
... Reaction chamber, 13 ... Powder backflow prevention weir, 14 ...
Knife Edge, 15... Buzz Filter, 16
...Powder holding container.
Claims (1)
合鎖が該シリコン微結晶粒子表面のシリコン原子
と結合して覆つて成り、100〜200℃加熱により、
前記−(SiH2)o−結合鎖より水素を40〜70原子%
放出することを特徴とする新規水素吸蔵物質。 2 シランガスを圧力0.1〜10Torrの下でシラン
ガス流量2〜30ml/分(標準状態)、供給電力22
×10-2W/cm2以下でグロー放電に付し、温度0℃
以下の冷却面に水素含有珪素化合物(シリコン微
結晶粒子の表面を、−(SiH2)o−結合鎖が該シリコ
ン微結晶粒子表面のシリコン原子と結合して覆つ
て成り、100〜200℃加熱により、前記−(SiH2)o
−結合鎖より水素を40〜70原子%放出する)を装
着させることを特徴とする新規水素吸蔵物質の製
造方法。[Claims] 1 The surface of a silicon microcrystalline particle is covered with -(SiH 2 ) o - bond chains bonded to silicon atoms on the surface of the silicon microcrystalline particle, and by heating at 100 to 200°C,
40 to 70 atom% of hydrogen from the -(SiH 2 ) o - bond chain
A new hydrogen storage material that releases hydrogen. 2 Silane gas under pressure 0.1 to 10 Torr, silane gas flow rate 2 to 30 ml/min (standard condition), supply power 22
×10 -2 W/cm 2 or less, subject to glow discharge, temperature 0℃
The following cooling surface is coated with a hydrogen-containing silicon compound (the surface of a silicon microcrystal particle is covered with -(SiH 2 ) o - bond chains bonded to the silicon atoms on the surface of the silicon microcrystal particle, and heated to 100 to 200°C. According to the above-mentioned −(SiH 2 ) o
- A method for producing a novel hydrogen storage material, characterized by attaching a compound (which releases 40 to 70 atomic percent of hydrogen from a bonded chain).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57013125A JPS58135102A (en) | 1982-01-29 | 1982-01-29 | Novel hydrogen-storage substance and its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57013125A JPS58135102A (en) | 1982-01-29 | 1982-01-29 | Novel hydrogen-storage substance and its production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58135102A JPS58135102A (en) | 1983-08-11 |
| JPS6236961B2 true JPS6236961B2 (en) | 1987-08-10 |
Family
ID=11824433
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57013125A Granted JPS58135102A (en) | 1982-01-29 | 1982-01-29 | Novel hydrogen-storage substance and its production |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58135102A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5899304U (en) * | 1981-12-28 | 1983-07-06 | 日本軌道工業株式会社 | Traveling road surface epoxy mortar paving machine |
-
1982
- 1982-01-29 JP JP57013125A patent/JPS58135102A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58135102A (en) | 1983-08-11 |
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