JPH0142887B2 - - Google Patents
Info
- Publication number
- JPH0142887B2 JPH0142887B2 JP62256430A JP25643087A JPH0142887B2 JP H0142887 B2 JPH0142887 B2 JP H0142887B2 JP 62256430 A JP62256430 A JP 62256430A JP 25643087 A JP25643087 A JP 25643087A JP H0142887 B2 JPH0142887 B2 JP H0142887B2
- Authority
- JP
- Japan
- Prior art keywords
- silicon
- modified silica
- boron
- derivative
- silica
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/09—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
- C07C29/10—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B35/00—Boron; Compounds thereof
- C01B35/08—Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
- C01B35/10—Compounds containing boron and oxygen
- C01B35/1009—Compounds containing boron and oxygen having molecular-sieve properties
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B35/00—Boron; Compounds thereof
- C01B35/08—Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
- C01B35/10—Compounds containing boron and oxygen
- C01B35/12—Borates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
- C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
- C07C2/66—Catalytic processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/86—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
- C07C2/862—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms
- C07C2/864—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms the non-hydrocarbon is an alcohol
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- C07C2521/08—Silica
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Silicon Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
本発明は、結晶性シリカに関連する新規合成物
質に係る。さらに詳述すれば、本発明は、ケイ素
及びホウ素の酸化物でなりかつ多孔性の結晶構造
を有する合成物質、該合成物質の製法及び該合成
物質の使用に関するものである。
各種文献によれば、ホウ素が平面配位又は四面
体配位を有しうる稠密な天然のホウケイ酸塩(非
多孔性物質である)が知られている。多孔性ガラ
スも公知であり、かかるガラスはガラス様物質を
化学的に作用せしめることにより得られる。これ
らの物質はその原材料に応じて、シリカ、アルカ
リ、アルミナ及びB2O3を含みうる。文献は、ホ
ウ素の配位がゼオライト形構造、すなわち規則正
しい多孔性の結晶構造であることを教示している
が、これまでのところ、かかる構造は得られてい
ない(Break ゼオライト・モレキユラー・シー
ブス(Zeolite Molecular Sieves)J.Wiley and
Sons社、ニユーヨーク、1974、第322頁)。
公知の方法は、米国特許第4049573号に記載の
如く、アルミニウム及びケイ素の酸化物からなる
ゼオライトにホウ素を含浸せしめることのみであ
る。この場合、ホウ素は結晶格子の一部を構成す
るよう格子内に入るものではない。
発明者らは、ケイ素に代わる置換体としてホウ
素を結晶格子に導入せしめることによつて変性せ
しめた結晶性シリカを開発した。
さらに、発明者らは、ホウ素がケイ素に代わる
置換用元素となる以外には、多孔質であり、よく
制御されかつゼオライト構造に近似した結晶構造
を有する新規物質を生成し得るとの知見を得て本
発明に至つた。
該物質(本明細書の以下の記載では、簡略化の
ため「ボラリツト(Boralite)A」と称する)
は、酸化物のモル比として、かつ無水状態として
次式により特徴ずけられる。
(0−1)R2O・(0−1)C2/oO
・B2O3・(8−30)SiO2
(式中、Rはテトラメチルアンモニウムカチオン
(TMA)であり、CはH+、NH4 +又は原子価n
の金属の如きカチオンである。)
なお、ボラリツトAの熱安定性はモル比
SiO2/B2O3が大きいことに関連する。
特に、か焼された後ではR2Oが存在しないこと
が望ましい(ただし、必ずしも厳密な意味ではな
い)。
上記式に相当するボラリツトAは特定の結晶構
造を有し、高温度(450℃ないし750℃)でか焼し
たH+形のものに関するX線回折スペクトルは第
1表に記載の特徴的なピークを示す。
The present invention relates to novel synthetic materials related to crystalline silica. More particularly, the present invention relates to a synthetic material made of oxides of silicon and boron and having a porous crystal structure, a process for making the synthetic material, and a use of the synthetic material. According to various literatures, dense natural borosilicates (which are non-porous materials) are known, in which boron can have planar or tetrahedral coordination. Porous glasses are also known, and such glasses are obtained by chemically acting on glass-like substances. Depending on their source, these materials can include silica, alkali, alumina and B2O3 . Although the literature teaches that the coordination of boron is a zeolite-type structure, i.e. an ordered porous crystal structure, so far such a structure has not been obtained (Break Zeolite Molecular Sieves). Molecular Sieves) J. Wiley and
Sons, New York, 1974, p. 322). The only known method is to impregnate a zeolite of aluminum and silicon oxides with boron, as described in US Pat. No. 4,049,573. In this case, the boron does not enter the crystal lattice to form part of it. The inventors have developed crystalline silica modified by introducing boron into the crystal lattice as a substitute for silicon. Furthermore, the inventors have found that boron, in addition to being a replacement element for silicon, can produce new materials that are porous, well-controlled, and have a crystalline structure similar to that of a zeolite. This led to the present invention. The substance (hereinafter referred to as "Boralite A" for the sake of brevity)
is characterized as the molar ratio of oxides and in the anhydrous state by the following formula: (0-1) R2O・(0-1)C2 / oO・B2O3・( 8-30 ) SiO2 (wherein, R is tetramethylammonium cation (TMA) and C is H + , NH 4 + or valence n
It is a cation such as a metal. ) The thermal stability of Volarit A is determined by the molar ratio
This is related to the fact that SiO 2 /B 2 O 3 is large. In particular, it is desirable (but not necessarily in a strict sense) that R 2 O be absent after calcination. Volatile A, which corresponds to the above formula, has a specific crystal structure, and the X-ray diffraction spectrum of the H + form calcined at high temperatures (450°C to 750°C) has the characteristic peaks listed in Table 1. shows.
【表】
モル比SiO2/B2O3、焼成温度及びカチオンの
性質の変化に伴つて、上記数値は若干変化する。
H+の代わりに他のカチオンが存在する場合に
は、通常のゼオライトのものと類似してスペクト
ルにわずかな変化を生ずる。
赤外線吸収スペクトルでは、導入されたホウ素
の量を関数として910ないし925cm-1の領域に特徴
的な吸収を示す。
ボラリツトAの製法は、水熱反応条件下、ケイ
素誘導体、ホウ素誘導体及び包接化剤(テトラメ
チルアンモニウム化合物)を、PH9ないし14、温
度110ないし220℃、期間1ないし30日間で反応さ
せることを特徴とする。
ホウ素及びケイ素の有機誘導体(たとえばホウ
酸トリアルキル及びオルトケイ酸テトラアルキル
エステル)を使用し、テフロン(登録商標)容
器、又はポリプロピレン、白金、その他の材料の
容器(アルカリ性溶液が結晶化容器から不純物を
抽出することを防止するため)において、水熱反
応を行なうことにより、高純度のボラリツトAが
得られる。
不純物が存在しないことは、ボラリツトAの特
有な性質(たとえば疎水性であること、このため
脱水力を持たないこと)を保証する。
非常に高い純度が要求されない場合には、各成
分について安価な原料を使用できる。たとえばホ
ウ素のついては、ホウ酸、ホウ酸ナトリウム及び
ホウ砂を使用でき、ケイ素については、コロイド
状シリカ、シリカゲル、ケイ酸ナトリウム、エア
ロジルなどを使用できる。さらに結晶化には、ガ
ラス、ステンレス鋼などで形成された容器を使用
できる。
かかる場合、ボリラツトAは反応体又は結晶化
容器に由来する不純物を含む場合がある。たとえ
ば、市販のシリカはAl2O32000ppm以下を含む
が、10000ppm程度のアルミナ含量では、他の性
質、たとえば疎水性及び脱水力が変化されること
があつたとしても、構造及び結晶学上の特性を変
化させるものではない。
アルカリ金属又はアルカリ土類金属の水酸化物
又はハロゲン化物の如き鉱化剤を添加することも
できる。
ボラリツトAは、高温度での熱処理及び水蒸気
の存在下における熱処理のいずれにおいても非常
に安定である。
本発明によるボラリツトAは、そのままで又は
好ましくはシリカ、アルミナ及びクレー様物質か
ら選ばれる不活性担体上に分散担持された状態で
触媒反応又は吸収処理で使用される。一般に、下
記の多数の反応で利用される。
1 トルエンをメタノールでアルキル化してキシ
レン、主としてパラ−キシレンを生成する反応
2 トルエンを不均化して主としてパラ−キシレ
ンを生成する反応
3 ジメチルエーテル及び/又はメタノール又は
他の低級アルコールのオレフイン類及び芳香族
類の如き炭化水素への変換反応
4 クラツキング及び水素化分解
5 ノルマル−パラフイン及びナフテンの異性化
6 オレフイン結合又はアセチレン結合を有する
化合物の重合
7 改質反応
8 オルト−キシレンの如きポリアルキル置換芳
香族化合物の異性化
9 芳香族類、特にトルエンの不均化
10 脂肪族カルボニル化合物の少なくとも部分的
芳香族炭化水素への変換反応
11 他のC8芳香族炭化水素からエチルベンゼン
の分離
12 炭化水素の水素添加及び脱水素
13 メタン化
14 酸化、特に内燃機関排出物の配化
15 含酸素脂肪族化合物の脱水
16 オレフインの高オクタン価燃料への変換
特に、本発明のボラリツトAは、メチル第3級
ブチルエーテルからメタノール及びイソブチレン
を生成する反応における触媒として有効に使用さ
れる。
上述した本発明の目的を説明するために、次に
いくつかの実施例について述べるが、これに限定
されるものではない。
実施例 1
CO2を含有しない雰囲気に維持したパイレツク
スガラス容器に、水酸化テトラメチルアンモニウ
ムの25%(重量)溶液132gを導入し、ついて撹
拌しながら、ホウ酸18.6gを加えた。
溶解後、なお撹伴を続けながら、オルトケイ酸
テトラエチルエステル187.5gを添加した。
反応混合物を撹拌しながら60℃に加熱した。反
応により白色の乳状沈殿が徐々に生成し、進行
中、オルトケイ酸エステルの加水分解によつて生
成するエタノールを同時に留去した。
12時間後、アルコールを完全に除去し、
KOH0.18g及び蒸留水を添加して全量を約300ml
とした。この段階で、反応混合物をテフロンで内
張りした静置オートクレーブに移し、145℃にお
ける水熱反応を開始し、12日間続けた。ついで、
このようにして得られた反応生成物を室温まで冷
却させ、フイルター上で集め、蒸留水で注意深く
洗浄し、120℃で乾燥した。
生成物は粒径約0.1ないし0.5μmの結晶よりな
るものであつた。
生成物の一部を750℃でか焼した。かかる生成
物はモル比SiO2/B2O3=11を有するものである。
H+形の場合のX線回折スペクトルは第1表のデ
ータと一致した。
赤外線吸収スペクトルでは、ホウ素に係る921
cm-1に特徴的な吸収バンド(従来のゼオライトで
は見ることができない)を示した。
実施例 2
この実施例は、コロイド状シリカを使用するボ
ラリツトAの調製を説明するものである。
実施例1と同様に操作し、かつ同じ順序で、水
酸化テトラメチルアンモニウムの25%(重量)溶
液210g、H3BO327g及びLudoxコロイド状シリ
カ(濃度40%)240gをパイレツクスガラス容器
に充填し、撹拌し、80℃に1時間加熱した後、反
応混合物を撹拌機付チタン製オートクレーブ(1
)に入れ、自然発生圧力下、150℃において水
熱反応を10日間実施した。
反応による結晶生成物をフイルター上で進め、
洗浄し、乾燥し、750℃において6時間か焼した。
生成物は、H+形の場合、第1表に示すX線回折
スペクトル及び917cm-1における赤外線吸収バン
ドを有するものであつた。さらに反応生成物は下
記の性質を示した。
実測密度(ヘリウム法):2.19g/cm3
酸性度(CsCl法):PH2.4
モル比SiO2/B2O3:12.3
参考例
内径8mmの電気加熱式管状反応器に、実施例1
に従つて調製した粒径14ないし30メツシユ
(ASTM、米国シリーズ)のボラリツトA触媒3
mlを充填した。
定量ポンプにより、反応器に、予熱管で予熱し
たメチル第3級ブチルエーテルを導入した。
反応器の下流に、6バールに設定した圧力チエ
ツク弁をを設けた。このチエツク弁に、適当に加
熱される試料採集装置を具備せしめ、圧力が低下
する際、反応器の流出物をガスクロマトグラフイ
ーに導入するようにした。
第2表に示す温度に加熱し、メチル第3級ブチ
ルエーテルを流量毎時6cm3(すなわち液空間速度
(LHSV)=2)で導入した。得られた結果を同じ
く第2表に示す。[Table] The above values change slightly with changes in the molar ratio SiO 2 /B 2 O 3 , calcination temperature, and cation properties. The presence of other cations instead of H + produces slight changes in the spectra similar to those of normal zeolites. The infrared absorption spectrum shows characteristic absorption in the region of 910 to 925 cm -1 as a function of the amount of boron introduced. The manufacturing method for Volarit A involves reacting a silicon derivative, a boron derivative, and an clathrating agent (tetramethylammonium compound) under hydrothermal reaction conditions at a pH of 9 to 14, a temperature of 110 to 220°C, and a period of 1 to 30 days. Features. Organic derivatives of boron and silicon (e.g., trialkyl borates and tetraalkyl orthosilicate esters) are used to remove impurities from the crystallization vessel, such as in Teflon vessels or vessels of polypropylene, platinum, or other materials. In order to prevent extraction), high purity volatile A can be obtained by carrying out a hydrothermal reaction. The absence of impurities guarantees the unique properties of volatile A, such as its hydrophobic nature and therefore no dehydrating power. If very high purity is not required, inexpensive raw materials can be used for each component. For example, for boron, boric acid, sodium borate, and borax can be used, and for silicon, colloidal silica, silica gel, sodium silicate, Aerosil, etc. can be used. Additionally, containers made of glass, stainless steel, etc. can be used for crystallization. In such cases, Borirat A may contain impurities originating from the reactants or the crystallization vessel. For example, commercially available silica contains less than 2000 ppm Al 2 O 3 , but at alumina contents of around 10 000 ppm, structural and crystallographic It does not change the characteristics. Mineralizing agents such as alkali metal or alkaline earth metal hydroxides or halides can also be added. Volarit A is very stable both when heat treated at high temperatures and in the presence of water vapor. Volarit A according to the invention is used in catalytic reactions or absorption treatments as such or dispersedly supported on an inert support, preferably chosen from silica, alumina and clay-like materials. It is commonly utilized in a number of reactions described below. 1 Reaction of alkylating toluene with methanol to produce xylene, mainly para-xylene 2 Reaction of disproportionation of toluene to produce mainly para-xylene 3 Olefins and aromatics of dimethyl ether and/or methanol or other lower alcohols 4. Cracking and hydrogenolysis 5. Isomerization of normal-paraffins and naphthenes 6. Polymerization of compounds with olefin or acetylene bonds 7. Modification reactions 8. Polyalkyl-substituted aromatics such as ortho-xylene Isomerization of Compounds 9 Disproportionation of Aromatics, Especially Toluene 10 Conversion of Aliphatic Carbonyl Compounds to At least Partial Aromatic Hydrocarbons 11 Separation of Ethylbenzene from Other C 8 Aromatic Hydrocarbons 12 Hydrogen of Hydrocarbons Addition and dehydrogenation 13 Methanation 14 Oxidation, especially the formulation of internal combustion engine emissions 15 Dehydration of oxygenated aliphatic compounds 16 Conversion of olefins to high octane fuels In particular, Volarit A of the present invention can be prepared from methyl tertiary butyl ether. Effectively used as a catalyst in reactions that produce methanol and isobutylene. In order to explain the above-mentioned object of the present invention, some examples will be described next, but the present invention is not limited thereto. Example 1 Into a Pyrex glass vessel maintained in a CO 2 -free atmosphere, 132 g of a 25% (by weight) solution of tetramethylammonium hydroxide was introduced, followed by the addition of 18.6 g of boric acid with stirring. After dissolution, 187.5 g of orthosilicate tetraethyl ester was added while stirring was continued. The reaction mixture was heated to 60°C with stirring. The reaction gradually produced a white milky precipitate, and during the reaction, ethanol produced by hydrolysis of the orthosilicate ester was simultaneously distilled off. After 12 hours, alcohol is completely removed,
Add 0.18g of KOH and distilled water to bring the total volume to about 300ml
And so. At this stage, the reaction mixture was transferred to a Teflon-lined static autoclave and a hydrothermal reaction at 145°C was initiated and continued for 12 days. Then,
The reaction product thus obtained was allowed to cool to room temperature, collected on a filter, carefully washed with distilled water and dried at 120°C. The product consisted of crystals with a particle size of about 0.1 to 0.5 μm. A portion of the product was calcined at 750°C. Such a product has a molar ratio SiO 2 /B 2 O 3 =11.
The X-ray diffraction spectrum for the H + form was consistent with the data in Table 1. In the infrared absorption spectrum, 921 related to boron
It showed a characteristic absorption band in cm -1 (which cannot be seen in conventional zeolites). Example 2 This example describes the preparation of Volatile A using colloidal silica. Working as in Example 1 and in the same order, 210 g of a 25% (by weight) solution of tetramethylammonium hydroxide, 27 g of H 3 BO 3 and 240 g of Ludox colloidal silica (40% concentration) are placed in a Pyrex glass container. After charging, stirring and heating to 80°C for 1 hour, the reaction mixture was transferred to a titanium autoclave (1 hour) with a stirrer.
), and a hydrothermal reaction was carried out at 150°C for 10 days under autogenous pressure. The crystalline product from the reaction is passed through a filter,
Washed, dried and calcined at 750°C for 6 hours.
The product, in its H + form, had the X-ray diffraction spectrum shown in Table 1 and an infrared absorption band at 917 cm -1 . Furthermore, the reaction product exhibited the following properties. Measured density (Helium method): 2.19 g/cm 3 Acidity (CsCl method): PH2.4 Molar ratio SiO 2 /B 2 O 3 : 12.3 Reference example Example 1 was placed in an electrically heated tubular reactor with an inner diameter of 8 mm.
Volarit A catalyst 3 with particle size 14 to 30 mesh (ASTM, US series) prepared according to
Filled with ml. Methyl tert-butyl ether, which had been preheated in a preheating tube, was introduced into the reactor by means of a metering pump. A pressure check valve set at 6 bar was installed downstream of the reactor. The check valve was equipped with a suitably heated sample collection device so that when the pressure was reduced, the reactor effluent was introduced into the gas chromatography. It was heated to the temperature shown in Table 2 and methyl tert-butyl ether was introduced at a flow rate of 6 cm 3 per hour (ie liquid hourly space velocity (LHSV)=2). The results obtained are also shown in Table 2.
Claims (1)
る置換元素としてホウ素を導入させてなる結晶性
変性シリカであつて、無水状態で、式(0−1)
R2O・(0−1)C2/oO・B2O3・(8−30)SiO2
(式中、Rはテトラメチルアンモニウムカチオン
であり、CはH+、NH4 +又は原子価nの金属の
如きカチオンである)に相当し、H+形の場合、
下記データに相当するX線回折スペクトルを有す
ることを特徴とする、結晶性変性シリカ。 【表】 【表】 【表】 2 結晶性シリカの結晶格子内に、ケイ素に代わ
る置換元素としてホウ素を導入させてなる結晶性
変性シリカであつて、無水状態で、式(0−1)
R2O・(0−1)C2/oO・B2O3・(8−30)SiO2
(式中、Rはテトラメチルアンモニウムカチオン
であり、CはH+、NH4 +又は原子価nの金属の
如きカチオンである)に相当し、H+形の場合、
下記データに相当するX線回折スペクトルを有す
る結晶性変性シリカの製法において、ケイ素誘導
体、ホウ素誘導体及びテトラメチルアンモニウム
化合物を、水熱条件下、PH9ないし14、温度110
ないし220℃で1ないし30日間反応させることを
特徴とする、結晶性変性シリカの製法。 【表】 3 特許請求の範囲第2項記載の製法において、
前記ケイ素誘導体がケイ素の有機誘導体である、
結晶性変性シリカの製法。 4 特許請求の範囲第3項記載の製法において、
前記ケイ素の有機誘導体がオルトケイ酸テトラア
ルキルエステルである、結晶性変性シリカの製
法。 5 特許請求の範囲第2項記載の製法において、
前記ホウ素誘導体がホウ酸である、結晶性変性シ
リカの製法。[Scope of Claims] 1 Crystalline modified silica in which boron is introduced as a substitutional element in place of silicon into the crystal lattice of crystalline silica, which in an anhydrous state has the formula (0-1)
R 2 O・(0-1)C 2/o O・B 2 O 3・(8-30)SiO 2
(wherein R is a tetramethylammonium cation and C is a cation such as H + , NH 4 + or a metal of valence n), in the H + form,
A crystalline modified silica characterized by having an X-ray diffraction spectrum corresponding to the following data. [Table] [Table] [Table] 2 Crystalline modified silica in which boron is introduced as a substitutional element in place of silicon into the crystal lattice of crystalline silica, which has the formula (0-1) in an anhydrous state.
R 2 O・(0-1)C 2/o O・B 2 O 3・(8-30)SiO 2
(wherein R is a tetramethylammonium cation and C is a cation such as H + , NH 4 + or a metal of valence n), in the H + form,
In a method for producing crystalline modified silica having an X-ray diffraction spectrum corresponding to the data below, a silicon derivative, a boron derivative, and a tetramethylammonium compound are heated under hydrothermal conditions at a pH of 9 to 14 and a temperature of 110.
A method for producing crystalline modified silica, which is characterized by reacting at a temperature of 1 to 220°C for 1 to 30 days. [Table] 3 In the manufacturing method described in claim 2,
the silicon derivative is an organic derivative of silicon;
Method for producing crystalline modified silica. 4 In the manufacturing method described in claim 3,
A method for producing crystalline modified silica, wherein the organic derivative of silicon is an orthosilicate tetraalkyl ester. 5. In the manufacturing method described in claim 2,
A method for producing crystalline modified silica, wherein the boron derivative is boric acid.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT24844/78A IT1096596B (en) | 1978-06-22 | 1978-06-22 | SYNTHETIC SILICA-BASED MATERIAL |
| IT24844A/78 | 1978-06-22 | ||
| IT22638A/79 | 1979-05-14 |
Related Child Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1030078A Division JPH0230612A (en) | 1978-06-22 | 1989-02-10 | Crystalline modified silica and production thereof |
| JP1030077A Division JPH01275417A (en) | 1978-06-22 | 1989-02-10 | Modified crystalline silica and method for its manufacture |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63123805A JPS63123805A (en) | 1988-05-27 |
| JPH0142887B2 true JPH0142887B2 (en) | 1989-09-18 |
Family
ID=11214909
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7826679A Granted JPS557598A (en) | 1978-06-22 | 1979-06-22 | Silicon based synthetic substance and method |
| JP62256430A Granted JPS63123805A (en) | 1978-06-22 | 1987-10-13 | Crystalline modified silica and manufacture |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7826679A Granted JPS557598A (en) | 1978-06-22 | 1979-06-22 | Silicon based synthetic substance and method |
Country Status (8)
| Country | Link |
|---|---|
| JP (2) | JPS557598A (en) |
| BE (1) | BE877205A (en) |
| BR (1) | BR7903970A (en) |
| CS (1) | CS257252B2 (en) |
| IT (1) | IT1096596B (en) |
| MW (1) | MW1879A1 (en) |
| ZA (1) | ZA792881B (en) |
| ZM (1) | ZM5579A1 (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4329328A (en) * | 1979-10-19 | 1982-05-11 | National Research Development Corporation | Method of synthesizing zincosilicate or stannosilicate or titanosilicate material |
| JPS57175722A (en) * | 1981-04-23 | 1982-10-28 | Japan Synthetic Rubber Co Ltd | Crystalline silicate compound |
| JPH062572B2 (en) * | 1982-02-19 | 1994-01-12 | 出光興産株式会社 | Method for producing crystalline silicate |
| JPS59107921A (en) * | 1982-12-10 | 1984-06-22 | Idemitsu Kosan Co Ltd | Crystalline borosilicic acid, its manufacture and manufacture of p-xylene using it |
| JPS59213441A (en) * | 1983-05-17 | 1984-12-03 | Idemitsu Kosan Co Ltd | Conversion catalyst for organic compound, its preparation and process for preparing organic compound using said catalyst |
| JPS61501981A (en) * | 1984-04-26 | 1986-09-11 | ユニオン カ−バイド コ−ポレ−シヨン | Titanium-silicate composition |
| JPS615028A (en) * | 1984-06-19 | 1986-01-10 | Res Assoc Util Of Light Oil | Preparation of alkyl-substituted aromatic hydrocarbon |
| IT1237804B (en) * | 1989-12-21 | 1993-06-17 | Eniricerche Spa | PREPARATION OF POROUS CRYSTALLINE BOROSILICATES |
| IT1270230B (en) | 1994-06-16 | 1997-04-29 | Enichem Sintesi | CATALYTIC COMPOSITION AND PROCESS FOR ALKYLATION OF AROMATIC COMPOUNDS |
| ITMI20112411A1 (en) | 2011-12-28 | 2013-06-29 | Eni Spa | METHOD TO IDENTIFY CATALYSTS SUITABLE FOR IMPROVING QUALITIES AS HYDROCARBURIC MIXTURE FUEL AND UPGRADING PROCESS THAT USES THEM |
| JP6108460B2 (en) * | 2013-10-08 | 2017-04-05 | 国立研究開発法人国立環境研究所 | Mesoporous silica incorporating a large amount of transition metal and method for producing the same |
| US9865871B2 (en) * | 2014-12-26 | 2018-01-09 | Semiconductor Energy Laboratory Co., Ltd. | Silicon oxide and storage battery |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IN146957B (en) * | 1976-10-18 | 1979-10-20 | Standard Oil Co |
-
1978
- 1978-06-22 IT IT24844/78A patent/IT1096596B/en active
-
1979
- 1979-06-11 ZA ZA792881A patent/ZA792881B/en unknown
- 1979-06-14 ZM ZM55/79A patent/ZM5579A1/en unknown
- 1979-06-21 BR BR7903970A patent/BR7903970A/en unknown
- 1979-06-21 CS CS794285A patent/CS257252B2/en unknown
- 1979-06-22 JP JP7826679A patent/JPS557598A/en active Granted
- 1979-06-22 BE BE0/195914A patent/BE877205A/en not_active IP Right Cessation
- 1979-06-22 MW MW18/79A patent/MW1879A1/en unknown
-
1987
- 1987-10-13 JP JP62256430A patent/JPS63123805A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| IT1096596B (en) | 1985-08-26 |
| BE877205A (en) | 1979-12-24 |
| MW1879A1 (en) | 1980-11-12 |
| BR7903970A (en) | 1980-03-11 |
| IT7824844A0 (en) | 1978-06-22 |
| JPH0116767B2 (en) | 1989-03-27 |
| ZM5579A1 (en) | 1980-10-21 |
| ZA792881B (en) | 1980-10-29 |
| JPS63123805A (en) | 1988-05-27 |
| CS257252B2 (en) | 1988-04-15 |
| JPS557598A (en) | 1980-01-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0223481B2 (en) | ||
| US4254297A (en) | Process for the conversion of dimethyl ether | |
| MX2011003386A (en) | Uzm-35 aluminosilicate zeolite, method of preparation and processes using uzm-35. | |
| JPH04222634A (en) | Catalytic hydrogenation dealkylation method for alkyl aromatic compounds | |
| IE48184B1 (en) | Modified silica and germania and their use as catalysts | |
| NL8006076A (en) | SYNTHETIC CRYSTALLINE BOROSILICATE MIXTURES AND PREPARATION THEREOF. | |
| JPH0142887B2 (en) | ||
| WO2012003313A2 (en) | Uzm-45 aluminosilicate zeolite, method of preparation and processes using uzm-45 | |
| JPS62501275A (en) | Crystalline magnesia-silica catalyst and its production method | |
| JPS5914407B2 (en) | Zeolite ZSM-34 and conversion method using it | |
| JPH0788217B2 (en) | Synthetic zeolite material and method for producing the same | |
| EP0113473B1 (en) | Novel zeolite catalyst and process for preparing same | |
| JPH04504857A (en) | Isoparaffin-olefin alkylation process | |
| US4708857A (en) | Process for preparing a crystalline iron-borosilicate | |
| US5683673A (en) | Process for the manufacture of a zeolite | |
| NL192292C (en) | Process for preparing a porous synthetic crystalline material. | |
| US4584415A (en) | Formation of alkyl ethers from alcohols and alkenes using AMS-1B crystalline borosilicate | |
| NO161060B (en) | SUSTAINABLE SILICON Dioxide-Based SYNTHETIC MATERIAL WITH POROE'S ZEOLITE-LIKE STRUCTURE AND PROCEDURE FOR ITS MANUFACTURING. | |
| EP0739308B1 (en) | Process for the manufacture of a zeolite | |
| NO161061B (en) | SUSTAINABLE SILICON Dioxide SOUTH-BASED SYNTHETIC MATERIAL WITH POROE'S ZEOLETIC SIMILAR STRUCTURE AND PROCEDURE FOR ITS MANUFACTURING. | |
| KR820001443B1 (en) | Process for preparation of sillica cased synthetic materials | |
| CS262430B2 (en) | Method of alkylating aromatic hydrocarbons or four-carbon-atoms hydrocarbons,olefins and/or saturated hydrocarbons |