JPH03164412A - Crystalline aluminophosphate and its production - Google Patents

Crystalline aluminophosphate and its production

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Publication number
JPH03164412A
JPH03164412A JP30339789A JP30339789A JPH03164412A JP H03164412 A JPH03164412 A JP H03164412A JP 30339789 A JP30339789 A JP 30339789A JP 30339789 A JP30339789 A JP 30339789A JP H03164412 A JPH03164412 A JP H03164412A
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JP
Japan
Prior art keywords
reaction mixture
ray diffraction
diffraction pattern
powder
al2o3
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
JP30339789A
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Japanese (ja)
Other versions
JP2890551B2 (en
Inventor
Hiroshi Okaniwa
宏 岡庭
Wataru Inaoka
稲岡 亘
Toru Nishimura
透 西村
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Tosoh Corp
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Tosoh Corp
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Priority to JP30339789A priority Critical patent/JP2890551B2/en
Publication of JPH03164412A publication Critical patent/JPH03164412A/en
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Publication of JP2890551B2 publication Critical patent/JP2890551B2/en
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Expired - Fee Related legal-status Critical Current

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  • Silicates, Zeolites, And Molecular Sieves (AREA)
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Abstract

PURPOSE:To easily produce a crystalline aluminophosphate having specified composition and X-ray diffraction pattern by mixing a phosphate source, an alumina source, water, ethylene glycol and dipropylamine in a specified ratio and holding the mixture at a specified temp. CONSTITUTION:A phosphate source, an alumina source, water, ethylene glycol and dipropylamine are mixed to obtain a reaction mixture. The molar ratios of the constituents of the reaction mixture are P2O5/Al2O3;=0.8 to 1.5, H2O/Al2 O3>=0, EG/Al2O3>=20, (EG+H2O)/Al2O3; 2.0 to 100 and DPA/Al2O3; 0.5 to 20 (EG is HOC2H4OH and DPA is (C3H7)2NH). The reaction mixture is held at 140-200 deg.C for 24-240hr under the autogenous pressure and crystallized. Consequently, a crystalline aluminophosphate having a skeletal structure shown by the chemical formula Al2O3.1.0+ or -0.2P2O5 in the molar ratio of the oxides on a dry basis and having a powder X-ray diffraction pattern shown in the table in the uncalcined state is obtained. The product is useful as the molecular sieve, catalyst, catalyst carrier, separating adsorbent, etc.

Description

【発明の詳細な説明】 く産業上の利用分野〉 本発明は、新規な結晶性アルミノ燐酸塩およびその製造
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Industrial Application Field The present invention relates to a novel crystalline aluminophosphate and a method for producing the same.

この新規な結晶性アルミノ燐酸塩は、燐およびアルミニ
ウムの酸素四面体を骨格構造の形成111位とするモレ
キュラーシーブであり、触媒,触媒担体,吸着分離剤等
として有用である。
This novel crystalline aluminophosphate is a molecular sieve with phosphorus and aluminum oxygen tetrahedrons forming the 111-position of the skeleton structure, and is useful as a catalyst, catalyst carrier, adsorption/separation agent, etc.

く従来の技術〉 以下に説明するとおり、本発明の結晶性アルミノ燐酸塩
は、無水基準で酸化物のモル比で式Al20i   1
.0±0.21’205で表される化学組成の骨格構造
を有し、6〜lOAの範囲内の大きさの細孔構造を有す
る。これに相当する結晶性アルミノ燐酸塩は、特開昭5
7−77015号公報および特開昭83−89412号
公報に、アルミノフォスフエートと称して開示されてい
る。
Prior Art> As explained below, the crystalline aluminophosphate of the present invention has the formula Al20i 1 in molar ratio of oxides on an anhydrous basis.
.. It has a skeletal structure with a chemical composition expressed as 0±0.21'205, and a pore structure with a size within the range of 6 to 1OA. The crystalline aluminophosphate corresponding to this is disclosed in Japanese Patent Application Laid-open No. 5
It is disclosed in Japanese Patent Application Laid-open No. 7-77015 and Japanese Patent Application Laid-Open No. 83-89412 under the name of aluminophosphate.

く発明が解決しようとする課題〉 本発明は、酸化物モル比および細孔径は従来知られてい
るものと同じであるが、結晶構造の新規な桔品性アルミ
ノ燐酸塩およびその製造方法を提供することを目的とす
る。
OBJECTS TO BE SOLVED BY THE INVENTION The present invention provides an aluminophosphate having a novel crystalline structure and a method for producing the same, although the oxide molar ratio and pore size are the same as those conventionally known. The purpose is to

く課題を解決するための手段および作用〉本発明の結晶
性アルミノ燐酸塩は、無水基準で酸化物のモル比で式 AI203   1.0±0.2P205で表される化
学組成の骨格構造を有し、かつ未焼成状態で実質上、表
1に示す粉末X線回折パターンを有することを特徴とす
るものである。
Means and Effects for Solving the Problems The crystalline aluminophosphate of the present invention has a skeletal structure with a chemical composition represented by the formula AI203 1.0±0.2P205 in molar ratio of oxide on an anhydrous basis. Moreover, it is characterized in that it substantially has a powder X-ray diffraction pattern shown in Table 1 in an unfired state.

本発明の結晶性アルミノ燐酸塩は、以降“TAP−l6
゜と称することもある。
The crystalline aluminophosphate of the present invention is hereinafter referred to as “TAP-16
It is sometimes called ゜.

表1 粉末X線回折パターン 面間隔 d (A)    ピーク強度10.37±0
.50       M〜S5.21±0.12   
     W4.40±0.09        M4
.05±0.07        M3.93±0.0
7       V S3.20±0.05     
   W3、00±0.04        W2.8
2±0.04       W〜M2,55±0.03
        W(表中、W,M,S,VSはそれぞ
れ、弱い,中位.強い,非常に強いを表す) この結晶性アルミノ燐酸塩は、燐およびアルミニウムの
酸素四面体を骨格構造の形成単位とし、ベンゼンを吸着
することおよび上記の粉末X線回折パターンから直径6
〜IOAの範囲内の大きさの細孔構造を有すると認めら
れるものである。
Table 1 Powder X-ray diffraction pattern spacing d (A) Peak intensity 10.37±0
.. 50M~S5.21±0.12
W4.40±0.09 M4
.. 05±0.07 M3.93±0.0
7V S3.20±0.05
W3, 00±0.04 W2.8
2±0.04 W~M2,55±0.03
W (In the table, W, M, S, and VS represent weak, medium, strong, and very strong, respectively.) This crystalline aluminophosphate has phosphorus and aluminum oxygen tetrahedrons as forming units of the skeletal structure. , diameter 6 from the adsorption of benzene and the above powder X-ray diffraction pattern.
It is recognized that the pore structure has a size within the range of ~IOA.

また、本発明のTAP−16の製造方法は、燐酸源,ア
ルミナ源,水,エチレングリコールおよびジプロピルア
ミンを混合して、酸化物のモル比で示して次の組或、 P2 0S /A 12 0s      0.8〜1
.5H20/Al20s       ミOEG/Al
20)        よ20(EG+H20)/A 
12 0x  20〜l00DPA/A lz Oi 
       O.5〜2.0(EGはHOC2 Hs
 OHを、DPAは(Ci Hy )2 NHを表す。
In addition, the method for producing TAP-16 of the present invention involves mixing a phosphoric acid source, an alumina source, water, ethylene glycol, and dipropylamine to form the following composition in terms of the molar ratio of oxides: P20S/A12 0s 0.8~1
.. 5H20/Al20s Mi OEG/Al
20) Yo20(EG+H20)/A
12 0x 20~100DPA/Alz Oi
O. 5-2.0 (EG is HOC2 Hs
OH represents (Ci Hy ) 2 NH, and DPA represents (Ci Hy )2 NH.

以下、同じ)を有する反応混合物を調,製し、該反応混
合物を140℃ないし200℃の温度に保持して結晶化
させることからなる。
The method consists of preparing a reaction mixture having the same formula (hereinafter the same) and maintaining the reaction mixture at a temperature of 140°C to 200°C to crystallize it.

この燐酸源およびアルミナ源は、特に限定されず、それ
ぞれ種々の含燐化合物および種々のアルミニウム化合物
を使用することができる。
The phosphoric acid source and alumina source are not particularly limited, and various phosphorus-containing compounds and various aluminum compounds can be used, respectively.

もっとも、燐酸源としてはオルト燐酸:アルミナ源とし
てはアルミニウムイソプロボキシドまたはブソイドベー
マイト永和酸化アルミニウムを使用するのが好ましい。
However, it is preferable to use orthophosphoric acid as the phosphoric acid source and aluminum isoproboxide or pseudoboehmite Eiwa aluminum oxide as the alumina source.

これらの原料は、反応混合物調製時に反応性の良いアル
ミノ燐酸ゲルを形成し、より短時間で結晶化させること
ができる。
These raw materials form an aluminophosphoric acid gel with good reactivity during the preparation of the reaction mixture, and can be crystallized in a shorter time.

そして、反応混合物の組成は、酸化物モル比で次の範囲
でなければならない。
The composition of the reaction mixture must be in the following range in terms of oxide molar ratio.

P20S /A I 2 o,      0.8 〜
1.5H 2 0 / A 1 2 0 3     
  ミOE G / A 1 2 0 s      
  よ20(EC+H2 0) /A l 2 0s 
 20〜100DPA/A I2 o,       
 o.s〜2.0なぜなら、P 2 0 s / A 
I 2 0 3 モル比が、0.8より小さいと、TA
P−18は得られるが、結晶性アルミナが不純物として
副生し;l,5より大きいと、ジブロビルアミンの燐酸
塩が副生する。
P20S/AI2o, 0.8~
1.5H20/A1203
MiOE G/A 120s
Yo20(EC+H20) /A l20s
20~100DPA/A I2o,
o. s ~ 2.0 because P 2 0 s / A
When the I 2 O 3 molar ratio is less than 0.8, TA
Although P-18 is obtained, crystalline alumina is produced as a by-product as an impurity; if it is larger than 1, 5, dibrobylamine phosphate is produced as a by-product.

(EG+H,O)/A l 2 0,%ル比が20より
小さいと、好適な粘度の反応混合物が得られないため撹
拌が困難となり、均一な反応混合物が得られず、不純物
の生成を招くことがあり;100より大きいとTAP−
18は得られるが、反応槽あたりの収量が小さく効率的
でない。DPA/At20,モル比が0.5より小さい
とTAP−16とは叉なった構造のアルミノ燐酸塩が副
生し;2.0より大きいとTAP−16は得られるが、
結晶化に著しく長時間を要する。
If the (EG+H,O)/A l 2 0,% ratio is less than 20, it will not be possible to obtain a reaction mixture with a suitable viscosity, making stirring difficult, making it impossible to obtain a homogeneous reaction mixture, and resulting in the formation of impurities. May be greater than 100
18 can be obtained, but the yield per reaction tank is small and not efficient. When the DPA/At20 molar ratio is smaller than 0.5, aluminophosphate with a structure different from that of TAP-16 is produced as a by-product; when it is larger than 2.0, TAP-16 is obtained, but
Crystallization takes an extremely long time.

反応混合物が不均一であると、不純物が副生ずることも
あるので、これらの原料は撹拌下に添加し、最終反応混
合物は実質上均質となるまで撹拌することが望ましい。
If the reaction mixture is heterogeneous, impurities may be produced as by-products, so it is desirable to add these raw materials with stirring and to stir the final reaction mixture until it is substantially homogeneous.

こうして得た最終反応混合物は、不純物の混入を防ぐた
め、例えばポリテトラフルオルエチレンの様な不活性プ
ラスチック材料でライニングしたステンレス製の密閉耐
圧容器を用いて結晶化するのがよい。
The final reaction mixture thus obtained is preferably crystallized in a closed pressure vessel made of stainless steel lined with an inert plastic material such as polytetrafluoroethylene to prevent contamination with impurities.

結晶化は、自生圧下、TAP−18の結晶が生成するま
で、140℃ないし200℃、好ましくは、160℃な
いし180℃の温度に保持することにより行われる。結
晶化の温度が140’Cより低いと結晶化に著しく長時
間を要し.  200”Cより高いと、TAP−16と
は構造の異なるアルミノ燐酸塩が生成してくる。通常、
上記の温度に約24時間ないし約240時間置くことに
よりTAP−16を得ることができる。
Crystallization is carried out under autogenous pressure by maintaining the temperature at 140°C to 200°C, preferably 160°C to 180°C, until crystals of TAP-18 are formed. If the crystallization temperature is lower than 140'C, crystallization takes a significantly long time. When the temperature is higher than 200"C, aluminophosphate with a different structure from TAP-16 is generated. Usually,
TAP-16 can be obtained by leaving it at the above temperature for about 24 hours to about 240 hours.

桔晶化後、生或物は濾過あるいは遠心分離のような通常
の分離方法により回収し、洗浄後、乾燥して細孔内にジ
プロピルアミンを一部含んだTAP−1(iが得られる
。このジプロピルアミンが/7 r[Lていても、粉末
X線回折パターンには影響しないので、そのままその測
定に供することができる。
After crystallization, the raw material is recovered by conventional separation methods such as filtration or centrifugation, washed, and dried to obtain TAP-1 (i) containing some dipropylamine in its pores. Even if this dipropylamine is /7 r[L, it does not affect the powder X-ray diffraction pattern, so it can be used as is for measurement.

本明細書における生成物の粉末X線回折は、フィリップ
ス(PIIILIPS )社製粉末X線回折装置PV1
70Gによる。また、線源にはCuK−α線を使用し、
可変式ダイバージェンススリットを用いて、測定サンプ
ル上のX線照射面積を一定にしてJ?j定する。
Powder X-ray diffraction of the product in this specification is performed using a powder X-ray diffractometer PV1 manufactured by PIIILIPS.
By 70G. In addition, CuK-α radiation is used as a radiation source,
Using a variable divergence slit, the X-ray irradiation area on the measurement sample is kept constant and J? i decide.

このジプロピルアミンを含んだTAP−16は、必要に
応じて、350℃ないし700 ”Cの焼成により容易
に分解除去することができる。この焼威によってTAP
−16の粉末X線回折パターンは実質的に変化せず、T
AP−18は高い耐熱性を有しているということができ
る。
This dipropylamine-containing TAP-16 can be easily decomposed and removed by firing at 350°C to 700''C, if necessary.
The powder X-ray diffraction pattern of -16 was virtually unchanged and T
It can be said that AP-18 has high heat resistance.

く発明の効果〉 以上説明したとおり、本発明の結晶性アルミノ燐酸塩は
、新規な結晶構造を有し、無水基準で酸化物のモル比で
式 Al20i   1.0±0.2PzOsで表される化
学組成の骨格構造および8−1OAの範囲内の大きさの
細孔構造を有するものであり、本発明の製造方法によれ
ば、この結晶性アルミノ燐酸塩を容易に製造することが
できる。
Effects of the Invention> As explained above, the crystalline aluminophosphate of the present invention has a novel crystal structure, and is expressed by the formula Al20i 1.0±0.2PzOs in molar ratio of oxides on an anhydrous basis. It has a skeletal structure of chemical composition and a pore structure of a size within the range of 8-1 OA, and according to the production method of the present invention, this crystalline aluminophosphate can be easily produced.

そして、この結晶性アルミノ燐酸塩は、耐熱性が高く、
必要に応じて触媒活性のある所望の金属を含浸などによ
り担持して、炭化水素転化あるいは酸化燃焼反応の触媒
として有用に使用できる。さらに細孔の大きさによる吸
着特性を利用して、その吸着剤、分子ふるいなどとして
有用に使用することができる。
This crystalline aluminophosphate has high heat resistance,
If necessary, a desired catalytically active metal can be supported by impregnation or the like, and it can be usefully used as a catalyst for hydrocarbon conversion or oxidative combustion reactions. Furthermore, by taking advantage of the adsorption characteristics due to the size of the pores, it can be usefully used as an adsorbent, a molecular sieve, and the like.

く実施例〉 本発明をさらに具体的に説明するために、以下に実施例
を示すが、本発明は以下の実施例によって限定されるも
のではない。
Examples> In order to explain the present invention more specifically, Examples are shown below, but the present invention is not limited to the following Examples.

実施例1 アルミニウムイソプロボキシド,オルトリン酸(85%
),ジーn−プロビルアミンおよびエチレングリコール
を混合して、次のモル組成の反応混合物を調製した。
Example 1 Aluminum isoproboxide, orthophosphoric acid (85%
), di-n-probylamine, and ethylene glycol to prepare a reaction mixture with the following molar composition.

P2 0s /A l 2 0*   1.0H2 0
/ A 1 2 0s    4.9EG/A1203
     30 n−D P A / A 1 2 0 3   1.0
(n−DPAは(n−C* }f,)2 NHを表す。
P2 0s /A l 2 0* 1.0H2 0
/ A120s 4.9EG/A1203
30 n-D P A / A 1 2 0 3 1.0
(n-DPA represents (n-C* }f,)2NH.

以下1.=jJじ) この反応混合物を、オートクレープに密閉し、定常撹袢
しつつ自生圧下180℃に加熱し、72時間この温度を
保持し、結晶性生成物を得た。これを濾過,水洗の後、
110℃で乾燥した。
Below 1. =jJji) This reaction mixture was sealed in an autoclave, heated to 180° C. under autogenous pressure with constant stirring, and maintained at this temperature for 72 hours to obtain a crystalline product. After filtering and washing with water,
It was dried at 110°C.

この生戊物は、表2および図1に示す粉末X線回折パタ
ーンを有するTAP−16であった。
This raw material was TAP-16 having a powder X-ray diffraction pattern shown in Table 2 and FIG.

この生或物の一部を600’Cで4時間焼成し、化学分
析をしたところ、次の組成を有していた。
A part of this raw material was fired at 600'C for 4 hours and chemically analyzed, and found to have the following composition.

Al20, ・0.99P 2 0 s表2 10.37 6,00 5.21 4.84 4.40 4.05 3,94 3.55 3,47 3.20 2.99 2.82 2.55 2,49 2.42 2.38 2,36 2.30 上記の生或物の一部を、600℃で4時間焼成した。こ
の焼或物の粉末X線回折パターンは、表3のとおりであ
り、実質的に未焼成のそれと同一であった。
Al20, ・0.99P 2 0 sTable 2 10.37 6,00 5.21 4.84 4.40 4.05 3,94 3.55 3,47 3.20 2.99 2.82 2.55 2,49 2.42 2.38 2,36 2.30 A part of the above raw material was baked at 600° C. for 4 hours. The powder X-ray diffraction pattern of this fired product is shown in Table 3, and was substantially the same as that of the unfired product.

表3 10.38 6,OI 5,l9 4.82 4.37 4803 3.93 3.54 3.47 3.l9 3.00 2.89 2,82 表3(つづき) d (A)    相対強度 2.72        1 2.80        1 2.56        14 2.411        5 2.41        3 2.39        3 2.35        4 2.29        6 2.27        2 (%) 標準マクベインーベーカー吸e量測定装置を111いて
、この焼或したTAP−18の吸着温度25℃における
1時間後の、n−ヘキサンおよびベンゼンの吸着容量を
測定し、表4に示した値を得た。
Table 3 10.38 6, OI 5, l9 4.82 4.37 4803 3.93 3.54 3.47 3. l9 3.00 2.89 2,82 Table 3 (continued) d (A) Relative intensity 2.72 1 2.80 1 2.56 14 2.411 5 2.41 3 2.39 3 2.35 4 2 .29 6 2.27 2 (%) Using a standard McBain-Baker adsorption measuring device, the adsorption capacity of n-hexane and benzene was determined after 1 hour at an adsorption temperature of 25°C for this calcined TAP-18. The values shown in Table 4 were obtained.

焼成したTAP−16は、分子直径が約6Aのベンゼン
を吸着することから、8Aより大きな細孔径を有してい
ることとなる。
Since the fired TAP-16 adsorbs benzene with a molecular diameter of about 6A, it has a pore diameter larger than 8A.

表4 分子直径 圧力  吸着量 A   Torr    wt% nヘキサン 4.3   22     6.851 
    8.9 ベンゼン   5.9    20     8.84
0    L0.9 尖施例2 アルミニウムイソブロポキシド,オルトリン酸(85%
).ジーn−プロビルアミン.およびエチレングリコー
ルを混合して、次のモル組或の反応混合物を調製した。
Table 4 Molecular diameter Pressure Adsorption amount A Torr wt% nHexane 4.3 22 6.851
8.9 Benzene 5.9 20 8.84
0 L0.9 Tip Example 2 Aluminum isopropoxide, orthophosphoric acid (85%
). G-n-probylamine. and ethylene glycol were mixed to prepare a reaction mixture with the following molar set:

P2 0s /A 12 03   1.0H20/A
 1 2 03    4.9EG/A 12 01 
    30 n−D P A / A I 20 3   1.5こ
の反応混合物を、オートクレープに密閉し、定常撹拌し
つつ自生圧下l80℃に加熱し、72時間この温度を保
持し、結晶性生戒物を得た。これを濾過,水洗の後、1
10℃で乾燥した。
P2 0s /A 12 03 1.0H20/A
1 2 03 4.9EG/A 12 01
30 n-D P A / A I 20 3 1.5 The reaction mixture was sealed in an autoclave and heated to 80° C. under autogenous pressure with constant stirring, and maintained at this temperature for 72 hours to form a crystalline raw material. I got it. After filtering and washing with water, 1
It was dried at 10°C.

この生或物は、表5に示す粉末XvA回折パターンを有
するTAP−18であった。
This raw material was TAP-18 having the powder XvA diffraction pattern shown in Table 5.

この生成物の一部を600℃で4時間焼成し、化学分析
をしたところ、次の組成を有していた。
A part of this product was calcined at 600° C. for 4 hours and chemically analyzed, and found to have the following composition.

A I 2 0 ] ・0。98P,05d  (A) 10.38 5.99 5.21 4,86 4,40 4.0B 3,93 3,55 3,47 3,20 3.00 2、82 2,56 2,50 2,43 2.36 2.30 表5 (%) 上記の生成物を実施例1と同一の条件で焼威し、その焼
或物の粉末X線回折および吸着の測定を行なった。粉末
X線回折パターンは、実質上上記の未焼成のもののそれ
と同じであり、吸着容量は表6のとおりであった。
A I 2 0] ・0.98P,05d (A) 10.38 5.99 5.21 4,86 4,40 4.0B 3,93 3,55 3,47 3,20 3.00 2,82 2,56 2,50 2,43 2.36 2.30 Table 5 (%) The above product was burned under the same conditions as in Example 1, and powder X-ray diffraction and adsorption measurements of the burnt product I did this. The powder X-ray diffraction pattern was substantially the same as that of the unfired product described above, and the adsorption capacity was as shown in Table 6.

表6 分子直径 圧力  吸着量 A   Torr    wt% nヘキサン 4.3   22     6.351 
    8.6 ベンゼン   5.9   20     8.640
    1(1.7 ?施例3 アルミニウムイソブロポキシド,オルトリン酸(85%
).ジーn−プロビルアミン,水,およびエチレングリ
コールを混合して、次のモル組成の反応混合物を調製し
た。
Table 6 Molecular diameter Pressure Adsorption amount A Torr wt% nHexane 4.3 22 6.351
8.6 Benzene 5.9 20 8.640
1 (1.7? Example 3 Aluminum isopropoxide, orthophosphoric acid (85%
). A reaction mixture with the following molar composition was prepared by mixing di-n-probylamine, water, and ethylene glycol.

P205/Al■Oi   1.0 ?2  0/ A  1  2  03     10
.0EC/Al  ■ 0,       30n−D
PA/A  12  03     1.0この反応混
合物を、オートクレープに密閉し、定常撹拌しつつ自生
圧下180℃に加熱し、48時lHfこの温度を保持し
、結晶性生成物を得た。これを濾過.水洗の後、110
℃で乾燥した。
P205/Al■Oi 1.0? 2 0/ A 1 2 03 10
.. 0EC/Al ■ 0, 30n-D
PA/A 12 03 1.0 The reaction mixture was sealed in an autoclave and heated to 180° C. under autogenous pressure with constant stirring and maintained at this temperature for 48 hours lHf to obtain a crystalline product. Filter this. After washing with water, 110
Dry at °C.

この生成物は、表4に示す粉末X線回折パターンを有す
るTAP−18であった。
The product was TAP-18 with the powder X-ray diffraction pattern shown in Table 4.

この生或物の一部を600℃で4時間焼成し、化学分析
をしたところ、次の組或を有していた。
A part of this raw product was baked at 600°C for 4 hours and chemically analyzed, and it was found to have the following composition.

A l 2 0 3  ・0.99P205表7 10.40 G.01 5,21 4,8B 4,40 4,05 3.94 3。55 3.47 3.20 3,00 2,83 2.55 2.50 2.43 2.39 2.37 2.29 4 図の簡単な説明 図1は、 実施例1で得られた未焼成のTAP−18の粉末X線回
折パターンを示す図である。
A l 2 0 3 ・0.99P205Table 7 10.40G. 01 5,21 4,8B 4,40 4,05 3.94 3.55 3.47 3.20 3,00 2,83 2.55 2.50 2.43 2.39 2.37 2.29 4 BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a diagram showing the powder X-ray diffraction pattern of unfired TAP-18 obtained in Example 1.

Claims (1)

【特許請求の範囲】 (1)無水基準で酸化物のモル比で式 Al_2O_3・1.0±0.2P_2O_5で表され
る化学組成の骨格構造を有し、かつ未焼成状態で実質上
表1に示す粉末X線回折パターンを有することを特徴と
する、結晶性アルミノ燐酸塩。 表1 粉末X線回折パターン ¥面間隔 d(A)¥ ¥ピーク強度¥ 10.37±0.50 M〜S 5.21±0.12  W 4.40±0.09  M 4.05±0.07  M 3.93±0.07  VS 3.20±0.05  W 3.00±0.04  W 2.82±0.04  W〜M 2.55±0.03  W (表中、W、M、S、VSはそれぞれ、弱い、中位、強
い、非常に強いを表す) (2)燐酸源、アルミナ源、水、エチレングリコールお
よびジプロピルアミンを混合して、酸化物のモル比で示
して次の組成、 P_2O_5/A1_2O_30.8〜1.5H_2O
/A1_2O_3≧0 EG/A1_2O_3≧20 (EG+ H_2O)/Al_2O_320〜100D
PA/Al_2O_30.5〜2.0で (EGはHOC_2H_5OHを、DPAはA(C_3
H_7)_2NHを表す) を有する反応混合物を調製し、該反応混合物を140℃
ないし200℃の温度に保持することを特徴とする、請
求項(1)記載の結晶性アルミノ燐酸塩を製造する方法
[Scope of Claims] (1) It has a skeletal structure with a chemical composition represented by the formula Al_2O_3・1.0±0.2P_2O_5 in molar ratio of oxides on an anhydrous basis, and in an unfired state substantially has a structure shown in Table 1 below. A crystalline aluminophosphate having a powder X-ray diffraction pattern shown in FIG. Table 1 Powder X-ray diffraction pattern\Plane spacing d(A)\Peak intensity\10.37±0.50 M~S 5.21±0.12 W 4.40±0.09 M 4.05±0 .07 M 3.93±0.07 VS 3.20±0.05 W 3.00±0.04 W 2.82±0.04 W~M 2.55±0.03 W (In the table, W , M, S, and VS represent weak, medium, strong, and very strong, respectively) (2) Mix a phosphoric acid source, an alumina source, water, ethylene glycol, and dipropylamine, and then Show the following composition, P_2O_5/A1_2O_30.8~1.5H_2O
/A1_2O_3≧0 EG/A1_2O_3≧20 (EG+H_2O)/Al_2O_320~100D
PA/Al_2O_30.5~2.0 (EG is HOC_2H_5OH, DPA is A(C_3
H_7)_2NH) was prepared, and the reaction mixture was heated at 140°C.
The method for producing crystalline aluminophosphate according to claim 1, characterized in that the temperature is maintained at a temperature of from 200°C to 200°C.
JP30339789A 1989-11-24 1989-11-24 Crystalline aluminophosphate and method for producing the same Expired - Fee Related JP2890551B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0768111A1 (en) * 1995-10-16 1997-04-16 Corning Incorporated Method of modifying a hydrocarbon adsorber and its use
KR970073723A (en) * 1996-05-17 1997-12-10 성기웅 Crystalline aluminophosphate molecular sieve composition having a novel structure and a process for producing the same
US6001320A (en) * 1995-10-12 1999-12-14 Corning Incorporated Method of adsorbing hydrocarbons
US6004896A (en) * 1996-09-30 1999-12-21 Corning Incorporated Hydrocarbon adsorbers, method of making and use therefor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6001320A (en) * 1995-10-12 1999-12-14 Corning Incorporated Method of adsorbing hydrocarbons
EP0768111A1 (en) * 1995-10-16 1997-04-16 Corning Incorporated Method of modifying a hydrocarbon adsorber and its use
KR970073723A (en) * 1996-05-17 1997-12-10 성기웅 Crystalline aluminophosphate molecular sieve composition having a novel structure and a process for producing the same
US6004896A (en) * 1996-09-30 1999-12-21 Corning Incorporated Hydrocarbon adsorbers, method of making and use therefor

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