JPH02157119A - Production of binderless zeolite molded product - Google Patents
Production of binderless zeolite molded productInfo
- Publication number
- JPH02157119A JPH02157119A JP31012588A JP31012588A JPH02157119A JP H02157119 A JPH02157119 A JP H02157119A JP 31012588 A JP31012588 A JP 31012588A JP 31012588 A JP31012588 A JP 31012588A JP H02157119 A JPH02157119 A JP H02157119A
- Authority
- JP
- Japan
- Prior art keywords
- clay
- zeolite
- type
- molded product
- kaolin
- 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
Links
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 68
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 68
- 239000010457 zeolite Substances 0.000 title claims abstract description 68
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 87
- 239000004927 clay Substances 0.000 claims abstract description 47
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000005995 Aluminium silicate Substances 0.000 claims abstract description 20
- 235000012211 aluminium silicate Nutrition 0.000 claims abstract description 20
- 239000000843 powder Substances 0.000 claims abstract description 14
- 238000001125 extrusion Methods 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 abstract description 17
- 238000000034 method Methods 0.000 abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 238000001179 sorption measurement Methods 0.000 abstract description 6
- 239000008188 pellet Substances 0.000 abstract description 4
- 238000001354 calcination Methods 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 2
- 238000010304 firing Methods 0.000 description 11
- 239000000243 solution Substances 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 6
- 238000002425 crystallisation Methods 0.000 description 5
- 230000008025 crystallization Effects 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical group [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 3
- 229910001424 calcium ion Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 239000012736 aqueous medium Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 235000012438 extruded product Nutrition 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052665 sodalite Inorganic materials 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- QMGYPNKICQJHLN-UHFFFAOYSA-M Carboxymethylcellulose cellulose carboxymethyl ether Chemical compound [Na+].CC([O-])=O.OCC(O)C(O)C(O)C(O)C=O QMGYPNKICQJHLN-UHFFFAOYSA-M 0.000 description 1
- 241000219112 Cucumis Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
- C01B33/28—Base exchange silicates, e.g. zeolites
- C01B33/2807—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures
- C01B33/2815—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures of type A (UNION CARBIDE trade name; corresponds to GRACE's types Z-12 or Z-12L)
- C01B33/283—Zeolitic silicoaluminates with a tridimensional crystalline structure possessing molecular sieve properties; Isomorphous compounds wherein a part of the aluminium ore of the silicon present may be replaced by other elements such as gallium, germanium, phosphorus; Preparation of zeolitic molecular sieves from molecular sieves of another type or from preformed reacting mixtures of type A (UNION CARBIDE trade name; corresponds to GRACE's types Z-12 or Z-12L) from a reaction mixture containing at least one aluminium silicate or aluminosilicate of a clay-type, e.g. kaolin or metakaolin or its exotherm modification or allophane
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Description
【発明の詳細な説明】
し産業上の利用分野]
本発明は、バインダレス4A型ゼオライト成型体の製造
方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a binderless 4A type zeolite molded body.
バインダレス4A型ゼオライト成型体は、吸j5、分離
及び精製用として有用な吸着剤である。また、カルシウ
ムイオン交換処理して5A型ゼオライトにすることによ
り、空気中の酸素、窒素の分離用吸着剤として優れた性
能を有するものとなる。The binderless 4A type zeolite molded body is a useful adsorbent for adsorption, separation and purification. Further, by performing calcium ion exchange treatment to form 5A type zeolite, it has excellent performance as an adsorbent for separating oxygen and nitrogen in the air.
[従来の技術]
バインダレスゼオライト成型体の製造には、種々の方法
か提案されている。[Prior Art] Various methods have been proposed for producing binderless zeolite molded bodies.
例えば、特開昭57−122932号公報には、合成ゼ
オライト
メタカオリン粘土
水酸化ナトリウム水溶液
の混合物を作り、該混合物を混練し、押出し成型して成
型体を形成し、該成型体をエージングした後、η1温下
て水酸化ナトリウム稀薄溶液で処理してゼオライト成型
体を結晶化させることからなる方法か開示されているが
、この方法では、成型の際メタカオリン即ちすでに焼結
されたカオリンを結合剤として使用することから、成型
体中の粘土を焼成させる工程かないこととなり、該成型
体は昇温下の水酸化ナトリウム水溶液中で劣化して、最
終的に焼成l占性化されてえられるバ・rシダレスゼオ
ライ1−成型体の機械的強度は低い値となる。For example, JP-A-57-122932 discloses that a mixture of synthetic zeolite metakaolin clay sodium hydroxide aqueous solution is prepared, the mixture is kneaded, extrusion molded to form a molded body, and the molded body is aged. , a method is disclosed which consists of crystallizing a zeolite molded body by treatment with a dilute sodium hydroxide solution at a temperature of Since the clay in the molded body is used as a clay material, there is no need for a step of firing the clay in the molded body, and the molded body deteriorates in an aqueous sodium hydroxide solution at an elevated temperature, and is finally fired to form a occupancy. - r Cedarless Zeolite 1 - The mechanical strength of the molded product is a low value.
更に、成型体中の粘土の量か40〜60重量%と多い為
、ゼオライト純分の高いバインダレスゼオライト成型体
を得ることは困難である。Furthermore, since the amount of clay in the molded body is as high as 40 to 60% by weight, it is difficult to obtain a binderless zeolite molded body with a high zeolite purity.
又、米国特許第311−9659号明細書には、反応性
に富むカオリン粘土を水酸化ナトリウムと反応させて予
め成型された本体を形成させ、更に水酸化ナトリウムと
反応さぜることからなるバインダレスゼオライトの製造
法が開示されている。U.S. Pat. No. 311-9659 discloses a binder made by reacting a highly reactive kaolin clay with sodium hydroxide to form a pre-shaped body, which is further reacted with sodium hydroxide. A method for producing less zeolite is disclosed.
更に、粘土に対して少量の成型したゼオライトを加える
ことから成る方法か例示されている。しかし、この方法
によれば、温浸工程および結晶化工程にかなりの時間を
必要とするばかりではなく、押出し物を更に水酸化ナト
リウム水溶液で処理する前に水分含有量を約30重皿%
以下になるようこ乾燥する必要がある。又、加えるゼオ
ライトに対して粘土の瓜か多い為、ゼオライト純分の+
4’4iいバインダレスゼオライト成型体を得ることか
困難である。Furthermore, a method is exemplified which consists of adding a small amount of shaped zeolite to the clay. However, this method not only requires a considerable amount of time for the digestion and crystallization steps, but also reduces the water content to about 30% before further treatment of the extrudates with aqueous sodium hydroxide solution.
It is necessary to dry it as follows. In addition, since there is a large amount of clay compared to the zeolite added, the zeolite pure content is +
It is difficult to obtain a binderless zeolite molded body with a height of 4'4i.
更に、特公昭43−9658号公報には、カオリン粘土
と微細に分割されたナトリウム水溶液中h A 33〜
67%との混合物を作って第1および第2段階の長時間
に4つたるすり混ぜを行った後、成型し、600〜70
0 ’Cて焼成してカオリン粘土をメタカオリン粘土に
転化し、該成形体を昇温下でアルカリ金属を含む水性媒
質で処理することからなるバインダレスゼオライトの製
造方法か開示されている。Furthermore, in Japanese Patent Publication No. 43-9658, kaolin clay and finely divided sodium aqueous solution hA 33~
After making a mixture with 67% and mixing in four barrels for a long time in the first and second stages, it was molded and
A process for producing a binderless zeolite is disclosed, which comprises converting kaolin clay into metakaolin clay by firing at 0'C and treating the compact with an aqueous medium containing an alkali metal at elevated temperature.
しかし、この方法によれば、成形体混合物中にカオリン
粘土をゼオライトに転化させる為のアルカリ源が含まれ
ておらず、次の水性媒質で処理する工程での反応速度か
遅い。この為、エーシングおよび結晶化に長時間を要す
る。又、カオリン粘土の量が比較的多くゼオライト純分
の高いバインダレスゼオライト成形体を?1することか
困難である。However, according to this method, the molded body mixture does not contain an alkali source for converting kaolin clay into zeolite, and the reaction rate in the next step of treating with an aqueous medium is slow. For this reason, ace and crystallization require a long time. Or a binderless zeolite molded body with a relatively large amount of kaolin clay and high zeolite purity? 1 is difficult to do.
[発明か解決しようとする課題]
従来の方法でつくったバインダレスゼオライトは、粘土
として反応性に富む焼成したものを用いており、その結
果、得られる成型体の機械的強度は低い値であった。又
、その製造工程もかなり後着1であり、焼成粘土を用い
ている為に押出し成型性かあまり良くないなどの欠点か
あった。[Problem to be solved by the invention] Binderless zeolite produced by conventional methods uses fired clay that is highly reactive, and as a result, the mechanical strength of the resulting molded product is low. Ta. In addition, the manufacturing process was quite advanced, and since fired clay was used, there were drawbacks such as poor extrusion moldability.
更に、反応性に富まない生の粘土を用いた場合において
も、その製造工程がかなり複雑であり、ゼオライト純分
の高い成形体を?11ることか困難であった。Furthermore, even when raw clay with low reactivity is used, the manufacturing process is quite complicated, making it difficult to produce molded bodies with high zeolite purity. 11 things were difficult.
本発明の1]的は、従来の方法より高い4A型ゼオライ
ト純分を含有し、すなわち不活性結合剤含有量の小さい
、優れた機械的強度及び高い吸着容量を有するバインダ
レス4A型ゼオライト成型体を製造する方法を提(」(
することにある。1] The object of the present invention is a binderless 4A zeolite molded product that contains a higher 4A zeolite purity than conventional methods, that is, has a small inert binder content, excellent mechanical strength, and high adsorption capacity. We present a method for manufacturing (''(
It's about doing.
[課題を解決するための手段および作用]高いゼオライ
ト純分を含有し、優れた機械的強度を]11つ成型体を
作る因子として、粘土の種類、ゼオライトと粘土と水酸
化ナトリウムの混合1.q合、焼成条件等が考えられる
。[Means and effects for solving the problem] Contains high zeolite purity and has excellent mechanical strength] 11 Factors for making a molded body include the type of clay, the mixture of zeolite, clay, and sodium hydroxide.1. Possible factors include q-coupling, firing conditions, etc.
本発明者はこれらの因子について鋭念検討を行った結果
、従来よりも比較的簡単な工程および操作によって、性
能の向上した成型体をうろことかできる方法を見出した
。As a result of careful study of these factors, the present inventors have discovered a method of producing a molded body with improved performance through relatively simpler steps and operations than in the past.
本発明の要旨は、合成4A型ゼオライト粉末、該合成4
A型ゼオライト粉末との合計に対して20〜30重瓜%
のカオリン型粘土および該カオリン型粘土を4A型ゼオ
ライトに転化させるための化学量論量の25%以下の水
酸化ナトリウムからなる混合物を、押5JIL成型し、
えられた成型体を焼成した後、濃度1.6〜3.0 m
ol/βの水酸化ナトリウム水溶液中で粘土を4A型ゼ
オライトに転化させることからなる、バインダレス4A
型ゼオライト成型体の製造方法に有り、以下、その詳細
について説明する。The gist of the present invention is a synthetic 4A type zeolite powder, the synthetic 4A type zeolite powder,
20-30% of melon based on the total amount with A-type zeolite powder
A mixture consisting of kaolin-type clay and sodium hydroxide in an amount of 25% or less of the stoichiometric amount for converting the kaolin-type clay into 4A-type zeolite is pressed and molded to 5JIL,
After firing the obtained molded body, the density is 1.6 to 3.0 m.
Binderless 4A, consisting of converting clay to type 4A zeolite in ol/β aqueous sodium hydroxide solution.
There is a method for producing a molded zeolite body, and the details thereof will be explained below.
本発明で用いられるゼオライトは、公知の方法、即ちア
ルミン酸ナトリウム及び珪酸ナトリウムから合成的に製
造される4A型合成ゼオライトである。The zeolite used in the present invention is a type 4A synthetic zeolite which is synthetically produced by known methods, ie from sodium aluminate and sodium silicate.
まず、4A型合成ゼオライトと上記の量のカオリン型粘
土及び水酸化ナトリウムとからなる混合物を、押111
シ成型し得るよう水分の調整を行い、押IJIL成型時
に押出し動力を低減させるよう潤滑剤を加えた後、全て
か均一となるよう混練する。First, a mixture consisting of 4A type synthetic zeolite, the above amounts of kaolin type clay, and sodium hydroxide was pressed in a press 111.
After adjusting the moisture content so that it can be molded, and adding a lubricant to reduce the extrusion power during IJIL molding, the mixture is kneaded so that it is uniform.
カオリン型粘土の量かそれと上記セオライI・とのご、
11に女、J して20重量%に/lY’jたないと、
十分な強度をもつ製品かえられない。いっぽう、30f
I!量%をこえると、ゼオライト純分の高い成形体をう
るのが困難となって性能か低下する。又、水酸化ナトリ
ウムの量がカオリン型粘土を4A型ゼオライトに転化す
るだめの化学的量論量の25%をこえると、ソーダライ
トの知き不純物を生成する傾向か増し、製品の品質が低
下することとなる。The amount of kaolin type clay and the above Ceorai I.
11, female, J and 20% by weight/lY'j,
I can't replace the product with sufficient strength. On the other hand, 30f
I! If the amount exceeds this amount, it becomes difficult to obtain a molded article with a high zeolite purity content, and the performance deteriorates. Also, if the amount of sodium hydroxide exceeds 25% of the stoichiometric amount for converting kaolin type clay into 4A type zeolite, the tendency of sodalite to generate impurities will increase and the quality of the product will deteriorate. I will do it.
混練によってえられた混合物を公知の押出し成型器で押
出して成型する。えられた成型体は、つぎの焼成の前に
、常法により、すなわぢ100〜120°Cで成型体中
の水分か約20重量%となるまで乾燥するのがよい。The mixture obtained by kneading is extruded and molded using a known extruder. The obtained molded product is preferably dried by a conventional method at 100 to 120° C. until the moisture content in the molded product becomes about 20% by weight before the next firing.
乾燥された成形体は、たとえば長さ5〜15mmのベレ
ットに整粒した後、カオリンを原料とする場合の焼成温
度である550〜650°Cの雰囲気11て焼成する。The dried compact is sized into pellets with a length of 5 to 15 mm, for example, and then fired in an atmosphere 11 at 550 to 650°C, which is the firing temperature when kaolin is used as a raw material.
焼成時間は、2時間量」二とれば十分である。このよう
な条件で焼成することによって、カオリン型粘土は、焼
結してメタカオリン型粘土となってゼオライト11−品
を強く結合する。粘」1中の有機物は、全て燃焼して無
くなる。叉、押出し成型助剤の潤滑剤も全て燃焼して無
くなり、この段階でゼオライトに転化し111ない不純
物は実質的に無視し得る程になる。A baking time of 2 hours is sufficient. By firing under such conditions, the kaolin type clay is sintered to become metakaolin type clay, which strongly binds the zeolite 11-product. All the organic matter in the viscosity 1 will burn and disappear. In addition, all the lubricant of the extrusion aid is burned away, and impurities that are not converted into zeolite at this stage can be virtually ignored.
次に、焼成された押出し成型体を少なくとも20重量%
以上になる様に加湿し、できれば水中に’fA ’/M
し、その細孔から吸右された空気等のガスを脱着させる
のかよい。この操作は、本発明にとって必須のものでは
ないか、次の水酸化ナトリウム水溶液による処理の際に
成型体かヒビ割れ、キレツなどを起こすおそれをなくす
には好ましい操作である。Next, at least 20% by weight of the fired extruded body
Humidify the water to a level above, and if possible, immerse it in water with 'fA'/M.
However, the gas such as air sucked in through the pores may be desorbed. This operation is not essential for the present invention, but is preferable in order to eliminate the possibility that the molded product will crack or break during the subsequent treatment with an aqueous sodium hydroxide solution.
押14″lし成型体を加湿操作した後、水酸化ナトリウ
ム水溶
する。エーシングの温度は常法の室温から40 ’Cの
範囲では殆ど影響はなくこの範囲の温度であれば細かい
温度制御を必要としない。After pressing for 14"l and humidifying the molded body, dissolve it in water with sodium hydroxide.The temperature of the icing has almost no effect in the range from the normal room temperature to 40'C, and if the temperature is within this range, fine temperature control is required. I don't.
又、エージングの時間についても1時間以上エーシング
すれば良く短時間である。これは先の焼成において、不
純物か無くなり、成型体中のカオリン粘土が実質的に1
00%ゼオライトに転化し得る反応性のメタカオリン粘
土に転移していることを示す。Furthermore, the aging time is short enough if the aging is performed for one hour or more. This is due to the impurities being eliminated during the previous firing, and the kaolin clay in the molded body is substantially reduced to 1.
00% indicates a transition to a reactive metakaolin clay that can be converted to zeolite.
次に、エージングされたメタカオリン粘土結合剤を含む
押出し成型体か浸漬されている水酸化ナトリウム水溶液
を常法の80℃以上、沸点以下に昇温しで押出し成型体
中のメタカオリン粘土結合剤を完全に4A型ゼオライト
に転化させる。もつとも、工業的な製造を考えれば低い
温度はど、ずなわち80°Cか有利である。又、昇温後
2時間経過すれば、はぼ100%ゼオライ!・に転化す
る。Next, the extrudate containing the aged metakaolin clay binder was immersed in a sodium hydroxide aqueous solution, which was heated to 80°C or higher and below the boiling point using a conventional method to completely remove the metakaolin clay binder in the extrudate. It is converted into type 4A zeolite. However, when considering industrial production, a lower temperature, ie, 80°C, is advantageous. Also, if 2 hours have passed after raising the temperature, it will be 100% Zeolite!・Transforms into
上記の水酸化ナトリウム水溶液の濃度を1 、13m。The concentration of the above sodium hydroxide aqueous solution was 1.13m.
/により低くすると、ゼオライトへの転化に長時間を要
して生産性か悪いだけてなく、ゼオラ−(1・純分の低
い押出し成型体となりがちであって好ましくない。いっ
ぽう、水酸化ナトリウム水溶lf&の濃度を3.0 m
ol/j!より高くすると、ソーダライトの如き不純物
を生成し、4A型ゼオライト純分の低い押出し成型体と
なり好ましくない。If it is lower than /, it takes a long time to convert to zeolite, resulting in poor productivity. The concentration of lf & 3.0 m
ol/j! If the temperature is higher, impurities such as sodalite are produced, resulting in an extruded product having a low purity of type 4A zeolite, which is not preferable.
以上のようにして実質的に100%ゼオライトに転化せ
しめた押出し成型体を、水酸化ナトリウム水溶液から取
出し、過剰の水酸化ナトリウムを水で充分洗浄し、乾燥
する。活性化するには、この乾燥によってえられたもの
をさらに焼成すればよい。The extruded product which has been substantially 100% converted to zeolite as described above is taken out from the aqueous sodium hydroxide solution, the excess sodium hydroxide is thoroughly washed with water, and the product is dried. In order to activate it, the product obtained by this drying may be further fired.
[発明の効果]
以上の説明から明らかな様に本発明によれば(1)簡単
な工程操作で「1.っ短時間のうちにカオリン型粘土を
4A型ゼオライトに転化させることかでき、
(2)優れた機械的強度を保持し、
(3)高いゼオライト純分を含有したバインダレス4A
ゼオライト押出し成型体を?1ノることかできる。又、
(4)完全に結晶化させた押出し成型体を洗浄し、塩化
カルシウム水溶液を用い昇温下で処理して、ナI・リウ
ムイオンをカルシウムイオンでイオン交換した後、過剰
のカルシウムを洗浄し乾燥及び焼成してt占性化するこ
とにより、高強度・同純分の孔径5オンクストロームの
カルシウム交換ゼオライト押出し成型体を?1Jること
もてきる。[Effects of the Invention] As is clear from the above explanation, according to the present invention, (1) kaolin type clay can be converted into 4A type zeolite in a short time by simple process operations; 2) Binderless 4A that maintains excellent mechanical strength and (3) contains high zeolite purity.
Zeolite extrusion molded body? I can only say 1 no. (4) The completely crystallized extrusion molded body is washed, treated with an aqueous calcium chloride solution at an elevated temperature to exchange sodium and lium ions with calcium ions, and then washed to remove excess calcium. By drying and calcining it to make it t-occupied, a calcium-exchanged zeolite extrusion molded body with a pore size of 5 angstroms and high strength and the same purity is produced. You can also get 1J.
[実施例] 以下の具体例における「部」は、重量による。[Example] "Parts" in the following specific examples are by weight.
実施例]
4A型セオラー(1−粉末100部に国産のカオリン型
粘土25部、水酸化ナトリウム2,26部を混合し、低
い動力で押出し成型し得る様、水分の調整を行いなから
、押出し助剤としてCMC(カルボキンメチルセルロー
ス)粉末3部を加えフラーミキサー中で均一になるよう
良く混合混練した。次に、この混練物を二軸型の押出し
器で151 〕
n1lnペレットに押出し成型し120°Cで乾燥後5
〜1、5 mmの長さに整粒し、マツフル炉を用い60
0°C雰囲気下で2時間焼成した。冷却後、この焼成ペ
レット200gを1リットルの水に浸漬して脱泡した後
、水1′Jノリし、 ]、G mol/ 1の水酸化ナ
トリウム水溶液中に入れ、40 ’Cで1時間ニージン
クし、史に80°Cて3時間放置して結晶化を完結させ
た。Example] Type 4A Theorer (1- Mix 100 parts of powder with 25 parts of domestically produced kaolin type clay and 2.26 parts of sodium hydroxide, adjust the moisture content so that it can be extruded with low power, and then extrude. Three parts of CMC (carboquine methyl cellulose) powder was added as an auxiliary agent and the mixture was thoroughly mixed and kneaded in a Fuller mixer so as to be uniform.Next, this kneaded product was extruded into pellets using a twin-screw extruder. After drying at 5 °C
The grains were sized to a length of ~1.5 mm and heated using a Matsufuru furnace at 60 mm.
It was baked for 2 hours in a 0°C atmosphere. After cooling, 200 g of the calcined pellets were immersed in 1 liter of water to defoam, rinsed with 1'J of water, placed in a sodium hydroxide aqueous solution of ], G mol/1, and kneaded at 40'C for 1 hour. The mixture was then left at 80°C for 3 hours to complete crystallization.
このものを洗浄し、乾燥さぜ、そして350 ’Cて1
11−!j間、焼成を占性化した。Wash this stuff, dry it, and heat it to 350'C.
11-! During the j period, the firing was made special.
X線回折によって結晶解IJ〒を行った結果、他の相が
全く存在ぜす、4A型ゼオライトへのほぼ完全な転化を
示した。この活性佳品の耐圧強度を本屋式硬度計を用い
て測定した結果5.6Kgであった。この11り性化品
を相対湿度80%のテンケータ中で16 +l:r間置
き、粒子強度をJIS−に−1464の方法で測定した
結果、0.4%であり、26.5%の水分吸着量を示し
た。Crystallization IJ by X-ray diffraction showed almost complete conversion to type 4A zeolite with no other phases present. The compressive strength of this active product was measured using a Honya type hardness tester and was found to be 5.6 kg. This 11-reinforced product was placed in a tensometer with a relative humidity of 80% for 16+l:r intervals, and the particle strength was measured using the method of JIS-1464, which was 0.4% and 26.5% moisture The amount of adsorption is shown.
又、このl:9性化品を相対湿度8096のデシケタ中
で1611’1間置くと26.5%の水分吸る゛を示]
2
した。このことは4A型ゼオライトへのほぼ完全な転化
を示している。Furthermore, when this l:9-modified product was placed in a desiccator with a relative humidity of 8096 for 1611'1, it absorbed 26.5% moisture].
2 I did. This indicates almost complete conversion to type 4A zeolite.
表 1
実施例2
実施例〕と同様な操作で押出し成型し、焼成した成型体
を水中に浸漬し脱泡した後、 1.9.2.22.5.
3.0 mol/jの水酸化ナトリウム水溶lfk中で
、それぞれ40℃で1時間ニージンクし、80°Cて3
時間放置し結晶化を完結させた。それらのものを洗浄し
乾燥後350°Cて1時間、焼成活性化しj二。Table 1 Example 2 Extrusion molding was performed in the same manner as in Example], and the fired molded body was immersed in water to defoam, and then 1.9.2.22.5.
Knee zinc in 3.0 mol/j sodium hydroxide aqueous solution lfk at 40°C for 1 hour, and then incubate at 80°C for 3 hours.
The mixture was allowed to stand for a while to complete crystallization. After washing and drying these items, they were activated by firing at 350°C for 1 hour.
そし7て、4A型ゼオライトへの完全な転化を確認すべ
く、X線回折によって結晶解析を行った結果、他の相は
全く認められなかった。更に、これらのものの耐圧強度
ならびに相対湿度8096ての粒子強度および水分吸着
量の411定を行った。Then, in order to confirm complete conversion to type 4A zeolite, crystal analysis was performed by X-ray diffraction, and as a result, no other phases were observed. Furthermore, the compressive strength, particle strength and water adsorption amount at a relative humidity of 8096 were determined.
その結果を表]に示す。The results are shown in Table].
1′3
実施例3゜
実施例1.の押出し成型体の成型組成を4A型ゼオライ
ト粉末100部、国産のカオリン型粘土42.9部、水
酸化ナトリウム3.86部に変えた以外は全く同様な操
作を行って、その物性を/III定した。その結果を表
2に示す。1'3 Example 3゜Example 1. Exactly the same procedure was performed except that the molding composition of the extrusion molded body was changed to 100 parts of 4A type zeolite powder, 42.9 parts of domestically produced kaolin type clay, and 3.86 parts of sodium hydroxide, and the physical properties were determined as /III Established. The results are shown in Table 2.
]4 表2 ′3.と全く同様な操作を行った。]4 Table 2 '3. I did exactly the same operation.
えられたものの物性を表3及び表4に示す。The physical properties of the obtained product are shown in Tables 3 and 4.
表3 (粘土25部の場合)
実施例4
粘土にジョーシアカオリンを用い、その量を4A型ゼオ
ライト粉末100部に対して25部、更に420部にし
た以外は実施例1.及び実施例]5
]
表4
(粘土42
9部の場合)
実施例5゜
実施例2.3.及び4.で得られたハインダレスゼオラ
イト成型体を塩化カルシウム水溶液でカルシウムイオン
交換処理し孔径5オンゲスi・ロムのカルシウム交換ゼ
オライトとじた。そのものを洗浄し、乾燥した後′35
0°Cて111.’j間焼成活性化し、−10°C,7
00torrでの窒素吸着量をA11l定した。その結
果を表5に示す。更に、相対湿度80%での水分吸容量
の7Ill+定を行った。Table 3 (In the case of 25 parts of clay) Example 4 Same as Example 1 except that Joshia kaolin was used as the clay and the amount was changed to 25 parts and then 420 parts to 100 parts of 4A type zeolite powder. and Example] 5 ] Table 4 (In the case of 9 parts of clay 42) Example 5゜Example 2.3. and 4. The Hinderless zeolite molded body obtained in the above was subjected to a calcium ion exchange treatment with an aqueous calcium chloride solution, and then a calcium-exchanged zeolite having a pore size of 5 Ω/m was sealed. After washing and drying it'35
111 at 0°C. Activate firing for -10°C, 7
The nitrogen adsorption amount at 00 torr was determined as A11l. The results are shown in Table 5. Furthermore, the water absorption capacity was determined at 7Ill+ at a relative humidity of 80%.
表5
]
比較例]
4A型セオラー(+−粉末1. O0部に国産のカオリ
ン型粘土1 (30部、水酸化ナトリウム9部を混合し
、水分の調整を行いなから押出し助剤としてCMC粉末
3部を加えマーラーミキザー中で均一になる様良く混練
した。次に、この混練物を実施例]、と全く同トlな操
作で処理し物性をfllll定した。Table 5] Comparative Example] 4A type Theoler (+- powder 1.0 parts, domestically produced kaolin type clay 1 (30 parts, sodium hydroxide 9 parts) were mixed, the moisture was adjusted, and then CMC powder was added as an extrusion aid. 3 parts were added and thoroughly kneaded in a Mahler mixer so that it became uniform.Then, this kneaded product was treated in exactly the same manner as in Example], and the physical properties were determined.
その結果を表6に示す。The results are shown in Table 6.
表6
を混合し、水分の調整を行いながら押出し助剤としてC
MC粉末3部を加えマーラーミギ→ノ゛−中で均一にな
る様良く混練した。ここでlJ−コ合された水酸化ナト
リウムの凰は粘土をゼオライトに転化せしめるための化
学量論量の35%である。次に、この混合物を実施例1
.と同様な操作で処理した。Table 6 was mixed with C as an extrusion aid while adjusting the moisture content.
3 parts of MC powder was added and kneaded well in a miller grinder to ensure uniformity. Here, the amount of sodium hydroxide combined is 35% of the stoichiometric amount for converting the clay to zeolite. Next, this mixture was prepared in Example 1.
.. It was processed in the same way.
X線回1ノiによって結晶解4j〒を行った11〜果、
他の相ソーグライドか生成していた。又、相対411度
80%での水分吸る量は230ゾロであり4 A ’=
’+リセオライI・純分の低い成型体が得られた。11 ~ Results of crystal solution 4j 〒 carried out by X-ray cycle 1noi,
Other phase Saw Glide was generated. Also, the amount of moisture absorbed at relative 411 degrees and 80% is 230 sol, and 4 A'=
'+ Liseolae I A molded body with low purity was obtained.
特11′1出願人 東ソー株式会社 比較例2Special 11'1 applicant: Tosoh Corporation Comparative example 2
Claims (1)
イト粉末との合計に対して20〜30重量%のカオリン
型粘土および該カオリン型粘土を4A型ゼオライトに転
化させるための化学量論量の25%以下の水酸化ナトリ
ウムからなる混合物を、押出し成型し、えられた成型体
を焼成した後、濃度1.6〜3.0mol/lの水酸化
ナトリウム水溶液中で粘土を4A型ゼオライトに転化さ
せることを特徴とする、バインダレス4A型ゼオライト
成型体の製造方法(1) Synthetic 4A type zeolite powder, 20 to 30% by weight of kaolin type clay based on the total of the synthetic 4A type zeolite powder, and a stoichiometric amount of 25% by weight for converting the kaolin type clay into 4A type zeolite. % or less of sodium hydroxide is extrusion molded, the resulting molded body is fired, and then the clay is converted into 4A type zeolite in an aqueous sodium hydroxide solution with a concentration of 1.6 to 3.0 mol/l. A method for producing a binderless 4A type zeolite molded body, characterized by
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JP63310125A JP2782744B2 (en) | 1988-12-09 | 1988-12-09 | Method for producing binderless zeolite molded body |
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JP63310125A JP2782744B2 (en) | 1988-12-09 | 1988-12-09 | Method for producing binderless zeolite molded body |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000013780A1 (en) * | 1998-09-03 | 2000-03-16 | Francesco Corigliano | Method for converting siliceous base particles into granular or monolithic forms |
EP2399951A1 (en) | 2010-06-25 | 2011-12-28 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Pellets and method for their manufacture |
WO2012024896A1 (en) * | 2010-08-23 | 2012-03-01 | 中国石油化工股份有限公司 | Non-adhesive molecular sieve catalyst and preparation method therefor |
CN104211082A (en) * | 2013-06-03 | 2014-12-17 | 中国石油大学(北京) | Synthetic method of 4A molecular sieve |
WO2016124843A1 (en) | 2015-02-02 | 2016-08-11 | Ceca S.A. | Zeolite adsorbents having a high external surface area and uses thereof |
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US7820869B2 (en) | 2008-06-30 | 2010-10-26 | Uop Llc | Binderless adsorbents and their use in the adsorptive separation of para-xylene |
US7812208B2 (en) | 2008-09-22 | 2010-10-12 | Uop Llc | Binderless adsorbents with improved mass transfer properties and their use in the adsorptive separation of para-xylene |
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Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
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US3119659A (en) | 1960-09-26 | 1964-01-28 | Union Carbide Corp | Process for producing molecular sieve bodies |
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1988
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Cited By (9)
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---|---|---|---|---|
WO2000013780A1 (en) * | 1998-09-03 | 2000-03-16 | Francesco Corigliano | Method for converting siliceous base particles into granular or monolithic forms |
EP2399951A1 (en) | 2010-06-25 | 2011-12-28 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Pellets and method for their manufacture |
DE102010030547A1 (en) | 2010-06-25 | 2011-12-29 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Pellets and process for their preparation |
WO2012024896A1 (en) * | 2010-08-23 | 2012-03-01 | 中国石油化工股份有限公司 | Non-adhesive molecular sieve catalyst and preparation method therefor |
US9861969B2 (en) | 2010-08-23 | 2018-01-09 | China Petroleum & Chemical Corporation | Binderless molecular sieve catalyst and a preparation method thereof |
CN104211082A (en) * | 2013-06-03 | 2014-12-17 | 中国石油大学(北京) | Synthetic method of 4A molecular sieve |
WO2016124843A1 (en) | 2015-02-02 | 2016-08-11 | Ceca S.A. | Zeolite adsorbents having a high external surface area and uses thereof |
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CN109761241A (en) * | 2018-12-27 | 2019-05-17 | 济南大学 | A method of utilizing alkaline matter activated clays pore-creating |
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