JP2010132530A - High-strength zeolite bead molding and method for producing the same - Google Patents

High-strength zeolite bead molding and method for producing the same Download PDF

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JP2010132530A
JP2010132530A JP2009199873A JP2009199873A JP2010132530A JP 2010132530 A JP2010132530 A JP 2010132530A JP 2009199873 A JP2009199873 A JP 2009199873A JP 2009199873 A JP2009199873 A JP 2009199873A JP 2010132530 A JP2010132530 A JP 2010132530A
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zeolite
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clay binder
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JP5747435B2 (en
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Shigeru Hirano
茂 平野
Taizo Kawamoto
泰三 河本
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Tosoh Corp
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Priority to CN200980139885.0A priority patent/CN102177093B/en
Priority to PCT/JP2009/068288 priority patent/WO2010050417A1/en
Priority to TW98136935A priority patent/TWI468345B/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/28Selection of materials for use as drying agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16Alumino-silicates
    • B01J20/18Synthetic zeolitic molecular sieves
    • B01J20/183Physical conditioning without chemical treatment, e.g. drying, granulating, coating, irradiation
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/14Type A
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/106Silica or silicates
    • B01D2253/108Zeolites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30Physical properties of adsorbents
    • B01D2253/302Dimensions
    • B01D2253/304Linear dimensions, e.g. particle shape, diameter
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/30Physical properties of adsorbents
    • B01D2253/302Dimensions
    • B01D2253/308Pore size

Abstract

<P>PROBLEM TO BE SOLVED: To solve the problem that shaped beads formed from zeolite and a clay binder by tumbling granulation are problematic in that the strength and abrasion resistance are poor. <P>SOLUTION: Shaped zeolite beads with an average diameter of 1.0-3.0 mm having compressive strength of ≥35 N (particularly ≥70 N) when hydrated and an abrasion resistance factor of ≤1.5% are obtained by subjecting a composition of at least 35 pts.wt. of water per 100 pts.wt. of zeolite and the clay binder combined by tumbling granulation to carry out molding in a bead shape and then adding ≤4 pts.wt. of clay binder of the molding (excluding the water content), subjecting the product to tumbling grading, drying, and firing. Preferably the zeolite crystals used are ≤5 μm, 10-50 pts.wt. of clay binder are used, and the same type of clay binder is used for molding and grading. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、高強度で、特に耐摩耗性の高いゼオライトビーズ成型体及びその製造方法に関するものである。例えば、自動車のエアコン用のフロン乾燥剤に用いられるゼオライトビーズ成型体は、エンジン駆動の振動によって粉化しない様に、特に高い強度及び耐磨耗性が要求されている。   The present invention relates to a zeolite bead molded body having high strength and particularly high wear resistance, and a method for producing the same. For example, a zeolite bead molded body used for a Freon desiccant for an air conditioner of an automobile is required to have particularly high strength and wear resistance so as not to be pulverized by vibration of an engine drive.

ゼオライトビーズ成型体は広く乾燥剤として用いられているが、最近では自動車用エアコンの乾燥剤としての需要が増大している。自動車用エアコンは使用時に振動にさらされるため、強度、磨耗性が低いと粉化すると目詰まりの原因となり、高強度、高耐磨耗性の乾燥剤が求められている。   Zeolite bead moldings are widely used as desiccants, but recently, the demand for desiccants for automobile air conditioners is increasing. Since air conditioners for automobiles are exposed to vibration during use, if the strength and wear resistance are low, powdering may cause clogging, and a desiccant with high strength and high wear resistance is required.

高強度、高耐磨耗性の乾燥剤を得る方法としては、例えばバインダーに縮合リン酸塩等の添加物を用いる方法、バインダーとして特殊な針状結晶のバインダーを用いる方法(特許文献2)、アルカリ性化合物で処理する方法(特許文献3、特許文献4)等が提案されている。しかし、いずれも特殊な原料や、特別の処理工程を必要とする方法であり、乾燥剤のコストアップの原因となっていた。   As a method of obtaining a desiccant having high strength and high abrasion resistance, for example, a method using an additive such as condensed phosphate as a binder, a method using a special needle-like crystal binder as a binder (Patent Document 2), A method of treating with an alkaline compound (Patent Document 3, Patent Document 4) and the like have been proposed. However, all of these methods require special raw materials and special processing steps, and have been the cause of increased costs for desiccants.

いずれの方法においても得られた成型体粒子を整粒し、成型体表面を滑らかにしたり、真球度を上げたりする効果が指摘されているが、十分な効果は得られていなかった。   In any of the methods, it has been pointed out that the obtained molded body particles are sized to smooth the surface of the molded body and increase the sphericity, but a sufficient effect has not been obtained.

他にも高強度のペレット成型体を転動整粒によって角をとる方法(特許文献5)も知られている。その様な方法では強度の高い粒子は得られるが、真球度の高い成型体は得られないため、自動車用のフロン乾燥剤には使用できなかった。   In addition, there is also known a method (Patent Document 5) in which a high-strength pellet molded body is rounded by rolling sizing. In such a method, particles having high strength can be obtained, but a molded product having a high sphericity cannot be obtained.

特開2001−261330JP 2001-261330 A 特開平11−314913号JP-A-11-314913 特開平4−198012号Japanese Patent Laid-Open No. 4-198012 特開平6−327968号JP-A-6-327968 特開平10−87322号JP-A-10-87322

本発明の目的は、特殊な原料や工程を用いることなく、ゼオライト、特に3A型ゼオライト(Kイオン交換A型ゼオライト)と粘土バインダーのビーズ成型体の強度(水和耐圧強度)及び耐摩耗性を向上する方法を提供するものである。   The object of the present invention is to increase the strength (hydration pressure resistance) and wear resistance of beads, especially 3A type zeolite (K ion exchange A type zeolite) and clay binder, without using special raw materials and processes. It provides a way to improve.

本発明者等は、ゼオライトビーズ成型体の水和耐圧強度及び耐磨耗性の向上について鋭意検討を重ねた結果、造粒後の転動整粒時に特定の範囲の粘土バインダーを加えることにより、成型体の水和耐圧強度と耐摩耗性が著しく向上することを見出し、本発明を完成させるに到ったものである。   As a result of intensive studies on the improvement of the hydration pressure strength and wear resistance of the zeolite bead molded article, the present inventors have added a specific range of clay binder during rolling sizing after granulation, It has been found that the hydration pressure strength and wear resistance of the molded product are remarkably improved, and the present invention has been completed.

以下、本発明のゼオライトビーズ成型体の製造方法を説明する。   Hereafter, the manufacturing method of the zeolite bead molded object of this invention is demonstrated.

本発明のゼオライトビーズ成型体の製造方法は、ゼオライトと粘土バインダー合わせて100重量部に対し、水分35重量部以上の組成物を転動造粒によりビーズ状に成型した後、成型体固形分重量(水分除く)に対して4重量部以下の粘土バインダーを添加して転動整粒した後、乾燥、焼成するものである。   The method for producing a zeolite bead molded body according to the present invention comprises molding a composition having a water content of 35 parts by weight or more into a bead shape by rolling granulation with respect to 100 parts by weight of the zeolite and the clay binder, and then molding the solid content weight. After adding 4 parts by weight or less of a clay binder (excluding moisture) and rolling and sizing, it is dried and fired.

本発明の方法において、成型時のゼオライトと粘土バインダーに対する水分量は少なすぎるとビーズ成型体が得られず、多すぎると成型体同士が付着して成型体が異常成長する。ゼオライトと粘土バインダー合わせて100重量部に対する水分量は用いる粘土バインダーの粒径、表面積によって調整幅があるが、少なくとも35重量部以上、特に35〜60重量部の範囲が好ましい。   In the method of the present invention, if the water content with respect to the zeolite and clay binder at the time of molding is too small, a bead molded body cannot be obtained, and if it is too much, the molded bodies adhere to each other and the molded body grows abnormally. The amount of water relative to 100 parts by weight of the zeolite and the clay binder is adjusted depending on the particle size and surface area of the clay binder used, but is preferably at least 35 parts by weight, particularly 35 to 60 parts by weight.

本発明では、上記の水分量の組成物をビーズ状に成型した後に、成型体固形分重量(水分除く)100重量部に対して4重量部以下の粘土バインダーを添加して転動整粒することによって強度及び耐摩耗性を向上させるものである。   In the present invention, the composition having the above water content is molded into beads, and then 4 parts by weight or less of a clay binder is added to 100 parts by weight of the solid content of the molded body (excluding water) to perform rolling sizing. This improves the strength and wear resistance.

本発明における成型及び整粒はビーズ状の成型体を成型できるものであれば特に限定はなく、一般的な転動整粒器、ドラム造粒器、回転式の筒状造粒器いずれも使用できる。   Molding and sizing in the present invention are not particularly limited as long as a bead-shaped molded body can be molded, and any of a general rolling granulator, drum granulator, and rotary cylindrical granulator can be used. it can.

粘土バインダーを含むゼオライトビーズ成型体は、整粒することによって成型体表面を滑らかにして耐摩耗性がある程度向上することは知られている。しかし、従来の整粒は、成型体表面に付着した異物の除去や、表面に平滑化による効果であり、その効果は限定的なものでしかなかった。   It is known that a zeolite bead molded body containing a clay binder is smoothened by adjusting the particle size to improve the wear resistance to some extent. However, the conventional sizing is an effect of removing foreign substances adhering to the surface of the molded body and smoothing the surface, and the effect is only limited.

本発明では、転動整粒時に粘土バインダーを特定の範囲で添加することにより、転動整粒時に成型体表面を清浄化するだけでなく、欠陥の補充及びより強固な保護層が形成され、少量のバインダー添加にも拘わらず、著しく強度が向上するものである。   In the present invention, by adding a clay binder in a specific range at the time of rolling sizing, not only cleaning the surface of the molded body at the time of rolling sizing, but also a defect replenishment and a stronger protective layer is formed, Despite the addition of a small amount of binder, the strength is remarkably improved.

本発明で転動整粒時に添加する粘土バインダーは、成型体固形分重量(転動造粒時のゼオライトと粘土バインダーの固形分重量で、水分除く)100重量部に対して4重量部以下、特に0.01〜3重量部、さらに0.1〜3重量部の範囲が好ましい。   In the present invention, the clay binder added at the time of rolling sizing is 4 parts by weight or less with respect to 100 parts by weight of the solid weight of the molded body (the solid weight of zeolite and clay binder at the time of rolling granulation, excluding moisture). In particular, a range of 0.01 to 3 parts by weight, and further 0.1 to 3 parts by weight is preferable.

転動整粒時に添加する粘土バインダーの添加量が、4重量部を超えて添加した場合、成型体の耐圧強度は向上するが、耐磨耗性が低下するという問題がある。   When the amount of the clay binder added during rolling sizing exceeds 4 parts by weight, the pressure resistance of the molded body is improved, but there is a problem that the wear resistance is lowered.

転動整粒時の水分量は、成型体固形分重量(水分除く。ゼオライト及び粘土バインダー。転動整粒時に添加した粘土バインダーを含む)100重量部に対して35重量部以上、特に35〜45重量部の範囲が好ましい。   The amount of water at the time of rolling sizing is 35 parts by weight or more, particularly 35 to 35 parts by weight with respect to 100 parts by weight of the solid weight of the compact (excluding moisture. Zeolite and clay binder. Including clay binder added at the time of rolling sizing). A range of 45 parts by weight is preferred.

転動整粒時に粘土バインダーを添加する際に粘土バインダーとともに水分を添加して水分量を調整することが好ましい。転動整粒時に粘土バインダーと共に添加する水分は、添加した粘土バインダーが成型体表面に保護層を形成し易くする効果がある。   When adding a clay binder during rolling sizing, it is preferable to adjust the amount of water by adding water together with the clay binder. The water added together with the clay binder at the time of rolling sizing has an effect of making the added clay binder easily form a protective layer on the surface of the molded body.

転動整粒時において、粒子同士の摩擦による温度上昇によって成型体が乾燥していると、粘土バインダーを添加して転動整粒を実施しても本発明の効果は十分に得られない。   At the time of rolling sizing, if the molded body is dried due to a temperature rise due to friction between particles, the effect of the present invention cannot be sufficiently obtained even if rolling sizing is performed by adding a clay binder.

本発明で用いる粘土バインダーは、成型に用いる粘土バインダーと整粒時に添加する粘土バインダーを同じ種類の粘土バインダーを用いることが好ましい。同一の粘土バインダーを用いることにより、少量の粘土バインダーの添加で特に耐磨耗性の高い成型体が得られる。   As the clay binder used in the present invention, it is preferable to use the same kind of clay binder used for molding and clay binder added at the time of granulation. By using the same clay binder, a molded product having particularly high wear resistance can be obtained by adding a small amount of clay binder.

本発明に用いるゼオライトに対する粘土バインダーは特に限定されるものでないが、カオリン系、ベントナイト系、タルク系、バイロフィライト系、モリサイト系、バーキュロライト系、モンモリロナイト系、クロライト系、ハロイサイト系等の粘土が例示でき、特に板状結晶であるカオリン粘土が好ましい。またゼオライトに対する粘土バインダーの添加量は最終的に得られる成型体中のゼオライト100重量部(水分除く)に対して10重量部以上50重量部以下、特に40重量部を超え50重量部以下が好ましい。バインダー量が少なすぎると強度が不十分であり、多すぎると単位重量当りの乾燥剤としての性能が低下する。   The clay binder for the zeolite used in the present invention is not particularly limited. The kaolin clay which is a plate-shaped crystal | crystallization is especially preferable. Further, the addition amount of the clay binder to the zeolite is preferably 10 parts by weight or more and 50 parts by weight or less, particularly more than 40 parts by weight and 50 parts by weight or less with respect to 100 parts by weight of the zeolite (excluding moisture) in the finally obtained molded body. . When the amount of the binder is too small, the strength is insufficient, and when it is too large, the performance as a desiccant per unit weight is lowered.

転動整粒時に添加される粘土バインダーが造粒時の成型体重量の4重量%以下であり、粘土バインダーは、ゼオライトに対して40重量部以上44重量部以下が好ましい。   The clay binder added at the time of rolling sizing is 4% by weight or less of the weight of the molded body at the time of granulation, and the clay binder is preferably 40 parts by weight or more and 44 parts by weight or less with respect to zeolite.

本発明で用いるゼオライトは特に限定はないが、自動車用エアコンの乾燥剤として用いる場合、フロンを吸着せず、水分のみを選択的に吸着するKイオン交換型A型ゼオライトであることが好ましい。   The zeolite used in the present invention is not particularly limited, but when used as a desiccant for an automotive air conditioner, it is preferably a K ion exchange type A zeolite that does not adsorb chlorofluorocarbon and selectively adsorbs only moisture.

3A型ゼオライト粉末は、公知の方法、すなわちアルミン酸ナトリウムおよびケイ酸ナトリウムとから合成されたナトリウムA型ゼオライト粉末を塩化カリウム水溶液中で、ゼオライト中のナトリウムイオンの35%以上をカリウムイオンで交換し、有効細孔径が3オングストロームの3A型ゼオライト粉末とすることができる。   3A-type zeolite powder is obtained by a known method, that is, sodium A-type zeolite powder synthesized from sodium aluminate and sodium silicate is exchanged with potassium ions in potassium chloride aqueous solution, and 35% or more of sodium ions in the zeolite are exchanged with potassium ions. The 3A-type zeolite powder having an effective pore diameter of 3 angstroms can be obtained.

本発明で用いるゼイライト結晶の粒径は5μm以下、特に3〜4μmであることが好ましい。ゼオライト結晶の粒径が大きすぎると、耐摩耗性が低下し易い。   The particle size of the zelite crystal used in the present invention is preferably 5 μm or less, particularly preferably 3 to 4 μm. When the particle size of the zeolite crystal is too large, the wear resistance tends to be lowered.

本発明における整粒時間は限定されるものではないが、短時間では十分な効果が得られないため、少なくとも10分以上、特に60分以上処理することが好ましい。   The sizing time in the present invention is not limited, but since a sufficient effect cannot be obtained in a short time, it is preferable to treat at least 10 minutes or more, particularly 60 minutes or more.

本発明では、ゼオライト乾燥剤の性能に悪影響をしない限りにおいて、粘土バインダーの他に分散剤や、成型助剤(CMC等の助剤)を含んでもよい。   In the present invention, as long as the performance of the zeolite desiccant is not adversely affected, in addition to the clay binder, a dispersant and a molding aid (an auxiliary agent such as CMC) may be included.

本発明の製造法における乾燥、焼成の条件は特に制限されるものではないが、水分の含有量が多い乾燥状態での焼成や、高温での焼成ではゼオライトが水熱劣化し、乾燥剤としての性能が低下する。乾燥時の水分含有量はig−loss換算で10〜32%、特に10〜25%、焼成温度は600〜800℃、特に600〜700℃の範囲で数時間〜10時間焼成する方法が例示できる。   The conditions for drying and calcination in the production method of the present invention are not particularly limited, but the zeolite is hydrothermally deteriorated when calcinated in a dry state with a high water content or calcinated at a high temperature. Performance decreases. The moisture content at the time of drying is 10 to 32% in terms of ig-loss, particularly 10 to 25%, and the firing temperature is 600 to 800 ° C, particularly 600 to 700 ° C, and the method of firing for several hours to 10 hours can be exemplified. .

乾燥、活性化の方法としては公知の方法を用い実施することができ、例えば、熱風乾燥機、電気マッフル炉、管状炉、回転炉などを用いればよい。   As drying and activation methods, known methods can be used. For example, a hot air dryer, an electric muffle furnace, a tubular furnace, a rotary furnace, etc. may be used.

本発明の方法では、ゼオライト結晶径が5μm以下、粘土バインダーが10重量部以上50重量部以下、特に40重量部を超え50重量部以下、水和耐圧強度35N(=3.57kgf)以上、特に70N(=7.14kgf)以上、耐磨耗率が1.5%以下、平均径が1.0〜3.0mmの範囲のゼオライトビーズ成型体を得ることができる。   In the method of the present invention, the zeolite crystal diameter is 5 μm or less, the clay binder is 10 parts by weight or more and 50 parts by weight or less, particularly more than 40 parts by weight and 50 parts by weight or less, the hydration pressure strength 35N (= 3.57 kgf) or more, It is possible to obtain a zeolite bead molded body having a wear resistance of 1.5% or less and an average diameter of 1.0 to 3.0 mm in a range of 70 N (= 7.14 kgf) or more.

ゼオライト結晶径は5μm以下、特に3〜5μmであることが好ましい。ゼオライト結晶径はSEM観察によって確認することができる。ゼオライト結晶径が5μmより大きくなると、耐磨耗性が低下し易い。   The zeolite crystal diameter is preferably 5 μm or less, particularly 3 to 5 μm. The zeolite crystal diameter can be confirmed by SEM observation. When the zeolite crystal diameter is larger than 5 μm, the wear resistance tends to be lowered.

最終的に得られるゼオライトビーズ成型体中の粘土バインダーは、ゼオライト(水分除く)100重量部に対して10重量部以上50重量部以下であり、特に40重量部を超え50重量部以下であることが好ましい。また用いる粘土バインダーは板状結晶で、ゼオライト粒子と同程度、あるいはそれより小さい結晶サイズのものが好ましい。バインダーが10重量部未満では強度、耐磨耗性が不十分であり、50重量部を超えると、乾燥剤(吸着剤)としての性能が低下する。   The clay binder in the finally obtained zeolite bead molded body is 10 parts by weight or more and 50 parts by weight or less, especially 40 parts by weight or more and 50 parts by weight or less with respect to 100 parts by weight of zeolite (excluding moisture). Is preferred. The clay binder used is a plate-like crystal, preferably having a crystal size comparable to or smaller than that of the zeolite particles. If the binder is less than 10 parts by weight, the strength and wear resistance are insufficient, and if it exceeds 50 parts by weight, the performance as a desiccant (adsorbent) decreases.

ゼオライトビーズ成型体の粒径は、1.0〜3.0mmの範囲であり、特に1.4〜2.5mmの範囲であることが好ましい。   The particle size of the zeolite bead molded body is in the range of 1.0 to 3.0 mm, and particularly preferably in the range of 1.4 to 2.5 mm.

本発明の方法で得られるゼオライトビーズ成型体は、従来の珪酸ソーダ等のガラス化剤を添加(含浸)したものではないため、靭性に優れ、なおかつガラス化剤による成型体細孔の閉塞がないため、吸着性能に優れている。珪酸ソーダ等のガラス化剤を添加した成型体であるかどうかは、電子顕微鏡で組織を確認することでできる。   Since the zeolite bead molded body obtained by the method of the present invention is not added (impregnated) with a conventional vitrifying agent such as sodium silicate, it has excellent toughness and does not block the pores of the molded body due to the vitrifying agent. Therefore, the adsorption performance is excellent. Whether or not it is a molded body to which a vitrifying agent such as sodium silicate is added can be confirmed by confirming the structure with an electron microscope.

本発明のゼオライトビーズ成型体の水和耐圧強度は35N(=3.57kgf)以上、特に70N(=7.14kgf)以上、耐摩耗性は1.5%以下である。耐摩耗性は特に1%以下であることが好ましい。本発明の耐圧強度、耐摩耗性はいずれも水和(相体湿度80%)した状態での性能である。乾燥(非水和)状態であればさらに高い耐圧強度、耐摩耗性は発揮されるが、実用において強度、磨耗が問題となるのは水和が進んだ状態である。本発明では、水和状態で耐圧強度、耐磨耗性が高いことに意義がある。   The zeolite bead molded body of the present invention has a hydration pressure strength of 35 N (= 3.57 kgf) or more, particularly 70 N (= 7.14 kgf) or more, and an abrasion resistance of 1.5% or less. The wear resistance is particularly preferably 1% or less. The pressure strength and wear resistance of the present invention are both performances in a hydrated state (phase humidity 80%). In a dry (non-hydrated) state, even higher pressure strength and wear resistance are exhibited, but in practice, strength and wear are problematic in a state of advanced hydration. In the present invention, it is significant that the compressive strength and the wear resistance are high in a hydrated state.

本発明での水和耐圧強度は、相対湿度80%で水和した試料をJIS−Z−8841に記載の造粒物−強度試験方法に記載されている造粒物の圧壊強度試験方法に基づき測定した値であり、耐摩耗性の測定は同じく水和した試料100mlと有機溶媒(トリクロルエチレン)55mlを試験用として汎用的なペイントコンディショナーで1時間振とうによる重量減少比によって測定した値である。   The hydration pressure strength in the present invention is based on a crushing strength test method for a granulated product described in a granulated product-strength test method described in JIS-Z-8841 for a sample hydrated at a relative humidity of 80%. It is a measured value, and the abrasion resistance is measured by a weight reduction ratio by shaking for 1 hour with a general-purpose paint conditioner using 100 ml of a hydrated sample and 55 ml of an organic solvent (trichloroethylene) for testing. .

本発明の製造方法では、ゼオライトと粘土バインダー合わせて100重量部に対し、水分35重量部以上の混合物を転動造粒によりビーズ状に成型した後、成型体重量に対して4重量部以下の粘土バインダーを添加して転動整粒した後、乾燥、焼成することにより、強度、耐摩耗性の高いゼオライト乾燥剤を製造することができる。本発明の方法で得られたゼオライトビーズ成型体は、強度、耐摩耗性に優れるものである。   In the production method of the present invention, a mixture of 35 parts by weight or more of moisture is formed into beads by rolling granulation with respect to 100 parts by weight of zeolite and clay binder, and then 4 parts by weight or less based on the weight of the molded body. A zeolite desiccant with high strength and high wear resistance can be produced by adding clay clay and rolling and sizing, followed by drying and firing. The zeolite bead molded body obtained by the method of the present invention is excellent in strength and wear resistance.

実施例1の成型体の整粒後の表面SEM像を示す図である。It is a figure which shows the surface SEM image after the sizing of the molded object of Example 1. FIG. 実施例2の成型体の整粒後の表面SEM像を示す図である。It is a figure which shows the surface SEM image after the sizing of the molded object of Example 2. FIG. 比較例1(未整粒の成型体)の表面SEM像を示す図である。It is a figure which shows the surface SEM image of the comparative example 1 (unshaped granulated body). 比較例3の成型体の整粒後の表面SEM像を示す図である。It is a figure which shows the surface SEM image after the sizing of the molded object of the comparative example 3. FIG.

以下発明を実施例で説明するが、本発明はこれらの実施例に限定されるものではない。   EXAMPLES Hereinafter, although an Example demonstrates this invention, this invention is not limited to these Examples.

(強度(水和耐圧強度)の測定方法)
相対湿度80%で水和したゼオライトビーズ成型体をJIS−Z−8841に記載の造粒物−強度試験方法に記載されている造粒物の圧壊強度試験方法に基づき測定する。硬度計を用い、常温、常圧の雰囲気において、試験片である粒状物の直径方向に、一定速度で加圧板を押し付けて圧縮負荷を加えたとき、ゼオライトビーズ成型体が耐えることができる最大荷重を測定する。
(Measurement method of strength (hydration pressure strength))
The zeolite bead molded body hydrated at 80% relative humidity is measured based on the granulated product crushing strength test method described in the granulated product-strength test method described in JIS-Z-8841. The maximum load that the zeolite bead compact can withstand when a compression load is applied by pressing the pressure plate at a constant speed in the diameter direction of the granular material, which is a test piece, in a normal temperature and normal pressure atmosphere using a hardness meter. Measure.

本発明では、木屋式デジタル硬度計(KHT−20型)により、直径1.4mm〜2.4mmの焼成後のゼオライトビーズ成型体を用い、直径方向の耐圧強度を、直径5mmの円柱状の加圧板によって測定した。加圧板はステンレス製のものを使用し、25個の耐圧強度測定を行った。   In the present invention, a fired zeolite bead molded body having a diameter of 1.4 mm to 2.4 mm is used to measure the pressure strength in the diametrical direction of a cylindrical column having a diameter of 5 mm, using a Kiya digital hardness meter (KHT-20 type). Measured with a pressure plate. A pressure plate made of stainless steel was used, and 25 pressure-resistant strengths were measured.

(摩耗率の測定方法)
相対湿度80%で水和したゼオライトビーズ成型体100mlとトリクロルエチレン55mlをネジ口瓶(130ml)に装填し、ペイントシェーカー(東洋精機製作所製)で1時間振とうさせた後の減少重量率を測定した。振とう後、1mmの篩で摩耗粉を分離し、重量変化を測定する。
(Measurement method of wear rate)
Measure the weight loss after loading 100 ml of zeolite bead hydrated at 80% relative humidity and 55 ml of trichloroethylene into a screw mouth bottle (130 ml) and shaking with a paint shaker (Toyo Seiki Seisakusho) for 1 hour. did. After shaking, wear particles are separated with a 1 mm sieve and the change in weight is measured.

実施例1
ゼオライト(Kイオン交換A型ゼオライト)100重量部にカオリン粘土を40重量部混合し、次にゼオライトとカオリン粘土合わせて100重量部に対して50重量部の水を混合し、転動造粒によって成型し、篩分けによって1.7mmφの予備成型体を得た。成型後の予備成型体の水分量(900℃焼成時のig−loss換算)は36重量部であった。当該成型体に成型に用いたものとは産地の異なるカオリン粘土を予備成型体の固形分100重量部に対して3重量部添加し、噴霧器によって成型体含有水分を37重量部に調整し、引き続き70分間転動整粒した。その後、乾燥し、680℃で5時間焼成した。
Example 1
40 parts by weight of kaolin clay is mixed with 100 parts by weight of zeolite (K ion exchange A-type zeolite), and then 50 parts by weight of water is mixed with 100 parts by weight of zeolite and kaolin clay. Molded and sieved to obtain a 1.7 mmφ preform. The water content of the preform after molding (calculated as ig-loss at 900 ° C. firing) was 36 parts by weight. 3 parts by weight of kaolin clay having a different production area from that used for molding to the molded body is added to 100 parts by weight of the solid content of the preform, and the moisture content of the molded body is adjusted to 37 parts by weight with a sprayer. Rolled and sized for 70 minutes. Then, it dried and baked at 680 degreeC for 5 hours.

得られたビーズ成型体の特性を表1に、整粒後の成型体断面(表面)を図1に示した。成型体表面に保護層の形成が確認された。   The characteristics of the obtained bead molded body are shown in Table 1, and the cross section (surface) of the molded body after sizing is shown in FIG. Formation of a protective layer was confirmed on the surface of the molded body.

実施例2
成型と転動整粒に同じ産地のカオリン粘土を用い、なおかつ転動整粒時に添加したバインダーを0.1重量部とした以外は実施例1と同様の処理を行った。
Example 2
The same treatment as in Example 1 was performed except that kaolin clay of the same production area was used for molding and rolling sizing, and the binder added during rolling sizing was 0.1 parts by weight.

得られたビーズ成型体の特性を表1に、整粒後の成型体断面(表面)を図2に示した。
成型体表面に保護層の形成が確認された。
Table 1 shows the characteristics of the obtained bead molded body, and FIG. 2 shows a cross section (surface) of the molded body after sizing.
Formation of a protective layer was confirmed on the surface of the molded body.

実施例3
ゼオライト(Kイオン交換A型ゼオライト)100重量部にカオリン粘土を43重量部混合し、次にゼオライトとカオリン粘土合わせて100重量部に対して55重量部の水を混合し、転動造粒によって成型し、篩分けによって1.7mmφの予備成型体を得た。成型後の予備成型体の水分量(900℃焼成時のig−loss換算)は38重量部であった。当該成型体に成型に用いたものと同じ産地のカオリン粘土を予備成型体の固形分100重量部に対して3重量部添加し、噴霧器によって成型体含有水分を39重量部に調整し、引き続き70分間転動整粒した。その後、乾燥し、680℃で5時間焼成した。
Example 3
43 parts by weight of kaolin clay is mixed with 100 parts by weight of zeolite (K ion exchange A-type zeolite), and then 55 parts by weight of water is mixed with 100 parts by weight of zeolite and kaolin clay. Molded and sieved to obtain a 1.7 mmφ preform. The water content of the pre-molded body after molding (ig-loss conversion at 900 ° C. firing) was 38 parts by weight. 3 parts by weight of kaolin clay from the same production area as that used for molding is added to the molded body in an amount of 100 parts by weight of the solid content of the preform, and the moisture content of the molded body is adjusted to 39 parts by weight with a sprayer. Rolled and sized for a minute. Then, it dried and baked at 680 degreeC for 5 hours.

得られたビーズ成型体の特性を表1に示した。   The properties of the obtained bead molded body are shown in Table 1.

比較例1
実施例1の予備成型体を転動整粒しないで実施例1と同様の処理を行った。
Comparative Example 1
The same process as in Example 1 was performed without rolling and sizing the preformed body of Example 1.

得られたビーズ成型体の特性を表1に、成型体断面(表面)を図3に示した。表面に凹凸が多く、水和耐圧強度、耐磨耗性いずれも不十分な成型体であった。   The characteristics of the obtained bead molded body are shown in Table 1, and the cross section (surface) of the molded body is shown in FIG. It was a molded product with many irregularities on the surface and insufficient hydration pressure strength and abrasion resistance.

比較例2
転動整粒時に添加する粘土バインダーを7重量部とした以外は、実施例1と同様の処理を行った。
Comparative Example 2
The same treatment as in Example 1 was performed except that 7 parts by weight of the clay binder added at the time of rolling sizing was used.

得られたビーズ成型体の特性を表1に示した。整粒時に添加する粘土バインダーが多いため、強度は向上したが、磨耗率の大きな成型体であった。成型体の表面には整粒時に形成された保護層形成が認められたが、バインダー単独の厚い層であり、成型体内部との構造の違いが顕著であった。   The properties of the obtained bead molded body are shown in Table 1. Since the clay binder added during sizing was large, the strength was improved, but the molded product had a large wear rate. The formation of a protective layer formed during sizing was observed on the surface of the molded body, but it was a thick layer of a binder alone, and the difference in structure from the inside of the molded body was remarkable.

比較例3
転動整粒時に添加する粘土バインダーを5重量部とした以外は、実施例1と同様の処理を行った。
Comparative Example 3
The same treatment as in Example 1 was performed except that 5 parts by weight of the clay binder added at the time of rolling sizing was used.

得られたビーズ成型体の特性を表1、成型体断面(表面)を図4に示した。比較例2に比べ磨耗率は改善されたが、十分ではなかった。転動整粒後の成型体表面を図3に示す。   Table 1 shows the characteristics of the obtained bead molded body, and FIG. 4 shows the cross section (surface) of the molded body. Although the wear rate was improved as compared with Comparative Example 2, it was not sufficient. The surface of the molded body after rolling sizing is shown in FIG.

本発明は、高強度で、特に耐摩耗性の高いゼオライトビーズ成型体及びその製造方法に関するものである。例えば、高い強度及び耐磨耗性が要求される自動車のエアコン用のフロン乾燥剤に利用することができる。   The present invention relates to a zeolite bead molded body having high strength and particularly high wear resistance, and a method for producing the same. For example, it can be used as a chlorofluorocarbon desiccant for automobile air conditioners that require high strength and wear resistance.

Figure 2010132530
Figure 2010132530

Claims (10)

ゼオライトと粘土バインダー合わせて100重量部に対し、水分35重量部以上の組成物転動造粒によりビーズ状に成型した後、前記成型体固形分重量(水分除く)に対して4重量部以下の粘土バインダーを添加して転動整粒し、乾燥、焼成するゼオライトビーズ成型体の製造法。 After 100 parts by weight of zeolite and clay binder are molded into beads by composition rolling granulation with a water content of 35 parts by weight or more, 4 parts by weight or less with respect to the solid weight of the molded body (excluding water) A method for producing a zeolite bead molded body in which a clay binder is added, rolling and sized, dried and fired. 転動整粒時の成型体中の水分を35重量部以上とする請求項1に記載の製造方法。 The manufacturing method of Claim 1 which makes the water | moisture content in the molded object at the time of rolling sizing 35 weight part or more. 粘土バインダーが板状結晶である請求項1又は2に記載の製造方法。 The production method according to claim 1 or 2, wherein the clay binder is a plate-like crystal. ゼオライトがKイオン交換型A型ゼオライトである請求項1乃至3のいずれかに記載の製造方法。 The production method according to any one of claims 1 to 3, wherein the zeolite is K ion exchange type A zeolite. ゼオライト結晶径が5μm以下である請求項4に記載の製造方法。 The production method according to claim 4, wherein the zeolite crystal diameter is 5 μm or less. ゼオライトビーズ成型体のゼオライトに対する粘土バインダーの総計が10重量部以上50重量部以下である請求項1乃至5のいずれかに記載の製造方法。 The manufacturing method according to any one of claims 1 to 5, wherein the total amount of the clay binder with respect to the zeolite in the zeolite bead molded body is 10 parts by weight or more and 50 parts by weight or less. ゼオライトに対する粘土バインダーの総計が40重量部を超え50重量部以下である請求項6に記載の製造方法。 The manufacturing method according to claim 6, wherein the total amount of the clay binder with respect to the zeolite is more than 40 parts by weight and 50 parts by weight or less. ゼオライト結晶が5μm以下、粘土バインダーが10重量部以上50重量部以下、水和耐圧強度35N以上、耐磨耗率が1.5%以下、ビーズ径が1.0〜3.0mmであるゼオライトビーズ成型体。 Zeolite beads having a zeolite crystal of 5 μm or less, a clay binder of 10 to 50 parts by weight, a hydration pressure strength of 35 N or more, an abrasion resistance of 1.5% or less, and a bead diameter of 1.0 to 3.0 mm Molded body. 粘土バインダーの総計が40重量部を超え50重量部以下である請求項8に記載のゼオライトビーズ成型体。 The zeolite bead molding according to claim 8, wherein the total amount of the clay binder is more than 40 parts by weight and 50 parts by weight or less. 水和耐圧強度が70N以上である請求項8又は請求項9に記載のゼオライトビーズ成型体。 The zeolite bead molded product according to claim 8 or 9, wherein the hydration pressure strength is 70 N or more.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08173799A (en) * 1994-10-28 1996-07-09 Tosoh Corp Desiccating agent and manufacture and use thereof
JPH1087322A (en) * 1996-09-13 1998-04-07 Tosoh Corp High strength and low wear zeolite granule, its production and adsorption separation method using same
JPH11314913A (en) * 1998-05-07 1999-11-16 Tosoh Corp High strength low wear zeolite granule and its production
JP2001226167A (en) * 1999-12-07 2001-08-21 Tosoh Corp Zeolite formed bead, production process of the same and adsorption/removal process using the same
JP2003002636A (en) * 2001-06-19 2003-01-08 Tosoh Corp Binder-less zeolite bead molding, manufacturing method for the same, and adsorbing and removing method using the same
JP2004123411A (en) * 2002-09-30 2004-04-22 Catalysts & Chem Ind Co Ltd Method for manufacturing zeolite microspheric formed body

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1080209A (en) * 1992-06-13 1994-01-05 唐山市华兴实业公司 Deodorant drier and manufacturing process thereof
DE19959957A1 (en) * 1999-12-13 2001-06-21 Sued Chemie Ag Platelet-shaped compacts
CN1190264C (en) * 2002-07-10 2005-02-23 上海化工研究院 Method for preparing massive dryer for refrigeration system
CN1219594C (en) * 2003-10-28 2005-09-21 许盛英 Natural desiccant and producing process thereof
CN1559665A (en) * 2004-03-09 2005-01-05 杜建中 Concave-convex rod clay composite drying agent
CN101195079A (en) * 2006-12-08 2008-06-11 刘昂峰 Hollow glass drying agent and method for producing the same

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08173799A (en) * 1994-10-28 1996-07-09 Tosoh Corp Desiccating agent and manufacture and use thereof
JPH1087322A (en) * 1996-09-13 1998-04-07 Tosoh Corp High strength and low wear zeolite granule, its production and adsorption separation method using same
JPH11314913A (en) * 1998-05-07 1999-11-16 Tosoh Corp High strength low wear zeolite granule and its production
JP2001226167A (en) * 1999-12-07 2001-08-21 Tosoh Corp Zeolite formed bead, production process of the same and adsorption/removal process using the same
JP2003002636A (en) * 2001-06-19 2003-01-08 Tosoh Corp Binder-less zeolite bead molding, manufacturing method for the same, and adsorbing and removing method using the same
JP2004123411A (en) * 2002-09-30 2004-04-22 Catalysts & Chem Ind Co Ltd Method for manufacturing zeolite microspheric formed body

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TW201033125A (en) 2010-09-16
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CN102177093A (en) 2011-09-07
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