JPS6319216B2 - - Google Patents
Info
- Publication number
- JPS6319216B2 JPS6319216B2 JP7559482A JP7559482A JPS6319216B2 JP S6319216 B2 JPS6319216 B2 JP S6319216B2 JP 7559482 A JP7559482 A JP 7559482A JP 7559482 A JP7559482 A JP 7559482A JP S6319216 B2 JPS6319216 B2 JP S6319216B2
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- cement
- water
- humidity
- curing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003463 adsorbent Substances 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 239000011398 Portland cement Substances 0.000 claims description 13
- 239000011230 binding agent Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 239000008188 pellet Substances 0.000 claims description 6
- 239000011324 bead Substances 0.000 claims description 5
- 229920006395 saturated elastomer Polymers 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 2
- 239000004568 cement Substances 0.000 description 30
- 239000000203 mixture Substances 0.000 description 12
- 238000001179 sorption measurement Methods 0.000 description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 7
- 239000010457 zeolite Substances 0.000 description 7
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000007791 dehumidification Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 241001494479 Pecora Species 0.000 description 1
- 240000007643 Phytolacca americana Species 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011083 cement mortar Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- -1 substituent cation Chemical class 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Drying Of Gases (AREA)
Description
【発明の詳細な説明】
本発明はペレツト状またはビード状の吸着剤を
ポルトランドセメントをバインダーとして成形す
る吸着剤成形体の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an adsorbent molded article by molding a pellet-like or bead-like adsorbent using Portland cement as a binder.
本発明はペレツト状またはビード状の吸着剤に
バインダーを加えて成形するカートリツジ型吸着
剤の製造方法に関するものである。 The present invention relates to a method for producing a cartridge-type adsorbent, which is formed by adding a binder to a pellet-like or bead-like adsorbent.
吸着剤の利用分野の1つに空気中の水分を吸着
除去する除湿剤としての利用がある。吸着剤によ
る除湿操作は歴史的にも古く、シリカゲル、アル
ミナゲルなどが、その表面の多孔性と水に対する
親和性により、それぞれの性能に応じて広く利用
されてきた。又、1954年リンデ社が発表した合成
ゼオライトは、その水蒸気特性と吸湿特性によつ
て新しいタイプの吸湿剤として注目されてきた。
吸湿剤として用いられる合成ゼオライトは主とし
てA型ゼオライトであり、置換カチオンにより細
孔径を異にし、NaAは約4Å、KAは約3Å、
CaAは約5Åの細孔径をもつている。フオージ
ヤサイトに属する合成ゼオライトXも、10Å前後
の細孔径を有し、吸湿剤として利用されるが、こ
の場合には共吸着により、水分と共に他の不純物
を同時に吸着する効果をねらつて利用される。ゼ
オライトXにもNaX(13X)、CaX(10X)の置換
型がある。 One of the fields of use of adsorbents is as a dehumidifier that adsorbs and removes moisture from the air. Dehumidification operations using adsorbents have a long history, and silica gel, alumina gel, etc. have been widely used depending on their performance due to their surface porosity and affinity for water. Synthetic zeolite, introduced by Linde in 1954, has attracted attention as a new type of moisture absorbent due to its water vapor and moisture absorption properties.
Synthetic zeolites used as moisture absorbers are mainly A-type zeolites, and the pore diameters differ depending on the substituent cation; NaA is approximately 4 Å, KA is approximately 3 Å,
CaA has a pore diameter of about 5 Å. Synthetic zeolite Ru. Zeolite X also has substitution types, NaX (13X) and CaX (10X).
これらの吸着剤は元来粉末状であり、吸湿剤と
して吸着塔に充填するために、不活性物質をバイ
ンダーとして成形され、多くはペレツト状あるい
はビード状成形品として用いられている。 These adsorbents are originally in powder form, and are molded using an inert material as a binder in order to be filled into an adsorption tower as a moisture absorbent, and are often used in the form of pellets or beads.
第1図に示す単塔式の除湿装置は、車輌等のエ
アブレーキ、計装空気源、スプレーガンなどの加
圧空気源に使用されるもので吸着剤としてはアル
ミナゲル、モレキユラーシープ等が内側の吸着層
2に充填されている。コンプレツサー1からの湿
潤空気は吸着層2を通過し除湿されて乾燥空気と
して元空気溜め4に、一部は再生空気溜め3に、
それぞれ送られる。圧力計12により検出された
圧力が設定値(6〜8Kg/cm2)の上限に近づく
と、圧力調節計13からの信号によりコンプレツ
サー1が停止する。それと同時に圧力調節計13
からの信号により装置内の加圧空気は排気装置1
0を通り大気に開放され、再生空気溜め3から逆
流した乾燥空気が吸着層2を流れて再生脱離が行
なわれる。再生空気溜め3の空気が消費されつく
すと再生が完了する。元空気溜め4の乾燥空気の
圧力が消費によつて低下し、設定圧の下限に至る
と圧力調節計13からの信号によりコンプレツサ
ー1が作動開始する。コンプレツサー1の作動開
始と同時に装置は密封されて、加圧下での吸着操
作が開始され、乾燥空気が元空気溜め4へ送られ
る。この時1部の乾燥空気は再生空気溜め3に充
填される。第1図中5,6,7,8は弁、9はオ
リフイス、11は加圧乾燥空気を使用する装置に
連通する管路である。 The single-column dehumidifier shown in Figure 1 is used for pressurized air sources such as air brakes of vehicles, instrumentation air sources, and spray guns.The adsorbent used is alumina gel, molecular sheep, etc. is filled in the inner adsorption layer 2. The humid air from the compressor 1 passes through the adsorption layer 2, is dehumidified, and is sent to the source air reservoir 4 as dry air, and a portion is sent to the regenerated air reservoir 3.
each will be sent. When the pressure detected by the pressure gauge 12 approaches the upper limit of the set value (6 to 8 kg/cm 2 ), the compressor 1 is stopped by a signal from the pressure regulator 13. At the same time, pressure regulator 13
The pressurized air inside the device is pumped out by the signal from the exhaust device 1.
0 and is exposed to the atmosphere, and dry air flowing back from the regeneration air reservoir 3 flows through the adsorption layer 2 to perform regeneration and desorption. When the air in the regeneration air reservoir 3 is completely consumed, the regeneration is completed. When the pressure of the dry air in the source air reservoir 4 decreases due to consumption and reaches the lower limit of the set pressure, the compressor 1 starts operating in response to a signal from the pressure regulator 13. Simultaneously with the start of operation of the compressor 1, the device is sealed, adsorption operation under pressure is started, and dry air is sent to the source air reservoir 4. At this time, a portion of the dry air is filled into the regeneration air reservoir 3. In FIG. 1, 5, 6, 7, and 8 are valves, 9 is an orifice, and 11 is a conduit communicating with a device that uses pressurized dry air.
しかしながら、このような除湿装置を例えば車
輌用に使用する場合には、使用中吸着層部分が振
動し、前記のようにペレツトあるいはビード状の
吸着剤を充填したのでは吸着剤が粉化してしまう
恐れがある。そこでこの種吸着剤の多くはペレツ
トまたはビード状の吸着剤にセメントや粘土など
のバインダーを加えて例えば円柱状に成形したも
のを、専用のカートリツジ容器に納めてカートリ
ツジタイプで使用される。 However, when such a dehumidifying device is used for a vehicle, for example, the adsorption layer vibrates during use, and if it is filled with pellet or bead-shaped adsorbent as described above, the adsorbent will powder. There is a fear. Therefore, most of this type of adsorbent is used in a cartridge type by adding a binder such as cement or clay to a pellet or bead-shaped adsorbent and forming it into, for example, a cylindrical shape and storing it in a special cartridge container.
ポルトランドセメントを吸着剤成形品のバイン
ダーとして使用することは簡便な方法であり又、
バインダーとしてのセメントも簡単にかつ非常に
安価に入手できるなど多くの長所があるが、従来
の成形体はセメントが水和により硬化し強度を有
するようになるためには、長時間の養生を必要と
する欠点があつた。 Using Portland cement as a binder for adsorbent molded products is a simple method, and
Cement as a binder has many advantages, such as being easily available and very inexpensive, but conventional compacts require long curing in order for the cement to harden through hydration and gain strength. There were some drawbacks.
本発明の発明者等は上記欠点を改良した吸着剤
成形体の製造法を見出すべく鋭意研究を実施した
結果、蒸気養生を行うことによつて早期に強度を
発現できる吸着剤成形体の製造方法を見出した。 The inventors of the present invention conducted intensive research to find a method for manufacturing an adsorbent molded body that improves the above-mentioned drawbacks, and as a result, they found a method for manufacturing an adsorbent molded body that can quickly develop strength by steam curing. I found out.
すなわち本発明は、ペレツト状またはビード状
の吸着剤をポルトランドセメントをバインダーと
して成形する吸着剤成形体の製造方法において、
前記ペレツト状またはビード状の吸着剤を飽和状
態まで吸水させ、しかる後にフロー値150〜280の
ポルトランドセメントペーストを混合し、形枠に
充填して成形の後、温度50〜100℃で温度と時間
の積が285度・時以上となるよう湿度90%以上の
雰囲気下で養生することによつて成形する吸着剤
成形体の製造方法を提案するものである。 That is, the present invention provides a method for producing an adsorbent molded body in which a pellet-like or bead-like adsorbent is molded using Portland cement as a binder.
The pellet-like or bead-like adsorbent is allowed to absorb water to a saturated state, and then Portland cement paste with a flow value of 150 to 280 is mixed, and after filling into a form and forming, it is heated at a temperature of 50 to 100°C for a certain period of time. This paper proposes a method for producing an adsorbent molded body, which is formed by curing in an atmosphere with a humidity of 90% or higher so that the product of 285 degrees/hour or higher.
さて、除湿用吸着剤にバインダーとしてセメン
トペーストを混合した場合、吸着剤はセメントペ
ーストの水分を吸着し、その結果混合物の湿り状
態が変動する。 Now, when cement paste is mixed as a binder with an adsorbent for dehumidification, the adsorbent adsorbs water in the cement paste, and as a result, the wet state of the mixture fluctuates.
又除湿用吸着剤は大気中に放置すれば、大気中
の水分をも吸着するから、その保管状態即ち大気
中に置かれた時間の長短や、大気の湿度などによ
つて大気中の水分の吸着量も異なり、そのために
ペーストからの水分吸着量も変化し、上記混合物
の湿り状態も異なつてくる。このように該混合物
の湿り状態を一定の範囲に制御することは非常に
困難である。その上水分吸着時には吸着熱を発生
するから、該混合物の湿り状態の制御をさらに困
難にする。 Also, if a dehumidifying adsorbent is left in the atmosphere, it will also adsorb moisture in the atmosphere, so the amount of moisture in the atmosphere will depend on its storage conditions, i.e. the length of time it is left in the atmosphere, and the humidity of the atmosphere. The amount of adsorption is also different, and therefore the amount of water adsorbed from the paste is also different, and the wet state of the mixture is also different. In this way, it is very difficult to control the wetness of the mixture within a certain range. Moreover, heat of adsorption is generated during water adsorption, making it even more difficult to control the wet state of the mixture.
このような困難さを取り除くために本発明で
は、あらかじめ吸着剤を飽和状態まで吸湿させ
る。吸湿の手段としては水中投入、一定湿度に保
たれた容器内での一定時間の放置、及び大気中へ
の長期間の放置などがあるが、簡単で確実な手段
は水中投入である。水中投入の後、網かごですく
つて水を切れば、飽和状態まで吸湿した吸着剤
(湿り吸着剤と称す)を得ることができる。 In order to eliminate such difficulties, the present invention allows the adsorbent to absorb moisture in advance to a saturated state. Methods for absorbing moisture include placing it in water, leaving it in a container kept at a constant humidity for a certain period of time, and leaving it in the atmosphere for a long period of time, but the simple and reliable method is to put it in water. After pouring into water, the water is drained by scooping in a mesh basket to obtain an adsorbent that has absorbed moisture to a saturated state (referred to as a wet adsorbent).
次に湿り吸着剤にポルトランドセメントと水を
加えて混合し、この混合物を所定形状の形枠に充
填して成形する。ポルトランドセメントの添加量
は湿り吸着剤100重量部に対し、10〜30重量部が
適している。これは成形体の強度と通気状態にお
ける圧力損失(圧損と称す)から選定したもので
ある。水の添加量は、成形性や成形体の強度を左
右する重要な因子である。 Next, Portland cement and water are added to the wet adsorbent and mixed, and this mixture is filled into a mold of a predetermined shape and molded. The appropriate amount of Portland cement to be added is 10 to 30 parts by weight per 100 parts by weight of the wet adsorbent. This was selected based on the strength of the molded body and the pressure loss (referred to as pressure loss) in the ventilated state. The amount of water added is an important factor that influences the moldability and strength of the molded product.
即ち水分量が少い場合には、成形時該混合物の
形枠内への均一な充填が困難であり、疎及び密の
部分が生じ成形体の強度の発現も悪い。逆に水分
量が多い場合には、該混合物中のセメントペース
トが流動し、成形体の下部にセメントがたまつて
しまい、この結果成形体の強度が不均一となるば
かりか、圧損が非常に大きくなつてしまう。 That is, when the moisture content is small, it is difficult to uniformly fill the mixture into the mold during molding, resulting in the formation of sparse and dense portions and poor strength development of the molded product. On the other hand, if the moisture content is high, the cement paste in the mixture will flow and cement will accumulate at the bottom of the compact, resulting in uneven strength of the compact and a significant pressure drop. It gets bigger.
従つて添加水量を適正な範囲に規定する必要が
あるが、ポルトランドセメントの粒度分布によつ
て、セメントペーストの流動性が異るため、一定
量の水分を添加した場合でも流動性に差が生じ、
その結果該混合物の成形性に影響を与える。そこ
で本発明者等は水分管理方法について鋭意研究を
重ねた結果、セメントのフロー値を150〜280に規
定することが有効であることを見出した。 Therefore, it is necessary to specify the amount of water added within an appropriate range, but the fluidity of cement paste varies depending on the particle size distribution of Portland cement, so even if a certain amount of water is added, there will be a difference in fluidity. ,
As a result, the moldability of the mixture is affected. As a result of extensive research into moisture management methods, the present inventors have found that it is effective to specify the flow value of cement at 150 to 280.
本発明におけるフロー値の規定および測定の方
法はつぎのとおりである。 The method of defining and measuring the flow value in the present invention is as follows.
フロー値の測定は、JISR5201(セメントの物理
試験方法)のセメントモルタルのフロー試験に準
拠し、フローテーブル、フローコーン、及びつき
棒は形状寸法等の仕様がJISR5201の規定に合致
するものを使用する。 The measurement of flow value is based on the cement mortar flow test of JISR5201 (Physical Test Method for Cement), and the flow table, flow cone, and rod should meet the specifications of JISR5201 in terms of shape and dimensions. .
セメントに予め秤量しておいた水を加え、よく
練り混ぜた後、乾燥した布でよくぬぐつたフロー
テーブル上の中央の位置に正しく置いたフローコ
ーンにセメントペーストを2層に詰める。 Add a pre-weighed amount of water to the cement, mix well, and then fill two layers of cement paste into a flow cone placed correctly in the center of a flow table that has been thoroughly wiped with a dry cloth.
各層は、つき棒の先端がその層の約1/2の深さ
まで入るよう、全面にわたつておのおの15回突
き、最後に不足分を補い表面をならす。 Poke each layer 15 times across the entire surface so that the tip of the stick penetrates about 1/2 the depth of that layer, and finally fill in the gaps and smooth the surface.
このようにしてセメントペーストをフローコー
ンに詰めた後、フローコーンを正しく上方に取り
去つてから該セメントペーストにJISR5201の規
定の方法で15秒間に15回落下運動を与え、セメン
トペーストがひろがつたのちの径を最大と認める
方向とこれに直角な方向とで測定し、その平均値
を、mmを単位とする整数値に丸めて、その絶体値
をフロー値とする。 After filling the cement paste into the flow cone in this way, the flow cone is correctly removed upwards, and the cement paste is subjected to a falling motion 15 times in 15 seconds using the method specified in JISR5201, until the cement paste has spread. The flow value is measured in the direction in which the flow diameter is considered to be the maximum and in the direction perpendicular to this direction, and the average value is rounded to an integer value in mm, and the absolute value is taken as the flow value.
このようにして準備されたセメントペーストと
吸着剤との混合物は、次に形枠に充填され、軽く
圧縮される。その後形枠を取付けた状態で約1日
間、室温で湿度90%以上の雰囲気下で湿空養生し
て形枠を取外し、次に温度50〜100℃、湿度90%
以上の雰囲気下で蒸気養生してセメントを早期に
固化させる。蒸気養生温度は高ければ短時間、低
ければ長時間を要し、一般には温度と時間の積で
表わすことが多い。本発明者らの実験では少くと
も285度・時、即ち例えば95℃で3時間が必要で、
好ましくは900〜2000度・時が必要である。養生
後は成形体が保有、吸着している水分を除去し賦
活するために200〜350℃で加熱し、専用ケースに
納めて固定することにより、カートリツジタイプ
の吸着体が得られる。 The mixture of cement paste and adsorbent prepared in this way is then filled into forms and lightly compacted. After that, with the form attached, it is cured in humid air at room temperature for about 1 day in an atmosphere with a humidity of 90% or more, and then the form is removed, and then the temperature is 50 to 100℃ and the humidity is 90%.
The cement is cured with steam in the above atmosphere to quickly solidify the cement. If the steam curing temperature is high, it will take a short time, and if it is low, it will take a long time, and it is generally expressed as the product of temperature and time. In the experiments conducted by the present inventors, at least 285 degrees/hour, that is, for example, 3 hours at 95 degrees Celsius, is required.
Preferably, a temperature of 900 to 2000 degrees/hour is required. After curing, the molded body is heated at 200 to 350°C in order to remove the moisture retained and adsorbed and to activate it, and is then placed in a special case and fixed to obtain a cartridge-type adsorbent.
以下本発明の作用効果を実施例により説明す
る。 The effects of the present invention will be explained below using examples.
実施例 1
粒径2mmのゼオライト4Aビードを水道水を入
れた容器に1時間浸漬し、その後、網かごに移し
て水切りを行つた。この湿り吸着剤100重量部と、
15重量部の普通ポルトランドセメントに水を加え
てフロー値200としたセメントペーストとを混合
し、内径150mmを金型に充填後、8Kg/cm2の圧力
をかけて高さ300mmとなるまで圧縮した。この物
を金型をつけたまま20℃、湿度95%の恒温恒湿室
内に1日静置後、金型を外し、種々の温度下、湿
度90〜95%で養生した。このものの圧縮強度を
JISA1108に従つて各時間毎に測定し第2図の結
果を得た。Example 1 Zeolite 4A beads with a particle size of 2 mm were immersed in a container containing tap water for 1 hour, and then transferred to a mesh basket to drain the water. 100 parts by weight of this wet adsorbent,
15 parts by weight of ordinary Portland cement was mixed with cement paste to give a flow value of 200 by adding water, and after filling a mold with an inner diameter of 150 mm, it was compressed under a pressure of 8 kg/cm 2 to a height of 300 mm. . After leaving the product with the mold attached in a constant temperature and humidity chamber at 20° C. and 95% humidity for one day, the mold was removed and the product was cured at various temperatures and humidity of 90 to 95%. The compressive strength of this thing is
Measurements were made at each hour according to JISA1108, and the results shown in Figure 2 were obtained.
第2図から95℃で3時間の養生即ち285度・時
の養生で圧縮強度は50Kg/cm2を越える。圧縮強度
の上昇がゆるやかとなるのは95℃で10時間(950
度・時)、80℃で10時間(800度・時)、50℃で18
時間(900度時)程度であり、95℃で24時間
(2280度・時)、50℃で24時間(1200度・時)も養
生すれば十分である。従つて養生条件は285度・
時以上好ましくは900度・時〜2000度・時である。 From Figure 2, the compressive strength exceeds 50 kg/cm 2 after curing at 95°C for 3 hours, that is, curing at 285°C. The increase in compressive strength becomes gradual after 10 hours at 95℃ (950℃).
degree/hour), 10 hours at 80℃ (800 degrees/hour), 18 hours at 50℃
curing at 95°C for 24 hours (2280°C/hr) or 50°C for 24 hours (1200°C/hr) is sufficient. Therefore, the curing conditions are 285 degrees.
The temperature is preferably 900 degrees/hour to 2000 degrees/hour.
また第2図から40℃以下では早期に高い強度が
得られないことが明らかである。同様に養生温度
は高い程強度が高いが、100℃を越えると加圧状
態での養生となるのが難点である。 Furthermore, from Fig. 2, it is clear that high strength cannot be obtained at an early stage at temperatures below 40°C. Similarly, the higher the curing temperature, the higher the strength, but the problem is that if the temperature exceeds 100°C, curing will be under pressure.
実施例 2
粒径2mmのゼオライト4Aビードを水道水を入
れた容器に1時間浸漬し、その後、網かごに移し
て水切りを行つた。この湿り吸着剤100重量部と、
15重量部の普通ポルトランドセメントに水を加え
て、所定のフロー値としたセメントペーストとを
混合し、内径150mmの金型に充填後8Kg/cm2の圧
力をかけて高さ300mmとなるまで圧縮した。この
物を金型を付けたまま20℃、湿度95%の恒温、恒
湿室内に1日静置後、金型を外し、更に60℃、90
〜95%湿度下で24時間蒸気養生を行つた。Example 2 Zeolite 4A beads with a particle size of 2 mm were immersed in a container containing tap water for 1 hour, and then transferred to a mesh basket to drain the water. 100 parts by weight of this wet adsorbent,
Add water to 15 parts by weight of ordinary Portland cement, mix with cement paste to the specified flow value, fill it into a mold with an inner diameter of 150 mm, and compress it under a pressure of 8 kg/cm 2 until it reaches a height of 300 mm. did. After leaving this item with the mold attached in a constant temperature and humidity room at 20℃ and 95% humidity for one day, remove the mold and further heat at 60℃ and 95% humidity.
Steam curing was performed for 24 hours under ~95% humidity.
蒸気養生後の成形体につきJISA1108に従つて
圧縮強度を測定した。フロー値と圧縮強度の関係
は第3図に示すとうりである。第3図において横
軸はフロー値、縦軸は圧縮強度を示す。 The compressive strength of the molded product after steam curing was measured according to JISA1108. The relationship between flow value and compressive strength is as shown in FIG. In FIG. 3, the horizontal axis shows the flow value and the vertical axis shows the compressive strength.
第3図から好ましいフロー値の範囲は150〜280
である。 From Figure 3, the preferred flow value range is 150 to 280.
It is.
実施例 3
実施例1と同様にして、湿り吸着剤100重量部
と、所定量の普通ポルトランドセメントに水を加
えてフロー値200としたセメントペーストとを混
合した後圧縮し直径150mm、高さ300mmの円柱状成
形体を得、実施例2と同様に1日湿空養生後金型
を外し60℃、湿度90〜95%の雰囲気で24時間蒸気
養生を行つた後前記JISA1108により圧縮強度を
測定した。セメント添加量と圧縮強度の関係は第
4図に示すとうりで、セメント添加量は10%以上
が好ましい。Example 3 In the same manner as in Example 1, 100 parts by weight of wet adsorbent and cement paste made by adding water to a predetermined amount of ordinary Portland cement to give a flow value of 200 were mixed and then compressed to form a mixture with a diameter of 150 mm and a height of 300 mm. A cylindrical molded body was obtained, and after curing in humid air for 1 day in the same manner as in Example 2, the mold was removed and steam curing was performed for 24 hours in an atmosphere of 60°C and humidity of 90 to 95%, and the compressive strength was measured according to JISA1108 mentioned above. did. The relationship between the amount of cement added and the compressive strength is shown in Figure 4, and the amount of cement added is preferably 10% or more.
実施例 4
実施例3と同様にして得られた成形体350℃で
1時間焼成して脱水した後、この物の通気圧力損
失を測定した。通気の方向は円柱の上下方向であ
り、円周方向からのガスリークがないよう側面は
シールした。使用ガスは窒素とし窒素ボンベから
6.5Kg/cm2の圧力で供給し、流量を200N/min
とした。セメント添加量と圧力損失との関係を第
5図に示す。Example 4 A molded article obtained in the same manner as in Example 3 was fired at 350° C. for 1 hour to dehydrate it, and then the ventilation pressure loss of this article was measured. The direction of ventilation was in the vertical direction of the cylinder, and the sides were sealed to prevent gas leakage from the circumferential direction. The gas used is nitrogen and comes from a nitrogen cylinder.
Supplied at a pressure of 6.5Kg/cm 2 and a flow rate of 200N/min
And so. Figure 5 shows the relationship between the amount of cement added and pressure loss.
セメント添加量が30%(湿り吸着剤100重量部
に対しセメント30重量部)を超えると圧力損失が
大となり好ましくない。 If the amount of cement added exceeds 30% (30 parts by weight of cement per 100 parts by weight of wet adsorbent), the pressure loss will increase, which is not preferable.
実施例 5
直径1.5mmで長さ3mmのゼオライト4Aペレツト
を水道水に入れた容器に1時間浸漬し、その後、
網かごに移して水切りを行つた。実施例1と同様
にこの湿り吸着剤100重量部と、15重量部の普通
ポルトランドセメントに水を加えてフロー値200
としたセメントペーストとを混合した後、圧縮
し、直径150mm、高さ300mmの円柱状成形体を得、
実施例2と同様に1日間の湿空養生後、金型を外
し60℃、湿度90〜95%雰囲気での24時間の蒸気養
生を行い、JISA1108により圧縮強度を測定した
ところ63Kg/cm2まで良好な結果が得られた。Example 5 Zeolite 4A pellets with a diameter of 1.5 mm and a length of 3 mm were soaked in a container of tap water for 1 hour, and then
I transferred it to a mesh basket and drained it. As in Example 1, water was added to 100 parts by weight of this wet adsorbent and 15 parts by weight of ordinary Portland cement to obtain a flow value of 200.
After mixing with cement paste, it was compressed to obtain a cylindrical molded body with a diameter of 150 mm and a height of 300 mm.
After curing in a humid air for 1 day in the same manner as in Example 2, the mold was removed and steam curing was performed for 24 hours at 60°C and a humidity of 90 to 95%.The compressive strength was measured according to JISA1108 and reached 63Kg/ cm2. Good results were obtained.
第1図はカートリツジ型吸着体を用いた除湿装
置の例示図、第2図は吸着剤成形体の養生時間と
圧縮強度との関係を示す説明図、第3図はセメン
トペーストのフロー値と吸着剤成形体の圧縮強度
との関係を示す説明図、第4図は吸着剤成形体の
セメント添加量と圧縮強度との関係を示す説明
図、第5図は吸着剤成形体のセメント添加量と圧
力損失との関係を示す説明図である。
Figure 1 is an illustration of a dehumidifying device using a cartridge-type adsorbent, Figure 2 is an explanatory diagram showing the relationship between curing time and compressive strength of an adsorbent molded body, and Figure 3 is an illustration of the flow value and adsorption of cement paste. An explanatory diagram showing the relationship between the compressive strength of the adsorbent molded body, Figure 4 is an explanatory diagram showing the relationship between the amount of cement added and the compressive strength of the adsorbent molded body, and Figure 5 is an explanatory diagram showing the relationship between the amount of cement added and the compressive strength of the adsorbent molded body. FIG. 3 is an explanatory diagram showing the relationship with pressure loss.
Claims (1)
ランドセメントをバインダーとして成形する吸着
剤成形体の製造方法において前記ペレツト状また
はビード状の吸着剤を飽和状態まで吸水させ、し
かる後にフロー値150〜280のポルトランドセメン
トペーストを混合し、形枠に充填して圧縮後、温
度50〜100℃で温度と時間の積が285度・時以上と
なるよう湿度90%以上の雰囲気下で養生すること
を特徴とする吸着剤成形体の製造方法。1. In a method for manufacturing an adsorbent molded body, in which adsorbent in the form of pellets or beads is molded using portland cement as a binder, the adsorbent in the form of pellets or beads is made to absorb water to a saturated state, and then the adsorbent is molded with portland cement having a flow value of 150 to 280. After mixing the paste and filling it into a form and compressing it, it is cured in an atmosphere with a humidity of 90% or more so that the product of temperature and time is 285 degrees / hours or more at a temperature of 50 to 100 degrees Celsius. A method for producing an adsorbent molded body.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7559482A JPS58193730A (en) | 1982-05-06 | 1982-05-06 | Production of adsorbent molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7559482A JPS58193730A (en) | 1982-05-06 | 1982-05-06 | Production of adsorbent molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58193730A JPS58193730A (en) | 1983-11-11 |
JPS6319216B2 true JPS6319216B2 (en) | 1988-04-21 |
Family
ID=13580673
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7559482A Granted JPS58193730A (en) | 1982-05-06 | 1982-05-06 | Production of adsorbent molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58193730A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63195227U (en) * | 1987-06-04 | 1988-12-15 | ||
JPH0444797U (en) * | 1990-07-25 | 1992-04-16 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9416975D0 (en) * | 1994-08-23 | 1994-10-12 | South Bank Univ Entpr Ltd | Air moving system |
-
1982
- 1982-05-06 JP JP7559482A patent/JPS58193730A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63195227U (en) * | 1987-06-04 | 1988-12-15 | ||
JPH0444797U (en) * | 1990-07-25 | 1992-04-16 |
Also Published As
Publication number | Publication date |
---|---|
JPS58193730A (en) | 1983-11-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11707729B2 (en) | Self-supporting structures having active materials | |
CN101531364B (en) | A kind of spherical activated carbon and its preparation method | |
Wang et al. | Experimental research of composite solid sorbents for fresh water production driven by solar energy | |
US2933455A (en) | Adsorbent briquets for combined odor and moisture removal | |
US4061807A (en) | Adsorbent body and method for making same | |
ZA200405401B (en) | Adsorbing material comprised of porous functional solid incorporated in a polymer matrix. | |
US20140239225A1 (en) | Water-Selective Adsorbent and Method for Producing Same | |
US2423702A (en) | Molded block of activated carbon in a porous casing of fireproofed carbon | |
JP2002355512A (en) | Method for manufacturing filter medium | |
US5427751A (en) | Method for using high capacity unsupported regenerable CO2 sorbent | |
US3234147A (en) | Hardened molecular sieve agglomerates and manufacture thereof | |
CN104492373A (en) | Diatomite-based composite porous ceramic material for adsorbing volatile organic pollutant and preparation method thereof | |
JPS6319216B2 (en) | ||
CA1079706A (en) | Gas-adsorbent propellant system | |
JP2005500155A (en) | Desiccant based on zeolite combined with clay, process for its production and use thereof | |
JPH0244579B2 (en) | ||
JPH08224468A (en) | Cylindrically pelletized carbon based adsorbent | |
Weber et al. | Adsorption equilibrium of light mercaptans on faujasites | |
JP2015509832A (en) | Desiccant-supporting honeycomb chemical filter and manufacturing method thereof | |
US3116131A (en) | Method and materials for disposing of radioactive waste | |
JPH0710330B2 (en) | Dry dehumidifier | |
US3917544A (en) | Agglomerated adsorbent products of molecular sieve grains | |
JPS63116727A (en) | Dry dehumidifying material | |
CN101327423A (en) | Spherical Granular Composite Material Containing Activated Carbon and Its Preparation Process | |
WO2016031474A1 (en) | Adsorbent |