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JP2003012380A - Method for producing water-repellent lightweight cellular concrete - Google Patents

Method for producing water-repellent lightweight cellular concrete

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Publication number
JP2003012380A
JP2003012380A JP2001194676A JP2001194676A JP2003012380A JP 2003012380 A JP2003012380 A JP 2003012380A JP 2001194676 A JP2001194676 A JP 2001194676A JP 2001194676 A JP2001194676 A JP 2001194676A JP 2003012380 A JP2003012380 A JP 2003012380A
Authority
JP
Japan
Prior art keywords
gas
cellular concrete
water
pressure
lightweight cellular
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001194676A
Other languages
Japanese (ja)
Other versions
JP4689091B2 (en
Inventor
Kensuke Aoki
謙介 青木
Shinya Okazaki
慎也 岡崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Kasei Corp filed Critical Asahi Kasei Corp
Priority to JP2001194676A priority Critical patent/JP4689091B2/en
Publication of JP2003012380A publication Critical patent/JP2003012380A/en
Application granted granted Critical
Publication of JP4689091B2 publication Critical patent/JP4689091B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【課題】 軽量気泡コンクリートの外表面および内部空
隙表面にアルキルアルコキシシランからなる撥水層を形
成した撥水性の軽量気泡コンクリートの製造方法を提供
すること。 【解決手段】 アルキルアルコキシシラン蒸気を軽量気
泡コンクリートに接触させて、撥水性軽量気泡コンクリ
ートを製造する方法において、アルキルアルコキシシラ
ン蒸気とキャリアガスの混合ガスを用い、ガス溜め容器
の混合ガスを、撥水層を形成しようとする軽量気泡コン
クリートが配置された反応容器内に、ガス圧力差によっ
て流入させる工程を少なくとも2回行う、撥水性の軽量
気泡コンクリートの製造方法。
(57) To provide a method for producing water-repellent lightweight cellular concrete in which a water-repellent layer made of alkylalkoxysilane is formed on the outer surface and inner void surface of lightweight cellular concrete. SOLUTION: In a method for producing water-repellent lightweight cellular concrete by bringing alkylalkoxysilane vapor into contact with lightweight cellular concrete, a mixed gas of alkylalkoxysilane vapor and carrier gas is used, and the mixed gas in a gas reservoir is repelled. A method for producing water-repellent lightweight aerated concrete, wherein the step of allowing a lightweight aerated concrete to be formed into a water layer to flow into a reaction vessel by a gas pressure difference is performed at least twice.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、建築材料として好
適に利用される、外表面および内部空隙表面に撥水層を
有する撥水性軽量気泡コンクリートの製造方法に関す
る。
TECHNICAL FIELD The present invention relates to a method for producing a water-repellent lightweight cellular concrete having a water-repellent layer on the outer surface and the inner void surface, which is preferably used as a building material.

【0002】[0002]

【従来の技術】軽量気泡コンクリートは、軽量かつ断熱
性に優れるため、建築材料として、ビルおよび住宅の外
壁材、床材、間仕切り材、天井材、屋根材等に広く使用
されている。しかしながら、多孔質体であるがゆえ、そ
の空隙内に水分を含み易く、過剰に吸水すると、断熱性
や強度が低下したり、寒冷地においては凍害の発生原因
になる等の問題がある。このことから、その施工にあた
っては、たとえば十分な防水効果が得られる塗装を施し
たり、撥水性のコーティング材を塗布したりする等、吸
水性が高い材料であることを十分考慮した設計が必須と
なっている。
2. Description of the Related Art Light weight cellular concrete is widely used as a building material for outer wall materials, floor materials, partition materials, ceiling materials, roofing materials and the like of buildings and houses because of its light weight and excellent heat insulating property. However, since it is a porous body, it easily contains water in its voids, and if it absorbs excessive water, there are problems that the heat insulating property and strength are deteriorated, and it causes frost damage in cold regions. For this reason, it is essential to design the product in consideration of its high water-absorption property, for example, by applying a coating that provides a sufficient waterproof effect or by applying a water-repellent coating material. Has become.

【0003】建築用軽量気泡コンクリートの吸水を防止
する方法としては、一般的には材料表面を塗装すること
が行われているが、軽量気泡コンクリートは多孔体であ
るために、その表面および切断面には内部空隙が露出す
ることによる凸凹が多く、塗装による防水効果を確実と
するためには、平滑面を有する材料よりも多くの塗料を
塗布することが必要である。また、現場における塗装に
おいては、温度や湿度などの塗装条件が物件によって異
なることもあり、ピンホールなどの発生を抑えた高品質
の塗装を行うことが難しいため、必要塗布量はさらに多
くなる傾向がある。
As a method of preventing water absorption of lightweight cellular concrete for construction, coating of the material surface is generally performed. However, since lightweight cellular concrete is a porous body, its surface and cut surface are Since there are many irregularities due to the exposure of internal voids, it is necessary to apply more paint than a material having a smooth surface in order to ensure the waterproof effect of painting. Also, when painting on-site, the coating conditions such as temperature and humidity may vary depending on the property, and it is difficult to perform high-quality painting with pinholes, etc. There is.

【0004】塗装条件が最適化された工場において塗装
を行った材料については、塗料量を必要以上に多くしな
くとも十分な防水性能を確保することも可能であるが、
建築材料は現場で切断加工する場合等も多いため、切断
面の防水性についてはやはり現場での塗装等に頼る必要
がある。このように、塗装によって多孔質系材料の吸水
を完全に防止するには、多量の塗料を用いる必要がある
ことからコスト高になるばかりでなく、ひび割れ等が発
生し易くなるという問題もある。
It is possible to secure sufficient waterproof performance for a material coated in a factory where the coating conditions are optimized, without increasing the amount of coating more than necessary.
Since building materials are often cut and processed on-site, it is necessary to rely on painting on the site for waterproofness of cut surfaces. As described above, in order to completely prevent the water absorption of the porous material by coating, it is necessary to use a large amount of coating material, so that not only the cost becomes high, but also cracks and the like are likely to occur.

【0005】そこで、軽量気泡コンクリートの吸水速度
を低減する方法として、特開昭58−55359号公
報、特開平3−54175号公報において、軽量気泡コ
ンクリート製造工程の原料スラリーにポリジメチルシロ
キサンを添加する方法が提案されている。しかしなが
ら、該方法においては、ポリジメチルシロキサンは原料
段階でスラリーに混入されるため、製造時の反応などに
も影響し、あまり多量には混入できない。従って、この
ような方法では、軽量気泡コンクリートの吸水し易いと
いう問題をある程度解決することはできるが、本質的に
吸水を防止するには至らず、防水のためには依然、高品
質の塗装が必要であった。
Therefore, as a method for reducing the water absorption rate of lightweight cellular concrete, in JP-A-58-55359 and JP-A-3-54175, polydimethylsiloxane is added to the raw material slurry in the lightweight cellular concrete manufacturing process. A method has been proposed. However, in this method, since polydimethylsiloxane is mixed in the slurry at the raw material stage, it affects the reaction at the time of production and cannot be mixed in too much. Therefore, although such a method can solve the problem that the lightweight cellular concrete easily absorbs water, it does not essentially prevent the absorption of water, and for waterproofing, high-quality painting is still required. Was needed.

【0006】また、特開平6−271371号公報にお
いて、軽量気泡コンクリートを密閉容器に入れ減圧状態
にした後、アルキルアルコキシシランの蒸気を流入させ
る方法が提案されている。しかし、この方法では、軽量
気泡コンクリートの内部まで十分な撥水性を有する撥水
層は得られなかった。そこで、従来から広く使用されて
いる軽量気泡コンクリートについて、その吸水性をさら
に低下させる技術が切望されている。
Further, Japanese Patent Application Laid-Open No. 6-271371 proposes a method in which a lightweight cellular concrete is put in a closed container to be decompressed and then a vapor of alkylalkoxysilane is introduced. However, with this method, a water-repellent layer having sufficient water repellency even inside the lightweight cellular concrete could not be obtained. Therefore, there has been a strong demand for a technique for further reducing the water absorption of lightweight cellular concrete that has been widely used in the past.

【0007】[0007]

【発明が解決しようとする課題】本発明は、軽量気泡コ
ンクリートの外表面および内部空隙表面にアルキルアル
コキシシランからなる撥水層を形成した撥水性の軽量気
泡コンクリートの製造方法を提供することを目的とす
る。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing a water-repellent lightweight cellular concrete in which a water-repellent layer made of alkylalkoxysilane is formed on the outer surface and the inner void surface of the lightweight cellular concrete. And

【0008】[0008]

【課題を解決するための手段】本発明者らは、上記課題
を解決するにあたり、キャリアガスを使用し、ガス溜め
容器内の混合ガスを反応容器内に繰り返して送り込むこ
とにより効果的に外表面および任意の切断面において撥
水性を示す撥水性の軽量気泡コンクリートが得られるこ
とを見出し、本発明を完成するに至った。即ち、本発明
は、[1] アルキルアルコキシシラン蒸気を軽量気泡
コンクリートに接触させて、撥水性軽量気泡コンクリー
トを製造する方法において、撥水層を形成しようとする
軽量気泡コンクリートを反応容器内に配置した後に、ガ
ス溜め容器中のアルキルアルコキシシラン蒸気とキャリ
アガスの混合ガスの圧力が反応容器の圧力よりも高い状
態で、ガス溜め容器と反応容器とを遮断しているガス開
閉手段を開き、ガス溜め容器の混合ガスをその圧力差に
よって、撥水層を形成しようとする軽量気泡コンクリー
トが配置された反応容器内に流入させた後、ガス開閉手
段を閉め、ガス溜め容器内の混合ガスの圧力を、その時
点における反応容器内の圧力より高くし、再度ガス開閉
手段を開き、反応容器にガス溜め容器の混合ガスを流入
させる工程を、少なくとも一回行うことを特徴とする、
撥水性の軽量気泡コンクリートの製造方法、[2] ア
ルキルアルコキシシラン蒸気を軽量気泡コンクリートに
接触させて、撥水性軽量気泡コンクリートを製造する方
法において、撥水層を形成しようとする軽量気泡コンク
リートを反応容器内に配置した後に、ガス溜め容器中の
アルキルアルコキシシラン蒸気とキャリアガスの混合ガ
スの圧力が反応容器の圧力よりも高い状態で、ガス溜め
容器と反応容器とを遮断しているガス開閉手段を開き、
ガス溜め容器の混合ガスをその圧力差によって、撥水層
を形成しようとする軽量気泡コンクリートが配置された
反応容器内に流入させた後、ガス開閉手段を閉め、反応
容器を開放もしくは減圧にした後に、再度ガス開閉手段
を開き、反応容器にガス溜め容器内の混合ガスを流入さ
せる工程を、少なくとも一回行うことを特徴とする、撥
水性の軽量気泡コンクリートの製造方法、である。
In order to solve the above problems, the inventors of the present invention effectively use the carrier gas and repeatedly feed the mixed gas in the gas storage container into the reaction container to effectively form the outer surface. Further, they have found that a water-repellent lightweight cellular concrete exhibiting water repellency on any cut surface can be obtained, and have completed the present invention. That is, the present invention relates to [1] a method for producing a water-repellent lightweight cellular concrete by bringing an alkylalkoxysilane vapor into contact with the lightweight cellular concrete, wherein the lightweight cellular concrete for forming a water-repellent layer is placed in a reaction vessel. After that, when the pressure of the mixed gas of the alkylalkoxysilane vapor and the carrier gas in the gas storage container is higher than the pressure of the reaction container, open the gas opening / closing means that shuts off the gas storage container and the reaction container, The pressure of the mixed gas in the gas storage container is closed after the mixed gas in the storage container is caused to flow into the reaction container in which the lightweight cellular concrete to form the water repellent layer is placed by the pressure difference. Is higher than the pressure inside the reaction vessel at that time, the gas opening / closing means is opened again, and the mixed gas in the gas storage vessel is caused to flow into the reaction vessel. Characterized in that the step is performed at least once,
Method for producing water-repellent lightweight cellular concrete, [2] In the method for producing water-repellent lightweight cellular concrete by contacting alkylalkoxysilane vapor with lightweight cellular concrete, reacting lightweight cellular concrete to form a water-repellent layer A gas opening / closing means that shuts off the gas reservoir container and the reaction container after the gas reservoir container is placed in the container and the pressure of the mixed gas of the alkylalkoxysilane vapor and the carrier gas in the gas reservoir container is higher than the pressure of the reaction container. Open
The mixed gas in the gas storage container was caused to flow into the reaction container in which the lightweight cellular concrete to form the water-repellent layer was placed by the pressure difference, and then the gas opening / closing means was closed to open or reduce the pressure of the reaction container. After that, the step of opening the gas opening / closing means again and causing the mixed gas in the gas storage container to flow into the reaction container is carried out at least once, and a method for producing a water-repellent lightweight cellular concrete.

【0009】本発明について、以下に詳細を説明する。
本発明において撥水性を付与させる軽量気泡コンクリー
トとしては、従来一般に製造されている軽量気泡コンク
リートで良く、例えば、珪石やセメント、生石灰、石膏
などを主成分に、アルミニウム粉などの気泡剤を混合し
て、得られた原料スラリーを型枠に注入し、切断に適し
た硬度になるまで養生した後、型枠から外して半硬化状
のモルタルブロックとし、これを緊張配設したピアノ線
などの線材で切断したものをオートクレーブ養生するこ
とにより製造されるものである。
The present invention will be described in detail below.
The lightweight cellular concrete that imparts water repellency in the present invention may be a lightweight cellular concrete that is conventionally generally produced, for example, silica stone or cement, quick lime, gypsum and the like as the main component, mixed with a foaming agent such as aluminum powder. Then, the resulting raw material slurry is poured into a mold and cured to a hardness suitable for cutting, then removed from the mold to form a semi-cured mortar block, and this is a wire rod such as a piano wire with tension. It is manufactured by subjecting the one cut in step 1 to autoclave curing.

【0010】本発明において、アルキルアルコキシシラ
ンとは、nを1から3の整数として、一般式を(R1n
Si(OR24-nで表すことができる。ここで、R1
炭素数1〜18のアルキル基であり、R2はアルキル基で
あれば特に限定はされないが、最も汎用的なメチル基、
エチル基が好ましい。nが2または3の場合、R1はそ
れぞれ同じであっても異なっていても良く、また、nが
1または2の場合にはR2はそれぞれ同じであっても異な
っていても良い。
In the present invention, an alkylalkoxysilane is represented by the general formula (R 1 ) n , where n is an integer from 1 to 3.
It can be represented by Si (OR 2 ) 4-n . Here, R 1 is an alkyl group having 1 to 18 carbon atoms, and R 2 is not particularly limited as long as it is an alkyl group, the most general-purpose methyl group,
The ethyl group is preferred. When n is 2 or 3, R 1 may be the same or different, and when n is 1 or 2, R 2 may be the same or different.

【0011】本発明において、キャリアガスとは、アル
キルアルコキシシラン蒸気に混入させ、撥水性を付与し
ようとする軽量気泡コンクリートを配置する反応容器内
の圧力よりも高い圧力の混合ガスを得る目的で使用する
ものである。該キャリアガスは、アルキルアルコキシシ
ランガスと極端な反応性を有さない限り、種類は特に限
定されない。例えば、ヘリウム、アルゴン、窒素などの
純物質であっても、空気などの混合物であっても良い。
In the present invention, the carrier gas is used for the purpose of obtaining a mixed gas having a pressure higher than the pressure in the reaction vessel in which the lightweight cellular concrete for imparting water repellency is mixed with the alkylalkoxysilane vapor. To do. The type of the carrier gas is not particularly limited as long as it has no extreme reactivity with the alkylalkoxysilane gas. For example, it may be a pure substance such as helium, argon, or nitrogen, or a mixture such as air.

【0012】また、キャリアのガスの圧力は、ガス溜め
容器内の混合ガス圧力を反応容器内の圧力よりも高く
し、ガス溜め容器から反応容器への速やかなガスの流入
を行うためには、20000Pa以上が好ましく、50
000Pa以上がより好ましく、100000Pa以上
が特に好ましい。しかし、該圧力を高くするには、製造
設備に相応の耐圧性能が必要となるため、あまり高い圧
力のキャリアガスを使用することは経済的でない。本発
明においては、キャリアガスの圧力は、3000000
Pa以下が好ましく、2000000Pa以下がより好
ましく、1600000Pa以下が特に好ましい。
The pressure of the carrier gas is set so that the pressure of the mixed gas in the gas storage container is higher than the pressure in the reaction container, so that the gas can quickly flow from the gas storage container into the reaction container. 20,000 Pa or more is preferable, 50
000 Pa or more is more preferable, and 100,000 Pa or more is particularly preferable. However, in order to increase the pressure, it is not economical to use a carrier gas having a too high pressure because the manufacturing equipment needs to have appropriate pressure resistance. In the present invention, the pressure of the carrier gas is 3,000,000.
Pa or less is preferable, 2000000 Pa or less is more preferable, and 1600000 Pa or less is particularly preferable.

【0013】キャリアガスとして、アルキルアルコキシ
シランと反応性を有さないガスを利用することにより、
ガス溜め容器内におけるアルキルアルコキシシランの不
必要な加水分解、脱水縮合の進行を防ぐことができる。
本発明における製造設備は、例えば、内部のガスを排出
可能な2個の密閉容器を、開閉可能なガス開閉手段、好
ましくは開閉可能なバルブを介して接続したものを使用
することができる。密閉容器は、使用するアルキルアル
コキシシラン蒸気とキャリアガスとの混合ガスの温度お
よび圧力に耐える材質、強度のもので作られたものであ
れば良く、容量は特に限定されない。アルキルアルコキ
シシラン蒸気およびキャリアガスは、容器中で加熱して
発生させてもよいし、あらかじめ他の設備で発生させた
蒸気を導入してもよい。
By using a gas having no reactivity with alkylalkoxysilane as a carrier gas,
It is possible to prevent unnecessary hydrolysis and dehydration condensation of the alkylalkoxysilane in the gas reservoir.
As the manufacturing facility in the present invention, it is possible to use, for example, two closed containers capable of discharging internal gas, which are connected via an openable / closable gas opening / closing means, preferably an openable / closable valve. The closed container may be made of a material and strength that can withstand the temperature and pressure of the mixed gas of the alkylalkoxysilane vapor used and the carrier gas, and the capacity is not particularly limited. The alkylalkoxysilane vapor and carrier gas may be generated by heating in a container, or vapor previously generated by other equipment may be introduced.

【0014】本発明において、ガス溜め容器とは、アル
キルアルコキシシラン蒸気およびキャリアガスを溜めて
おく容器であって、内部のガスを排出可能な密閉容器を
言う。反応容器とは、撥水性を付与しようとする軽量気
泡コンクリートを配置する容器であって、内部のガスの
排出可能な密閉容器を言う。本発明においては、アルキ
ルアルコキシシラン蒸気とキャリアガスとの混合ガスを
入れたガス溜め容器と、撥水性を付与しようとする軽量
気泡コンクリートを配置した反応容器とを、バルブ等の
ガス開閉手段を介して接続した装置を用い、ガス溜め容
器のガス圧力を反応容器のガス圧力よりも高い状態でガ
ス開閉手段を開く。そうすると、ガス溜め容器内の混合
ガスがその圧力差によって反応容器に流入するともに軽
量気泡コンクリート内部にまで到達する。この混合ガス
中のアルキルアルコキシシラン蒸気は、軽量気泡コンク
リート表面および内部空隙表面において加水分解・脱水
縮合を進行し、撥水性を発現させる。
In the present invention, the gas storage container is a container for storing the alkylalkoxysilane vapor and the carrier gas, and is a closed container capable of discharging the internal gas. The reaction container is a container in which a lightweight cellular concrete for imparting water repellency is arranged, and is a closed container from which gas inside can be discharged. In the present invention, a gas storage container containing a mixed gas of an alkylalkoxysilane vapor and a carrier gas, and a reaction container in which a lightweight cellular concrete for imparting water repellency is arranged, through a gas opening / closing means such as a valve. The gas opening / closing means is opened in a state in which the gas pressure in the gas reservoir is higher than the gas pressure in the reaction vessel by using the connected device. Then, the mixed gas in the gas storage container flows into the reaction container due to the pressure difference and reaches the inside of the lightweight cellular concrete. The alkylalkoxysilane vapor in the mixed gas promotes hydrolysis / dehydration condensation on the surface of the lightweight cellular concrete and the surface of the internal voids, thereby exhibiting water repellency.

【0015】軽量気泡コンクリートブロック体の内部深
くまでアルキルアルコキシシラン蒸気を導入するための
推進力となるのは、ガス溜め容器と反応容器との圧力差
に起因するガス圧力差である。ここで言うガス圧力差と
は、ガス開閉手段開放直後での反応容器内圧力とガス開
放手段開放直前での反応容器内圧力との差、すなわちア
ルキルアルコキシシランを含むガスを流入させたことに
よる反応容器内圧力の上昇分のことである。この推進
力、すなわちガス圧力差が十分でないと、内部まで撥水
性を発現させることはできない。
The driving force for introducing the alkylalkoxysilane vapor deep into the lightweight cellular concrete block is the gas pressure difference resulting from the pressure difference between the gas storage container and the reaction container. The gas pressure difference referred to here is the difference between the pressure inside the reaction vessel immediately after opening the gas opening / closing means and the pressure inside the reaction vessel immediately before opening the gas opening means, that is, the reaction due to the introduction of the gas containing alkylalkoxysilane. It is the amount of increase in the pressure inside the container. If this driving force, that is, the gas pressure difference is not sufficient, water repellency cannot be exhibited even inside.

【0016】軽量気泡コンクリートの板厚は、さまざま
な種類のものがあり、内部まで撥水性を発現させるのに
必要なガス圧力差は一概には言えないが、例えば100
mm厚の軽量気泡コンクリートの場合には約25000
Pa以上、好ましくは33000Pa以上、更に好まし
くは50000Pa以上の圧力差を必要とする。反応容
器のガス圧力の下限はいわゆる真空状態であり、アルキ
ルアルコキシシラン蒸気のみを使用した場合には、ガス
溜め容器と反応容器との間の圧力差は、最大でも当該温
度におけるアルキルアルコキシシランの蒸気圧までであ
り、それ以上にすることは原理的に不可能である。
There are various types of plate thickness of lightweight cellular concrete, and the gas pressure difference required to develop water repellency to the inside cannot be said unconditionally, but for example, 100
Approximately 25,000 for mm thick lightweight cellular concrete
A pressure difference of Pa or higher, preferably 33000 Pa or higher, more preferably 50,000 Pa or higher is required. The lower limit of the gas pressure in the reaction vessel is a so-called vacuum state, and when only the alkylalkoxysilane vapor is used, the pressure difference between the gas storage vessel and the reaction vessel is the vapor of the alkylalkoxysilane at the temperature at the maximum. It is up to pressure, and it is impossible in principle to exceed it.

【0017】アルキルアルコキシシランは、一般的に蒸
気圧はそれほど大きくなく、高い蒸気圧を持つアルキル
アルコキシシランガスを得るためには、より高い温度が
必要になる。また、アルキル基やアルコキシル基の炭素
数が大きい場合には、特にその傾向が強くなる。一方、
撥水性発現に寄与するのはアルキル基であり、一般的に
大きなアルキル基の方が、高い撥水性を示す。従って、
高い撥水性を得るには大きなアルキル基を有したアルキ
ルアルコキシシランを使用することがより有効になる
が、その場合には、軽量気泡コンクリート内部まで速や
かに充填させるのに必要なガス圧力差を得るために必要
な温度は高くなってしまう。これを行おうとすれば、よ
り高温に耐える設備が必要になる上、むやみに温度を上
げてもアルキルアルコキシシランの分解が起こってしま
い、アルキルアルコキシシランによっては必要なガス圧
力差が得られない場合もある。また、撥水性を付与しよ
うとする軽量気泡コンクリートにとっても、通常の製造
条件よりも高い温度にさらされることは好ましくない。
Alkylalkoxysilanes generally do not have a large vapor pressure, and higher temperatures are required to obtain an alkylalkoxysilane gas having a high vapor pressure. Further, when the alkyl group or the alkoxyl group has a large number of carbon atoms, the tendency becomes particularly strong. on the other hand,
An alkyl group contributes to the development of water repellency, and generally a larger alkyl group exhibits higher water repellency. Therefore,
It is more effective to use an alkylalkoxysilane having a large alkyl group to obtain high water repellency, but in that case, the gas pressure difference required to quickly fill the inside of lightweight cellular concrete is obtained. Therefore, the temperature required for it becomes high. If you try to do this, you will need equipment that can withstand higher temperatures, and even if you raise the temperature unnecessarily, the alkylalkoxysilane will decompose, and if the required gas pressure difference cannot be obtained depending on the alkylalkoxysilane. There is also. Further, even for lightweight cellular concrete to impart water repellency, it is not preferable to expose it to a temperature higher than usual manufacturing conditions.

【0018】そこで、本発明は、キャリアガスを利用す
ることによって、アルキルアルコキシシラン単独では十
分な蒸気圧を得られない温度条件であっても、推進力と
なる、ガス溜め容器と反応容器とのガス圧力差を十分な
大きさにすることができることを見出したものでもあ
る。しかしながら、キャリアガスを使用する場合、混合
ガス中に含まれるアルキルアルコキシシラン蒸気は、ア
ルキルアルコキシシラン蒸気単独で十分な圧力差を確保
できる温度で撥水性付与を行う場合よりも希薄であるの
で、たとえ軽量気泡コンクリート内部まで混合ガスが到
達していても、撥水層を形成するためには不十分な量で
ある場合が多い。
Therefore, according to the present invention, by using a carrier gas, a gas storage container and a reaction container, which act as a driving force even under a temperature condition where a sufficient vapor pressure cannot be obtained by alkylalkoxysilane alone, are used. It was also found that the gas pressure difference can be made sufficiently large. However, when a carrier gas is used, the alkylalkoxysilane vapor contained in the mixed gas is leaner than the case where the alkylalkoxysilane vapor alone imparts water repellency at a temperature at which a sufficient pressure difference can be secured. Even if the mixed gas reaches the inside of the lightweight cellular concrete, it is often an insufficient amount for forming the water repellent layer.

【0019】このような場合は、処理温度を高くしてア
ルキルアルコキシシラン蒸気の含有割合を大きくする方
法もあるが、キャリアガスとアルキルアルコキシシラン
蒸気との混合割合を調整すれば、任意のガス圧力の混合
ガスが得られることから、1回目の撥水層形成操作に引
き続いて、ガス開閉手段を閉じた後に、ガス溜め容器の
ガス圧力をその時点における反応容器のガス圧力以上に
なるように、ガス溜め容器内をアルキルアルコキシシラ
ン蒸気とキャリアガスで満たし、ガス開閉手段を開き、
再び反応容器に混合ガスを送り込むことが可能である。
このように、ガス溜め容器から反応容器に、繰り返しア
ルキルアルコキシシラン蒸気を含む混合ガスを送ること
により、目的とする撥水性能を示す撥水層を外表面およ
び内部空隙表面に有した軽量気泡コンクリートを得るた
めに十分なアルキルアルコキシシラン蒸気を供給するこ
とができるので、優れた撥水性軽量気泡コンクリートを
得ることが可能になる。
In such a case, there is a method of increasing the treatment temperature to increase the content ratio of the alkylalkoxysilane vapor. However, if the mixing ratio of the carrier gas and the alkylalkoxysilane vapor is adjusted, the gas pressure can be adjusted to an arbitrary value. Since the mixed gas of is obtained, following the first water-repellent layer forming operation, after closing the gas opening / closing means, the gas pressure of the gas reservoir container is set to be equal to or higher than the gas pressure of the reaction container at that time. Fill the gas reservoir with alkylalkoxysilane vapor and carrier gas, open the gas opening / closing means,
It is possible to feed the mixed gas into the reaction vessel again.
Thus, by repeatedly sending the mixed gas containing the alkylalkoxysilane vapor from the gas storage container to the reaction container, a lightweight cellular concrete having a water repellent layer exhibiting the desired water repellent performance on the outer surface and the inner void surface. Since sufficient alkylalkoxysilane vapor can be supplied to obtain the water-repellent, excellent water-repellent lightweight cellular concrete can be obtained.

【0020】また、1回目の撥水層形成操作に引き続い
て、ガス開閉手段を閉じた後に、反応容器を開放する
か、減圧にした後に反応容器を密閉し、ガス開閉手段を
開放してガス溜め容器内の混合ガスを反応容器に流入さ
せることで、優れた撥水性軽量気泡コンクリートを得る
ことが可能になる。たとえば、アルキルアルコキシシラ
ンの中でも、ヘキシルトリエトキシシラン(アルキル基
の炭素数6)やオクチルトリエトキシシラン(アルキル
基の炭素数8)、あるいはそれ以上の大きさのアルキル
基を有するアルキルアルコキシシランの場合、軽量気泡
コンクリート製造に一般的に用いられる温度180℃で
あっても蒸気圧が低く、軽量気泡コンクリート板厚が厚
い場合などには、アルキルアルコキシシラン蒸気単独で
十分なガス圧力差を確保することは難しく、本発明に示
すように、キャリアガスを利用してガス圧力差を調整
し、繰り返しアルキルアルコキシシラン蒸気を反応容器
に送り込む方法や、アルキルアルコキシシラン蒸気を反
応容器に送り込んだ後に、いったん反応容器を開放する
か減圧し、再びアルキルアルコキシシラン蒸気を送り込
む方法が、優れた撥水性軽量気泡コンクリートを製造す
る上で非常に有効になる。
Further, following the first operation of forming the water-repellent layer, after closing the gas opening / closing means, the reaction vessel is opened, or the pressure is reduced and then the reaction vessel is closed, and the gas opening / closing means is opened to open the gas. By allowing the mixed gas in the storage container to flow into the reaction container, an excellent water-repellent lightweight cellular concrete can be obtained. For example, among alkylalkoxysilanes, in the case of hexyltriethoxysilane (alkyl group having 6 carbon atoms), octyltriethoxysilane (alkyl group having 8 carbon atoms), or alkylalkoxysilane having an alkyl group having a larger size , If the vapor pressure is low even at a temperature of 180 ° C, which is generally used for the production of lightweight aerated concrete, and the thickness of the lightweight aerated concrete is large, ensure sufficient gas pressure difference with the alkylalkoxysilane vapor alone. Is difficult, as shown in the present invention, a gas pressure difference is adjusted by using a carrier gas, and a method of repeatedly feeding an alkylalkoxysilane vapor into a reaction vessel or a method of feeding an alkylalkoxysilane vapor into a reaction vessel and then reacting once Open the container or reduce the pressure and How to feed the steam become very effective in producing excellent water repellency lightweight concrete.

【0021】本発明において、ガス溜め容器から反応容
器に混合ガスを送り込む操作は数分〜数十分程度の極め
て短い時間間隔で行うことが可能である。撥水性付与工
程が短時間の場合など、一部未反応のアルキルアルコキ
シシランが、軽量気泡コンクリート外表面および内部空
隙表面に存在して、十分な撥水性を発現することができ
ない場合があるが、この場合には室温で数日〜数週間放
置することにより反応が進行し、撥水性が発現するよう
になる。撥水性発現をさらに促進するためには加熱処理
を行うことが効果的であり、60℃〜180℃で0.5
〜5時間程度加熱することが好ましい。ここで、加熱方
法は特に限定されないが、一般的な熱風加熱や遠赤外線
加熱または、水蒸気加熱などを使用することができる。
In the present invention, the operation of feeding the mixed gas from the gas reservoir to the reaction vessel can be carried out at an extremely short time interval of several minutes to several tens of minutes. In the case where the water repellency imparting step is short, but partially unreacted alkylalkoxysilane is present on the outer surface of the lightweight cellular concrete and the surface of the inner voids, and it may not be possible to exhibit sufficient water repellency, In this case, the reaction proceeds by leaving it at room temperature for several days to several weeks, so that the water repellency is exhibited. It is effective to carry out a heat treatment in order to further promote the development of water repellency.
It is preferable to heat for about 5 hours. Here, the heating method is not particularly limited, but general hot air heating, far infrared heating, steam heating, or the like can be used.

【0022】上記したように、軽量気泡コンクリート内
部への浸透は、アルキルアルコキシシラン蒸気とキャリ
アガスとの混合ガスのガス圧力と反応容器内のガス圧力
との圧力差が推進力となるため、混合ガスのガス圧力は
軽量気泡コンクリートが置かれた反応容器内のガス圧力
よりも高く設定することが重要であり、その圧力差は大
きい方が早く、確実に内部まで浸透するが、被撥水性付
与物となる軽量気泡コンクリートの総容積および板厚、
また、ガス溜め容器と反応容器の容量比などによって最
も効率的、経済的な値を設定することができる。
As described above, the permeation into the lightweight aerated concrete is caused by the pressure difference between the gas pressure of the mixed gas of the alkylalkoxysilane vapor and the carrier gas and the gas pressure in the reaction vessel, which is the driving force. It is important to set the gas pressure of the gas higher than the gas pressure in the reaction vessel in which the lightweight cellular concrete is placed. The larger the pressure difference, the faster the gas permeates into the interior, but the water-repellent property is imparted. Total volume and thickness of lightweight cellular concrete,
Further, the most efficient and economical value can be set depending on the volume ratio of the gas storage container and the reaction container.

【0023】本発明は、ガス溜め容器にアルキルアルコ
キシシランとキャリアガスとの混合ガスを入れ、反応容
器に軽量気泡コンクリートを配置し、ガス溜め容器内の
混合ガスのガス圧力を反応容器内のガス圧力よりも高く
した後に、それらの容器をつなぐガス開閉手段を一定時
間開放した後にガス開閉手段を閉じ、その後ガス溜め容
器にアルキルアルコキシシラン蒸気とキャリアガスとの
混合ガス(反応容器内よりも高いガス圧力を有する。)
を導入し、再度ガス遮開閉手段を一定時間開放する操作
を少なくとも1回行うものである。これによって、より
多くのアルキルアルコキシシランを軽量気泡コンクリー
ト内部に送り込むことができ、優れた撥水性軽量気泡コ
ンクリートを得ることができる。
In the present invention, a gas mixture of an alkylalkoxysilane and a carrier gas is put in a gas container, a lightweight cellular concrete is placed in the reaction container, and the gas pressure of the mixed gas in the gas container is set to the gas in the reaction container. After making the pressure higher than the pressure, the gas opening / closing means connecting these containers is opened for a certain period of time, and then the gas opening / closing means is closed, and then a mixed gas of alkylalkoxysilane vapor and carrier gas in the gas storage container (higher than that in the reaction container Has gas pressure.)
Is introduced and the operation of opening and closing the gas shut-off means again and again for a certain period of time is performed at least once. As a result, more alkylalkoxysilane can be fed into the lightweight cellular concrete, and an excellent water-repellent lightweight cellular concrete can be obtained.

【0024】また、1回目の撥水層形成操作に引き続い
て、ガス開閉手段を閉じた後に、反応容器を開放する
か、減圧にした後に該反応容器を密閉し、ガス開閉手段
を開放してガス溜め容器内の混合ガスを反応容器に流入
させるという操作を少なくとも1回行うことで、優れた
撥水性軽量気泡コンクリートを得ることが可能になる。
反応容器を開放または減圧にする時、反応容器内に存在
する未反応のアルキルアルコキシシラン蒸気が一部系外
に排出される可能性があるが、その量を減らすため、反
応容器を開放または減圧にする前に、該温度で0.5〜
5時間保持して撥水層形成を促進することが好ましい。
Following the first water-repellent layer forming operation, after closing the gas opening / closing means, the reaction vessel is opened, or after the pressure is reduced, the reaction vessel is closed and the gas opening / closing means is opened. By performing the operation of flowing the mixed gas in the gas reservoir into the reaction container at least once, it becomes possible to obtain an excellent water-repellent lightweight cellular concrete.
When the reaction vessel is opened or depressurized, unreacted alkylalkoxysilane vapor existing in the reaction vessel may be partly discharged to the outside of the system.To reduce the amount, open or depressurize the reaction vessel. 0.5 to 0.5 at the temperature before
It is preferable to hold for 5 hours to promote the formation of the water-repellent layer.

【0025】更に、これらの操作を組み合わせて行うこ
とも可能である。即ち、1回目の撥水層形成操作に引き
続いて、ガス開閉手段を閉じた後に、反応容器を開放す
るか、減圧にし、一方ガス溜め容器にはアルキルアルコ
キシシラン蒸気とキャリアガスとの混合ガスを導入し、
再度ガス開閉手段を一定時間開放するという操作を行
い、優れた撥水性軽量気泡コンクリートを得ることも可
能である。
Furthermore, it is also possible to combine these operations. That is, following the first water-repellent layer forming operation, after closing the gas opening / closing means, the reaction vessel is opened or depressurized, while the mixed gas of alkylalkoxysilane vapor and carrier gas is placed in the gas reservoir vessel. Introduced,
It is also possible to obtain an excellent water-repellent lightweight cellular concrete by repeating the operation of opening the gas opening / closing means for a certain period of time.

【0026】[0026]

【発明の実施の形態】以下に、本発明における実施例を
記す。
Embodiments of the present invention will be described below.

【0027】[0027]

【実施例1】ヒーターにより加熱可能な内寸法200m
m×200mm×250mm(内容積10L)の密閉容
器2台を、バルブを介して接続した装置を用い、一方を
ガス溜め容器として、もう一方を反応容器として用い
た。軽量気泡コンクリート(商品名:へーベル、旭化成
建材(株)製)から、長さ200mm、幅100mm、
厚さ50mmの試料を切り出し、試験片として用いた。
[Embodiment 1] Inner size 200 m that can be heated by a heater
An apparatus was used in which two sealed containers each measuring m × 200 mm × 250 mm (internal volume 10 L) were connected via a valve, one was used as a gas reservoir and the other was used as a reaction container. From lightweight cellular concrete (trade name: Hebel, manufactured by Asahi Kasei Corporation), length 200 mm, width 100 mm,
A sample having a thickness of 50 mm was cut out and used as a test piece.

【0028】ガス溜め容器にプロピルトリエトキシシラ
ン(KBE−3033、信越化学工業(株)製)25gを入
れ、容器内の空気を真空ポンプ(ダイアフラム真空ポン
プ、DAH−60)で1300Paまで排気した後、14
5℃に加熱した。プロピルトリエトキシシランの蒸気圧
は27000Paとなった。さらに、このガス溜め容器
中にキャリアガスとして窒素ガスを注入し、全体の圧力
を47000Paまで上げた。一方、反応容器に上記の
軽量気泡コンクリート試験片を入れ、145℃に加熱
後、反応容器内を5000Paに減圧した。その後、バ
ルブを10秒間開放すると、両容器の圧力差によってガ
ス溜め容器から反応容器にプロピルトリエトキシシラン
蒸気および窒素の混合ガスが流入し、反応容器は260
00Paとなった。バルブを閉めた後、各容器の温度を
保持したまま5分間放置すると、ガス溜め容器内に残存
しているプロピルトリエトキシシランが蒸発し、僅かに
圧力上昇が認められた。
25 g of propyltriethoxysilane (KBE-3033, manufactured by Shin-Etsu Chemical Co., Ltd.) was placed in a gas reservoir, and the air in the container was exhausted to 1300 Pa by a vacuum pump (diaphragm vacuum pump, DAH-60). , 14
Heated to 5 ° C. The vapor pressure of propyltriethoxysilane became 27,000 Pa. Further, nitrogen gas was injected as a carrier gas into the gas storage container to raise the total pressure to 47,000 Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container, heated to 145 ° C., and then the pressure inside the reaction container was reduced to 5000 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of propyltriethoxysilane vapor and nitrogen flowed into the reaction container from the gas reservoir container due to the pressure difference between the two containers, and the reaction container was 260
It became 00 Pa. After the valves were closed, when the temperature of each container was maintained for 5 minutes, the propyltriethoxysilane remaining in the gas reservoir container was evaporated, and a slight pressure increase was observed.

【0029】更に、ガス溜め容器内の圧力が10000
0Paになるまで窒素を注入した後、再度バルブを10
秒間開き、プロピルトリエトキシシラン蒸気と窒素の混
合ガスを反応容器にさらに送り込んだ。反応容器は、圧
力63000Paとなった。バルブを閉じた後、反応容
器を145℃で1時間保持した。得られた試験片を長さ
方向の中央部で切断した幅100mm、厚さ50mmの
切断面上を幅方向に外表面近傍(外表面より約1mm)
2点および中央部に25mm間隔で3点、厚さ方向に外
表面近傍(外表面より約1mm)2点および中央部に1
2.5mm間隔で3点、合計25箇所における水の接触
角を、協和界面化学(株)製の接触角計(CA-DT型)で
測定したところ、すべての測定点において、水の接触角
は約130度となり、均一な撥水性を有することが確認
できた。
Furthermore, the pressure in the gas reservoir is 10,000
After injecting nitrogen to 0 Pa, set the valve to 10 again.
After opening for 2 seconds, a mixed gas of propyltriethoxysilane vapor and nitrogen was further fed into the reaction vessel. The pressure of the reaction container became 63,000 Pa. After closing the valve, the reaction vessel was kept at 145 ° C. for 1 hour. The obtained test piece was cut at the central portion in the length direction, and the vicinity of the outer surface in the width direction (about 1 mm from the outer surface) on the cut surface having a width of 100 mm and a thickness of 50 mm.
2 points and 3 points at 25 mm intervals in the center, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface) and 1 in the center
The contact angle of water at 25 points at 3 points at 2.5 mm intervals was measured with a contact angle meter (CA-DT type) manufactured by Kyowa Interface Science Co., Ltd. Was about 130 degrees, and it was confirmed to have uniform water repellency.

【0030】[0030]

【実施例2】実施例1と同様の装置、軽量気泡コンクリ
ート試験片を用い、ガス溜め容器にプロピルトリエトキ
シシラン25gを入れ、容器内の空気を実施例1と同様
に真空ポンプで排気した後、145℃に加熱した。プロ
ピルトリエトキシシランの蒸気圧は27000Paとな
った。さらに、このガス溜め容器中にキャリアガスとし
て窒素ガスを注入し、全体の圧力を100000Paま
で上げた。一方、反応容器に上記の軽量気泡コンクリー
ト試験片を入れ、145℃に加熱後、反応容器内を50
00Paに減圧した。その後、バルブを10秒間開放す
ると、両容器の圧力差によってガス溜め容器から反応容
器にプロピルトリエトキシシラン蒸気と窒素の混合ガス
が流入し、反応容器は52500Paとなった。バルブ
を閉じた後、ガス溜め容器内は液体で存在しているプロ
ピルトリエトキシシランが蒸発し、僅かに圧力上昇が認
められた。
Example 2 Using the same apparatus as in Example 1 and a lightweight cellular concrete test piece, 25 g of propyltriethoxysilane was placed in a gas reservoir, and the air in the container was evacuated by a vacuum pump as in Example 1. Heated to 145 ° C. The vapor pressure of propyltriethoxysilane became 27,000 Pa. Further, nitrogen gas was injected as a carrier gas into the gas storage container to raise the total pressure to 100,000 Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container and heated to 145 ° C.
The pressure was reduced to 00 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of propyltriethoxysilane vapor and nitrogen flowed into the reaction vessel from the gas reservoir vessel due to the pressure difference between both vessels, and the reaction vessel reached 52500 Pa. After closing the valve, propyltriethoxysilane, which was present as a liquid in the gas reservoir, was evaporated and a slight pressure increase was observed.

【0031】反応容器を145℃で1時間保持した後、
ガス溜め容器内に窒素を注入して圧力を100000P
aに上げ、反応容器内を5000Paに減圧してからバ
ルブを10秒間開放すると、ガス溜め容器から反応容器
にプロピルトリエトキシシランの混合ガスが流入し、反
応容器は52500Paとなった。バルブを閉じた後、
反応容器を145℃で1時間保持した。得られた試験片
を長さ方向の中央部で切断した幅100mm、厚さ50
mmの切断面上を幅方向に外表面近傍(外表面より約1
mm)2点および中央部に25mm間隔で3点、厚さ方
向に外表面近傍(外表面より約1mm)2点および中央
部に12.5mm間隔で3点、合計25箇所における水
の接触角を、協和界面化学(株)製の接触角計(CA-DT
型)で測定したところ、すべての測定点において、水の
接触角は約130度となり、均一な撥水性を有すること
が確認できた。
After keeping the reaction vessel at 145 ° C. for 1 hour,
Inject nitrogen into the gas reservoir to adjust the pressure to 100,000P.
When the pressure in the reaction vessel was reduced to 5000 Pa and the valve was opened for 10 seconds, the mixed gas of propyltriethoxysilane flowed into the reaction vessel from the gas reservoir and the reaction vessel reached 52500 Pa. After closing the valve,
The reaction vessel was held at 145 ° C for 1 hour. The obtained test piece was cut at the center in the length direction to have a width of 100 mm and a thickness of 50.
Around the outer surface in the width direction on the cut surface of mm (about 1 mm from the outer surface
mm) 2 points and 3 points at 25 mm intervals in the center, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface) and 3 points at 12.5 mm intervals in the center, a total of 25 contact angles of water. Is a contact angle meter (CA-DT manufactured by Kyowa Interface Science Co., Ltd.
It was confirmed that the contact angle of water was about 130 degrees at all measurement points, and that it had uniform water repellency.

【0032】[0032]

【実施例3】実施例1と同様の装置、軽量気泡コンクリ
ート試験片を用い、ガス溜め容器にヘキシルトリエトキ
シシラン25gを入れ、容器内の空気を実施例1と同様
に真空ポンプで排気した後、180℃に加熱した。ヘキ
シルトリエトキシシランの蒸気圧は27000Paとな
った。さらに、このガス溜め容器中にキャリアガスとし
て窒素ガスを注入し、全体の圧力を47000Paまで
上げた。一方、反応容器に上記の軽量気泡コンクリート
試験片を入れ、180℃に加熱後、反応容器内を500
0Paに減圧した。その後、バルブを10秒間開放する
と、両容器の圧力差によってガス溜め容器から反応容器
にヘキシルトリエトキシシラン蒸気および窒素の混合ガ
スが流入し、反応容器は26000Paとなった。バル
ブを閉めた後、各容器の温度を保持したまま5分間放置
すると、ガス溜め容器内に残存しているヘキシルトリエ
トキシシランが蒸発し、僅かに圧力上昇が認められた。
更にガス溜め容器内の圧力が100000Paになるま
で窒素を注入した後、再度バルブを10秒間開き、ヘキ
シルトリエトキシシラン蒸気と窒素の混合ガスを反応容
器にさらに送り込んだ。反応容器は、圧力63000P
aとなった。バルブを閉じた後、反応容器を180℃で
1時間保持した。
[Example 3] Using the same apparatus as in Example 1 and a lightweight cellular concrete test piece, 25 g of hexyltriethoxysilane was placed in a gas reservoir, and the air in the container was evacuated by a vacuum pump as in Example 1. , Heated to 180 ° C. The vapor pressure of hexyltriethoxysilane was 27,000 Pa. Further, nitrogen gas was injected as a carrier gas into the gas storage container to raise the total pressure to 47,000 Pa. On the other hand, the above lightweight cellular concrete test piece was put into a reaction container, heated to 180 ° C., and then the inside of the reaction container was heated to 500 ° C.
The pressure was reduced to 0 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of hexyltriethoxysilane vapor and nitrogen flowed into the reaction container from the gas reservoir container due to the pressure difference between both containers, and the reaction container became 26000 Pa. After the valves were closed, when the temperature of each container was maintained for 5 minutes, the hexyltriethoxysilane remaining in the gas reservoir container was evaporated, and a slight pressure increase was observed.
Further, nitrogen was injected until the pressure in the gas storage container reached 100,000 Pa, the valve was opened again for 10 seconds, and a mixed gas of hexyltriethoxysilane vapor and nitrogen was further fed into the reaction container. Pressure of reaction vessel is 63000P
It became a. After closing the valve, the reaction vessel was kept at 180 ° C. for 1 hour.

【0033】得られた試験片を長さ方向の中央部で切断
した幅100mm、厚さ50mmの切断面上を幅方向に
外表面近傍(外表面より約1mm)2点および中央部に
25mm間隔で3点、厚さ方向に外表面近傍(外表面よ
り約1mm)2点および中央部に12.5mm間隔で3
点、合計25箇所における水の接触角を、協和界面化学
(株)製の接触角計(CA-DT型)で測定したところ、す
べての測定点において、水の接触角は約150度とな
り、均一な撥水性を有することが確認できた。
The test piece obtained was cut at the center in the lengthwise direction, and two points near the outer surface (about 1 mm from the outer surface) in the widthwise direction on the cut surface having a width of 100 mm and a thickness of 50 mm and a 25 mm interval at the center. At 3 points, 2 points near the outer surface (about 1 mm from the outer surface) in the thickness direction, and 3 at 12.5 mm intervals in the center.
The contact angle of water at a total of 25 points was measured with a contact angle meter (CA-DT type) manufactured by Kyowa Interface Science Co., Ltd., and the contact angle of water was about 150 degrees at all measurement points. It was confirmed to have uniform water repellency.

【0034】[0034]

【実施例4】実施例1と同様の装置、軽量気泡コンクリ
ート試験片を用い、ガス溜め容器にヘキシルトリエトキ
シシラン25gを入れ、容器内の空気を実施例1と同様
に真空ポンプで排気した後、180℃に加熱した。ヘキ
シルトリエトキシシランの蒸気圧は27000Paとな
った。さらに、このガス溜め容器中にキャリアガスとし
て窒素ガスを注入し、全体の圧力を100000Paま
で上げた。一方、反応容器に上記の軽量気泡コンクリー
ト試験片を入れ、180℃に加熱後、反応容器内を50
00Paに減圧した。その後、バルブを10秒間開放す
ると、両容器の圧力差によってガス溜め容器から反応容
器にヘキシルトリエトキシシラン蒸気と窒素の混合ガス
が流入し、反応容器は52500Paとなった。バルブ
を閉じた後、ガス溜め容器内は液体で存在しているプロ
ピルトリエトキシシランが蒸発し、僅かに圧力上昇が認
められた。
[Example 4] Using the same apparatus as in Example 1 and a lightweight cellular concrete test piece, 25 g of hexyltriethoxysilane was placed in a gas reservoir, and the air in the container was evacuated by a vacuum pump as in Example 1. , Heated to 180 ° C. The vapor pressure of hexyltriethoxysilane was 27,000 Pa. Further, nitrogen gas was injected as a carrier gas into the gas storage container to raise the total pressure to 100,000 Pa. On the other hand, the above lightweight cellular concrete test piece was put into a reaction vessel, heated to 180 ° C., and then heated to 50 ° C. in the reaction vessel.
The pressure was reduced to 00 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of hexyltriethoxysilane vapor and nitrogen flowed into the reaction container from the gas reservoir container due to the pressure difference between both containers, and the reaction container became 52500 Pa. After closing the valve, propyltriethoxysilane, which was present as a liquid in the gas reservoir, was evaporated and a slight pressure increase was observed.

【0035】反応容器を180℃で1時間保持した後、
ガス溜め容器内に窒素を注入して圧力を100000P
aに上げ、反応容器内を5000Paに減圧してからバ
ルブを10秒間開放すると、ガス溜め容器から反応容器
にヘキシルトリエトキシシランの混合ガスが流入し、反
応容器は52500Paとなった。バルブを閉じた後、
反応容器を180℃で1時間保持した。得られた試験片
を長さ方向の中央部で切断した幅100mm、厚さ50
mmの切断面上を幅方向に外表面近傍(外表面より約1
mm)2点および中央部に25mm間隔で3点、厚さ方
向に外表面近傍(外表面より約1mm)2点および中央
部に12.5mm間隔で3点、合計25箇所における水
の接触角を、協和界面化学(株)製の接触角計(CA-DT
型)で測定したところ、すべての測定点において、水の
接触角は約150度となり、均一な撥水性を有すること
が確認できた。
After keeping the reaction vessel at 180 ° C. for 1 hour,
Inject nitrogen into the gas reservoir to adjust the pressure to 100,000P.
When the pressure in the reaction vessel was reduced to 5000 Pa and the valve was opened for 10 seconds, the mixed gas of hexyltriethoxysilane flowed into the reaction vessel from the gas reservoir vessel, and the reaction vessel reached 52500 Pa. After closing the valve,
The reaction vessel was kept at 180 ° C. for 1 hour. The obtained test piece was cut at the center in the length direction to have a width of 100 mm and a thickness of 50.
Around the outer surface in the width direction on the cut surface of mm (about 1 mm from the outer surface
mm) 2 points and 3 points at 25 mm intervals in the center, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface) and 3 points at 12.5 mm intervals in the center, a total of 25 contact angles of water. Is a contact angle meter (CA-DT manufactured by Kyowa Interface Science Co., Ltd.
The contact angle of water was about 150 degrees at all measurement points, and it was confirmed that the sample had uniform water repellency.

【0036】[0036]

【比較例1】実施例1に記載した方法に対し、プロピル
トリエトキシシランと窒素との混合ガスを1回だけ反応
容器に送り込んだ段階での撥水性を調べたものである。
実施例1と同様の装置、軽量気泡コンクリート試験片を
用い、ガス溜め容器にプロピルトリエトキシシラン25
gを入れ、該容器内の空気を実施例1と同様に真空ポン
プで排気した後、145℃に加熱した。プロピルトリエ
トキシシランの蒸気圧は27000Paとなった。ここ
で、ガス溜め容器に窒素ガスを加え、全体の圧力を47
000Paまで上げた。一方、反応容器に上記の軽量気
泡コンクリート試験片を入れ、145℃に加熱後、反応
容器内を5000Paに減圧した。その後、バルブを1
0秒間開放すると、両容器の圧力差によってガス溜め容
器から反応容器にプロピルトリエトキシシラン蒸気およ
び窒素の混合ガスが流入し、反応容器は26000Pa
となった。バルブを閉じた後、反応容器を145℃で1
時間保持した。
Comparative Example 1 In comparison with the method described in Example 1, the water repellency was examined when the mixed gas of propyltriethoxysilane and nitrogen was fed into the reaction vessel only once.
Using the same apparatus as in Example 1 and a lightweight cellular concrete test piece, propyltriethoxysilane 25 was placed in a gas reservoir.
g was added, the air in the container was evacuated by a vacuum pump as in Example 1, and then heated to 145 ° C. The vapor pressure of propyltriethoxysilane became 27,000 Pa. At this point, add nitrogen gas to the gas reservoir and adjust the total pressure to 47
Raised to 000Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container, heated to 145 ° C., and then the pressure inside the reaction container was reduced to 5000 Pa. Then turn the valve 1
When opened for 0 seconds, a mixed gas of propyltriethoxysilane vapor and nitrogen flows from the gas reservoir to the reaction vessel due to the pressure difference between the two vessels, and the reaction vessel has a pressure of 26000 Pa.
Became. After closing the valve, place the reaction vessel at 145 ° C for 1 hour.
Held for hours.

【0037】得られた試験片を長さ方向の中央部で切断
した幅100mm、厚さ50mmの切断面上を幅方向に
外表面近傍(外表面より約1mm)2点および中央部に
25mm間隔で3点、厚さ方向に外表面近傍(外表面よ
り約1mm)2点および12.5mm間隔で3点、合計
25箇所における水の接触角を、協和界面化学(株)製
の接触角計(CA-DT型)で測定したところ、表面から1
2.5mm以内の22点においては水の接触角が約13
0度であったが、表面から12.5mmを越える深さの
3点においては、接触角は90度に満たなかった。撥水
性が発現している部分の詳細を調べるため、切断面の幅
方向の中央において、厚さ方向に5mm間隔で水の接触
角を測定したところ、表面から20mm以内である点で
は約130度であったが、中央部の1点では90度に満
たなかった。
The obtained test piece was cut at the center in the length direction, and two points were formed in the width direction on the cut surface having a width of 100 mm and a thickness of 50 mm in the vicinity of the outer surface (about 1 mm from the outer surface) and at intervals of 25 mm in the center. At 3 points, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface), and 3 points at 12.5 mm intervals, for a total of 25 contact angles of water. When measured with (CA-DT type), 1 from the surface
The contact angle of water is about 13 at 22 points within 2.5 mm.
Although it was 0 degree, the contact angle was less than 90 degrees at three points with a depth exceeding 12.5 mm from the surface. In order to investigate the details of the water-repellent part, the contact angle of water was measured at 5 mm intervals in the thickness direction at the center of the cut surface in the width direction, and it was about 130 degrees at a point within 20 mm from the surface. However, it was less than 90 degrees at one point in the central part.

【0038】[0038]

【比較例2】実施例2に記載した方法に対し、プロピル
トリエトキシシランと窒素との混合ガスを1回だけ反応
容器に送り込んだ段階での撥水性を調べたものである。
実施例1と同様の装置、軽量気泡コンクリート試験片を
用い、ガス溜め容器にプロピルトリエトキシシラン25
gを入れ、容器内の空気を実施例1と同様に真空ポンプ
で排気した後、145℃に加熱した。プロピルトリエト
キシシランの蒸気圧は27000Paとなった。さら
に、このガス溜め容器中にキャリアガスとして窒素を注
入し、全体の圧力を100000Paまで上げた。一
方、反応容器に上記の軽量気泡コンクリート試験片を入
れ、145℃に加熱後、反応容器内を5000Paに減
圧した。その後、バルブを10秒間開放すると、両容器
の圧力差によってガス溜め容器から反応容器にプロピル
トリエトキシシラン蒸気と窒素の混合ガスが流入し、反
応容器は52500Paとなった。バルブを閉じた後、
反応容器を145℃で1時間保持した。
Comparative Example 2 In comparison with the method described in Example 2, the water repellency was examined when the mixed gas of propyltriethoxysilane and nitrogen was fed into the reaction vessel only once.
Using the same apparatus as in Example 1 and a lightweight cellular concrete test piece, propyltriethoxysilane 25 was placed in a gas reservoir.
After adding g, the air in the container was evacuated with a vacuum pump as in Example 1, and then heated to 145 ° C. The vapor pressure of propyltriethoxysilane became 27,000 Pa. Further, nitrogen was injected as a carrier gas into the gas reservoir to raise the total pressure to 100,000 Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container, heated to 145 ° C., and then the pressure inside the reaction container was reduced to 5000 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of propyltriethoxysilane vapor and nitrogen flowed into the reaction vessel from the gas reservoir vessel due to the pressure difference between both vessels, and the reaction vessel reached 52500 Pa. After closing the valve,
The reaction vessel was held at 145 ° C for 1 hour.

【0039】得られた試験片を長さ方向の中央部で切断
した幅100mm、厚さ50mmの切断面上を幅方向に
外表面近傍(外表面より約1mm)2点および中央部に
25mm間隔で3点、厚さ方向に外表面近傍(外表面よ
り約1mm)2点および中央部に12.5mm間隔で3
点、合計25箇所における水の接触角を、協和界面化学
(株)製の接触角計(CA-DT型)で測定したところ、表
面から12.5mm以内の22点においては水の接触角
が約130度であったが、表面から12.5mmを越え
る深さの3点においては、接触角は90度に満たなかっ
た。撥水性が発現している部分の詳細を調べるため、切
断面の幅方向の中央において、厚さ方向に5mm間隔で
水の接触角を測定したところ、表面から20mm以内で
ある点では約130度であったが、中央部の1点では9
0度に満たなかった。
The test piece obtained was cut at the center in the lengthwise direction, and two points near the outer surface (about 1 mm from the outer surface) in the widthwise direction on the cut surface having a width of 100 mm and a thickness of 50 mm and a 25 mm interval at the center. At 3 points, 2 points near the outer surface (about 1 mm from the outer surface) in the thickness direction, and 3 at 12.5 mm intervals in the center.
The contact angle of water at a total of 25 points was measured with a contact angle meter (CA-DT type) manufactured by Kyowa Interface Science Co., Ltd., and the contact angle of water was 22 points within 12.5 mm from the surface. Although it was about 130 degrees, the contact angle was less than 90 degrees at three points with a depth exceeding 12.5 mm from the surface. In order to investigate the details of the water-repellent part, the contact angle of water was measured at 5 mm intervals in the thickness direction at the center of the cut surface in the width direction, and it was about 130 degrees at a point within 20 mm from the surface. However, one point in the center was 9
It was less than 0 degrees.

【0040】[0040]

【比較例3】実施例3に記載した方法に対し、ヘキシル
トリエトキシシランと窒素との混合ガスを1回だけ反応
容器に送り込んだ段階での撥水性を調べたものである。
実施例1と同様の装置、軽量気泡コンクリート試験片を
用い、ガス溜め容器にヘキシルトリエトキシシラン25
gを入れ、容器内の空気を実施例1と同様に真空ポンプ
で排気した後、180℃に加熱した。ヘキシルトリエト
キシシランの蒸気圧は27000Paとなった。さら
に、このガス溜め容器中にキャリアガスとして窒素ガス
を注入し、全体の圧力を47000Paまで上げた。一
方、反応容器に上記の軽量気泡コンクリート試験片を入
れ、180℃に加熱後、反応容器内を5000Paに減
圧した。その後、バルブを10秒間開放すると、両容器
の圧力差によってガス溜め容器から反応容器にヘキシル
トリエトキシシラン蒸気および窒素の混合ガスが流入
し、反応容器は26000Paとなった。バルブを閉じ
た後、反応容器を180℃で1時間保持した。
COMPARATIVE EXAMPLE 3 In comparison with the method described in Example 3, the water repellency was examined when the mixed gas of hexyltriethoxysilane and nitrogen was fed into the reaction vessel only once.
Using a device similar to that of Example 1 and a lightweight cellular concrete test piece, hexyltriethoxysilane 25 was placed in a gas reservoir.
After adding g, the air in the container was evacuated by a vacuum pump as in Example 1, and then heated to 180 ° C. The vapor pressure of hexyltriethoxysilane was 27,000 Pa. Further, nitrogen gas was injected as a carrier gas into the gas storage container to raise the total pressure to 47,000 Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container, heated to 180 ° C., and the pressure inside the reaction container was reduced to 5000 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of hexyltriethoxysilane vapor and nitrogen flowed into the reaction container from the gas reservoir container due to the pressure difference between both containers, and the reaction container became 26000 Pa. After closing the valve, the reaction vessel was kept at 180 ° C. for 1 hour.

【0041】得られた試験片を長さ方向の中央部で切断
した幅100mm、厚さ50mmの切断面上を幅方向に
外表面近傍(外表面より約1mm)2点および中央部に
幅方向に25mm間隔で3点、厚さ方向に外表面近傍
(外表面より約1mm)2点および中央部に12.5m
m間隔で3点、合計25箇所における水の接触角を、協
和界面化学(株)製の接触角計(CA-DT型)で測定した
ところ、表面から12.5mm以内の22点においては
水の接触角が約150度であったが、表面から12.5
mmを越える深さの3点においては、接触角は90度に
満たなかった。撥水性が発現している部分の詳細を調べ
るため、切断面の幅方向の中央において、厚さ方向に5
mm間隔で水の接触角を測定したところ、表面から20
mm以内である点では約150度であったが、中央部の
1点では90度に満たなかった。
The test piece obtained was cut at the central portion in the lengthwise direction, and two points near the outer surface (about 1 mm from the outer surface) in the widthwise direction on the cut surface having a width of 100 mm and a thickness of 50 mm and the widthwise direction at the central portion. 3 points at 25 mm intervals, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface) and 12.5 m in the center
The contact angle of water at a total of 25 points at 3 points at m intervals was measured with a contact angle meter (CA-DT type) manufactured by Kyowa Interface Science Co., Ltd., and water was detected at 22 points within 12.5 mm from the surface. Contact angle was about 150 degrees, but 12.5 from the surface
The contact angle was less than 90 degrees at three points with a depth exceeding mm. In order to investigate the details of the part where water repellency is expressed, 5 in the thickness direction at the center of the cut surface in the width direction.
When the contact angle of water was measured at mm intervals, it was 20
It was about 150 degrees at a point within mm, but it was less than 90 degrees at one point in the central portion.

【0042】[0042]

【比較例4】実施例4に記載した方法に対し、ヘキシル
トリエトキシシランと窒素との混合ガスを1回だけ反応
容器に送り込んだ段階での撥水性を調べたものである。
実施例1と同様の装置、軽量気泡コンクリート試験片を
用い、ガス溜め容器にヘキシルトリエトキシシラン25
gを入れ、容器内の空気を実施例1と同様に真空ポンプ
で排気した後、180℃に加熱した。ヘキシルトリエト
キシシランの蒸気圧は27000Paとなった。さら
に、このガス溜め容器中にキャリアガスとして窒素を注
入し、全体の圧力を100000Paまで上げた。一
方、反応容器に上記の軽量気泡コンクリート試験片を入
れ、180℃に加熱後、反応容器内を5000Paに減
圧した。その後、バルブを10秒間開放すると、両容器
の圧力差によってガス溜め容器から反応容器にヘキシル
トリエトキシシラン蒸気と窒素の混合ガスが流入し、反
応容器は52500Paとなった。バルブを閉じた後、
反応容器を180℃で1時間保持した。
COMPARATIVE EXAMPLE 4 In comparison with the method described in Example 4, the water repellency was examined when the mixed gas of hexyltriethoxysilane and nitrogen was fed into the reaction vessel only once.
Using a device similar to that of Example 1 and a lightweight cellular concrete test piece, hexyltriethoxysilane 25 was placed in a gas reservoir.
After adding g, the air in the container was evacuated by a vacuum pump as in Example 1, and then heated to 180 ° C. The vapor pressure of hexyltriethoxysilane was 27,000 Pa. Further, nitrogen was injected as a carrier gas into the gas reservoir to raise the total pressure to 100,000 Pa. On the other hand, the above lightweight cellular concrete test piece was placed in a reaction container, heated to 180 ° C., and the pressure inside the reaction container was reduced to 5000 Pa. After that, when the valve was opened for 10 seconds, a mixed gas of hexyltriethoxysilane vapor and nitrogen flowed into the reaction container from the gas reservoir container due to the pressure difference between both containers, and the reaction container became 52500 Pa. After closing the valve,
The reaction vessel was kept at 180 ° C. for 1 hour.

【0043】得られた試験片を長さ方向の中央部で切断
した幅100mm、厚さ50mmの切断面上を幅方向に
外表面近傍(外表面より約1mm)2点および中央部に
25mm間隔で3点、厚さ方向に外表面近傍(外表面よ
り約1mm)2点および12.5mm間隔で3点、合計
25箇所における水の接触角を、協和界面化学(株)製
の接触角計(CA-DT型)で測定したところ、表面から1
2.5mm以内の22点においては水の接触角が約15
0度であったが、表面から12.5mmを越える深さの
3点においては、接触角は90度に満たなかった。撥水
性が発現している部分の詳細を調べるため、切断面の幅
方向の中央において、厚さ方向に5mm間隔で水の接触
角を測定したところ、表面から20mm以内である点で
は約150度であったが、中央部の1点では90度に満
たなかった。
The obtained test piece was cut at the central portion in the lengthwise direction, and two points near the outer surface (about 1 mm from the outer surface) in the widthwise direction on the cut surface having a width of 100 mm and a thickness of 50 mm and a 25 mm interval at the central portion. At 3 points, 2 points near the outer surface in the thickness direction (about 1 mm from the outer surface), and 3 points at 12.5 mm intervals, for a total of 25 contact angles of water. When measured with (CA-DT type), 1 from the surface
At 22 points within 2.5 mm, the water contact angle is about 15
Although it was 0 degree, the contact angle was less than 90 degrees at three points with a depth exceeding 12.5 mm from the surface. In order to examine the details of the water-repellent part, the contact angle of water was measured at 5 mm intervals in the thickness direction at the center of the cut surface in the width direction, and it was about 150 degrees at a point within 20 mm from the surface. However, it was less than 90 degrees at one point in the central part.

【0044】[0044]

【発明の効果】本発明に記した方法によれば、軽量気泡
コンクリート表面および内部空隙表面にアルキルアルコ
キシシランからなる撥水層を形成することによって撥水
性能を発現する撥水性軽量気泡コンクリートの製造方法
において、同一のアルキルアルコキシシランに対して
は、従来よりも低温での処理が可能になる。さらには、
蒸気圧が低いために軽量気泡コンクリート内部まで蒸気
として浸透させることが困難であった、大きなアルキル
基を有するアルキルアルコキシシランを撥水剤として用
いることが容易になり、種々の撥水性軽量気泡コンクリ
ートをより簡単に製造可能である。
According to the method of the present invention, the production of a water-repellent lightweight cellular concrete that exhibits water-repellent performance by forming a water-repellent layer made of an alkylalkoxysilane on the surface of the lightweight cellular concrete and the surface of the internal voids. In the method, the same alkylalkoxysilane can be treated at a lower temperature than before. Moreover,
It was difficult to permeate the inside of lightweight cellular concrete as vapor due to its low vapor pressure. It became easy to use an alkylalkoxysilane having a large alkyl group as a water repellent, and various water repellent lightweight cellular concretes were It is easier to manufacture.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 アルキルアルコキシシラン蒸気を軽量気
泡コンクリートに接触させて、撥水性軽量気泡コンクリ
ートを製造する方法において、撥水層を形成しようとす
る軽量気泡コンクリートを反応容器内に配置した後に、
ガス溜め容器中のアルキルアルコキシシラン蒸気とキャ
リアガスの混合ガスの圧力が反応容器の圧力よりも高い
状態で、ガス溜め容器と反応容器とを遮断しているガス
開閉手段を開き、ガス溜め容器の混合ガスをその圧力差
によって、撥水層を形成しようとする軽量気泡コンクリ
ートが配置された反応容器内に流入させた後、ガス開閉
手段を閉め、ガス溜め容器内の混合ガスの圧力を、その
時点における反応容器内の圧力より高くし、再度ガス開
閉手段を開き、反応容器にガス溜め容器の混合ガスを流
入させる工程を、少なくとも一回行うことを特徴とす
る、撥水性の軽量気泡コンクリートの製造方法。
1. A method for producing a water-repellent lightweight cellular concrete by bringing an alkylalkoxysilane vapor into contact with the lightweight cellular concrete, after arranging the lightweight cellular concrete for forming a water-repellent layer in a reaction vessel,
When the pressure of the mixed gas of the alkylalkoxysilane vapor and the carrier gas in the gas storage container is higher than the pressure of the reaction container, open the gas opening / closing means that isolates the gas storage container from the reaction container, and open the gas storage container. After the mixed gas is caused to flow into the reaction container in which the lightweight cellular concrete to form the water repellent layer is placed by the pressure difference, the gas opening / closing means is closed, and the pressure of the mixed gas in the gas storage container is changed to The pressure in the reaction vessel at the time point is made higher, the gas opening / closing means is opened again, and the step of causing the mixed gas of the gas reservoir vessel to flow into the reaction vessel is performed at least once. Production method.
【請求項2】 アルキルアルコキシシラン蒸気を軽量気
泡コンクリートに接触させて、撥水性軽量気泡コンクリ
ートを製造する方法において、撥水層を形成しようとす
る軽量気泡コンクリートを反応容器内に配置した後に、
ガス溜め容器中のアルキルアルコキシシラン蒸気とキャ
リアガスの混合ガスの圧力が反応容器の圧力よりも高い
状態で、ガス溜め容器と反応容器とを遮断しているガス
開閉手段を開き、ガス溜め容器の混合ガスをその圧力差
によって、撥水層を形成しようとする軽量気泡コンクリ
ートが配置された反応容器内に流入させた後、ガス開閉
手段を閉め、反応容器を開放もしくは減圧にした後に、
再度ガス開閉手段を開き、反応容器にガス溜め容器内の
混合ガスを流入させる工程を、少なくとも一回行うこと
を特徴とする、撥水性の軽量気泡コンクリートの製造方
法。
2. A method for producing a water-repellent lightweight cellular concrete by bringing an alkylalkoxysilane vapor into contact with the lightweight cellular concrete, after arranging the lightweight cellular concrete for forming a water-repellent layer in a reaction vessel,
When the pressure of the mixed gas of the alkylalkoxysilane vapor and the carrier gas in the gas storage container is higher than the pressure of the reaction container, open the gas opening / closing means that isolates the gas storage container from the reaction container, and open the gas storage container. After the mixed gas is caused to flow into the reaction vessel in which the lightweight cellular concrete to form the water-repellent layer is placed by the pressure difference, after closing the gas opening / closing means and opening or reducing the pressure of the reaction vessel,
A method for producing a water-repellent lightweight cellular concrete, characterized in that the step of opening the gas opening / closing means again and injecting the mixed gas in the gas reservoir into the reaction vessel is performed at least once.
JP2001194676A 2001-06-27 2001-06-27 Method for producing water-repellent lightweight cellular concrete Expired - Fee Related JP4689091B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002761A (en) * 2001-06-25 2003-01-08 Asahi Kasei Corp Method for producing water-repellent lightweight cellular concrete
JP2007512217A (en) * 2003-11-28 2007-05-17 ライプニッツ−インスティトゥート フィア ノイエ マテリアーリエン ゲマインニュッツィゲ ゲゼルシャフト ミット ベシュレンクタ ハフトゥンク Insulation
JP2009126760A (en) * 2007-11-27 2009-06-11 Institute Of National Colleges Of Technology Japan Dyeing method of lightweight cellular concrete board for building wall material
JP2014521579A (en) * 2011-07-27 2014-08-28 エボニック デグサ ゲーエムベーハー Method for producing hydrophobic heat insulating molded body

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59116165A (en) * 1982-12-23 1984-07-04 旭硝子株式会社 Method of imparting “hot” water properties to lightweight cellular concrete
JPH06271371A (en) * 1993-03-19 1994-09-27 Nichias Corp Method for producing water repellent calcium silicate-based compact
JP2003002761A (en) * 2001-06-25 2003-01-08 Asahi Kasei Corp Method for producing water-repellent lightweight cellular concrete

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59116165A (en) * 1982-12-23 1984-07-04 旭硝子株式会社 Method of imparting “hot” water properties to lightweight cellular concrete
JPH06271371A (en) * 1993-03-19 1994-09-27 Nichias Corp Method for producing water repellent calcium silicate-based compact
JP2003002761A (en) * 2001-06-25 2003-01-08 Asahi Kasei Corp Method for producing water-repellent lightweight cellular concrete

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002761A (en) * 2001-06-25 2003-01-08 Asahi Kasei Corp Method for producing water-repellent lightweight cellular concrete
JP2007512217A (en) * 2003-11-28 2007-05-17 ライプニッツ−インスティトゥート フィア ノイエ マテリアーリエン ゲマインニュッツィゲ ゲゼルシャフト ミット ベシュレンクタ ハフトゥンク Insulation
JP2009126760A (en) * 2007-11-27 2009-06-11 Institute Of National Colleges Of Technology Japan Dyeing method of lightweight cellular concrete board for building wall material
JP2014521579A (en) * 2011-07-27 2014-08-28 エボニック デグサ ゲーエムベーハー Method for producing hydrophobic heat insulating molded body
US9233986B2 (en) 2011-07-27 2016-01-12 Evonik Degussa Gmbh Method for producing hydrophobic, heat-insulating mouldings
EP2736979B1 (en) * 2011-07-27 2016-04-27 Evonik Degussa GmbH Method for producing hydrophobic, heat-insulating mouldings

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