JPS6120512B2 - - Google Patents
Info
- Publication number
- JPS6120512B2 JPS6120512B2 JP5154678A JP5154678A JPS6120512B2 JP S6120512 B2 JPS6120512 B2 JP S6120512B2 JP 5154678 A JP5154678 A JP 5154678A JP 5154678 A JP5154678 A JP 5154678A JP S6120512 B2 JPS6120512 B2 JP S6120512B2
- Authority
- JP
- Japan
- Prior art keywords
- autoclave
- pressure
- temperature
- concrete
- 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
- 238000001723 curing Methods 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical group O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 229920006395 saturated elastomer Polymers 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 27
- 238000000576 coating method Methods 0.000 description 16
- 239000000843 powder Substances 0.000 description 13
- 239000011248 coating agent Substances 0.000 description 12
- 238000001035 drying Methods 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 7
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 239000004568 cement Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000010454 slate Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
【発明の詳細な説明】
本発明は、オートクレーブ養生処理されたコン
クリート製品が乾燥状態で、かつ高温度を保持し
た状態で取出されるようにした方法及び装置に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for removing autoclaved concrete products in a dry state and at a high temperature.
コンクリート製品のオートクレーブ養生は、コ
ンクリート製品の養生時間を著しく短縮し、型枠
の回転率、出荷効率等を向上し、経済性に有利な
ために多用されている。しかしこれらは単に養生
時間を短縮する目的のみで、養生処理された製品
は出来る限り低温冷却した後取出されることが殆
どである。そのために養生時間(通常飽和水蒸気
圧10〜15気圧で数時間)経過後単にオートクレー
ブ内の水蒸気を徐々に放出させながら、温度及び
圧力を低下せしめ、大気圧に達してから蓋を開放
して製品を取出す方法が実施されている。 Autoclave curing of concrete products is widely used because it significantly shortens the curing time of concrete products, improves formwork rotation rate, shipping efficiency, etc., and is economically advantageous. However, these methods are only for the purpose of shortening the curing time, and in most cases, the curing-treated products are cooled to as low a temperature as possible before being taken out. To do this, after curing time (usually several hours at a saturated steam pressure of 10 to 15 atm), the temperature and pressure are lowered while gradually releasing the steam inside the autoclave, and once atmospheric pressure is reached, the lid is opened and the product is finished. A method is being implemented to extract the
近年コンクリート製品としてスレート瓦、コン
クリート瓦が陶器瓦に代つてその良好な寸法安定
性と低価格のために利用度が増大している。しか
し、コンクリート製瓦そのまゝでは美観と耐水性
が劣るため、耐候性の良い合成樹脂(例えばウク
リル系塗料)の塗装されたものが使用されるよう
になつて来ている。 In recent years, slate tiles and concrete tiles have been increasingly used as concrete products, replacing ceramic tiles because of their good dimensional stability and low cost. However, concrete tiles as they are are inferior in appearance and water resistance, so tiles coated with weather-resistant synthetic resin (for example, Ukrylic paint) are being used.
この樹脂塗装は工場生産の場合、溶性塗料を用
いる場合は溶剤の揮散に伴う大気汚染の点で実施
が制限される傾向にあり、他方溶性塗料はコンク
リート中に含まれる水分とアルカリによつて塗膜
性能の発揮が阻害されやすく、取扱いに細心の注
意が要求され、これにともなつて不良品の発生が
多くなりやすいという欠点がある。これに対し、
粉体塗装はこのような問題が発生しないために近
年脚光をあびつつある。しかしこの粉体塗装にお
いては、粉体塗着後の溶融成膜に際し、コンクリ
ート製品中に含有される吸蔵気体及び水分の加熱
による気化膨張によつて溶融した塗膜中に泡が発
生し、樹脂膜の泡突起部分の機械的安定性の不
良、この部分の欠落による耐水性の低下はもとよ
り著しく美感を損つた製品となり易い欠点があつ
た。このため、コンクリート瓦を高温に加熱し包
蔵水分の大部分を揮散せしめた後、昇温すること
なく粉体樹脂を塗着融着せしめ成膜硬化すること
によつて気泡のない樹脂塗膜を形成する方法も提
案されている。 When this resin coating is produced in a factory, the use of soluble paint tends to be restricted due to the air pollution caused by the volatilization of the solvent. The disadvantage is that the performance of the membrane is easily inhibited, careful handling is required, and as a result, the number of defective products is likely to increase. In contrast,
Powder coating has been gaining attention in recent years because it does not cause such problems. However, in this powder coating, bubbles are generated in the molten coating film due to vaporization expansion due to heating of occluded gases and moisture contained in the concrete product during melt film formation after powder coating, and the resin In addition to the poor mechanical stability of the foam protrusion portion of the membrane and the drop in water resistance due to the lack of this portion, there were also disadvantages in that the product was likely to have a significantly poor aesthetic appearance. For this reason, after heating the concrete tile to a high temperature to volatilize most of the contained moisture, a resin coating without bubbles is created by applying powdered resin, fusing and curing the concrete tile without raising the temperature. A method for forming such a structure has also been proposed.
上述の如きセメント瓦は通常常圧蒸気養生と水
中養生または常圧蒸気養生とオートクレーブ養生
によつて製造されているが、現在、オートクレー
ブ処理工程と粉体塗装工程とを有機的に結合され
た堤案は殆ど考慮されず、常法によつてオートク
レーブ処理された製品を一度冷却した後、或いは
オートクレーブ内圧が大気圧に達した後、製品を
取出し、直ちに高温加熱炉に導入し脱水工程を経
た後、粉体樹脂塗装工程によつて処理する提案が
現在かなり合理的なものとされている。通常のオ
ートクレーブ養生したセメント瓦は、オートクレ
ーブより取出した直後の含有水分が3〜4%程度
であつて、水中養生したセメント瓦の含有水分7
〜12%に比較すればかなりの改善が認められる。
しかし粉体塗装に要求される含有水分は1%以下
このましくは0.5%以下であつて、この状態まで
乾燥させるには尚かなりの乾燥設備が必要とな
る。 Cement roof tiles such as those mentioned above are usually manufactured by atmospheric pressure steam curing and underwater curing, or normal pressure steam curing and autoclave curing, but currently, cement roof tiles are manufactured by organically combining the autoclave treatment process and the powder coating process. This idea is rarely considered, and after the product has been autoclaved in a conventional manner and once cooled, or after the internal pressure of the autoclave has reached atmospheric pressure, the product is taken out and immediately introduced into a high-temperature heating furnace to undergo a dehydration process. , the proposal of processing by a powder resin coating process is currently considered to be quite reasonable. A normal cement tile cured in an autoclave has a moisture content of about 3 to 4% immediately after being removed from the autoclave, while a cement tile cured in water has a moisture content of 7%.
This is a considerable improvement compared to ~12%.
However, the moisture content required for powder coating is 1% or less, preferably 0.5% or less, and a considerable amount of drying equipment is required to dry the powder to this state.
以上の如き現状において、本発明においては、
オートクレーブ養生後のコンクリート製品を取り
出す際に、該製品の温度を低下することなく、直
ちに粉体塗装の可能な包蔵水分1〜0.5%以下の
乾燥状態でオートクレーブ容器より製品を取り出
す方法を提案するものであつて、製品取出後直ち
に粉体塗装工程に導入することにより、粉体塗装
前の予備乾燥加熱処理行程を著しく短縮するか、
或いは全く省略することが可能となる新しいオー
トクレーブ処理方法および該装置を提案するもの
である。 In the current situation as described above, in the present invention,
This project proposes a method for taking out a concrete product from an autoclave container after curing in an autoclave, without lowering the temperature of the product, and in a dry state with a potential moisture content of 1 to 0.5% or less, which allows immediate powder coating. By introducing it into the powder coating process immediately after taking out the product, the pre-drying heat treatment process before powder coating can be significantly shortened, or
Alternatively, we propose a new autoclave processing method and apparatus that can be omitted entirely.
すなわち、本発明の方法は、コンクリート成型
物をオートクレーブ内において高温高圧の飽和水
蒸気圧下に数時間保持してコンクリートの養生硬
化が終了し、製品を取り出す際に、オートクレー
ブ内の加圧水蒸気を外部に徐々に放出する際に、
高温度の加圧ガス(空気、CO2等)を徐々に導入
して、オートクレーブ内の水蒸気を高温乾燥ガス
と置換せしめながら徐々にオートクレーブ内の圧
力を低下せしめ、これが大気圧に達した後、オー
トクレーブの蓋を開きコンクリート製品を取り出
す方法である。この方法によつて、コンクリート
製品の含水率が1%以下に乾燥させた、しかも高
い温度を維持した製品が得られるという特徴を有
し、粉体塗装に必要な乾燥と高温の状態が一挙に
得られ、直ちにこの粉体塗装工程への移行を可能
にするものである。 That is, in the method of the present invention, a concrete molded product is held in an autoclave under high temperature and high pressure saturated steam pressure for several hours to complete curing and hardening of the concrete, and when the product is taken out, the pressurized steam in the autoclave is gradually released to the outside. When releasing into
High-temperature pressurized gas (air, CO 2 , etc.) is gradually introduced to replace the water vapor in the autoclave with high-temperature dry gas, and the pressure inside the autoclave is gradually lowered. After this reaches atmospheric pressure, This method involves opening the autoclave lid and taking out the concrete product. This method has the characteristic that it is possible to obtain concrete products that are dried to a moisture content of 1% or less while maintaining a high temperature, and the drying and high temperature conditions required for powder coating are all achieved at once. This allows immediate transition to the powder coating process.
上記本発明方法において、オートクレーブ内水
蒸気を外部に放出すと同時に高温高圧の乾燥ガス
を導入することにより、オートクレーブ内におい
て圧力の急激な低下と温度低下が抑制されると同
時に水蒸気成分のみが徐々に低下する。この水蒸
気成分の低下は、高い含水率のコンクリート製品
中の水分を気化放出するように作用し、該製品の
乾燥作用が進行する。最終的にはオートクレーブ
内には乾燥ガスで置換された状態に達するため
に、コンクリート製品の水蒸気は著しく低下し、
乾燥された状態となるのである。 In the above method of the present invention, by releasing the water vapor inside the autoclave to the outside and simultaneously introducing high-temperature, high-pressure drying gas, a sudden drop in pressure and temperature within the autoclave is suppressed, and at the same time only the water vapor component is gradually removed. descend. This reduction in water vapor content acts to evaporate and release moisture in concrete products with a high moisture content, and the drying action of the products progresses. Eventually, the autoclave reaches a state where it is replaced with dry gas, so the water vapor in the concrete product decreases significantly.
It will be in a dry state.
コンクリート製品の温度はオートクレーブ内温
度すなわちオートクレーブ内に導入される乾燥ガ
スの温度以下に低下しないので、この導入ガスの
温度を調節することによつて、コンクリート製品
の取出温度を調整することができる。なお、この
乾燥ガスの加熱は、オートクレーブ内の圧力以上
加圧された乾燥ガスを、オートクレーブより放出
される加圧水蒸気と熱交換させることにより、こ
の水蒸気温度程度にまで他の加熱源を用いること
なく効率的に加熱することが出来るので、極めて
経済的に実施することが可能となる。 Since the temperature of the concrete product does not fall below the temperature inside the autoclave, that is, the temperature of the drying gas introduced into the autoclave, the temperature at which the concrete product is taken out can be adjusted by adjusting the temperature of the introduced gas. The drying gas is heated by exchanging heat between the drying gas, which is pressurized above the pressure inside the autoclave, and the pressurized steam released from the autoclave, so that the temperature of this steam can be reached without using any other heating source. Since heating can be performed efficiently, it can be carried out extremely economically.
オートクレーブ内の圧力を低下させるには、コ
ンクリート製品の取出しに高温度が必要な場合に
は、この温度に加熱された乾燥加圧ガスをオート
クレーブ内に導入し、かつ、オートクレーブ内部
の水蒸気濃度が著しく低下した状態に達した後、
乾燥加圧ガスの導入を止め、オートクレーブ内の
ガスを徐々に放出すると、オートクレーブ内の温
度を低下することなく、圧力のみを低下すること
ができる。この場合の圧力低下速度は、コンクリ
ート製品中の水分が殆ど無い状態なのでコンクリ
ート製品中のガス急激膨張による爆裂現象が起り
難いので通常の場合にくらべかなり速かに低下さ
せることができる。 In order to reduce the pressure inside the autoclave, if a high temperature is required to take out the concrete product, dry pressurized gas heated to this temperature is introduced into the autoclave, and the water vapor concentration inside the autoclave is significantly reduced. After reaching a degraded state,
By stopping the introduction of dry pressurized gas and gradually releasing the gas inside the autoclave, only the pressure can be lowered without lowering the temperature inside the autoclave. The rate of pressure drop in this case can be reduced much faster than in normal cases, since there is almost no moisture in the concrete product, so explosion phenomena due to rapid expansion of gas in the concrete product are unlikely to occur.
また、コンクリート製品取出温度が低い場合、
乾燥加圧ガスを初めから導入せずに、まづオート
クレーブ内加圧水蒸気を放出して、オートクレー
ブ内の温度がほぼ必要温度に低下した後、この温
度の乾燥加圧ガスを導入し、オートクレーブ内の
蒸気濃度が低下後、減圧操作を行うことによつ
て、必要温度の製品を取出すことができる。この
場合、乾燥加圧ガスの圧力は高い圧力の必要がな
く、必要とする温度の飽和水蒸気圧より多少高め
の圧力でよい。 In addition, if the concrete product removal temperature is low,
Without introducing dry pressurized gas from the beginning, first release the pressurized steam inside the autoclave, and after the temperature inside the autoclave has decreased to almost the required temperature, dry pressurized gas at this temperature is introduced, and the pressure inside the autoclave is After the vapor concentration has decreased, the product at the required temperature can be taken out by performing a pressure reduction operation. In this case, the pressure of the dry pressurized gas does not need to be high, and may be slightly higher than the saturated water vapor pressure at the required temperature.
なお、この場合、最初から高圧乾燥ガスを導入
しても支障なく、ガス温度のみ必要な温度附近に
調節したガを導入するとよい。 In this case, there is no problem even if high-pressure drying gas is introduced from the beginning, and it is preferable to introduce only the gas temperature adjusted to around the required temperature.
また、高温度の加圧ガスとしてCO2あるいは燃
焼ガス等を使用した場合には、コンクリート製品
の表面あるいは表面近傍の水酸化カルシウムなど
のアルカリ成分はガス中のCO2あるいはその他の
酸性ガス成分によつて中和されてアルカリ度が低
下する。このために、粉体塗装後の塗膜の接着
力、耐久性が向上する。 In addition, when CO 2 or combustion gas is used as a high-temperature pressurized gas, alkaline components such as calcium hydroxide on or near the surface of concrete products are converted to CO 2 or other acidic gas components in the gas. As a result, it is neutralized and the alkalinity decreases. For this reason, the adhesion and durability of the coating film after powder coating are improved.
以上の如き本発明方法を実施するためのオート
クレーブ装置は、図の如く、加圧水蒸気発生用ボ
イラー1とオートクレーブ容器3とをバルブ2を
介して連結し、水蒸気排出管4のバルブ5を容器
側3に設けた熱交換器6(通常ドレイントラツプ
を設けるが図示しない)と被加熱側の加圧ガス源
7(通常エアーコンプレツサー)とを導管8で連
結し、加熱ガス系側の導管9は保温され、バルブ
10を介して容器3に連結されれたものである。
なお、容器3には温度計11と湿度計12とを設
ける。 As shown in the figure, an autoclave apparatus for carrying out the method of the present invention as described above connects a boiler 1 for pressurized steam generation and an autoclave container 3 via a valve 2, and connects a valve 5 of a steam discharge pipe 4 to a container side 3. A conduit 8 connects a heat exchanger 6 (usually equipped with a drain trap, not shown) and a pressurized gas source 7 (usually an air compressor) on the side to be heated, and a conduit 9 on the heating gas system side. is kept warm and connected to the container 3 via a valve 10.
Note that the container 3 is provided with a thermometer 11 and a hygrometer 12.
加圧ガス源7にエアーコンプレツサーを用いた
ときは導管8の途中にドレイントラツプ、あるい
は他に脱湿器を設ける。なお、ガス源7に乾燥さ
れた窒素、炭酸ガス、その他の高圧ガス(通常ボ
ンベ)を用いる場合には脱湿器は不要である。 When an air compressor is used as the pressurized gas source 7, a drain trap or other dehumidifier is provided in the middle of the conduit 8. Note that when using dried nitrogen, carbon dioxide, or other high-pressure gas (usually in a cylinder) as the gas source 7, a dehumidifier is not necessary.
添付図面は本発明のコンクリート製品の養生装
置の実施例を示す概略図である。
1……加圧水蒸気発生用ボイラー、2……バル
ブ、3……オートクレーブ容器、4……水蒸気排
出管、5……バルブ、6……熱交換器、7……加
圧ガス源、10……バルブ、11……温度計、1
2……湿度計。
The accompanying drawings are schematic diagrams showing an embodiment of the concrete product curing device of the present invention. DESCRIPTION OF SYMBOLS 1... Boiler for pressurized steam generation, 2... Valve, 3... Autoclave container, 4... Steam discharge pipe, 5... Valve, 6... Heat exchanger, 7... Pressurized gas source, 10... Valve, 11...Thermometer, 1
2...Hygrometer.
Claims (1)
いて、高温、高圧の飽和水蒸気圧下に保持し養生
時間経間後オートクレーブ内の圧力を低減するよ
うに際し、オートクレーブ内の残留水蒸気を外部
に放出すると同時に、高温の乾燥加圧ガスをオー
トクレーブ内に導入しながらオートクレーブ内の
水蒸気を高温乾燥ガスと置換せしめつつ、オート
クレーブ内圧力を低下せしめ、大気圧に達した後
オートクレーブの蓋を開いて高温のコンクリート
養生処理物を取り出すことを特徴とするコンクリ
ート製品の養生方法。 2 オートクレーブ内に導入される高温乾燥加圧
ガスがコンプレツサーで加圧された空気を、オー
トクレーブより排出される水蒸気と熱交換せしめ
たガスであることを特徴とする特許請求の範囲第
1項記載のコンクリート製品の養生方法。 3 オートクレーブ容器3にバルブ2を介して加
圧水蒸気発生用ボイラ1を接続すると共に、バル
ブ5付の水蒸気排出管4を接続し、又該オートク
レーブ容器3にバルブ10を介して加圧ガス源7
を接続したコンクリート製品の養生装置。 4 特許請求の範囲第3項記載のコンクリート製
品の養生装置であつて、該蒸気排出管4と加圧ガ
ス源2とが熱交換器6を介して互に結合されてい
るコンクリート製品の養生装置。[Claims] 1. When a concrete molded product is held in an autoclave at high temperature and high pressure under saturated steam pressure, and when the pressure in the autoclave is reduced after a curing period, the residual steam in the autoclave is released to the outside. At the same time, high-temperature dry pressurized gas is introduced into the autoclave to replace the water vapor in the autoclave with high-temperature dry gas, reducing the pressure inside the autoclave, and after reaching atmospheric pressure, the autoclave lid is opened and the high-temperature concrete is heated. A method for curing concrete products, characterized by taking out a cured product. 2. The high temperature dry pressurized gas introduced into the autoclave is a gas obtained by heat-exchanging air pressurized by a compressor with water vapor discharged from the autoclave. Curing method for concrete products. 3 Connect the boiler 1 for pressurized steam generation to the autoclave container 3 via the valve 2, connect the steam discharge pipe 4 with the valve 5, and connect the pressurized gas source 7 to the autoclave container 3 via the valve 10.
A curing device for concrete products connected to 4. A curing device for concrete products according to claim 3, wherein the steam exhaust pipe 4 and the pressurized gas source 2 are connected to each other via a heat exchanger 6. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5154678A JPS54143426A (en) | 1978-04-28 | 1978-04-28 | Curing concrete product and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5154678A JPS54143426A (en) | 1978-04-28 | 1978-04-28 | Curing concrete product and apparatus therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54143426A JPS54143426A (en) | 1979-11-08 |
| JPS6120512B2 true JPS6120512B2 (en) | 1986-05-22 |
Family
ID=12890011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5154678A Granted JPS54143426A (en) | 1978-04-28 | 1978-04-28 | Curing concrete product and apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS54143426A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3326492C2 (en) * | 1983-07-22 | 1986-10-30 | Sicowa Verfahrenstechnik für Baustoffe GmbH & Co KG, 5100 Aachen | Process for hardening moldings made from binder-containing, porous lightweight building materials |
| JPH01242450A (en) * | 1988-03-22 | 1989-09-27 | Sekisui Chem Co Ltd | Production of fiber reinforced and hardened cement body |
| JP4694937B2 (en) * | 2005-10-03 | 2011-06-08 | 学校法人 中央大学 | Curing method in the manufacture of highly durable cement-based molded products |
-
1978
- 1978-04-28 JP JP5154678A patent/JPS54143426A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54143426A (en) | 1979-11-08 |
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