JPH0380141A - Production of extrusion-molded cement product - Google Patents
Production of extrusion-molded cement productInfo
- Publication number
- JPH0380141A JPH0380141A JP21241989A JP21241989A JPH0380141A JP H0380141 A JPH0380141 A JP H0380141A JP 21241989 A JP21241989 A JP 21241989A JP 21241989 A JP21241989 A JP 21241989A JP H0380141 A JPH0380141 A JP H0380141A
- Authority
- JP
- Japan
- Prior art keywords
- cement
- asbestos
- extrusion
- extrusion molding
- blast furnace
- 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.)
- Pending
Links
- 239000004568 cement Substances 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 238000001125 extrusion Methods 0.000 claims abstract description 23
- 239000010425 asbestos Substances 0.000 claims abstract description 21
- 229910052895 riebeckite Inorganic materials 0.000 claims abstract description 21
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 239000002893 slag Substances 0.000 claims abstract description 11
- 229920013820 alkyl cellulose Polymers 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims description 10
- 235000012438 extruded product Nutrition 0.000 claims description 5
- 239000012783 reinforcing fiber Substances 0.000 claims description 5
- 238000000465 moulding Methods 0.000 abstract description 16
- 230000020169 heat generation Effects 0.000 abstract description 6
- 125000002768 hydroxyalkyl group Chemical group 0.000 abstract description 3
- 229920000049 Carbon (fiber) Polymers 0.000 abstract description 2
- 239000003513 alkali Substances 0.000 abstract description 2
- 239000004917 carbon fiber Substances 0.000 abstract description 2
- 239000010440 gypsum Substances 0.000 abstract description 2
- 229910052602 gypsum Inorganic materials 0.000 abstract description 2
- 239000012779 reinforcing material Substances 0.000 abstract 1
- 238000004904 shortening Methods 0.000 abstract 1
- 239000000835 fiber Substances 0.000 description 16
- 229920003086 cellulose ether Polymers 0.000 description 4
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 description 4
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 description 3
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229920000609 methyl cellulose Polymers 0.000 description 3
- 239000001923 methylcellulose Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- -1 etc. added thereto Substances 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 description 1
- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 1
- 229920001479 Hydroxyethyl methyl cellulose Polymers 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 238000009408 flooring Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 description 1
- 229920013819 hydroxyethyl ethylcellulose Polymers 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 239000000021 stimulant Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【発明の詳細な説明】
(従来の技術)
近年、セメントに対し20重量部程度のアスベスト繊維
、骨材等を添加した混合物に水を添加混練したものを所
望の形状のダイス形状に押出成形することによって作ら
れたセメント板体及び、アスベスト/セメント板等が、
建築物の外壁材、屋根材、床材等に用いられている。[Detailed Description of the Invention] (Prior Art) In recent years, a mixture of cement with about 20 parts by weight of asbestos fibers, aggregates, etc. added thereto, water added and kneaded, is extruded into a die shape of a desired shape. Cement boards and asbestos/cement boards made by
It is used for building exterior wall materials, roofing materials, flooring materials, etc.
かかる卯出成形品の製造において使用されるアスベスト
繊維は補強繊維として添加した場合、混練物中の分散が
極めてよく、さらに押出成形物に与える保形性能に優れ
、また保水性能も保有している。またかかる押出成形品
の寸法安定性の付与ならびに必要強度形成のため行う1
70°C以上の高温度における水蒸気圧力釜による養生
においても、アスベストが有する耐熱性により、強度補
強繊維としての充分な効果を発揮することができる。When added as reinforcing fibers, the asbestos fibers used in the production of such undeformed products are extremely well dispersed in the kneaded material, and have excellent shape-retaining properties for extruded products, as well as water-retaining properties. . In addition, 1 is carried out in order to impart dimensional stability to such extruded products and to form the necessary strength.
Even during curing in a steam pressure cooker at a high temperature of 70° C. or higher, asbestos' heat resistance allows it to exhibit sufficient effects as a strength-reinforcing fiber.
上記に示すような、押出成形体製造に必要となる補強繊
維性能、すなわち分散性、保形性、保水性、耐熱性を同
時に有する繊維としてアスベストは他に類のない繊維と
してもっばら押出成形用の補強繊維として使われている
。Asbestos is a unique fiber that is especially suitable for extrusion molding as a fiber that simultaneously has the reinforcing fiber properties required for the production of extrusion moldings, such as dispersibility, shape retention, water retention, and heat resistance, as shown above. It is used as a reinforcing fiber.
しかしながら、近年アスベストの有する独特な繊維形状
に起因するとみられるところの発ガン性が問題となって
おり、アスベストを用いないか、もしくはその添加量を
極力少なくした系で良好な押出成形体を得る技術の完成
が望まれている。石綿に変わる繊維としては、すてに有
機系の繊維が検討されてきているが、いずれも分散性が
悪くアスベスト繊維に変えて押出成形を行おうとすると
、アスベスト使用時に比べて成形機内での発熱量が多く
、そのためセメント質材料の硬化が速まり成形機内でセ
メントが硬化してしまい成形途中で成形が不可能となる
ことが多い。However, in recent years, carcinogenicity, which is thought to be caused by the unique fiber shape of asbestos, has become a problem, and good extrusion molded products can be obtained by using systems that do not use asbestos, or that add as little amount of asbestos as possible. It is hoped that the technology will be perfected. Organic fibers have been considered as fibers to replace asbestos, but all of them have poor dispersibility and when extrusion molding is attempted in place of asbestos fibers, they generate more heat in the molding machine than when asbestos is used. Since the amount is large, the hardening of the cementitious material is accelerated and the cement hardens in the molding machine, often making molding impossible during the molding process.
一方アスベスト含有のセメント押出成形においても押出
成形時にはその戊形用組成物に多くの圧力がかかり、ア
スベストの有する保水能だけては成形体内に均一に水を
保水させ良好な押出成形をすることができないので、押
出成形体が凝結固化するまでの間組成物同士を粘着させ
、押出成形ダイス形状で吐出した成形体をその形状のま
ま保持するため、有機系のバインダーが使用される。こ
れらバインダーとして特公昭43−7134にあるよう
なメチルセルロース、ヒドロキシプロピルメチルセルロ
ース、ポリエチレンオキサイド、ヒドロキシエチルセル
ロース、カルホキジメチルヒドロキシエチルセルロース
などの水溶性セルロスエーテル、ポリアクリル酸ソーダ
、カゼイン等が提唱され、なかでもセメント、骨材等の
分散性能にすぐれ、保水性能と粘着性に優れるアルキル
セルロース及び/またはヒドロキシアルキルアルキルセ
ルロースがもっばら使用されている。また、これらを添
加するとセメントの凝結時間に遅れが生じることが特開
昭55−19581に記載されており、押出成形中に成
形組成物が硬化して成形困難となるのを防ぐためのセル
ロースエーテルの使用も提唱されている。従ってこれら
セルロースエーテルを添加することである程度の硬化遅
延が図られ成形機内での発熱によるトラブルを解消でき
ることは周知のことである。またカルシュラム塩などの
セメント硬化遅延剤等を添加してセメントの硬化時間を
遅らせることも行われている。On the other hand, even in the extrusion molding of cement containing asbestos, a lot of pressure is applied to the shaping composition during extrusion molding, and asbestos' water retention ability alone makes it difficult to uniformly retain water within the molded body and perform good extrusion molding. Since this is not possible, an organic binder is used in order to make the compositions adhere to each other until the extrudate is solidified and to maintain the shape of the molded product discharged from the extrusion molding die. As these binders, water-soluble cellulose ethers such as methylcellulose, hydroxypropylmethylcellulose, polyethylene oxide, hydroxyethylcellulose, and carboxydimethylhydroxyethylcellulose, sodium polyacrylate, and casein have been proposed as described in Japanese Patent Publication No. 43-7134, among others. Alkyl cellulose and/or hydroxyalkylalkyl cellulose are often used because they have excellent dispersion performance for cement, aggregate, etc., and excellent water retention performance and adhesiveness. Furthermore, it is stated in JP-A-55-19581 that the addition of these substances causes a delay in the setting time of cement, and that cellulose ether is used to prevent the molding composition from hardening during extrusion molding, making molding difficult. The use of has also been proposed. Therefore, it is well known that by adding these cellulose ethers, curing can be delayed to some extent and troubles caused by heat generation in the molding machine can be solved. Additionally, cement hardening retarders such as calsulam salt are added to delay the hardening time of cement.
(発明が解決しようとする課題)
しかしながら50°C以上もの発熱が予想されるような
アスベスト以外の繊維を使った押出成形等ではこれらの
添加剤による押出成形を可能とするためにはこれらの添
加剤を1%以上添加する必要があり原料コスト的にも不
利となったり、有機物が多くセメント硬化体に混入する
のは成形体の耐久性のためにも好ましくなく、これら有
機物を極力添加せず硬化時間を遅らせることができる成
形方法の完成が望まれていた。(Problem to be solved by the invention) However, in extrusion molding using fibers other than asbestos where heat generation of 50°C or more is expected, these additives must be added to enable extrusion molding. It is necessary to add 1% or more of the agent, which is disadvantageous in terms of raw material cost, and it is undesirable for the durability of the molded product to have a large amount of organic matter mixed in with the hardened cement product, so these organic materials are not added as much as possible. It has been desired to complete a molding method that can delay curing time.
(課題を解決するための手段)
本発明者らはこれら事実に鑑み鋭意検討した結果高炉ス
ラグ/セメント重量比を70/30−90710として
混合した材料を用い、かつこの混合材料100重量部に
対してアルキルセルロース及び/またはヒドロキシアル
キルアルキルセルロスを03−2重量%使用して押出成
形し、10000以上の温度でオートクレーブ養生する
ことでアスベスト以外の代替繊維を含む押出成形におい
て、50℃を越えるような発熱があっても成形機内での
硬化が生じることなく、かつ強度ある成形体ができるこ
とをみいだし本発明を完成した。(Means for Solving the Problems) The inventors of the present invention have made extensive studies in view of these facts, and have found that, using a material mixed with a blast furnace slag/cement weight ratio of 70/30-90710, and based on 100 parts by weight of this mixed material, Extrusion molding using 03-2% by weight of alkyl cellulose and/or hydroxyalkylalkyl cellulose and curing in an autoclave at a temperature of 10,000 or higher allows extrusion molding containing alternative fibers other than asbestos to exceed 50 °C. We have completed the present invention by discovering that even with excessive heat generation, hardening does not occur in the molding machine and a strong molded product can be produced.
高炉スラグと水の混合物は一般にアルカリ性の刺激剤の
存在のもとで硬化して必要な強度がでる無機材料として
知られている。一般にその高炉スラグのセメントに対す
る割合として70%以下として使用しないと必要な強度
がある硬化体ができないとされている。本発明者らはこ
の高炉スラグ/セメント比を検討した結果、高炉スラグ
の量が70%−90%である高炉スラグ/セメント混合
材料においても、アルキルセルロース/及びまたはヒド
ロキシアルキルアルキルセルロースを添加して成形しオ
ートクレーブで100℃以上の温度で加圧養生すること
で、充分な強度のでる成形体ができることをみいだした
。A mixture of blast furnace slag and water is generally known as an inorganic material that hardens in the presence of alkaline stimulants to develop the necessary strength. Generally, it is said that unless the ratio of blast furnace slag to cement is 70% or less, a hardened product with the necessary strength cannot be obtained. As a result of studying this blast furnace slag/cement ratio, the present inventors found that even in a blast furnace slag/cement mixed material in which the amount of blast furnace slag is 70% to 90%, alkyl cellulose/and hydroxyalkyl alkyl cellulose can be added. It has been found that by molding and curing under pressure in an autoclave at a temperature of 100°C or higher, a molded product with sufficient strength can be produced.
高炉スラグ量が70%以下であると50°C以上に成形
体が成形機内で暖められた時の硬化時間の遅れが少なく
本発明の目的を達しない。If the amount of blast furnace slag is less than 70%, the object of the present invention will not be achieved because there will be too little delay in curing time when the compact is heated in the molding machine to 50° C. or higher.
一方、成形直後の成形体の初期強度を得るべく石膏等の
アルカリ刺激剤を適当量好ましくは1050%の範囲で
使用することは本発明の目的を阻害するものではない。On the other hand, the use of an appropriate amount of an alkaline stimulant such as gypsum, preferably in the range of 1050%, in order to obtain the initial strength of the molded product immediately after molding does not impede the object of the present invention.
本発明で使用するアルキルセルロース及びまたはヒドキ
シアルキルアルキルセルロースとしては、メチルセルロ
ース、エチルセルロース、ヒドロキシエチルメチルセル
ロス、ヒドロキシプロピルメチルセルロース、ヒドロキ
シエチルエチルセルロース等の水に溶けるものはいずれ
も使用できる。これらセルロースエテルの添加量として
は高炉スラグ/セメント混合物100重量部に対して0
3−2重量%が望ましい。03%以下であると、成形物
に充分な保水性を与えず成形困難である。また、2重量
%を越えることはコスト的に不利となるばかりでなく、
成形体の強度が弱くなることがあり好ましくない。As the alkylcellulose and/or hydroxyalkylalkylcellulose used in the present invention, any water-soluble cellulose such as methylcellulose, ethylcellulose, hydroxyethylmethylcellulose, hydroxypropylmethylcellulose, and hydroxyethylethylcellulose can be used. The amount of these cellulose ethers added is 0 to 100 parts by weight of the blast furnace slag/cement mixture.
3-2% by weight is desirable. If it is less than 0.03%, the molded product will not have sufficient water retention properties and will be difficult to mold. Moreover, exceeding 2% by weight is not only disadvantageous in terms of cost, but also
This is not preferable because the strength of the molded product may become weak.
本発明で使用するアスベスト代替繊維としては耐熱温度
が高いカーボン繊維、耐アルカリガラス繊維、アラミド
繊維、ロックウール等の繊維が好ましいが低温でオート
クレーブ養生すれば本発明の効果が発揮できることから
、比較的耐熱温度の低い粉砕パルプ繊維、ポリプロピレ
ン繊維、ポリヒニルアルコール繊維等があげられる。添
加量としては2−20重量%が好ましい。As the asbestos substitute fiber used in the present invention, fibers such as carbon fiber, alkali-resistant glass fiber, aramid fiber, and rock wool, which have a high heat resistance temperature, are preferable. Examples include pulverized pulp fibers, polypropylene fibers, and polyhinyl alcohol fibers that have low heat resistance. The amount added is preferably 2-20% by weight.
また本発明はアスベストのみの添加で添加量を多くして
成形中に発熱が高くなる場合にも有用となる。The present invention is also useful when only asbestos is added in a large amount, resulting in high heat generation during molding.
(実施例) 以下本発明を実施例及び比較例により説明する。(Example) The present invention will be explained below with reference to Examples and Comparative Examples.
実施例1〜4及び比較例1.2
表1配合による混合物を双腕型ニーダ−により混練し、
石川時(株)製真空押出成形機Y−22型より幅75m
m厚み6mmのシートを押出成形し、成形性を比較した
。Examples 1 to 4 and Comparative Example 1.2 The mixtures according to the formulations in Table 1 were kneaded using a double-arm kneader,
Width 75m from Y-22 type vacuum extrusion molding machine manufactured by Ishikawa Toki Co., Ltd.
A sheet with a thickness of 6 mm was extrusion molded, and the moldability was compared.
バインダ
l)信越化学工業(株)製 90SH−100000ヒ
ドロキシプロピルメチルセルロース(HPMC)2)信
越化学工業(株)製 5M−8000メチルセルロー
ス(MC)
本発明に該当する実施例1〜4は比較例1.2に対し、
成形機内温度が50°C以上の高温においても押出成形
物の硬化を生じることなく、良好な押出成形性が得られ
た。Binder 1) 90SH-100000 hydroxypropyl methylcellulose (HPMC, manufactured by Shin-Etsu Chemical Co., Ltd.) 2) 5M-8000 methylcellulose (MC, manufactured by Shin-Etsu Chemical Co., Ltd.) Examples 1 to 4 corresponding to the present invention are Comparative Example 1. For 2,
Good extrusion moldability was obtained without causing any hardening of the extruded product even when the temperature inside the molding machine was as high as 50° C. or higher.
(発明の効果)
本発明の押出成形方法によれば、分散の悪いアスベスト
代替繊維を用いたノンアスベスト押出成形において、成
形機内での発熱による無機質硬化時間の早まりを極力少
なくして成形機内での閉塞による押出成形不能トラブル
をなくすことができる。(Effects of the Invention) According to the extrusion molding method of the present invention, in non-asbestos extrusion molding using asbestos substitute fibers with poor dispersion, the acceleration of the inorganic curing time due to heat generation in the molding machine is minimized, and the inorganic curing time is minimized. It is possible to eliminate troubles in which extrusion cannot be performed due to blockages.
Claims (1)
いて、高炉スラグ/セメント重量比を70/30−90
/10として混合した材料と、この混合材料100重量
部に対して0.3−2重量%のアルキルセルロース及び
/またはヒドロキシアルキルアルキルセルロースとを含
む押出成形用組成物を所望の形状に押出成形した後、オ
ートクレーブで100℃以上の温度で加圧養生して押出
成形体を硬化させるセメント押出成形物の製造方法1. In extrusion molding containing reinforcing fiber materials other than asbestos, the blast furnace slag/cement weight ratio is 70/30-90.
An extrusion molding composition containing 0.3-2% by weight of alkylcellulose and/or hydroxyalkylalkylcellulose based on 100 parts by weight of this mixed material was extruded into a desired shape. A method for producing a cement extruded product, which is then cured under pressure in an autoclave at a temperature of 100°C or higher to harden the extruded product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21241989A JPH0380141A (en) | 1989-08-18 | 1989-08-18 | Production of extrusion-molded cement product |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21241989A JPH0380141A (en) | 1989-08-18 | 1989-08-18 | Production of extrusion-molded cement product |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0380141A true JPH0380141A (en) | 1991-04-04 |
Family
ID=16622277
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21241989A Pending JPH0380141A (en) | 1989-08-18 | 1989-08-18 | Production of extrusion-molded cement product |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0380141A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5545297A (en) * | 1992-08-11 | 1996-08-13 | E. Khashoggi Industries | Methods for continuously placing filaments within hydraulically settable compositions being extruded into articles of manufacture |
US5549859A (en) * | 1992-08-11 | 1996-08-27 | E. Khashoggi Industries | Methods for the extrusion of novel, highly plastic and moldable hydraulically settable compositions |
US7157608B2 (en) | 2002-06-07 | 2007-01-02 | Daiso Co., Ltd. | Process for producing allyl ether |
-
1989
- 1989-08-18 JP JP21241989A patent/JPH0380141A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5545297A (en) * | 1992-08-11 | 1996-08-13 | E. Khashoggi Industries | Methods for continuously placing filaments within hydraulically settable compositions being extruded into articles of manufacture |
US5549859A (en) * | 1992-08-11 | 1996-08-27 | E. Khashoggi Industries | Methods for the extrusion of novel, highly plastic and moldable hydraulically settable compositions |
US7157608B2 (en) | 2002-06-07 | 2007-01-02 | Daiso Co., Ltd. | Process for producing allyl ether |
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