TW315346B - - Google Patents

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TW315346B
TW315346B TW85110153A TW85110153A TW315346B TW 315346 B TW315346 B TW 315346B TW 85110153 A TW85110153 A TW 85110153A TW 85110153 A TW85110153 A TW 85110153A TW 315346 B TW315346 B TW 315346B
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Taiwan
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dispersion liquid
thermoplastic resin
wet
dispersion
liquid
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TW85110153A
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Chinese (zh)
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Kawasaki Steel Co
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Priority claimed from JP7033512A external-priority patent/JPH08224792A/en
Priority claimed from JP7038530A external-priority patent/JP2907321B2/en
Priority claimed from JP7038531A external-priority patent/JP2915316B2/en
Priority claimed from JP7038532A external-priority patent/JPH08232187A/en
Priority claimed from JP7298577A external-priority patent/JPH09136969A/en
Application filed by Kawasaki Steel Co filed Critical Kawasaki Steel Co
Application granted granted Critical
Publication of TW315346B publication Critical patent/TW315346B/zh

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經濟部中央標準局貝工消費合作社印製 315346 A7 ___B7_ 五、發明説明_( l ). 本發明係關於繊維強化熱塑性樹脂薄片之製造設備及 製法。 有一種習知之複合化技術，係利用熱塑性樹脂在成形 上之特性，添加髙彈性率嫌維，作爲賦與高強度，高剛性 之手段。所獲得之繊維強化熱塑性樹脂複合材料，被利用 作爲需要有輕置化，髙剛φ及髙強度之各種結構構件用之 素材。這種素材通常是矩陣狀之熱塑性樹脂被加熱到融點 以上後成形爲一定形狀，特別是一種適合利用壓機來成形 或適合做成大型零件之板狀或薄片狀之素材，被稱作可壓 印薄片（Stampable sheet )，從_輕量化播求或藉一體 化成形之低成本化之優點，即從削減零件數或減低裝配過 程數之觀點，多被採用在汽車之座椅背，後封裝（rear package )，’一雔成形天板材料等汽車用結構零件，而其 他部分之採用也正在擴展中。 可壓印薄片之代表性製法有應用抄紙技術之濕式製造 法（抄紙法）▲。此項技術係在水系溶液中使嫌維碎塊與熱 塑性樹脂分散（分散過程），而在網目帶上抄造分散液而 調製不織布狀之薄膜（抄紙過程），將如薄膜加熱加壓後 硬化（薄片化過程）以製成可壓印薄片者。其連績製造法 掲示在，例如日本特開昭60 — 158227號》 抄紙法可壓印薄片之薄膜係使用如第1圖所示之製造 裝置，以下述方式連績製造出來。 此製造裝置由原料調製部1 ，薄膜抄紙部1 0，乾燥 部40，及捲取部50，構成。 本紙張尺度適用中國國家梂準（CNS ) A4規格（210X297公釐） (請先閲讀背面之注f項再填寫本頁)Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 315346 A7 ___B7_ V. Description of the invention _ (l). The present invention relates to the manufacturing equipment and manufacturing method of reinforced thermoplastic resin sheet. There is a conventional compounding technique that utilizes the characteristics of thermoplastic resins in molding and adds high elasticity and low-dimensional elasticity as a means of imparting high strength and high rigidity. The obtained reinforced thermoplastic resin composite material is used as a material for various structural members requiring light weight, high rigidity φ and high strength. This kind of material is usually a matrix-like thermoplastic resin heated above the melting point and then shaped into a certain shape, especially a plate-like or sheet-like material suitable for forming with a press or suitable for making large parts. Stampable sheet (Stampable sheet), from _ lightweight broadcast request or by the advantages of low cost by integrated molding, that is, from the point of view of reducing the number of parts or assembly process, it is mostly used in the seat back of the car. Package (rear package), 'a car forming top plate materials and other automotive structural parts, and the use of other parts is also expanding. Representative manufacturing methods for embossable sheets include the wet manufacturing method (papermaking method) using papermaking technology ▲. This technology is to disperse the suspected dimensional fragments and the thermoplastic resin in an aqueous solution (dispersion process), and make a non-woven film by making a dispersion on the mesh belt (papermaking process). Thinning process) to make embossable thin sheets. The continuous manufacturing method is shown in, for example, Japanese Unexamined Patent Publication No. 60-158227. The papermaking method can be used to imprint thin films using the manufacturing equipment shown in Figure 1 and manufactured in the following manner. This manufacturing apparatus is composed of a raw material preparation unit 1, a film papermaking unit 10, a drying unit 40, and a take-up unit 50. The paper size is applicable to China National Standards (CNS) A4 (210X297mm) (please read note f on the back and fill in this page)

A7 315346 ___B7_ 五、發明説明（2 ) (請先閱讀背面之注$項再填寫本頁) 原料調整部1設置備有攪拌機2之分散槽3 ，在此分 散槽3之上方配設有，貯藏熱塑性樹脂之樹脂供應裝置4 ，及貯藏補強用纖維之補強用嫌維供應裝置5。 將樹脂供應裝置4之熱可塑性樹脂，與補強用織維供 應裝置5之補強用嫌維，以一定之比例，探入存放有包含 界面活性劑或增粘劑之水#溶液之分散槽3內，再加以攪 拌以調製原料液之分散液C·以定量泵浦6吸出調製成之 分散液C，以叫做岐管裝置之分配裝置20分配'·到多數之 多岐管9，而送進薄膜抄造部1 0。 經濟部中央揉準局貝工消费合作社印製 在薄膜抄造部10配設有，向一個方向連績移動之無 端之網目帶1 1 ，接觸其背面配置之吸入相12，以及， 載置在此等上面之頭箱1 3。分散液C則經由進口管3 0 送進網目帶上。再者，網目帶1 1備有貫穿表裹面之細孔 ，可將固體成分之補強用嫌維及熱塑性樹脂與水系溶液分 離開。分散液C由減壓狀態之吸入箱1 2吸引，在具有較 熱塑性樹脂之粒徑爲細之網目之網目帶1 1上，成薄片狀 抄取（過濾）補強用嫌維與熱塑性樹脂。抄取之補強用纖 維與熱可塑性樹脂之不織布狀之混合物稱作薄膜（web )。此薄膜W在這個階段呈濕潤狀態，因此需通過乾燥部 4 0。 乾燥部4 0備有連設在網目帶1 1下游之運送帶4 1 與乾燥室4 2，可連績狀乾燥抄造之薄膜》在此乾燥過程 去除水分，同時施加熱塑性樹脂之融點以上之溫度’使樹 脂溶融，使補強用嫌維之交絡更爲強固。如此獲得之乾燥 本紙張尺度適用中國國家標準（CNS ) A4洗格（210X297公釐） -5 - 315346 A7 B7_ 五、發明説明—（3 ) 薄膜之破斷阻力很高，形態保持性優異，而在捲取部5 0 之捲軸51捲成滾简狀。 (請先閲讀背面之注意事項再填寫本資) 亦可再依實際需要，適宜切斷此薄膜施加熱壓，使熱 塑性樹脂充分滲進嫌維間》道種狀態之製品稱作1凝結片 〃 "''Consolidated sheet 〃。一般是以這種、凝結片’作 爲成形材料。. 抄紙法可壓印薄片之大部分之品質，特性係在抄造過 程中決定，其中尤以保持單位面稹之重置分布均句，對抑 制厚度差，補強用嫌維含置之差，消除特性變動等特別重 要。 經濟部中夬棣準局貝工消費合作杜印袈 單位面積之重置分布，大體上可分成發生在製造線之 長度方向（以下有時簡稱爲流線方向），及在宽度方向發 生者。前者多是以泵浦等所代表之供料系統之脈動造成， 其防止技術散見在習知文獻。另一方面，後者之宽度方向 之單位面積之重量分布不均之抑制方式是，將普通經由一 根配置送來之·原料（液），令其向寬度方向均勻擴大，但 如後述，這不是在可壓印薄片之濕式製造法能夠容易解決 之課題。 而且，寬度方向之單位面稹之重量分布，因下述理由 ，對補強用纖維配向狀態也有重大之影響。亦即，如'果在 寬度方向發生單位面稹之重量有大小差別時，供給頭箱之 原料分散液必然會向單位面積之重量小，吸引阻力較小之 部分流進多一點，因此會發生偏流。嫌維會沿著流向排列 ，因此偏流一發生，必定引起局部性之織維之配向異常’ 本紙張尺度適用中國國家標準（CNS ) A4规格（2l〇X29?公釐） A7 315346 ___B7_ 五、發明説明（4 ) 甚至於成爲可壓印薄片之翹曲等之原因。 (請先閲讀背面之注^h項再填寫本頁) 亦即，寬度方向之單位面稹之重量分布之均勻化，係 .獏得均質特性之薄片之必要條件。 此寬度方向之單位面積之重置分布之均勻化，可藉由 分散液中之固形物（補強用纖維與熱可塑性樹脂）之組成 均勻，且以寬度方向均等之流置將該分散液供給抄紙面上 而實現》擔負達成此目的之機能者，即爲岐管裝置及進口 管（manifoldofinlet)。 玆說明現行之濕式製造設備之兩者之問題點，及在本 發明之解決重點如下。 *(傳統之）岐管裝置 岐管裝置2 0之功能是在向進口管3 0之寬度方向， 以均勻之流量，均勻之固態物澳度供應分散液。亦即，岐 管裝置2 0之任務在於，將從分散槽3通過配管流向頭箱 1 3之分散液.之流動向寬度方向擴展。 經濟部中夬標準局貝工消费合作社印簟 對此岐管裝置之形狀從以往就在進行各種檢討。例如 在製紙業界，一般都是使用如揭示在紙漿技術協會誌（ 1993年1月1日發行）第47卷第1號P102，截 面積慢慢縮小之推拔（taper )型岐管裝置。第9圖表 示其大概。依照文獻，頭箱1 3之向寬度方向之流置非常 均勻。而固態物主要是紙漿（木材嫌維）*其濃度均勻， 分配性也無問題。 傅統之嫌維強化熱塑性樹脂薄片之濕式製造設備，也 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X 297公釐) ~ ~ ' 經濟部中央標準局属工消费合作社印製 A7 __B7__五、發明説明（5 ) 是移轉造紙技術，而採用此推拔型岐管裝置。然而，如果. 將推拔型岐管裝置應用在可壓印薄片之抄紙法時，卻發現 固態物濃度分配並不見得如紙漿濃度那麽均勻分配•其理 由如下。 構成可壓印薄片之捕強用織維與熱可塑性樹脂之比重 及幾何形狀通常是不相同的*代表性之補強用嫌維有玻璃 纖維，碳嫌維，不銹嫌維等。例如採玻璃嫌維時，其比重 爲2. 54,縱橫比（嫌維長度/嫌維徑）爲l x 10β 〜5 X 1 Ο β 。 另一方面，當作矩陣（matrix )使用之熱塑性樹脂 之比重大概是在0. 9〜1. 5之範園。而爲了抑制製造 成本，通常是用1 mm左右之粒狀物。這時之縱橫比頂多 是2。 如第9圖所示，推拔型岐管裝置除了還流到原料線之 部分循環流以'外，係將從流入口 I η流入之分散液向垂直 方向轉換方向.，而介由多岐管9送至頭箱1 3。這時，液 體中之固態物會受到依存於其形態（縱橫比）之慣性力。 亦即，縱橫比較補強用嫌維小很多（即慣性力大很多）之 熱塑性樹脂在流入多岐管9之出口附近之方向轉換不很充 分而被彈至循環出口 J 〇之傾向很大。因此，熱塑性樹脂 會集中在推拔型岐管裝置之前端附近。反之，縱橫比較大 (慣性力較小）之補強角嫌維則因爲很容易追隨分散液之 流動，因而不會有上述情況。亦即，起因於上述熱塑性樹 脂之慣性力，在岐管裝置內部發生固態物濃度之不均勻。 本紙張尺度逍用中國國家梂準（CNS ) Α4规格（210Χ297公釐) ~ -8 - (請先閲讀背面之注意事項再填寫本頁) 訂A7 315346 ___B7_ V. Description of invention (2) (Please read the note $ item on the back and then fill in this page) The raw material adjustment section 1 is provided with a dispersion tank 3 equipped with a mixer 2, and is provided above the dispersion tank 3 for storage Resin supply device 4 for thermoplastic resins, and supply device 5 for reinforcing fibers for storing reinforcing fibers. The thermoplastic resin of the resin supply device 4 and the reinforcement dimension of the reinforcement fabric supply device 5 are probed into a dispersion tank 3 containing a water # solution containing a surfactant or a thickener at a certain ratio , And then stir to prepare the raw material liquid dispersion C. Use the quantitative pump 6 to suck out the prepared dispersion liquid C, and distribute it with the distribution device 20 called manifold device. Department 10. Printed by the Peking Consumer Cooperative of the Central Ministry of Economic Affairs of the Ministry of Economic Affairs and equipped in the film manufacturing department 10, the endless mesh belt 1 1 moving in one direction, touching the suction phase 12 arranged on the back of it, and, placed here Wait for the head box 1 3 above. The dispersion liquid C is fed into the mesh belt through the inlet pipe 30. In addition, the mesh belt 11 is provided with fine holes through the surface of the surface, which can separate the solid component reinforcement thermoplastic resin and the water-based solution. The dispersion liquid C is sucked by the suction box 12 in a decompressed state, and the mesh belt 11 having a finer mesh diameter than the thermoplastic resin is copied (filtered) into a thin sheet to reinforce the suspected thermoplastic resin. The non-woven mixture of the reinforced fiber and the thermoplastic resin copied is called a web. This film W is in a wet state at this stage, so it needs to pass through the drying section 40. The drying section 40 is equipped with a conveyor belt 4 1 and a drying chamber 4 2 connected downstream of the mesh belt 1 1 to continuously dry the manufactured film. In this drying process, the moisture is removed and the melting point of the thermoplastic resin is applied above the melting point. The temperature 'melts the resin and makes the reinforcement and dimensionality stronger. The scale of the dried paper thus obtained is applicable to the Chinese National Standard (CNS) A4 wash grid (210X297mm) -5-315346 A7 B7_ 5. Description of the invention-(3) The film has a high breaking resistance and excellent shape retention. The winding shaft 51 of the winding unit 50 is rolled into a roll shape. (Please read the precautions on the back before filling in the capital.) According to actual needs, it is suitable to cut this film and apply hot pressing to make the thermoplastic resin fully penetrate into the space. The product in the state of Dao is called 1 coagulation sheet. " '' Consolidated sheet 〃. Generally, this kind of coagulated sheet 'is used as a molding material. . The papermaking method can imprint most of the quality of the sheet. The characteristics are determined during the papermaking process. In particular, the reset distribution of the unit surface is maintained, which is used to suppress the difference in thickness and reinforce the difference between the included dimensions and eliminate Changes in characteristics are particularly important. The reset distribution of the unit area of the Ministry of Economic Affairs of the Ministry of Economic Affairs and Industry, Pui Kong Consumer Cooperation Co., Ltd. can be roughly divided into the length direction of the manufacturing line (hereinafter sometimes referred to as the streamline direction) and the width direction. The former is mostly caused by the pulsation of the feeding system represented by pumps, etc., which prevents the technology from being scattered in the conventional literature. On the other hand, the way to suppress the uneven weight distribution per unit area in the width direction of the latter is to send the raw material (liquid) normally through a single arrangement to make it expand evenly in the width direction, but as described later, this is not A problem that can be easily solved in the wet manufacturing method of embossable sheets. In addition, the weight distribution of unit grain in the width direction has a significant influence on the alignment state of the reinforcing fiber for the following reasons. That is to say, if there is a difference in the weight of the unit surface in the width direction, the raw material dispersion liquid supplied to the head box will inevitably flow into the part with a small weight per unit area, and the part with less suction resistance will flow in more, so it will occur Bias. The suspected dimensions will be arranged along the flow direction, so as soon as the bias occurs, it will definitely cause a local anomaly in the alignment of the weaving dimension 'This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (2lOX29? Mm) A7 315346 ___B7_ V. Invention Explanation (4) It may even cause the warp of the embossable sheet. (Please read the note ^ h on the back before filling in this page) That is, the uniformity of the weight distribution of the unit planes in the width direction is a necessary condition for the tapir to obtain a thin sheet with uniform characteristics. The uniformity of the reset distribution per unit area in the width direction can be uniformed by the composition of the solids (reinforcing fiber and thermoplastic resin) in the dispersion liquid, and the dispersion liquid can be supplied to the "On paper" is the function of the manifold and inlet tube. The problems of both the current wet manufacturing equipment and the key points of the solution of the present invention are as follows. * (Traditional) Manifold device The function of the manifold device 20 is to supply the dispersion liquid with a uniform flow rate and a uniform solid substance in the width direction of the inlet tube 30. That is, the task of the manifold device 20 is to spread the flow of the dispersion liquid flowing from the dispersion tank 3 to the head box 13 through the piping in the width direction. The Ministry of Economic Affairs, China National Bureau of Standardization, Beigong Consumer Cooperative Inquiry has conducted various reviews of the shape of the manifold device in the past. For example, in the paper industry, a taper type manifold device, such as that disclosed in the Pulp Technology Association Journal (issued on January 1, 1993) Vol. 47, No. 1, P102, is gradually used to reduce the cross-sectional area. The ninth graph shows its approximate. According to the literature, the flow of the head box 13 in the width direction is very uniform. The solid matter is mainly pulp (wood is too dimensional) * its concentration is uniform, and its distribution is no problem. Fu Tong ’s wet-type manufacturing equipment for thermoplastic resin sheets is also suitable for China ’s national standard (CNS) A4 specification (210X 297 mm) ~ ~ 'A7 __B7__ printed by the Industrial and Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (5) It is a transfer papermaking technology, and this push-type manifold device is adopted. However, if the push-type manifold device is applied to the papermaking method of embossable sheets, it is found that the solid matter concentration distribution is not necessarily evenly distributed as the pulp concentration. The reason is as follows. The specific gravity and geometric shape of the woven fabric and thermoplastic resin constituting the embossable sheet are usually different. * Representative reinforcing fabrics include glass fiber, carbon fabric, stainless steel, etc. For example, when the glass is dimensionally dimensioned, its specific gravity is 2.5, and the aspect ratio (distance dimension / distance dimension) is l x 10β ~ 5 X 1 Ο β. 5 的 范 园。 On the other hand, the specific gravity of the thermoplastic resin used as a matrix (matrix) is about 0.9 ~ 1.5. In order to suppress the manufacturing cost, usually about 1 mm granular material is used. At this time, the aspect ratio is at most 2. As shown in Fig. 9, in addition to the partial circulation flow flowing to the raw material line of the push-out manifold device, the dispersion liquid flowing in from the inlet I η is changed in the vertical direction. The multi-manifold 9送到 头 箱 1 3. At this time, the solid matter in the liquid will receive an inertial force depending on its form (aspect ratio). That is, the thermoplastic resin with a much smaller dimension (that is, a much larger inertial force) for reinforcement of the aspect ratio tends to bounce to the circulation outlet J 〇 because the direction of the flow into the vicinity of the outlet of the manifold 9 is not sufficiently changed. Therefore, the thermoplastic resin is concentrated near the front end of the push-type manifold device. Conversely, the reinforcement angle with a larger aspect ratio (smaller inertial force) is more likely to follow the flow of the dispersion liquid, so this will not happen. That is, due to the inertial force of the thermoplastic resin described above, unevenness in the concentration of solid matter occurs inside the manifold device. The size of this paper is in accordance with China National Standards (CNS) Α4 specification (210Χ297mm) ~ -8-(please read the precautions on the back before filling this page)

VI 315346 A7 B7 經濟部中央棣準局貝工消費合作社印製 五、發明説明（6 ) 此項不均勻化在傳統之可壓印薄片之濕式製造設備引起薄. 膜之寬度方向之單位面稹之重量分布不均，’進而招致製品 薄片之簿曲強度或彎曲彈性等之力學特性之不均匀，以及 厚度大小等品質參差不一之問題。 因此，本發明之目的在於，提供一種備有，不受起因 於固態物之形態差之慣性力之影響，可均勻分配固態物濃 度之新穎岐管裝置之嫌維強化熱塑性樹脂薄片之濕式製造 裝置。 * 傅統之進口管 如第1圖所示，在岐管裝置2 0分配給多岐管9之分 散液，被導引至進口管3 0，合流而成二度空間液流而送 給網目帶11。亦即，進口管30可以說是，將岐管裝置 2 0以多數之「線」送來之分散液改變成「面」之液體流 ，而供應給網目帶11之裝置。 在傅統之.可壓印薄片之濕式製造設備，爲了要抄造單 位面稹之重置均勻之薄膜，將進口管3 0之容稹加大，以 發揮分散液C之混合，整流效果。 然而，進口管3 0之不妥適之大容量化，不僅無法控 制從出口 E送出之液流之擺動，反而會增長擺動。此之所 謂擺動’指的是液流從出口 E不依流線方向畢直流出，而 是向左右擺動而流出之瑝象，其發生主要是起因於分散液 C之動壓及流量之不均。 第2點是抄紙法程序特有之問題。在抄紙法.補強用 (請先閲讀背面之注意^項再填寫本頁) 取· ,ιτ 本紙張尺度逋用中國國家橾準（CNS ) Α4规格（210Χ297公釐） 經濟部中央橾準局貝工消費合作社印裝 A7 B7五、發明説明（7 ). 纖維與熱塑性樹脂有時由發泡液（foam )输送，若有流 速降低之部分，會分離成泡沫（空氣含量）較多之部分， 與沒有泡沫之水系溶液，因此分散液之固態物運送能力會 降低，澳度及單位面稹之重置之均勻化會相當困難。這種 分散液之流速下降，在例如會產生分散液滯留之構造部分 特別容易發生.。 , 亦即，在抄紙法會被要求，不使流速下降，可抑制分 散液具有之很大之動壓而加以整流之極度困難之課題。即 ，本發明之目的在於提供一種，可以抑制因原料分散液之 動壓及因此而發生之擺動之影響所造成之單位面稹之重量 分布不均之纖維強化熱塑性樹脂薄片之濕式製造設備。 本發明之纖維強化熱塑性樹脂薄片之濕式製造設備之 特徵在於，具備有，從形狀呈垂直軸旋轉體而用以分配包 含補強用嫌維及樹脂之分散液之岐管裝置，具備有可使該 分散液至少碰撞壁面一次之構造之緩衝型進口管*及具備 有可使該分散.液滯留在移動之無端網目帶上至一定深度以 上之構造之充滿液體型頭箱，所成之群中選擇之至少一種 裝置。 加之，本發明之嫌維強化熱塑性樹脂薄片之濕式製造 設備之特徼在於，具備有上述垂直軸旋轉體形狀之岐管裝 置，及緩衝型進口管。 加之，本發明之繊維強化熱塑性樹脂薄片之濕式製造 設備之特徵在於，具備有上述垂直軸旋轉體形狀之岐管裝 置，及充滿液體型頭箱。 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X297公釐） (請先聞讀背面之注意事項再填寫本頁) -10 - 經濟部中央梯準局貝工消費合作社印裝 A7 B7五、發明説明（8 ) 加之，本發明之嫌維強化熱塑性樹脂薄片之濕式製造. 設備之特徵在於，具備有上述緩衝型進口管，及充滿液體 型頭箱。 加之，本發明之嫌維強化熱塑性樹脂薄片之濕式製造 設備之特徵在於，具備有上述垂直軸旋轉體形狀之岐管裝 置，緩衝型進口管，以及，充滿液體型頭箱。 加之，上述垂直軸旋轉體形狀之岐管裝置可在同一髙 度備有同徑之分配流出口。 加之，上述垂直軸旋轉體形狀之岐管裝置可備有，從 垂直軸旋轉對稱面之切線方向導入上述分散液之流入口。 加之，上述垂直軸旋轉體形狀之岐管裝置可備有，在 該垂直軸旋轉體形狀之中心軸上，從垂直上方導入分散液 之流入口。 加之，上述垂直軸旋轉體形狀之岐管裝置在其內部備 有，成水平旋轉之攪拌裝置，其攪拌軸與該垂直軸旋轉體 形狀之中心軸-一致》 加之，上述垂直軸旋轉體形狀之岐管裝置可在以該垂 直軸旋轉體形狀之中心軸爲中心之大體一個同心圓上，以 相等間隔配設上述分散液之分配流出口。 加之，上述垂直軸旋轉體形狀之岐管裝置之上述分配 流出口，可以朝垂直上方開口。 加之，上述緩衝型進口管可以具備有，在上述分散液 之流出口有跟分散液之吸引過濾領域同寬之開縫狀之開口 構造》 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X297公釐） ~ (請先閲讀背面之注意事項再填寫本\8〇 訂 315846 經濟部中央標準局属工消費合作社印裝 A7 B7五、發明説明（9 ) 加之，上述緩衝型進口管可以具備有，.用以在上述分 散液之流出口形成與分散液之吸引過濾領域同寬之開縫狀 開口，而可調節開口度之限幅（.Slice )板。 加之，上述緩衝型進口管可以在上述分散液之流動方 向，分開間隔備有多片限幅板。 加之，上述緩衝型進口管可具備有，可使上述分散液 至少碰撞與流線方向反方向之壁面一次之構造。 加之，上述緩衝型進口管之內容部分可在上述分散液 之吸引過濾領域之寬度方向區隔成多數區域，將該分散液 導入各區域，同時在各區域之前方且在上述開縫狀開口之 後方，具有可使分散液流會合之構造。 加之，上述緩衝型進口管之內容部分可具備有，在上 述分散液之吸引過濾領域之寬度方向區隔成多數區域， 可將該分散液導入各區域，同時可使上述分散液至少碰撞 與流線方向反方向之壁面一次之構造，並可具備有，在各 區域之前方且·在上述開縫狀開口之後方，使分散液流會合 之構造。而且，在上述分散液之流動方向，分開間隔備有 一片或多片限幅板* 加之，上述緩衝型進口管可使上述區域中位於最外側 之區域之截面稹較其他區域爲狹小。 加之*在上述充滿液體型頭箱，上述一定深度係指流 入頭箱之分散液之擺動不會到達上述網目帶上之深度，爲 其特徵。 加之，本發明之嫌維強化熱塑性樹脂薄片之濕式製造 ^---：---.---^ ^ ―Γ (請先閲讀背面之注意事項再填寫本頁) 訂 本紙诛尺度適用中國國家標準（CNS ) A4规格（210 X297公釐） 經濟部中央梂準局—工消費合作杜印袈 A7 ____B1 五、發明説明（10) 力法*係將包含補強用繊維與熱塑性樹脂之分散液，從岐 管裝置通過進口管，供給移動中之無端網目帶上，一面吸 弓[過濾而抄取片狀之薄膜之嫌維強化熱塑性樹脂薄片之濕 式製造方法，其特徵在於，將在該岐管裝置分岐之分散液 ，導入以隔壁將該進口管之入口部均等分隔成多數區域之 小流路，令分散液碰撞到g小流路之壁面而轉向，以減低 動壓，然後使分散液合流，再通過開縫狀之分散液流出口 以調整分散液之波狀擺動，同時使液流前頭平坻化，而供 給網目帶上。 加之，本發明之嫌維強化熱塑性樹脂薄片之濕式製造 方法，係將包含補強用織維及熱塑性樹脂之分散液，從岐 管裝置通過進口管，供給移動中之無端網目帶上，一面吸 引過濾而抄取片狀之薄膜之嫌維強化熱塑性樹脂薄片之濕 式製造方法，其特徵在於，在宽度方向兩端部提髙在上述 進口管內流動之分散液之流速，然後通過開縫狀之分散液 流出口調整分1散液之波狀擺動，同時使液流前頭平坦化， 而供給網目帶上。 加之，本發明之織維強化熱塑性樹脂薄片之濕式製造 方法，係將包含補強用繊維及熱塑性樹脂之分散液，從岐 管裝置通過進口管，供給移動中之無端網目帶上，一面吸 引過濾而抄取片狀之薄膜之嫌維強化熱塑性樹脂薄片之濕 式製造方法，其特徵在於，在載置於該分散液之吸引過濾 領域上之頭箱內部，令分散液滯留在網目帶上，使由該進 口管吐出之分散液所具有之擺動不到達網目帶。 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X297公釐) ~ -13 - L---：---.--Λ --.---訂I*-----{ Γ (請先Μ讀背面之注意事項再填寫本頁) 315346 A7 經濟部中央揉準局員工消费合作社印裝 B7五、發明説明（11 ) * 本發明之岐管裝置 推拔型岐管裝置要將慣性力大之粒子狀固態物均勻分 配壓頭箱之宽度方向是很困難。要解決道個問題，必須要 有，作用於固態物之慣性力之影響不易顯現，並使流入口 至供應分配口之距離爲一定之岐管裝置構造。本發明人等 即根據此等瞭解，終於發$，具有垂直軸旋轉體形狀之岐 管裝置對固態物，尤其是對慣性力大之粒子狀固態物之均 勻分配很有效。 本發明之岐管裝置呈垂直軸旋轉體形狀，在同一高度 備有同徑之分配流出口。在此所稱之垂直軸旋轉體係指具 有以垂直方向之軸爲中心之軸對稱形外殼之立方體。最爲 單純之垂直軸旋轉體形狀，係例如側面之全部爲垂直軸對 稱曲面，上面與下面分別爲平面之圓筒。另有其他各種形 狀，例如上下面不一定是平面，圓錐面，半球面等都可以 •由於採用垂直軸旋轉體形狀，可以例如第2圖以模式方 式表示，很容易產生迴旋流或放射狀之上下循環流。這時 ，對分散液中之捕強用嫌維或熱塑性樹脂，主要是作用有 對應離垂直軸旋轉體形狀之中心軸（以下簡稱爲中心軸） 之距離大小之離心力，因此可以防止傅統之推拔型岐管裝 置之慣性力之影響。而且，分散液中之固態物會乘著上述 液體流，沿著垂直軸旋轉對稱曲面上昇而到達同一高度之 分配流出口，因此，不論是那一個分配流出口’從分散液 流入口起之軌跡均相同。如此，從那一個分配流出口都會 均勻吐出固態物濃度相同之分散液。 本紙張尺度逍用中國國家梂準（CNS ) A4规格（210X297公釐） ~ -14 - (請先閲讀背面之注意事項再填寫本頁) A7 B7 35346 五、發明説明（l2 ) 上述垂直軸旋轉體形狀之岐管裝置之槽高與槽徑之比. 可因分散液之性質而改變，例如在最單純之園筒形狀，應 以0. 3〜3之範圍最爲合適。 請 先 聞 讀 背 ίι 之 注 意 事 項 再 上述岐管裝置可以在下部備有從垂直軸對稱曲面之切 線方向導入分散液之流入口。藉此可產生如第2圖所示之 迴旋流與上下循環流。再f，爲了要有效產生道些流動， 將下面形成爲園錐面，半球面等形狀較爲有效》爲了要使 迴旋流充分到達岐管裝置之整個內部，分配流出口之位置 最好儘置接近岐管裝置之底面。同時，爲了要確保從分散 液流入口至分配流出口間有充分之移動距離，岐管裝置之 槽長最好是原料分散液之供應管內徑之5倍以上。 訂 經濟部中央揉準局貝工消费合作社印袋 另一方面*上述岐管裝置也可以在中心軸上備有，可 從垂直上方導入分散液之流入口。如第4圖所示之一個例 子，從流入口 2 1流入之分散液將沿著中心軸垂直下降， 接著被引導至內殼之垂直軸旋轉對稱曲面2 6而上昇，而 被引至分配流出口 2 5。如此，在岐管裝置內可很容易上 下循環流動，因此不論是那一個分配流出口，從流入口起 之補強用繊維或熱塑性樹脂之軌跡實質上均相同。亦即， 無論從那一個分配流出口均可流出固態物澳度均匀.之分散 液。 同時，上述岐管裝置可備有水平旋轉攪拌裝置。該攪 拌裝置之攪拌軸與岐管裝置之中心軸一致。第4圖示有一 例，藉此攪拌，可很容易產生與第2圖以模式方式表示有 一樣之迴旋流與上下循環流，達成分散液中之固態物之均 本紙張尺度適用中國國家揉準（CNS ) A4規格（210 X 297公釐） -15 - 經濟部中央樣準局貝工消費合作社印製 A7 一 B7五、發明説明（l3) 勻分配。攪拌翼另要有將液體之流動推擠向半徑方向之機 能即可以，例如透平型，螺旋槳型，葉片型等均可利用。 同時爲了要使迴旋流到達岐管裝置之整個內部，攪拌翼之 位置最好是儘可能接近岐管裝置之底面。再者，攪拌翼之 位置亦有抑制補強用嫌維之二次凝集之效果。岐管裝置與 攪拌翼之直徑比，可依產丰對均勻分配固態物最有效之迴 旋流而決定之，例如最單純之圚筒形狀爲例時，以1. 5 〜5之值最合適。 上述岐管裝置可以在以中心軸爲中心之大體一個同心 圖上，相等間隔備有分配流出口。如此按排，乘著迴旋流 而至同心圃上之各分配流出口之固態物之流動距離將大致 完全相等，流出之液體之濃度將更上一層嚴密均勻化。 同時，上述分散液可用發泡分散液。申請專利範圍第 6項至第1 1項之發明也可適用在不一定有泡沬存在之分 散液，但若用發泡分散液，形態差或比重差較之固態物會 被同時捕捉在泡膜面，因此不易產生分離，可在送液過程 中維持均勻之混合狀態。 惟，使用發泡分散液時，會另外產生泡沫與水分離之 問題。根據本發明人等之經驗，如第3圖A所示之一個例 子，曾有岐管裝置內之分散液分離成，與流入分散液之成 分相同之部分，及顯然泡沫較多成爲滯留之部分S。在泡 沫滯留部分S內有補強用嫌維存在，但沒有熱塑性樹脂存 在。從各分配流出口會流出分散液與泡沫滯留液S之混合 物，但從泡沬滯留液之混合比率髙之流出口會流出補強用 本紙張尺度適用中國國家樑準（CNS ) A4規格（210X297公釐） " -16 - (請先聞讀背面之注意事項再填寫本頁) A7 B7 經濟部中央橾準局貝工消费合作社印製 五、發明説明（14 ) 嫌維濃度很髙之發泡分散液。亦即，產生泡沫滯留液S時 會引起固態物之不均勻分配。 這種泡沫滯留液產生現象，若在岐管裝置內全區域將 分散液保持在流動狀態則可有效防止。因此，適宜考慮岐 管裝置之大小，將分散液流入條件或上述水平旋轉攪拌裝 置之運轉條件合適化最爲f要。而且，若考慮泡沬滯留液 是集中存在於分散液之上層•將分散液之分配流出口儘置 配設在岐管裝置上部，以防止泡沫滯留液肥大化·也是十分 有效。 而且，爲了消除上述泡沫滯留液，上述岐管裝置可以 將分配流出口配設在岐管裝置之上面，朝向垂直上方，藉 此，可使漂浮之泡沫連同分散液一起朝向垂直上方確資流 出，不會在岐管裝置內有泡沫滯留。 * 本發明之進口管 本發明之·緩衝型進口管要在網目帶上之整個寬度方向 ’將分散液之流量均勻化而送到網目帶上最重要的一點是 ’如何降低從岐管裝置多路分岐強力送給進口管输入側之 分散液之動壓。 在緩衝型進口管，此分散液之動壓之降低，可以使從 岐管裝置供給進口管之分散液至少碰撞接近分散液流入口 而面向此流入口之分散液碰撞面一次以轉換方向，而達成 *此分散液碰撞面係例如第7圖所示，進口管呈箱形時， 選擇其後面，上面，下面或後面任一內壁。這時之動壓降 (請先閲讀背面之注意事項再填寫本頁)VI 315346 A7 B7 Printed by Beigong Consumer Cooperative of the Central Bureau of Economics and Trade of the Ministry of Economic Affairs 5. Description of the invention (6) This unevenness causes thinness in the traditional wet-type manufacturing equipment for embossable sheets. The unit surface in the width direction of the film The uneven distribution of the weight of 紹 further leads to the unevenness of the mechanical properties such as the bending strength or bending elasticity of the product sheet, and the uneven quality of the thickness. Therefore, the object of the present invention is to provide a wet-type manufacturing of a susceptible dimension-reinforced thermoplastic resin sheet of a novel manifold device capable of uniformly distributing the concentration of solid matter without being affected by the inertial force caused by the difference in the shape of the solid matter Device. * Fu Tongzhi's inlet pipe As shown in Figure 1, the distribution liquid distributed to the multi-manifold 9 in the manifold device 20 is led to the inlet pipe 30, merged to form a two-dimensional space flow and sent to the mesh belt 11. That is, the inlet pipe 30 can be said to be a device that changes the dispersion liquid sent from the manifold device 20 by a plurality of "lines" into a "surface" liquid flow and supplies it to the mesh belt 11. In Fu Tongzhi's wet-type manufacturing equipment for embossable thin sheets, in order to make a uniform thin film for the resetting of the unit surface grain, the volume of the inlet pipe 30 is increased to exert the mixing and rectifying effect of the dispersion liquid C. However, the improper large capacity of the inlet pipe 30 cannot only control the swing of the liquid flow sent from the outlet E, but will increase the swing. The so-called "swing" refers to the phenomenon that the liquid flow flows out from the outlet E without flowing in the direction of the streamline, but flows to the left and right, and its occurrence is mainly due to the unevenness of the dynamic pressure and flow rate of the dispersion liquid C. The second point is a problem unique to the papermaking process. In the papermaking method. For reinforcement (please read the notes on the back ^ item first and then fill out this page). Take this paper size using the Chinese National Standard (CNS) Α4 specification (210 × 297 mm) Central Ministry of Economic Affairs A7 B7 printed by the Industrial and Consumer Cooperatives 5. Description of the invention (7). Fibers and thermoplastic resins are sometimes transported by foam. If there is a decrease in flow rate, it will be separated into a part with more foam (air content). Compared with aqueous solutions without foam, the solids transport capacity of the dispersion will be reduced, and the homogenization of the reset of the unit and the unit surface will be quite difficult. Such a decrease in the flow rate of the dispersion liquid is particularly likely to occur in a structure part where the dispersion liquid stays, for example. , That is, the papermaking method is required to reduce the flow rate, and it is extremely difficult to rectify the large dynamic pressure of the dispersed liquid while suppressing it. That is, an object of the present invention is to provide a wet-type manufacturing apparatus for a fiber-reinforced thermoplastic resin sheet that can suppress the uneven distribution of the weight per unit surface caused by the dynamic pressure of the raw material dispersion and the resulting oscillation. The wet-type manufacturing equipment of the fiber-reinforced thermoplastic resin sheet of the present invention is characterized by being equipped with a manifold device for distributing a dispersion liquid containing a reinforcing susceptible dimension-retaining resin from a rotating body having a vertical axis shape. A buffer-type inlet pipe * with a structure where the dispersion liquid collides with the wall surface at least once, and a liquid-filled head box with a structure capable of dispersing the liquid. The liquid remains on the moving endless mesh belt to a certain depth or more. Choose at least one device. In addition, the wet-type manufacturing equipment of the dimensionally-strengthened thermoplastic resin sheet of the present invention is characterized by being equipped with a manifold device having the shape of a rotating body with a vertical axis as described above, and a buffer-type inlet tube. In addition, the wet-type manufacturing equipment of the vinyl-reinforced thermoplastic resin sheet of the present invention is characterized by being provided with a manifold device in the shape of a rotating body with a vertical axis as described above, and a liquid-filled head box. The paper size is applicable to the Chinese National Standard (CNS) A4 (210X297mm) (please read the notes on the back and then fill out this page) -10-A7 B7, printed by the Beigong Consumer Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs Description of the invention (8) In addition, the wet manufacturing of the dimensionally-strengthened thermoplastic resin sheet of the present invention. The equipment is characterized by having the above-mentioned buffer-type inlet pipe and a liquid-filled head box. In addition, the wet-type manufacturing equipment of the dimension-reinforced thermoplastic resin sheet of the present invention is characterized by including the above-mentioned vertical-axis rotating body-shaped manifold device, a buffer-type inlet tube, and a liquid-filled head box. In addition, the manifold device in the shape of a rotating body with a vertical axis can be provided with a distribution outlet of the same diameter at the same height. In addition, the manifold device in the shape of the rotating body of the vertical axis may be provided to introduce the inflow port of the dispersion liquid from the tangent direction of the plane of rotation symmetry of the vertical axis. In addition, the manifold device in the shape of the vertical-axis rotating body may be provided with an inflow port for introducing the dispersion liquid from vertically above on the central axis of the shape of the vertical-axis rotating body. In addition, the above-mentioned manifold device in the shape of the rotating body of the vertical axis is equipped with a stirring device that rotates horizontally, and its stirring axis is consistent with the central axis of the shape of the rotating body of the vertical axis. The manifold device may arrange the distribution outlets of the dispersion liquid at equal intervals on a substantially concentric circle centered on the central axis of the shape of the rotating body of the vertical axis. In addition, the distribution outlet of the manifold device in the shape of a rotating body with a vertical axis may open vertically upward. In addition, the above-mentioned buffer type inlet pipe may be provided with a slit-like opening structure having the same width as the dispersion filtration and filtration field at the outflow port of the dispersion liquid. "This paper standard is applicable to the Chinese National Standard (CNS) A4 specification ( 210X297mm) ~ (Please read the precautions on the back before filling in this book. Order 8 315846 Printed by the Industrial and Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 V. Description of invention (9) In addition, the above-mentioned buffered import tubes can be provided Yes, it is used to form a slit-shaped opening with the same width as the suction filtration area of the dispersion liquid at the outflow port of the above dispersion liquid, and a slice (.Slice) plate with adjustable opening degree. In addition, the above buffer type inlet pipe can In the flow direction of the dispersion liquid, a plurality of limiter plates are provided at spaced intervals. In addition, the buffer-type inlet pipe may be provided with a structure that allows the dispersion liquid to collide at least once against a wall surface opposite to the direction of the streamline. The content of the buffer inlet tube can be divided into a plurality of areas in the width direction of the suction filtration area of the dispersion liquid, and the dispersion liquid can be introduced into each area. In front of each area and behind the slit-shaped opening, it has a structure that allows the dispersion liquid to converge. In addition, the content of the buffer-type inlet pipe may be provided in the width direction of the suction filtration area of the dispersion Divided into multiple areas, the dispersion can be introduced into each area, at the same time, the dispersion can be struck at least once against the wall surface opposite to the direction of the streamline, and can be provided in front of each area and Behind the slit-shaped opening, the structure of the dispersion liquid meets. In addition, in the flow direction of the above-mentioned dispersion liquid, one or more limiter plates * are provided at spaced apart intervals. The cross section of the outer area is narrower than the other areas. Plus * In the above liquid-filled head box, the above-mentioned certain depth means that the swing of the dispersion liquid flowing into the head box does not reach the depth above the mesh belt, which is characteristic. , The wet manufacturing of the suspected dimension-strengthened thermoplastic resin sheet of the present invention ^ ---: ---.--- ^ ^ Γ (Please read the precautions on the back before filling this page) The scale of the revised version is applicable to the Chinese National Standard (CNS) A4 (210 X297 mm). The Central Bureau of Economic Affairs of the Ministry of Economic Affairs-Industry and Consumer Cooperation Du Yinhua A7 ____B1 V. Description of the invention (10) The force law * system will include reinforcement Wet manufacturing method of the dispersion liquid with thermoplastic resin is supplied from the manifold device through the inlet pipe to the moving endless mesh belt and sucks the bow [filtering and copying the film-like film of the dimension-reinforced thermoplastic resin sheet. The feature is that the dispersion liquid divided in the manifold device is introduced into a small flow path that divides the inlet portion of the inlet pipe into a plurality of areas with a partition wall, so that the dispersion liquid hits the wall surface of the g small flow path and turns to reduce After dynamic pressure, the dispersion liquid is merged, and then the slit-shaped dispersion liquid outlet is used to adjust the wave swing of the dispersion liquid, and at the same time, the front of the liquid flow is flattened and supplied to the mesh belt. In addition, the wet manufacturing method of the suspected dimension-reinforced thermoplastic resin sheet of the present invention supplies the dispersing liquid containing the reinforcing fabric and the thermoplastic resin from the manifold device through the inlet pipe to the moving endless mesh belt, attracting The wet-type manufacturing method of the dimensionally-strengthened thermoplastic resin sheet by filtering and copying a sheet-like film is characterized in that the flow velocity of the dispersion liquid flowing in the inlet pipe is raised at both ends in the width direction, and then passes through the slit-like shape The dispersion liquid outlet is adjusted to a wave-like swing of 1 dispersion, and at the same time, the front of the liquid flow is flattened and supplied to the mesh belt. In addition, the wet manufacturing method of the dimension-reinforced thermoplastic resin sheet of the present invention supplies the dispersion liquid containing the reinforcing dimension and the thermoplastic resin from the manifold device through the inlet pipe to the moving endless mesh belt while attracting and filtering The wet manufacturing method of the suspected dimension-reinforced thermoplastic resin sheet from which the sheet-like film is copied is characterized in that the dispersion liquid is retained on the mesh belt inside the head box placed on the suction filtration field of the dispersion liquid, The swing of the dispersion liquid discharged from the inlet pipe does not reach the mesh belt. The size of this paper is applicable to the Chinese National Standard (CNS) A4 (210X297mm) ~ -13-L ---: ---.-- Λ --.--- Subscribe I * ----- {Γ (Please read the precautions on the back first and then fill out this page) 315346 A7 Printed B7 by the Consumer Cooperative of the Ministry of Economic Affairs, Central Bureau of Industry and Commerce B. V. Description of the invention (11) * The manifold device of the present invention is a push-and-pull manifold device. It is difficult to evenly distribute the particulate solid matter with large inertia force in the width direction of the indenter box. To solve this problem, it is necessary to have a manifold device structure in which the influence of the inertial force acting on solid objects is not easy to appear, and the distance between the inflow port and the supply and distribution port is fixed. Based on this knowledge, the present inventors finally issued that the manifold device having the shape of a rotating body with a vertical axis is effective for the uniform distribution of solid objects, especially particulate solid objects with a large inertial force. The manifold device of the present invention has the shape of a rotating body with a vertical axis, and has distribution outlets of the same diameter at the same height. The vertical axis rotation system referred to herein refers to a cube having an axisymmetrical shell centered on the vertical axis. The simplest shape of the vertical axis rotating body is, for example, all the sides are vertical axis symmetry curved surfaces, and the upper and lower surfaces are flat cylinders, respectively. There are other various shapes, such as the upper and lower faces are not necessarily flat, conical, hemispherical, etc. • Due to the shape of the rotating body with a vertical axis, it can be represented in a mode as shown in Figure 2, for example. Circulate up and down. At this time, the dimensional or thermoplastic resin used for the trapping strength in the dispersion mainly acts on the centrifugal force corresponding to the distance from the central axis of the shape of the rotating body of the vertical axis (hereinafter referred to as the central axis). The influence of the inertial force of the manifold device. Moreover, the solids in the dispersion will ride the above-mentioned liquid flow and rise along the vertical axis of rotation and symmetry to reach the distribution outlet of the same height. Therefore, no matter which distribution outlet's trajectory from the dispersion liquid inlet Are the same. In this way, the dispersion liquid with the same solid concentration will be evenly discharged from the distribution outlet. The size of this paper is in accordance with Chinese National Standard (CNS) A4 specification (210X297mm) ~ -14-(please read the precautions on the back before filling in this page) A7 B7 35346 5. Description of the invention (l2) The rotation of the above vertical axis The ratio of the groove height and the groove diameter of the manifold device of the body shape can be changed due to the nature of the dispersion, for example, in the simplest cylindrical shape, the range of 0.3 ~ 3 should be the most suitable. Please read the notes on the back first. Then the above manifold device can be equipped with a flow inlet for introducing the dispersion liquid from the tangent direction of the vertical axis symmetry curved surface at the lower part. This can produce a swirling flow and a circulating flow as shown in Figure 2. Furthermore, in order to effectively generate some flow, it is more effective to form the lower surface as a conical surface, a hemispherical surface, etc. In order to allow the swirling flow to reach the entire interior of the manifold device, the location of the distribution outlet is preferably located Close to the bottom of the manifold device. At the same time, in order to ensure a sufficient moving distance from the dispersion liquid inlet to the distribution outlet, the groove length of the manifold device is preferably more than 5 times the inner diameter of the raw material dispersion liquid supply pipe. On the other hand * The above-mentioned manifold device can also be provided on the central axis, and the inlet of the dispersion liquid can be introduced from above vertically. As an example shown in Fig. 4, the dispersion liquid flowing in from the inlet 21 will vertically fall along the central axis, and then will be guided to the vertical axis of the inner shell rotationally symmetrical curved surface 26, and will be led to the distribution flow Exit 2 5. In this way, it is easy to circulate up and down in the manifold device, so no matter which distribution outflow port, the trajectory of reinforcement or thermoplastic resin from the inflow port is substantially the same. That is to say, no matter from which distribution outlet, the solid matter can flow out evenly. At the same time, the above manifold device can be equipped with a horizontal rotation stirring device. The stirring axis of the stirring device coincides with the central axis of the manifold device. There is an example in the fourth picture. With this stirring, it is easy to produce the same swirling flow and up-and-down circulation flow as the mode shown in the second figure, to achieve the uniformity of the solids in the dispersion. (CNS) A4 specification (210 X 297 mm) -15-Printed A7-B7 by the Beigong Consumer Cooperative of the Central Prototype Bureau of the Ministry of Economy V. Invention description (l3) Evenly distributed. The stirring wing can also have the function of pushing the flow of the liquid in the radial direction, for example, turbine type, propeller type, blade type, etc. can be used. At the same time, in order for the swirling flow to reach the entire interior of the manifold device, the position of the stirring wing is preferably as close as possible to the bottom surface of the manifold device. In addition, the position of the stirring wing also has the effect of suppressing the secondary agglutination of the reinforcing dimension. 5 〜5 的 值。 The diameter ratio of the manifold device and the stirring wing can be determined according to the most effective swirling flow of Sanfeng for the even distribution of solids. For example, in the simplest shape of the cylinder, the value of 1.5 ~ 5 is most suitable. The aforementioned manifold device may be provided with distribution outlets at equal intervals on a substantially concentric diagram centered on the central axis. In this way, the flow distance of the solids by the swirling flow to the distribution outlets on the concentric garden will be approximately exactly the same, and the concentration of the outflowing liquid will be more uniformly uniform. Meanwhile, the above-mentioned dispersion liquid may be a foaming dispersion liquid. The inventions in the 6th to 11th patent applications can also be applied to dispersions that do not necessarily have foam, but if foaming dispersions are used, solids with poor morphology or specific gravity will be trapped in the foam at the same time. The membrane surface is therefore not easy to separate, and can maintain a uniform mixing state during the liquid feeding process. However, when foaming dispersion liquid is used, the problem of separation of foam and water is additionally generated. According to the experience of the present inventors, as an example shown in Fig. 3A, the dispersion liquid in the manifold device was separated into the same parts as the components flowing into the dispersion liquid, and it became apparent that more foam became the stagnation part S. In the foam retention portion S, there is a reinforcing dimension, but no thermoplastic resin exists. The mixture of the dispersion liquid and the foam retention liquid S will flow out from each distribution outflow, but the outflow outlet from the mixing ratio of the foam retention liquid will flow out and be reinforced. This paper standard is applicable to the Chinese National Liang Zhun (CNS) A4 specification (210X297 %) &Quot; -16-(Please read the precautions on the back first and then fill out this page) A7 B7 Printed by the Central Bureau of Economic Affairs of the Ministry of Economic Affairs, Beigong Consumer Cooperative V. Description of the invention (14) The foam with high density Dispersions. That is, when the foam retentate S is generated, it causes uneven distribution of the solid matter. This phenomenon of foam retention liquid can be effectively prevented if the dispersion liquid is kept in a flowing state in the entire area of the manifold device. Therefore, it is appropriate to consider the size of the manifold device, and it is most necessary to optimize the inflow conditions of the dispersion liquid or the operating conditions of the above-mentioned horizontal rotary stirring device. In addition, if it is considered that the foam retention liquid is concentrated on the upper layer of the dispersion liquid, it is very effective to arrange the distribution outlet of the dispersion liquid at the upper part of the manifold device to prevent the foam retention liquid from becoming enlarged. In addition, in order to eliminate the foam retention liquid, the manifold device can arrange the distribution outlet on the manifold device and face vertically upwards, thereby allowing the floating foam and the dispersion liquid to flow out vertically upwards. There will be no foam stagnation in the manifold. * The inlet pipe of the present invention The buffer inlet pipe of the present invention has to 'uniform the flow of the dispersion liquid and send it to the mesh belt in the entire width direction of the mesh belt'. The most important point is how to reduce the number of slave manifold devices. Lufenqi strongly sends the dynamic pressure of the dispersion on the input side of the inlet pipe. In the buffer type inlet pipe, the reduction of the dynamic pressure of the dispersion liquid can make the dispersion liquid supplied from the manifold device to the inlet pipe at least collide with the dispersion liquid inlet and face the inlet of the dispersion liquid collision surface once to change the direction, and Achieved * This dispersion liquid collision surface is shown in Figure 7, for example, when the inlet pipe is box-shaped, select any of the inner wall behind, above, below or behind. The dynamic pressure drop at this time (please read the notes on the back before filling this page)

，1T 本紙張尺度適用中國國家揉準（CNS ) Α4規格（210Χ297公釐） 經濟部中央標準局負工消费合作社印裝 315346 A? B7 五、發明説明（15 ) 低效果係愈是後者愈優。藉此碰撞，可將從多岐管9噴出 之噴流之動壓變換成亂流之動能而衰減掉。 在上述進口管，要將噴流之混亂之動壓能量，亦即， 要將變換成波狀擺動之分散液流加以整流，必須令其通過 寬度大，髙度方向較窄之開縫狀之分散液流出口 E。開縫 狀開口之大小，即開度可f量對進口管之分散液供應置， 速度等加以決定。 上述進口管之分散液流出口，以例如第6»或第7圖 所示，開口於流線方向之相反方向特別有效。由於令多岐 管9噴出之液流碰撞於後壁面，然後180°轉向，得以 高效率抑制噴流之動壓》 在上述進口管，由於使液流之搖擺（水平方向之擺動 流）小形化，可提髙緩衝效果。爲此可以不使經由多岐管 流入進口管之分散液立即合流，而是將分散液引導進入使 用隔壁將進口管入口部區隔成多數區域所構成之小流路內 。具體上是，例如第7圖所示，使用隔壁將進口管寬度方 向分隔成多數區域，而將分散液引進該分隔而成之每一小 流路。藉此，可將流動之混亂及搖擺之大小限制在該小流 路之範圍，使其較易控制。各區域相互間要完全隔離而各 自獨立，阻止流動相互干擾。 而且爲了要進一步由上述進口管，將平坦之液流送給 網目帶’令分散液在上述各區域之前方（以下有時簡稱爲 下游側。再者，本發明在某些地方稱分散液流過來的方向 爲上游，流過去的方向稱作下游），且在開縫狀開口之後 本紙張尺度適用中國國家標準（CNS ) A4規格（21〇X297公董） —----：---.---^ 农 l· — (請先閱讀背面之注意事項再填寫本頁) 訂 -18 - 86. 4. A7 B7， 1T This paper scale is applicable to China National Standard (CNS) Α4 specification (210Χ297mm) Printed by the National Bureau of Standards of the Ministry of Economic Affairs, 315346 A? B7 5. Invention description (15) The lower the effect, the better the latter . By this collision, the dynamic pressure of the jet flow from the multiple manifold 9 can be converted into turbulent kinetic energy and attenuated. In the above inlet pipe, in order to rectify the chaotic dynamic pressure energy of the jet flow, that is, to rectify the dispersing liquid flow transformed into a wave shape, it must be made to pass through a slit-like dispersion with a large width and a narrow high direction Liquid outlet E. The size of the slit-shaped opening, that is, the amount of opening can be determined by the supply and speed of the dispersion in the inlet pipe. For example, as shown in Fig. 6 »or Fig. 7, the dispersion liquid outlet of the inlet pipe is particularly effective when it is opened in the direction opposite to the direction of the streamline. Since the liquid flow from the multi-manifold 9 collides with the rear wall surface and then turns 180 °, the dynamic pressure of the spray flow can be efficiently suppressed. In the above inlet pipe, the sway of the liquid flow (horizontal oscillating flow) can be made smaller Improve the cushioning effect. For this reason, the dispersion liquid flowing into the inlet pipe through the multi-manifold can be immediately merged, but the dispersion liquid can be led into a small flow path formed by partitioning the inlet portion of the inlet pipe into a plurality of areas using a partition wall. Specifically, as shown in Fig. 7, for example, the partition wall is used to divide the inlet pipe in the width direction into a plurality of areas, and the dispersion liquid is introduced into each of the divided small flow paths. In this way, the size of the chaos and sway of the flow can be limited to the range of the small flow path, making it easier to control. All areas should be completely isolated from each other and independent of each other to prevent the flow from interfering with each other. Moreover, in order to further pass the inlet pipe, the flat liquid flow is sent to the mesh belt to make the dispersion liquid in front of the above regions (hereinafter sometimes referred to as the downstream side. In addition, the present invention is called the dispersion liquid flow in some places) The direction of coming is upstream, and the direction of passing is called downstream), and after the slit-shaped opening, the paper size is applicable to the Chinese National Standard (CNS) A4 specification (21〇X297 Gongdong) ------: --- .--- ^ Nongl · — (Please read the precautions on the back before filling out this page) Order -18-86. 4. A7 B7

煩請委員明示86、年 月 日所提之 修iE-i無變更内容i准予修0E1C , 經濟部中央梯準局負工消费合作社印装 五、發明説明（16) 〜/ 方（以下有時簡稱爲上游側）會合。如果不使流過各面域 之分散液合流，而如第1 〇圖A所示直接通過開縫狀之流 出口 E時，由於各區域f之隔壁g之厚度存在，會在網目 帶上形成斜向之液流R1，妨礙單位面稹之重量之均勻化 0 在某種條件下，在上述各區域之下游合流之分敗液在 到達分散液流出口之間，受到壁面尤其是側壁面之阻力， ^邊&度方向兩端部之流速有時會稍爲下降。因此，如果由岐 管裝置送給之分散液之流速保持全宽度範園均相同之情形 下，有時可能不受到側壁面之阻力影響之中央部分會超前 ，其結果，分散液在到達流出口以前便產生拋物線狀或台 形狀之流速分布。當此液流受到開縫狀之分散液流出口 E 之集束作用之壓力損耗時，便如第1 0圖B所示，產生由 中央部向端部之斜流R 2，以補償該流速之宽度方向之不 均勻。此斜流R 2會在薄膜之宽度方向兩端部產生單位面 積之重置不均勻或織維排列不均之情事。 這種現象可以藉提高進口管內流動之分散液之宽度方 向兩端部之流速，予以解決。在上述進口管，若使流過位 於進口管內最外側區域之分散液之流速較內側區域爲髙， •藉此補償兩側壁附近之流速之下降，使其在通過開縫狀流 出口後，仍形成平坦之流速分布，較爲有效。具體上是在 上述進口管，例如第7圖C所示，使位於最外側區域之截 面稹較其他TE域狹窄。縮小外側區域之截面稹之程度可考 置分散液之供應流董及上述合流部分之長度而決定之。依 本紙張尺度逋用中國國家揉準（CNS)A4規格（ 210X297公釐）_ ” - (請先閱讀背面之注$項再填寫本I) 策. 訂 經濟部中央標隼局員工消费合作杜印氧 315346 A7 ___B7__五、發明説明_( π ) 照此方法時，因爲絲毫未操作分散液之流入流量，因此不. 會影響到在岐管裝置之流量配分，及補強用嫌維與熱塑性 '樹脂之分配，可保證均勻之單位面稹之重量分布。 要使流路寬度較爲狹窄可以採取插入縮幅小板，或從 最初就加厚流路壁等手段，但要對應如上述之抄造條件之 變動，則可以預先準備各琴厚度之縮幅小板，再依各種條 件更換即可。再者，爲了減輕側壁面對分散液造成之阻力 之影響，當然以使用摩擦阻力較小之素材（鐵佛·龍等）較 爲有效。 上述開縫狀流出口能夠以各種方法形成，舉例言之， 可如第7圖A所示，利用可調節開度之限幅板形成，其操 作性，汎用性均髙。限幅板3 了最好是從垂直或上方向分 散液流出口成下坡方式設置。如果從下方以上坡方式設置 限幅板，有時會滯留分散液，並不理想。 又如第7圓A所示，若在上述進口管沿分散液之流動 方向分開間隔.設置多片限幅板，整流之效果會更爲確實》 * 本發明之頭箱 本發明人等發現，在頭箱1 3將固態物澳度及流置均 勻之分散液供給網目帶1 1上，以達成薄膜之寬度方向單 位面積之重量分布之均勻化之簡易方法•爲達成此目的， 如第8圖所示之一個例子，藉從進口管2 0送給頭箱1 3 之分散液C在網目帶11上滯留之構造I使分散液C之動 壓及起因於此之擺動不到達網目帶11之方法較爲有效。 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X297公釐）~~~~' -zU - (請先閲讀背面之注意事項再填寫本頁) 經濟部中央揉隼局貝工消费合作社印裝 A7 _B7______ 五、發明説明（丨8 ). 藉此，在連績製造方式，亦可進行相當於所謂批次方式之 抄紙，而不容易產生單位面積之重量不均匀之情事。若以 較分散液中之熱塑性樹脂粒子之末尾沈降速度爲大之速度 ，藉吸引泵浦1 2吸引滯留在網目帶1 1上之分散液c， 則可防止補強用嫌維與熱塑性樹脂之分離。亦可同樣防止 使用發泡分散液時之泡沫與水之分離。令此分散液c滯留 之深度可考量分散液C之粘度，固態物濃度及供應流置， 由吸引泵浦1 2之液體吸引流置，網目帶1 1之·行駛速度 ，以及傾斜角度，滯留部1 5之底面稹等而決定。 〔實驗例〕 玆參照附圖說明本發明之實驗例如下。實驗例之纖維 強化熱塑性樹脂薄片之濕式製造裝置整體系統在以下所述 以外之部分，也可以與第1圖相同。 〔裝置例1〕 第3圖表示實驗所使用之垂直軸旋轉體形狀之岐管裝 置之一。第3圖A表示側面圖，第3圖B表示上面圖。呈 圓筒形狀，其內徑爲4 1 Omm，髙度爲3 0 Omm。從 岐管裝置2 0之切線方向供應原料之分散液之流入口 2 1 (內徑5 Omm)設置在岐管裝置2 0之底面側面部，其 方向與圓筒型岐管裝置乏切線方向一致。同時，在下面 2 3設置突起於岐管裝置內部之圓錐台狀之引導部2 4， 以助長上下循環流及迴旋流之形成。在上面2 2設有6個 本紙張尺度適用中國國家梂準（CNS ) A4規格（210X297公釐） ~~ (請先閲讀背面之注意Ϋ項再填寫本頁)I would like to ask the committee to express 86. The amendments iE-i mentioned in the year, month, and day have no changes. I am allowed to repair 0E1C. The Central Escalation Bureau of the Ministry of Economic Affairs prints and prints the consumer cooperatives. Is the upstream side) meeting. If the dispersion liquid flowing through each surface area is not merged and directly passes through the slit-shaped outflow port E as shown in Fig. 10, the thickness of the partition wall g in each area f will be formed on the mesh belt The oblique flow R1 hinders the homogenization of the weight of the unit surface hull. 0 Under certain conditions, the split liquid that merges downstream of the above-mentioned areas is affected by the wall surface, especially the side wall surface, before reaching the dispersion liquid outlet. The resistance, the flow velocity at both ends of the ^ side & degree direction may decrease slightly. Therefore, if the flow rate of the dispersion liquid supplied by the manifold device is kept the same over the entire width, sometimes the central part that may not be affected by the resistance of the side wall surface will lead, and as a result, the dispersion liquid before reaching the outlet This produces a parabolic or table-shaped flow velocity distribution. When this liquid flow is subjected to pressure loss due to the bundling effect of the slit-shaped dispersion liquid outlet E, as shown in Figure 10, a diagonal flow R 2 is generated from the center to the end to compensate for the flow rate. Unevenness in the width direction. This oblique flow R 2 may cause uneven resetting of the unit area or uneven arrangement of the weave dimensions at both ends in the width direction of the film. This phenomenon can be solved by increasing the flow velocity in the width direction of the dispersion liquid flowing in the inlet pipe. In the above inlet pipe, if the flow velocity of the dispersion liquid flowing through the outermost area in the inlet pipe is higher than that in the inner area, • thereby compensating for the decrease in the flow velocity near the two side walls, so that after passing through the slit-shaped outlet, It still forms a flat flow velocity distribution, which is more effective. Specifically, in the above-mentioned inlet pipe, for example, as shown in Fig. 7C, the cross section of the outermost region is narrower than other TE regions. The extent to which the cross-section of the outer region is reduced can be determined by considering the length of the supply flow of the dispersion liquid and the aforesaid confluence. Use the Chinese National Standard (CNS) A4 specification (210X297mm) _ "-(please read the note $ item on the back and fill in this I) policy according to the size of the paper. Make an order for consumer consumption cooperation of the Central Standard Falcon Bureau of the Ministry of Economic Affairs Oxygen printing 315346 A7 ___B7__ V. Description of invention _ (π) When this method is used, the flow of the dispersion liquid is not operated at all, so it does not. It will affect the flow distribution in the manifold device, as well as the use of reinforcement and thermoplasticity. 'The distribution of resin can ensure a uniform weight distribution per unit area. To narrow the width of the flow path, you can insert a small plate, or thicken the wall of the flow path from the beginning, but it must correspond to the above. For the changes of the copying conditions, you can prepare small plates of various thicknesses in advance, and then replace them according to various conditions. Furthermore, in order to reduce the influence of the resistance caused by the dispersion liquid on the side wall, of course, use the one with lower friction resistance The material (Tiefo · Long, etc.) is more effective. The slit-like outflow port can be formed by various methods, for example, it can be formed using a limiter plate with adjustable opening as shown in Figure 7A, and its operation Sex, pan Even if the limiter plate 3 is installed, it is best to set the dispersion liquid outlet from the vertical or upward direction into a downward slope. If the limiter plate is installed from the downward to the upward slope, the dispersion liquid may be retained, which is not ideal. As shown in the 7th circle A, if the inlet pipe is spaced apart along the flow direction of the dispersion liquid, the effect of rectification will be more certain if multiple limiter plates are provided "* The head box of the present invention has found that The head box 13 supplies a solid substance and a uniformly dispersed dispersion to the mesh belt 11 to achieve a simple method of uniformizing the weight distribution per unit area in the width direction of the film. • For this purpose, as shown in Figure 8 In the example shown, the structure I of the dispersion liquid C fed from the inlet pipe 20 to the head box 1 3 stays on the mesh belt 11 so that the dynamic pressure of the dispersion liquid C and the oscillation caused by it do not reach the mesh belt 11 The method is more effective. This paper scale is applicable to the Chinese National Standardization (CNS) A4 specification (210X297mm) ~~~~ '-zU-(Please read the precautions on the back and then fill out this page) Central Falcon Bureau of the Ministry of Economic Affairs Beigong Consumer Cooperative Printed A7 _B7______ V. Description of Invention丨 8). In this way, in the continuous manufacturing method, papermaking equivalent to the so-called batch method can also be carried out, and it is not easy to cause uneven weight per unit area. If the end of the thermoplastic resin particles in the dispersion is relatively small The settling speed is a large speed, and the suction pump 12 is used to attract the dispersion liquid c that remains on the mesh belt 11 to prevent the separation of the reinforcing dimension and the thermoplastic resin. It can also prevent the use of foamed dispersion liquid. Separation of foam and water. The depth of the dispersion c can be determined by the viscosity of the dispersion C, the concentration of solids and the supply flow. The liquid is drawn by the suction pump 1 2 and the mesh belt 11 travel speed , And the angle of inclination is determined by the bottom surface of the retention part 15 and the like. [Experimental Example] The experimental example of the present invention is described below with reference to the drawings. The overall system of the wet-type manufacturing apparatus for the fiber-reinforced thermoplastic resin sheet of the experimental example may be the same as in Fig. 1 except for the parts described below. [Apparatus example 1] FIG. 3 shows one of the manifold devices in the shape of a rotating body with a vertical axis used in the experiment. Figure 3 A shows a side view, and Figure 3 B shows a top view. It has a cylindrical shape with an inner diameter of 4 1 Omm and a high degree of 3 O Omm. The inlet 2 1 (inner diameter 5 Omm) of the dispersion liquid supplying the raw material from the tangential direction of the manifold device 20 is provided on the side surface of the bottom surface of the manifold device 20, and its direction is consistent with the direction of the tangent of the cylindrical manifold device. . At the same time, a truncated cone-shaped guide portion 24 protruding inside the manifold device is provided on the lower surface 23 to facilitate the formation of up-down circulating flow and swirling flow. There are 6 on top 2 2 This paper standard is applicable to China National Standard (CNS) A4 specification (210X297mm) ~~ (please read the note Ϋ on the back before filling this page)

、1T 315346 修正 Β7, 1T 315346 Amendment Β7

丁 ^ 五、發明説明（19HDing ^ V. Description of the invention (19H

分配流出口25A(內徑20mm)(流出管群A)，在 園筒側面2 6之上面2 2起距離H= 6 5mm之位置設6 個分配流出口25B(內徑20mm)(流出管群B)， 此等以相等間隔共設12個。流出管群A之6個分配流出 口2 5係在內徑4 1 〇mm之岐管裝置2 0之上面2 2， 以相等間隔設B在直徑3 9 0mm之同心園上。同時在岐 管裝置上面2 2，配設兩處確認泡沫滯留用之放氣口 2 8 鋰濟部中央標準局貝工消费合作社印簟 第4圖表 岐管裝置。第 呈園筒形狀， 將原料之分散 5 0 m m )設 而在下面2 3 搅拌裝置2 4 流出口 2 5 A 圚所示之岐管 另一方面 用之推拔型岐 係側面圖。此 設之2 4根多 入岐管裝置之 出而再度流入 流出口 9每一 示資驗所使 4圓A表示 其內徑爲4 液供給岐管 置在岐管裝 設置有外徑 a。其搅拌 ，2 5 B » 裝置相同。 ，在第1 1 管裝置。第 岐管設備在 岐管（以下 流ft爲1 6 之循環流量 根之流量設 用之另一個 側面圖，第 0 c m，長 裝置2 0之 置之上面2 2 5 0 mm 軸與岐管裝 及放氣口 2 圖表示傳統 1 1圖A係 其推拔部側 稱爲分配流 4 0 L / m 爲 2 0 0 L 定成跟採用 垂直軸旋轉髏形狀之 4圖B表示上面圖。 度爲4 0 0 cm。可 流入口 2 1 (內徑 2之圓形平面中心。 之6葉片型水平旋轉 置中心軸一致。分配 8之設置要領與第3 之濕式製造設備所使 上面圖，第1 1圚B 面備有以相等間隔配 出口 .）9。分散液流 i η，從岐管裝置流 / m i η，而將分配 上述垂直軸旋轉髓形 (請先聞讀背面之注$項再填寫本買) :衣_ 訂 本紙張尺度逍用中國围家標準（CNS ) Α4規格（2.10X297公羞) -22 - 315346 A7 經濟部中央揉準局貝工消費合作社印装 ___Έ7_五、發明説明（2〇 ). 狀之岐管裝置2 0時之流量相同。分散液之取樣係從第1. ，3，8，15，19 ’ 2 2之6根分配流出口 9取樣。 第1根分配流出口與第2 2根分配流出口之距離爲 1 3 4 0 m m。 使用這些岐管裝置，如下述進行分散液之濃度分配性 能之比較試驗。 〔實施例1 _ 1〕 在發泡水性液添加直徑1 1 Mm，長度1 3mm之玻 璃纖維（GF)與平均粒徑〇. 9mm之聚丙烯（PP) 粒子，調製成原料之分散液。GF、PP之分散液中之重 置濃度均爲〇· 35%。以360L/min之流量，將 此分散液從流入口 2 1供給第3圖所示之垂直軸旋轉體形 狀之岐管裝置2 0。以流入口 2 1之截面稹除供應流量所 得之平均速度爲3m/s。同時，分配流出口 2 5每一根 之流置爲6 O.L/mi η。在向岐管裝置2 0供應分散液 後立刻從放氣口 2 8擠出系統內之空氣，再經過5分鐘時 同時在各分散液流出口2 5Α (流出管群Α)或2 5 Β ( 流出管群Β )對分散液取樣。並在取樣後打開放氣口 2 8 確認在岐管裝置上部是否產生泡沬滯留。而對流出管群A 及B分別進行兩次上述操作，但打開後立即有分散液流出 ，未看到有發生泡沫滯留之徴兆。 對如此從各分配流出口取樣之分散液進行吸引過濾， 取出玻璃嫌維與P P粒子，經過1 0 〇°C乾燥後秤其重量 本紙張尺度適用中國國家梂準（CNS ) A4規格（210X297公釐) "~ -23 - (請先閣讀背面之注意事項再填寫本頁) 經濟部中央棣準局貝工消費合作杜印装 ΰ 上 5 3 4 6 Α7 _____Β7_五、發明説明（21 ) 。復在6 0 0°C之空氣環境下使P P粒子燃燒，而量剩下 之玻璃嫌維之重置。 以此方法求得流出管群A及B之各分配流出口之G F 濃度及P P濃度。再者，在該項實驗，分散液濃度之均勻 分配性之指標使用變動係數CV值。所謂CV值，係以從 各分配流出口流出之補強@嫌維或熱塑性樹脂之泡液中之 重量平均澳度除其重量澳度之標準偏差值之值以％表示者 »cv值大表示均勻分配性低。 其結果示於表1。流出管群A之濃度分配性較流出管 群B稍爲優異，但其差很小。 〔實施例1 一 2〕 使用第4圖所示垂直軸旋轉體形狀之岐管裝置20， 將透平型攪拌霣之周速設定爲2 . 6 m / s ，與實施例1 1同樣進行分散液之取樣。在取樣後立刻打開放氣口 2 8 ，但與實施例·1 — 1同樣t開放後立即有分散液流出。 其結果示於表1。流出管群A之濃度分配性較流出管 群B稍爲優異，但其差很小。 〔實施例1 一 3〕 使用第4圖所示之垂直軸旋轉體形狀之岐管裝置，將 透平型攪拌翼之周速設定爲1. 3m/s ，而與實施例1 -2同樣對分散液取樣。 對流出管群A於取樣後立即打開放氣口 2 8，打開後 本紙張尺度邊用中國國家標準（CNS ) A4規格（210X297公釐） ' — -24 - (請先閲讀背面之注意事項再填寫本頁) 經濟部中央樣準局員工消費合作社印製 A7 ___B7_五、發明説明（22 ) 立刻有分散液流出。但使用流出管群B時，取樣後立即打 開放氣口 2 8時，則先排出接近氣體狀之泡沬，接著流出 泡液。從這個事實可以看出，岐管裝置2 0內必是如第4 園以模式方式表示發生泡沬滯留現象。 其結果示於表1。流出管群A之GF濃度分配性，較 流出管群B好很多。本實施例因使用流出管群B時發生泡 沫滯留，所補捉之補強用纖維會不定時從分散流出口流出 ，因此可以說是已引起固態物澳度之參差·不一。- 〔比較例1〕 使用第1 1圖所示尺寸之推拔型岐管裝置，與實施例 1 - 1同樣進行分散液之取樣，作爲比較例子。其結果示 於表1 ，可看出PP濃度之CV值較大。復在第13圖描 繪進行取樣之各分配流出口之分散液中之PP濃度》從此 圖可以看出，推拔型岐管裝置將P P粒子彈至循環流出口 〇 崖 〔裝置例2〕 實驗所使用之進口管列示如下》 傳統型進口管1: 如以模式方式示於第1 3圖，以髙6 4mm，長 700mm，寬1 500mm之尺寸，其前端部上面被縮 徑成向分散液之出口朝下之斜坡。在背面配設有連接從岐 本紙張尺度適用中國國家梂準（CNS ) A4規格（210X297公釐） 1.r___：---.__Λ^ LI (請先閲讀背面之注意事項再填寫本頁)Distribution outlet 25A (inner diameter 20mm) (outflow pipe group A), 6 distribution outlets 25B (inner diameter 20mm) (outflow pipe group) are provided at a distance of H = 65 mm from the upper side 2 6 of the cylindrical tube 2 2 B), a total of 12 are set at equal intervals. The 6 distribution outlets 25 of the outflow pipe group A are the upper surface 2 2 of the manifold device 20 with an inner diameter of 4 10 mm, and B are arranged at equal intervals on a concentric circle with a diameter of 390 mm. At the same time, 2 on the manifold device 2 are equipped with two air vents for confirming the retention of foam. 2 8 Limon Ministry of Economy, Central Standards Bureau, Beigong Consumer Cooperative Incorporated Ink 4th figure Manifold device. The first is in the shape of a cylinder, dispersing the raw materials 50 mm). The lower side 2 3 agitator 2 4 outflow port 2 5 A manifold shown on the other hand side view of the push-type manifold used. This set of 24 multi-inlet manifolds exits again and flows into the outflow port. 9 For each laboratory, 4 circles A indicates that the inner diameter is 4 fluid supply manifolds. The manifold is equipped with an outer diameter a. The stirring is the same as the 2 5 B »device. , In the first 1 1 tube device. The second manifold device is on the manifold (the other side view of the flow setting of the circulatory flow root with the downstream ft of 16), the upper part of the 0 cm, long device 2 0 2 2 5 0 mm shaft and the manifold And the vent 2 Figure shows the traditional 1 1 Figure A is the side of the pushing part called the distribution flow 4 0 L / m is 2 0 0 L is set to follow the shape of the vertical axis of rotation of the skull 4 Figure B shows the above figure. 4 0 0 cm. Flowable inlet 2 1 (center of the circular plane of the inner diameter 2. The 6-blade type horizontal rotation is set to the central axis. The setting method of allocation 8 is the same as that of the third wet manufacturing equipment. 1 The B-side is equipped with outlets at equal intervals.) 9. The dispersion flow i η, the flow from the manifold device / mi η, and the above-mentioned vertical axis rotating medulla will be distributed (please read the note item on the back first (Fill in this buy again): clothing _ book size standard Chinese standard (CNS) Α4 specification (2.10X297 public shame) -22-315346 A7 Printed by the Central Bureau of Economic Development of the Ministry of Economic Affairs Beigong Consumer Cooperative ___ Έ7_ 五3. Description of the invention (2〇). The flow rate at the same time as the manifold device 20 is the same. The sampling of the dispersion is from No. 1, 3, 8, 15, 19 2 6 out of 6 distribution outlets are sampled. The distance between the first distribution outlet and the second 2 distribution outlets is 1 3 4 0 mm. Using these manifold devices, the concentration distribution performance of the dispersion is performed as follows Comparative test. [Example 1_1] Glass fiber (GF) with a diameter of 1 1 Mm and a length of 13 mm and polypropylene (PP) particles with an average particle diameter of 0.9 mm were added to the foamed aqueous liquid to prepare a dispersion of raw materials The reset concentration in the dispersion of GF and PP is 0.35%. At a flow rate of 360 L / min, this dispersion is supplied from the inlet 21 to the shape of the vertical axis rotating body shown in Figure 3 Pipe device 20. The average velocity obtained by dividing the supply flow rate by the cross-section of the inlet 21 is 3 m / s. At the same time, the flow of each outlet of the distribution outlet 25 is 6 OL / mi η. 2 0 After the dispersion liquid is supplied, the air in the system is squeezed out from the air outlet 28, and after 5 minutes, at the same time, each dispersion liquid outlet 25 A (outflow tube group A) or 2 5 B (outflow tube group B) pair Sampling the dispersion. After sampling, open the vent port 2 8 to confirm whether foam retention has occurred in the upper part of the manifold. On the other hand, the above operations were performed twice for the outflow tube groups A and B, but immediately after opening, the dispersion liquid flowed out, and there was no sign of foam retention. The dispersion liquid sampled from each distribution outflow port was suction filtered. Take out the glassy dimension and PP particles, and weigh them after drying at 100 ° C. The paper size is applicable to China National Standards (CNS) A4 (210X297mm) " ~ -23-(Please read the first one on the back Matters needing attention and then fill out this page) The Ministry of Economic Affairs, Central Bureau of Precision Industry, Beigong Consumer Cooperation Du Printing Co., Ltd. 5 3 4 6 Α7 _____ Β7_ V. Description of the invention (21). In the air environment of 600 ° C, the P particles are burned, and the remaining glass is reset. In this way, the G F concentration and P P concentration of the distribution outlets of the outflow tube groups A and B are obtained. Furthermore, in this experiment, the index of uniform distribution of the concentration of the dispersion liquid used the value of the variation coefficient CV. The so-called CV value refers to the value of the standard deviation value of the weighted average degree in degrees of the weighted degree of reinforcement in the foaming liquid flowing out of each distribution outflow from the distribution @ 维维 or thermoplastic resin. Low distribution. The results are shown in Table 1. The concentration distribution of the outflow tube group A is slightly better than that of the outflow tube group B, but the difference is very small. [Examples 1-2] Using the manifold device 20 in the shape of a rotating body with a vertical axis as shown in FIG. 4, the circumferential speed of the turbine-type stirring head was set to 2.6 m / s, and dispersion was carried out in the same manner as in Example 11. Liquid sampling. The gas release port 2 8 was opened immediately after sampling, but the dispersion liquid flowed out immediately after opening as in Example 1-1. The results are shown in Table 1. The concentration distribution of the outflow tube group A is slightly better than that of the outflow tube group B, but the difference is very small. [Examples 1 to 3] Using the manifold device in the shape of a rotating body with a vertical axis as shown in FIG. 4, the circumferential speed of the turbine-type stirring blade was set to 1.3 m / s, and the same as in Examples 1-2 Sample the dispersion. For the outflow tube group A, immediately open the bleed port 2 8 after sampling. After opening, the size of the paper uses the Chinese National Standard (CNS) A4 specification (210X297mm) '— -24-(please read the precautions on the back before filling in This page) Printed A7 ___B7_ by the Staff Consumer Cooperative of the Central Prototype Bureau of the Ministry of Economic Affairs. 5. Description of the invention (22) Dispersion immediately flowed out. However, when using the outflow tube group B, when the gas port 28 is opened immediately after sampling, the bubble that is nearly gaseous is discharged first, and then the bubble liquid flows out. From this fact, it can be seen that in the manifold device 20, the bubble retention phenomenon must be expressed in a pattern as in the fourth garden. The results are shown in Table 1. The GF concentration distribution of outflow tube group A is much better than outflow tube group B. In this embodiment, foam retention occurs when the outflow tube group B is used, and the reinforced fibers that are captured may flow out of the dispersion outflow from time to time. Therefore, it can be said that it has caused unevenness and unevenness of solid matter. -[Comparative Example 1] Using a push-out type manifold device of the size shown in FIG. 11, the dispersion liquid was sampled in the same manner as in Example 1-1 as a comparative example. The results are shown in Table 1. It can be seen that the CV value of the PP concentration is large. As shown in Figure 13, the PP concentration in the dispersion at each of the distribution outlets where sampling is performed. From this figure, it can be seen that the push-type manifold device ejects PP particles to the circulation outlet. [Example 2] Laboratory The inlet pipes used are listed as follows. "Traditional inlet pipe 1: As shown in Figure 1 3 in a model manner, with a size of 6 4 mm, length 700 mm, and width 1 500 mm, the top of the front end is reduced in diameter to a dispersion liquid. The slope with the exit facing down. Equipped with a connection from the back to the back. The paper size is applicable to China National Standard (CNS) A4 specification (210X297mm) 1.r ___: ---.__ Λ ^ LI (Please read the precautions on the back before filling this page)

、1T -25 - A7 B7 五、發明説明（23 ) 管裝置引來之分配供應管9之軟管之內徑2.0 mm之噴嘴 3 3共2 4個。各噴嘴3 3間有相同之間隔。分散液至網 目帶之出口係高度1 Omm之開縫狀開口。 緩衝型進口管1: 如第5圖以模式方式表示，係髙1 〇 〇mm，長 1 00mm，寬1 500mm之箱狀，在其上面以柑等間 隔配設有可連接從岐管裝置引來之分配供應管9_·之軟管之 內徑2 0mm之噴嘴3 3共2 4個。分散液至網目帶之出 口係高度10mm之開縫狀開口。 緩衝型進口管2 : 如第6圖以模式方式表示，係高2 5 0mm，長 經濟部中央梂準局負工消費合作社印製 (請先閱讀背面之注意Ϋ項再填寫本頁) 2 0 0mm，寬1 5 0 0mm之箱狀，中央部從底面垂直 立設有高1 5 〇mm之擋板3 1 A。在背面以相同間隔配 設有6個用以·連接從岐管裝置引來之分配供應管9之軟管 之內徑2 0mm之彎頭形狀之噴嘴3 3。噴嘴3 3出口之 開口 33A，以相隔50mm之距離而對著進口管30之 底面。分散液至網目帶之出口係高度1 〇mm之開縫狀開 口。 緩衝型進口管3 : 以模式方式在第7圖A表示側面圖，第7圖B表示上 面圖。係高65mm，寬1 500mm，全長700mm 本紙伕尺度適用中國國家梂準（CNS ) A4規格（210X297公釐） 經濟部中央梯隼局身工消費合作社印製 315346 A7 _B7_五、發明説明（24 ) 之箱狀，上游在整個寬度以相等間隔設有長度4 0 Omm. 之2 3片隔壁3 1 ，分隔成2 4個平行之分割流路3 2。 在各分割流路3 2之上游部，於其上面分別安裝有用以連 接來自岐管裝置之分配供應管9之軟管之內徑2 0 mm之 彎頭形狀之噴嘴33，噴嘴33出口之開口 33A，以相 隔5 0mm之距離面對著^口管3 0後壁面3 0A。 在該等隔壁3 1之前端前方，隔著有1 0 0mm間隔 之會合部3 5設有兩片限幅板36，37。各限·幅板3 6 、3 7係以向後方以4 5°角度傾斜插入之可上下滑動之 板體形成。第1限幅板3 6設置在其開度爲0mm之狀態 時其前端（下端）與隔壁3 1前端之距離爲1 0 0mm之 位置，第2限幅板3 7則設置在與隔壁3 1之前端之距離 300mm之位置。各限幅板36 ，37之開度可自由調 整。 〔實施例2 -’ 1〕 〇分散液調製條件 在分散槽1調製發泡水性液，添加直徑1 1 ，平 均長度13mm之玻璃纖維0. 4重量％，與平均粒徑 0. 9mm之粒狀聚丙烯0. 6重量％，加以攪拌，使其 分散調製成分散液C。 ◦抄紙條件 以第1 1圖所示之推拔型岐管裝置2 0，將以 本紙張尺度適用中國國家梯準（CNS ) A4规格（210X297公釐） (請先閲讀背面之注意事項再填寫本頁) 浪l· 訂 -27 - B7 _ 五、發明説明（25 ) 1 4 4 0 L/m i η之流置送液之分散液C分配到分配供 應管9，經第5圖所示之緩衝型進口管1 ，供給以5· 0 m/mi η之速度移動之網目帶1 1上（網目200/zm ，實效抄紙寬度1500mm) ’進行目標之單位面稹之 重量1 500g/ni之薄膜W之抄造。 〇試驗結果 ’ 將所獏得之薄膜W乾燥後，在寬度方向分軏成3 0份 ，而分別測置其單位面稹之重童β再者’單位面稹之重置 分布之指標，係與實驗例1同樣採用變動係數C v。其結 果示於表2。 〔實施例2 — 2〕 使用第6圖所示之緩衝型進口管2，以跟實施例2 -1同樣之條件進行薄膜之抄造及評估。結果示於表2 » 〔實施例2 - 3〕 經濟部中央梂準局員工消費合作社印策 (請先閲讀背面之注意事項再填寫本頁) 使用第7圖A，Β所示之緩衝型進口管.3，以跟實施 例2 - 1同樣之條件進行薄膜之抄造及評估：》再者，將進 口管之第1限幅板3 6之前端提髙，使其不觸及分散液c 液面。第2限幅板37之開度爲1 〇mm。結果示於表2 〇 〔實施例2 — 4〕 本紙張尺度邊用中國國家標準（CNS ) A4規格（210><297公釐） ~ . — 經濟部中央揉準局貝工消費合作社印製 A7 B7 五、發明説明i： 26 ) 使用第7圖A，B之緩衝型進口管3，以跟實施例2 - 1同樣之條件進行薄膜之抄造及評估。本實施例之第1 限幅板3 6之開度爲1 5mm，第2限幅板3 7之開度爲 1 Omm。結果示於表2。 〔實施例2 — 5〕 * 如第7圖C之上面圖所示*將縮幅小板插入緩衝型進 口管3最外側之分割流路，進行實驗·內接於隔-壁3 1及 進口管之側壁3 8插入縮幅小板3 9，使插入後之流路截 面稹爲插入前之8 0%。縮幅小板3 9之前端部愈往前端 板厚逐漸欒小，以免在流路出口附近因與隔壁3 1之板厚 差致促進扇狀流之產生。 進口管之第1限幅板3 6之開度設定爲1 5mm，第 2限幅板3 7之開度爲1 〇mm，以跟實施例2_ 1同樣 之條件進行薄膜之抄造及評估》結果示於表2。 〔比較例2〕 使用第1 3圖所示之傳統型進口管，以跟實施例2 - 1同樣之條件進行薄膜之抄造及評估。結果一併示於表2 〇 〔裝置例3〕 以模式方式在第8圖A表示實施例3所使用之充滿液 體型頭箱13之側面圖。頭箱之滯留部15之寬度與網目 本紙張尺度適用中國國家標準（CNS ) Α4规格（210X 297公釐） (請先閲讀背面之注意事項再填寫本頁) *ΤΓ 315346 經濟部中央標準局真工消费合作社印装 A7 __B7__五、發明説明<：27 ). 帶1 1大致同寬，而位於其直上方，上面成從後部向前端 部之下坡斜面。其構造是加髙此滯留部1 5之髙度’使分 散液C能維持一定之深度滯留在網目帶11上。本資施例 之頭箱之髙度爲3 0 Omm。 〔實施例3〕 , 使用第11圖所示之推拔型岐管裝置’第13圖所示 之傳統型進口管及充滿液體型頭箱1 3,以跟貧施例2 -1同樣之條件抄造薄膜。網目帶上之分散液之滯留深度爲 2 0 0mm。將所得之薄膜乾燥後向寬度方向3 0分割， 而分別測量其單位面積之重置，求出變動係數C V。其結 果示於表2 » 〔實驗例4〕 組合本發明之垂直軸旋轉體形狀之岐管裝置，緩衝型 進口管及充滿液體型頭箱，進行寬度方向單位面積之重置 更爲均勻之薄膜之抄造》 〔實施例4 — 1〕 使用具有與第4圖所示岐管裝置相同之固態物分配性 能，在上面以同心圃上相等間隔設置2 4個分配流出口之 垂直軸旋轉體形狀之岐管裝置，第6圖所示之緩衝型進口 管，以跟實施例2 - 2相同之條件抄造薄膜。將所獲得之 薄膜加以乾燥後，在寬度方向3 0分割，而分別測量其單 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） ~ I---K-----《.策 l· — (請先閲讀背面之注意事項再填寫本頁) 訂、 1T -25-A7 B7 V. Description of the invention (23) The nozzles of the inner diameter of 2.0 mm of the hose of the distribution and supply pipe 9 introduced by the pipe device 3 3 24 pieces in total. The nozzles 3 and 3 have the same interval. The outlet of the dispersion liquid to the mesh belt is a slit-shaped opening with a height of 1 Omm. Buffer-type inlet pipe 1: As shown in figure 5 in a model manner, it is a box-shaped box with a height of 100 mm, a length of 100 mm, and a width of 1500 mm. Above it is arranged at equal intervals with oranges. A total of 24 nozzles 3 3 with an inner diameter of 20 mm from the hose of the distribution supply pipe 9_ ·. The outlet from the dispersion to the mesh belt is a slit-shaped opening with a height of 10 mm. Buffered inlet pipe 2: As shown in figure 6 as a model, it is 2 50 mm high and is printed by the Ministry of Economic Affairs, Central Bureau of Labor, and Consumer Cooperative (please read the note Ϋ on the back and fill in this page) 2 0 A box shape of 0mm and a width of 1500mm. The baffle 3 1A with a height of 1500mm is set upright in the center from the bottom. At the same interval on the back, six elbow-shaped nozzles 33 for connecting the hose of the distribution supply pipe 9 from the manifold device with an inner diameter of 20 mm are arranged. The opening 33A of the outlet of the nozzle 33 faces the bottom surface of the inlet pipe 30 at a distance of 50 mm. The outlet from the dispersion to the mesh belt is a slit-shaped opening with a height of 10 mm. Buffer-type inlet pipe 3: The side view is shown in Figure 7 in a schematic manner, and the top view is shown in Figure 7 B. The system is 65mm high, 1 500mm wide and 700mm long. The paper size is applicable to the Chinese National Standard (CNS) A4 (210X297mm). Printed 315346 A7 _B7_ by the Ministry of Economic Affairs, Central Falcon Bureau, Workers and Consumers Cooperative. ) In the shape of a box, the upstream of the whole width is provided at equal intervals with a length of 40 Omm. 2 3 pieces of partition walls 3 1 are divided into 24 parallel divided flow channels 3 2. At the upstream of each divided flow path 32, an elbow-shaped nozzle 33 with an inner diameter of 20 mm for connecting the hose from the distribution supply pipe 9 of the manifold device to the opening of the outlet of the nozzle 33 is installed 33A, facing the rear wall surface 30A of the mouth tube 30 at a distance of 50mm. In front of the front ends of the partition walls 31, two limiting plates 36, 37 are provided via a junction 35 with a spacing of 100 mm. Each of the limiting and limiting plates 3 6 and 3 7 is formed by a slidable plate body inserted obliquely at an angle of 45 ° to the rear. The first limiter plate 36 is set at a position where the distance between the front end (lower end) and the front end of the partition wall 3 1 is 100 mm when the opening degree is 0 mm, and the second limiter plate 3 7 is set at a distance from the partition wall 3 1 The distance between the front end and 300mm. The opening of each limiter 36 and 37 can be adjusted freely. [Example 2-'1] 〇 Dispersion liquid preparation conditions A foaming aqueous liquid was prepared in the dispersion tank 1, and glass fibers with a diameter of 1 1 and an average length of 13 mm of 0.4% by weight were added, and the average particle size was 0.9 mm. Polypropylene 0.6% by weight, stirred and dispersed to prepare dispersion C. ◦The paper-making conditions are based on the push-out manifold device 20 shown in Figure 11 and the paper standard will be applied to the Chinese National Standard (CNS) A4 specification (210X297mm) (please read the precautions on the back before filling in (This page) Lang l · ding-27-B7 _ V. Description of the invention (25) 1 4 4 0 Dispersion C of L / mi η flow delivery liquid is distributed to the distribution supply pipe 9, as shown in Figure 5 Buffer-type inlet tube 1, supplying mesh belt 1 1 that moves at a speed of 5.0 m / mi η (mesh 200 / zm, effective papermaking width 1500mm) 'target film with a unit weight of 1 500g / ni W made up. 〇Test results' After drying the tapir film W, split it into 30 parts in the width direction, and measure the heavy child β of the unit surface grain separately. The index of the reset distribution of the unit surface grain is As in Experimental Example 1, the coefficient of variation C v is used. The results are shown in Table 2. [Example 2-2] Using the buffer-type inlet pipe 2 shown in FIG. 6, the film was fabricated and evaluated under the same conditions as in Example 2-1. The results are shown in Table 2 »[Examples 2-3] Printed by the Employees’ Consumer Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs (please read the precautions on the back before filling out this page) Use the buffered imports shown in Figure 7 A, B Tube .3, the film was copied and evaluated under the same conditions as in Example 2-1: "In addition, the front end of the first limiting plate 36 of the imported tube was raised so that it would not touch the liquid surface of the dispersion c. . The opening degree of the second limiter plate 37 is 10 mm. The results are shown in Table 2 〇 [Examples 2-4] The paper size is printed using the Chinese National Standard (CNS) A4 specification (210 > < 297 mm) ~. — Printed by the Beigong Consumer Cooperative of the Ministry of Economic Affairs A7 B7 V. Description of the invention i: 26) Using the buffer-type inlet tube 3 in Figures A and B of Figure 7, the film was fabricated and evaluated under the same conditions as in Example 2-1. In this embodiment, the opening of the first limiter plate 36 is 15 mm, and the opening of the second limiter plate 37 is 10 mm. The results are shown in Table 2. [Embodiment 2-5] * As shown in the upper figure of Figure 7 C * Insert the narrowing plate into the outermost divided flow path of the buffer-type inlet tube 3, conduct the experiment · Inscribed on the partition wall 3 1 and the inlet The side wall 38 of the tube is inserted into the narrowing plate 39 so that the cross section of the flow path after insertion is 80% before insertion. The thickness of the small plate 3 9 is increased from the front end to the front end. The plate thickness gradually decreases, so as not to promote the fan-shaped flow near the outlet of the flow path due to the difference in plate thickness with the partition wall 3 1. The opening of the first limiting plate 3 6 of the inlet tube is set to 15 mm, and the opening of the second limiting plate 3 7 is 10 mm, and the film was copied and evaluated under the same conditions as in Example 2_1.示 于 表 2。 Shown in Table 2. [Comparative Example 2] Using the conventional inlet tube shown in Figure 13 and under the same conditions as in Example 2-1, the film was fabricated and evaluated. The results are shown in Table 2 together. [Apparatus Example 3] A side view of the liquid-filled head box 13 used in Example 3 is schematically shown in FIG. 8A. The width of the retention section 15 of the first box and the size of the net paper are applicable to the Chinese National Standard (CNS) Α4 specification (210X 297 mm) (please read the precautions on the back and then fill out this page) * ΤΓ 315346 Industrial and Consumer Cooperative Printed A7 __B7__ V. Description of the invention <: 27). The belt 1 1 is approximately the same width, and is located directly above it, and the upper surface is a downward slope from the rear to the front. Its structure is to increase the high degree of this retention portion 15 so that the dispersion liquid C can stay on the mesh belt 11 at a certain depth. The height of the head box in this example is 30 Omm. [Embodiment 3], using the push-type manifold device shown in FIG. 11 'the conventional inlet pipe shown in FIG. 13 and the liquid-filled head box 1 3, under the same conditions as the poor embodiment 2 -1 Copying film. The retention depth of the dispersion liquid on the mesh belt is 200 mm. After the obtained film was dried, it was divided into 30 in the width direction, and the reset per unit area was measured to obtain the coefficient of variation C V. The results are shown in Table 2 »[Experimental Example 4] The vertical axis rotating body-shaped manifold device of the present invention is combined with a buffer-type inlet tube and a liquid-filled head box to perform a more uniform film reset in the width direction per unit area The copying "[Embodiment 4-1] The shape of a vertical axis rotating body having the same solid material distribution performance as the manifold device shown in FIG. 4 and having 24 distribution outlets arranged at equal intervals on the concentric garden The manifold device, the buffer-type inlet tube shown in Fig. 6, made the film under the same conditions as in Example 2-2. After the obtained film is dried, it is divided into 30 in the width direction, and the size of the single paper is measured respectively to apply the Chinese National Standard (CNS) A4 specification (210X297 mm) ~ I --- K ----- " . 策 l · — (Please read the precautions on the back before filling out this page)

位面稹之重置，求出變動係數CV値。其結果示於表3。 〔實施例4 — 2〕 使用跟實施例4 — 1相同之岐管裝置，及第7圖A， B所示之緩衝型進口管，以跟資施例2 - 4同樣之條件抄 造薄膜。將所獲得之薄膜加以乾燥後，在寬度方向3.0分 割，而分別測量單位面稹之重置，求出變動係數（：乂値_。 其結果示於表3。 〔實施例4 — 3〕 使用跟實施例4 - 1同之垂直軸旋轉體形狀之岐管裝 置，第8圇B及C分別表示其側面圖及背面圖之緩衝型進 口管及充滿液體型頭箱，以跟實施例3相同之條件抄造薄 膜。 經濟部中央揉準局貝工消费合作社印簟 (請先聞讀背面之注$項再填寫本頁) 本實施例之特長在於，在充滿液體型頭箱1 3，縱向 設置具有與第7圖A，B所示之緩衝型進口管同等性能之 進口管這一點。亦即，此縱向緩衝型進口管係介由進口管 分隔壁3 0 B，一體形成在充滿液體型頭箱1 3之滯留部 1 5之流線方向後方側，分散液流入口 3 3係面對進口管 之底面之分散液碰撞面3 0 A開口。分散液C在碰撞分散 液碰撞面3 0 A而反轉後，成爲上昇流在由垂直之隔壁 31分隔之區域內±昇，在位於隔壁31上方之會合部 3 5合流，再從進口管分隔壁3 0 B上端部之溢流口 E溢 出而.流入滯留部1 5。這時之限幅板3 6係由配設在湓流 本紙張尺度適用中國國家標準（CNS ) A4规格（210X297公釐）~ '一" A7 B7_ 五、發明説明（29 ) 出口 E上之蓋體之水平板所形成，令其接觸到從溢流出口. E溢出之分散液C之液面，以抑制液面之擺動，將其整流 成穩定之液流。 將所獏得之薄膜加以乾燥後，在寬度方向3 0分割， 而分別測量其單位面稹之重置，求出變動係數C V。其結 果示於表3。 r (表1 ) -----L---r--《装 l· — (請先閲讀背面之注意事項再填寫本頁) 經濟部中央樣準局貝工消費合作社印製 岐管裝置 流出管群 C V值 形狀 GF PP 資施例1-1 第3圖 A 1.08 0.78 第3圖 B 1. 40 1.10 實施例1-2 第4圖 A 0.63 1.01 第4圓 B 1.30 1.10 實施例1-3 第4圖 A 0.81 1.02 第4圓 B 3.22 2.86 比較例1 第1 1圖 ' 1. 87 4.70 本紙張尺度適用中國國家梯準（CNS ) A4規格（210X297公釐） 訂 經濟部中央揉準局負工消費合作社印装 5 3 46 A7 B7 五、發明説明（30 ) (表2 ) 岐管裝 置形狀 進口管 •形狀 分散液 滯留部 深度 寬度方向 單位面稹 重置CV值 實施例2-1 第11圖 第5圖 3 0mm 4.5 資施例2-2 第11圖 第5圓. 3 0mm 3.1 實施例2-3 第1 1圖 第7圖 3 0 mm 2. 3 實施例2-4 第11圖 第7圖a，b 3 0mm 2.1 實施例2-5 第1 1圖 第7圖C 3 0mm 2.0 比較例2 第11圚 第13圖 3 0 mm 6.5 實施例3 第11圖 第1 3圖 2 0 0mm 2. 5 (請先閱婧背面之注意Ϋ項再填寫本頁) Γ 本紙張尺度適用中國國家揉準（CNS ) A4規格（210X.297公釐） A7 B7 經濟部中央樣準局男工消費合作社印裝 五、發明説明（31 ) (表3 ) 岐管裝 置形狀 進口管 0狀 分散液 滯留部 深度 寬度方向 單位面稹 重置CV值 實施例4-1 圓筒型 第6圖 3 0 mm 2.2 實施例4-2 圓筒型 第7圖a, b 3 0 mm 1.2 實施例4-3 圓筒型 第8圖b，c 2 0 0mm 0. 9 k —--,,---1---C 衣-- (請先閲讀背面之注意事項再填寫本頁) 訂 本紙張尺度適用中國國家橾準（CNS ) A4规格（210X·297公釐） -34 - 315346 86_ 年 ;4•月2^^正______ A7 B7 鋰濟部中央梂準局負工消費合作社印«. 五、發明説明（32) 〔圖面之簡單說明〕 〔圖1〕 顯示以往之織維强化熱塑性樹脂薄片之裝置 〔圖2〕 顯示將發明中歧管液雅分散流的具雅化圖形。 〔圖3 A及3 B〕After resetting the plane plane, find the coefficient of variation CV. The results are shown in Table 3. [Example 4-2] Using the same manifold device as in Example 4-1, and the buffer type inlet pipe shown in FIGS. 7A and B, the film was fabricated under the same conditions as in Example 2-4. After the obtained film was dried, it was divided into 3.0 in the width direction, and the reset of the unit plane was measured separately, and the coefficient of variation was calculated (: 乤 _. The results are shown in Table 3. [Examples 4-3] Use The manifold device with the same vertical axis rotating body shape as in Example 4-1, 8th B and C show the buffer inlet port and liquid-filled head box in the side view and back view, respectively, to be the same as in Example 3 The condition is to make a thin film. The Ministry of Economic Affairs Central Bureau of Accreditation Bureau Beigong Consumer Cooperative Ink (please read the note $ item on the back and then fill out this page) The specialty of this example is that the liquid-filled head box 13 is installed vertically This is an inlet pipe with the same performance as the buffer inlet pipe shown in Figure 7 A and B. That is, the longitudinal buffer inlet pipe is formed integrally on the liquid-filled head through the inlet pipe partition wall 3 0 B The retention portion 15 of the tank 1 3 is located on the rear side in the streamline direction, and the dispersion liquid inlet 3 3 faces the dispersion liquid collision surface 3 0 A at the bottom surface of the inlet pipe. The dispersion liquid C collides with the dispersion liquid collision surface 3 0 A And after the reversal, it becomes an ascending current divided by the vertical partition 31 ± L within the area, merge at the junction 35 located above the partition 31, and then overflow from the overflow port E at the upper end of the inlet pipe partition 3 0 B and flow into the stagnation portion 15. The limiter plate 3 6 at this time It is formed by the horizontal plate of the Chinese standard (CNS) A4 specification (210X297mm) ~ '一 " A7 B7_ equipped with the size of the paper, and the description of the invention (29) The horizontal plate of the cover on the export E, Make it come into contact with the liquid surface of the dispersion liquid C overflowing from the overflow outlet. E to suppress the swing of the liquid surface and rectify it into a stable liquid flow. After drying the obtained tapir, in the width direction 3 0 Divide and measure the reset of the unit surface grain separately, and find the coefficient of variation CV. The results are shown in Table 3. r (Table 1) ----- L --- r-- 《装 l · — (Please Read the precautions on the back first and then fill out this page) CV value shape GF PP of the outflow pipe group of the manifold device printed by the Beigong Consumer Cooperative of the Central Sample Bureau of the Ministry of Economic Affairs GF PP Investment Example 1-1 Figure 3 A 1.08 0.78 Figure 3 B 1. 40 1.10 Example 1-2 Figure 4 A 0.63 1.01 4th circle B 1.30 1.10 Example 1-3 Figure 4 A 0.81 1.02 4th circle B 3.22 2. 86 Comparative Example 1 Figure 1 1 '1. 87 4.70 This paper scale is applicable to China National Standards (CNS) A4 specifications (210X297 mm). Printed by the Ministry of Economic Affairs, Central Bureau of Standards and Customs Consumer Cooperatives 5 3 46 A7 B7 5 2. Description of the invention (30) (Table 2) Manifold device shape inlet pipe • shape dispersion liquid retention part depth width direction unit surface hump reset CV value Example 2-1 Figure 11 Figure 5 Figure 3 0mm 4.5 Example 2 -2 Figure 11 circle 5. 3 0mm 3.1 Example 2-3 Figure 1 1 Figure 7 Figure 3 0 mm 2. 3 Example 2-4 Figure 11 Figure 7 a, b 3 0mm 2.1 Example 2 -5 Figure 1 Figure 1 Figure 7 C 3 0mm 2.0 Comparative Example 2 Figure 11 Figure 13 Figure 3 0 mm 6.5 Example 3 Figure 11 Figure 1 3 Figure 2 0 0mm 2. 5 (Please read the note on the back of Jing first Ϋ Item and then fill out this page) Γ This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X.297mm) A7 B7 Printed by the Central Sample Bureau of the Ministry of Economic Affairs, Male Workers' Consumer Cooperative V. Invention description (31) (31) ( Table 3) Manifold device shape inlet pipe 0-shaped dispersion liquid retention portion depth width direction unit surface 稹 reset CV value Example 4-1 Cylindrical type Figure 6 0 mm 2.2 Example 4 -2 Cylindrical Figure 7 a, b 3 0 mm 1.2 Example 4-3 Cylindrical Figure 8 b, c 2 0 0mm 0.9 k —-- ,, --- 1 --- C -(Please read the precautions on the back before filling in this page) The size of the revised paper is applicable to China National Standard (CNS) A4 (210X · 297mm) -34-315346 86_ year; April • March 2 ^^ 正______ A7 B7 Printed by the Cooperative Consumer Cooperative of the Central Bureau of the Ministry of Lithium and Economics. 5. Description of the invention (32) [Simple description of the drawing] [Figure 1] A device for displaying the conventional woven-strengthened thermoplastic resin sheet (Figure 2 〕 Shows an elegant graphic of the elegant dispersion of the manifold fluid in the invention. [Figure 3 A and 3 B]

具體描繪本發明裝置之一，圖3 A係截面圖，圖3 B 係平面圖。 〔圖4 A及4 B〕 具體描繪本發明之另一裝置，圖4 A係截面圖，圖4 B係平面圖。 〔圖5〕 本發明具體化進口管之截面·圖。 〔圓6〕 本發明另一具髏化進口管之截面圇。 〔圖 7 A、7 B 及 7 C〕 描繪本發明數個具體化進口管。 圖7 A係截面圖，圖7 B係平面圖，及圖7 C係另一 具體化進口管之平面圖。 〔圖 8A、8B 及 8C〕 描繪本發明之頭箱。 圖8 A係例3頭箱截面圖，圚8 B係例4頭箱截面圆 ，圓8 C係圖8 B具镰頭箱，之背面圖。 .〔圖9〕顯示以往推拔式歧管。 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐> (請先聞讀背面之注$項再填寫本頁) ----訂 _ ΛSpecifically depicting one of the devices of the present invention, FIG. 3 is a sectional view of FIG. 3, and FIG. 3 is a plan view of B. [FIG. 4 A and 4 B] Another device of the present invention is specifically described, FIG. 4 A is a cross-sectional view, and FIG. 4 B is a plan view. [Fig. 5] The cross section and drawing of the inlet pipe embodied in the present invention. [Round 6] Another cross-sectional wall of the present invention has a skull-shaped inlet pipe. [Figures 7 A, 7 B, and 7 C] depict several embodied inlet pipes of the present invention. Figure 7 is a sectional view of Figure A, Figure 7 is a plan view of Figure B, and Figure 7 is a plan view of another specific inlet pipe. [Figures 8A, 8B, and 8C] depict the head box of the present invention. Figure 8 Sectional view of the head box of the A series of Example 3, and the cross section of the head box of the Example 4 of the B series of the B box, and the circle 8 C of Figure 8 B with a sickle box. . [Figure 9] shows the conventional push-type manifold. This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm> (please read the $ item on the back and then fill in this page) ---- Subscribe _ Λ

A7 B7 五、發明説明（33) 〔圖 1 Ο A 及 1 Ο B〕 圊1 Ο A係本發明之依此例顯示接進開縫狀之進口管 (請先聞讀背面之注項再填寫本買) ，圖10A係包含間隔部分，圖10B係不包含間隔部分 〔圖11A及圚11B〕顯示以往推拔式歧管。 〔圖1 2〕描繪圖1 1進行取樣之各分配出口分散液 中之P P澳度。 〔圖1 3〕顯示以往推拔式歧管之截面圖。 〔符號說明〕 1 原料調製部 9 多歧管 10 薄膜抄造部 1 1 網目帶 12 吸入箱 13 頭箱 15 滯留部 經濟部中央揉準局貝工消费合作社印装 2 0 分配裝置 2 1 流入口 24a 水平旋轉攪拌裝置 2 5 A 分配流出口（流出管群A) 2 5 B 分配流出口（流出管群B) 2 6 圓简側面 3 0 進口管 本紙張尺度逍用中國困家橾率（CNS ) A4规格（210X297公釐） -36 - 五、發明説明（34) 3 1 間 隔 壁 3 2 分 割 流 路 3 3 喷 嘴 3 A 噴 嘴 出 □ 開 P 3 5 ST 合 部 3 6 · 、3 7 限 幅 板 3 8 側 壁 3 9 幅 縮 小 板 4 0 乾 燥 部 5 0 捲 取 部 C 分 散 液 E 分 散 液 出 □ W 薄 膜 A7 B7 ·*·- Λ « I--------Λ>------ir-------Λ (請先聞讀背面之注$項再填寫本頁) 經濟部中央標準局te：工消费合作社印裝 本紙張尺度逍用中國國家橾準（CNS ) A4规格（210X297公釐） -37 -A7 B7 Fifth, the description of the invention (33) [Figure 1 Ο A and 1 Ο B] 圊 1 Ο A is the inlet pipe of the invention shown in this example into the slit (please read the note on the back and fill in (Buy), Fig. 10A series includes a spacer portion, and Fig. 10B series does not include a spacer portion (Figs. 11A and 11B) shows a conventional push-type manifold. [Fig. 12] Describe the P P O in the dispersion liquid of each distribution outlet sampled in Fig. 11. [Fig. 13] A cross-sectional view showing a conventional push-type manifold. [Description of symbols] 1 Raw material preparation section 9 Multi-manifold 10 Film manufacturing section 1 1 Mesh belt 12 Suction box 13 Head box 15 Printed by the Central Ministry of Economic Affairs, Ministry of Economic Affairs, Beigong Consumer Cooperative 2 2 Distribution device 2 1 Inlet 24a Horizontal rotating stirring device 2 5 A Distributing outflow (outflow tube group A) 2 5 B Distributing outflow (outflow tube group B) 2 6 Round and simple side 3 0 Inlet tube paper size free use Chinese trapped household rate (CNS) A4 specification (210X297 mm) -36-V. Description of the invention (34) 3 1 Partition wall 3 2 Split flow path 3 3 Nozzle 3 A Nozzle outlet □ Open P 3 5 ST Joint 3 6 ·, 3 7 Limiter 3 8 Side wall 3 9 Reduction plate 4 0 Drying section 5 0 Winding section C Dispersion E Dispersion out □ W Film A7 B7 · * ·-Λ «I -------- Λ > ---- --ir ------- Λ (please read the $ item on the back and then fill in this page) Central Bureau of Standards of the Ministry of Economic Affairs te: Printed copies of the paper size of the Industrial and Consumer Cooperative Society China National Standard (CNS) A4 specification (210X297mm) -37-

Claims (1)

8888 ABCD 經濟部中央標隼局具工消費合作社印製 六、申請專利範圍 1. 一種纖維強化熱塑性樹脂薄片之濕式製造設備’ N 其特徴爲，具備有從下列之群中選擇之至少一種裝置 .r (a )呈垂直軸旋轉體形狀，用以分配包含補強用嫌 維及樹脂之分散液之岐管裝置（manifold )， (b )具備有可使該分散液至少碰撞壁面一次之構造 之緩衝型進口管（inlet )， (c)具備有可使該分散液滯留在移動之無端網目帶 上至一定深度以上之構造之充滿液體型頭箱（head Box ) ° 2. 如申請專利範圍第1項所述之嫌維強化熱塑性樹 脂薄片之濕式製造設備，其特徴爲，具備有上述垂直軸旋 轉體形狀之岐管裝置，及緩衝型進口管。 3. 如申請專利範圍第1項所述之嫌維強化熱塑性樹 脂薄片之濕式製造設備，其特徵爲，具備有上述垂直軸旋 轉體形狀之岐.管裝置，及充滿液體型頭箱》 4. 如申請專利範圍第1項所述之織維強化熱塑性樹 脂薄片之濕式製造設備，其特徵爲，具備有上述緩衝型進 口管，及充滿液體型頭箱。 5. 如申請專利範圍第1項所述之纖維強化熱塑性樹 脂薄片之濕式製造設備，其特徵爲，.具備有上述垂直軸旋 轉體形狀之岐管裝置，緩衝型進口管，以及，充滿液體型 頭箱。 6. 如申請專利範圍第1項所述之繊維強化熱塑性樹 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） (請先閲讀背面之注意事項再填寫本頁)8888 ABCD Printed by the Central Standard Falcon Bureau of the Ministry of Economic Affairs. Co., Ltd. 6. The scope of the patent application 1. A wet-type manufacturing facility for fiber-reinforced thermoplastic resin sheets. N It is characterized by having at least one device selected from the following groups .r (a) is in the shape of a rotating body with a vertical axis, and is used to distribute a manifold containing a dispersion of reinforcing susceptible resin, (b) with a structure that allows the dispersion to hit the wall at least once Buffer inlet tube (inlet), (c) A liquid-filled head box (head box) with a structure that allows the dispersion to stay on the moving endless mesh belt to a certain depth or more ° The wet-type manufacturing equipment for the heat-resistant thermoplastic resin sheet described in item 1 is characterized by being equipped with a manifold device having the shape of a rotating body with a vertical axis as described above, and a buffer-type inlet tube. 3. The wet-type manufacturing equipment for suspected dimension-strengthened thermoplastic resin sheet as described in item 1 of the patent scope, which is characterized by a manifold device with the shape of the vertical axis rotating body and a liquid-filled head box 4 . Wet-type manufacturing equipment for woven-strengthened thermoplastic resin sheets as described in item 1 of the patent scope, characterized by the above-mentioned buffer-type inlet pipe and liquid-filled head box. 5. The wet-type manufacturing equipment for the fiber-reinforced thermoplastic resin sheet as described in item 1 of the patent scope is characterized by a manifold device with the shape of the above-mentioned vertical axis rotating body, a buffer-type inlet pipe, and, filled with liquid Type head box. 6. As described in item 1 of the patent scope, the dimension-strengthened thermoplastic tree is in accordance with the Chinese National Standard (CNS) A4 (210X297mm) (Please read the precautions on the back before filling this page) -35 — A8 B8 C8 ____ D8 六、申請專利範圍 脂薄片之濕式製造設備，其特徵爲，上述垂直軸旋轉體形 狀之岐管裝置在同一髙度備有同徑之分配流出口。 7. 如申請專利範園第6項所述之嫌維強化熱塑性樹 脂薄片之濕式製造設備，其特徴爲，上述垂直軸旋轉體形 狀之岐管裝置備有，從垂直軸旋轉對稱面之切線方向導入 上述分散液之流入口。 8. 如申請專利範圍第6項所述之嫌維強化熱塑性樹 脂薄片之濕式製造設備，其特徴爲，上述垂直軸旋轉體形 狀之岐管裝、置備有，在該垂直軸旋轉體形狀之中心軸上， 從垂直上方導入分散液之流入口。 9. 如申請專利範圍第8項所述之繅維強化熱塑性樹 脂薄片之濕式製造設備，其特徵爲，上述垂直軸旋轉體形 狀之岐管裝置在內部備有，成水平旋轉之攪拌裝置，其携 拌軸與該垂直軸旋轉體形狀之中心軸一致。 經濟部中夹梯隼局買工消資合作社印製 (請先閲讀背面之注意事項再填寫本頁) 10. 如申請專利範園第6項至第9項中任一項所述 之繊維強化熱塑性樹脂薄片之濕式製造設備，其特徵爲， 上述垂直軸旋轉體形狀之岐管裝置，在以該垂直軸旋轉體 形狀之中心軸爲中心之大體一個同心圖上，以相等間隔設 有上述分散液之分配流出口。 11. 如申請專利範圍第10項所述之嫌維強化熱塑 性樹脂薄片之濕式製造設備，其特徴爲，上述垂直軸旋轉 體形狀之岐管裝置之上述分配流出口朝垂直上方開口。 12. 如申請專利範圍第1項所述之纖維強化熱塑性 樹脂薄片之濕式製造設備’其特徵爲’上述緩衝型進口管 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） -36 - 經濟部中央標準局W5；工消費合作社印袈 A8 BS C8 D8 七、申請專利範圍 具備有，在上述分散液之流出口有跟分散液之吸引過濾領 域同寬之開縫狀之開口構造。 1 3 .如申請專利範圍第1 2項所述之繅維強化熱塑 性樹脂薄片之濕式製造設備，其特徴爲，上述緩衝型進口 管具備有，用以在上述分散液之流出口形成與分散液之吸 引過濾領域同寬之開縫狀開口，而可調節開口度之限幅（ s 1 i ce )板。 1 4 .如申請專利範圍第1 3項所述之嫌維.強化熱塑 性樹脂薄片之濕式製造設備，其特徵爲，上述緩衝型進口 管在上述分散液之流動方向，分開間隔備有多片限副板。 1 5 .如申請專利範圍第1 2項至第1 4項中之任一 項所述之纖維強化熱塑性樹脂薄片之濕式製造設備，其特 徵爲，上述緩衝型進口管具備有，可使上述分散液至少碰 撞與流線方向反方向之壁面一次之構造。 16. 如申請專利範團第12項至第14項中之任一 項所述之嫌維.強化熱塑性樹脂薄片之濕式製造設備，其特 徵爲，上述緩衝型進口管之內容部分在上述分散液之吸引 過濾領域之寬度方向區隔成多數區域，可將該分散液導入 各區域，同時在各區域之前方且在上述開縫狀開口之後方 ，具有可使分散液流會合之構造。 17. 如申請専利範圍第1項所述之嫌維強化熱塑性 樹脂薄片之濕式製造設備，其特徵爲，上述緩衝型進口管 之內容部分具備有，在上述分散液之吸引過濾領域之寬度 方向區隔成多數區域，可將該分散液導入各區域，同時可 本紙張尺度逍用中國國家標準（CNS ) A4洗格（210X297公釐） (請先聞讀背面之注意ί項再填寫本頁) 、1T 一丨 -37 - 315346 A8 B8 C8 D8 六、申請專利範圍 (請先閲讀背面之注意事項再填寫本頁) 使上述分散液至少碰撞與流線方向反方向之壁面一次之構 造，並具備有，在各區域之前方且在上述開縫狀開口之後 方，使分散液流會合之構造，而且，在上述分散液之流動 方向，分開間隔備有一片或多片板。 1 8 ·如申請專利範圍m- S/mm第ι 7項所述之纖 維強化熱塑性樹脂薄片之濕式設備，其特徵爲，上述 緩衝型進口管之上述區域中位於最外側之區域之截面積較 其他區域爲癍小。 1 9 .如申請專利範園第ι項所述之纖維強化熱塑性 樹脂薄片之濕式製造設備，其特徴爲，在上述充滿液體型 頭箱，上述一定深度係指流入頭箱之分散液之搖動不會到 達上述網目帶上之深度。 2 0.—種纖維強化熱塑性樹脂薄片之濕式製造方法 ，係將包含補強用纖維及熱塑性樹脂之分散液，從岐管裝 置通過進口管，供給移動中之無端網目帶上，一面吸引過 濾而抄取片狀.之薄膜之織維強化熱塑性樹脂薄片之濕式製 造方法，其特徵爲， 經濟部中央標準局爲工消費合作社印製 將在該岐管裝置分岐之分散液，導入以隔壁將該進口 管之入口部均等分隔成多數區域而成之小流路，令分散液 碰撞到該小流路之壁面而轉向，以降低動壓，然後使分散 液合流，再通過開縫狀之分散液流出口以調整分散液之波 狀擺動，同時使液流前頭平坦化，而供給網目帶上。 21. —種嫌維強化熱塑性樹脂薄片之濕式製造方法 ，係將包含補強用嫌維及熱塑性樹脂之分散液，從歧管裝 本尺度適用中國國家梂準（CNS ) A4规格（210X297公釐i -38 - At Ο _______ D8 k、申請專利範圍 置通過進口管，供給移動中之無端網目帶上， 濾而抄取片狀之薄膜之繊維強化熱塑性樹脂薄 造方法，其特徵爲， 在寬度方向兩端部提高在上述進口管內流 之流速，然後通過開縫狀之分散液流出口調整 狀擺動，同時使液流前頭平坦化，而供給網目 2 2.—種織維強化熱塑性樹脂薄片之濕 ，係將包含補強用嫌維及熱塑性樹脂之分散液 置通過進口管，供給移動中之無端網目帶上， 濾而抄取片狀之薄膜之繊維強化熱塑性樹脂薄 造方法，其特徵爲， 在載置該分散液之吸引過濾領域上之頭箱 散液滯留在網目帶上，使由該進口管吐出之分 之擺動不到達網目帶。 一面吸引過 片之濕式製 動之分散液 分散液之波 帶上。 式製造方法 ，從岐管裝 一面吸引過 片之濕式製 內部，令分 散液所具有 (請先閲讀背面之注意Ϋ項再填寫本頁) 、1T 經濟部中央標率局貝工消費合作社印製 本紙張尺度逋用中國國家標準（CNS ) Α4規格（210Χ297公釐） 39-35 — A8 B8 C8 ____ D8 VI. Scope of patent application Wet manufacturing equipment for grease sheets is characterized in that the manifold device in the shape of the rotating body of the vertical axis has distribution outlets of the same diameter at the same high degree. 7. The wet-type manufacturing equipment for suspected dimension-strengthened thermoplastic resin sheet as described in item 6 of the patent application park is characterized in that the above-mentioned vertical-axis rotating body-shaped manifold device is provided with a tangent to the rotation symmetry plane from the vertical axis Introduce the inflow of the above dispersion in the direction. 8. The wet-type manufacturing equipment for suspected dimension-strengthened thermoplastic resin sheet as described in item 6 of the patent application scope is characterized in that the above-mentioned vertical-axis rotating body-shaped manifold is installed and provided, and the vertical-axis rotating body-shaped manifold On the central axis, the inlet of the dispersion liquid is introduced from vertically above. 9. The wet-type manufacturing equipment for reel-strengthened thermoplastic resin sheet as described in item 8 of the patent application range, characterized in that the vertical-axis rotating body-shaped manifold device is provided inside and a horizontally rotating stirring device, The carrying axis is consistent with the central axis of the shape of the rotating body of the vertical axis. Printed by the Buying, Consumers, and Consumers Cooperatives of the Falcon Bureau of the Chinese Ministry of Economic Affairs (please read the precautions on the back before filling out this page) A wet-type manufacturing facility for thermoplastic resin sheets, characterized in that the manifold device in the shape of the vertical-axis rotating body is provided at equal intervals on a substantially concentric figure centered on the central axis of the shape of the vertical-axis rotating body Distribute outflow of dispersion liquid. 11. The wet-type manufacturing equipment for suspected dimension-strengthened thermoplastic resin sheets as described in item 10 of the scope of the patent application is characterized in that the distribution outlet of the manifold device in the shape of a rotating body with a vertical axis opens vertically upward. 12. The wet manufacturing equipment for the fiber-reinforced thermoplastic resin sheet as described in item 1 of the patent application scope is characterized in that the above-mentioned buffered imported tube paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm)- 36-Central Bureau of Standards W5 of the Ministry of Economic Affairs; Industrial and Consumer Cooperatives A8 BS C8 D8 7. The scope of patent application is provided. The outlet of the above-mentioned dispersion liquid has a slit-like opening structure with the same width as the suction filtration field of the dispersion liquid . 1 3. The wet-type manufacturing equipment for reel-strengthened thermoplastic resin sheet as described in item 12 of the patent application scope is characterized in that the buffer type inlet pipe is provided for forming and dispersing at the outflow port of the dispersion liquid The suction filtration area of the liquid is the same as the wide slit-like opening, and the limit (s 1 i ce) plate with adjustable opening degree can be adjusted. 14. Wet manufacturing equipment for reinforced thermoplastic resin sheet as described in item 13 of the patent application scope, characterized in that the buffer inlet pipe is provided with a plurality of pieces spaced apart in the flow direction of the dispersion liquid Limited vice board. 15. The wet-type manufacturing equipment for fiber-reinforced thermoplastic resin sheets as described in any one of claims 12 to 14 in the patent application range, characterized in that the buffer type inlet pipe is provided with The structure that the dispersion liquid collides with the wall surface at least once opposite to the direction of the streamline. 16. Wet manufacturing equipment for reinforced thermoplastic resin sheets as described in any one of items 12 to 14 of the Patent Application Panel, characterized in that the content of the above-mentioned buffer type inlet pipe is dispersed in the above The liquid suction filtration area is divided into a plurality of areas in the width direction, and the dispersion liquid can be introduced into each area, and at the same time, it has a structure that allows the dispersion liquid flow to converge in front of each area and after the slit-like opening. 17. The wet-type manufacturing equipment for suspected dimension-strengthened thermoplastic resin sheet as described in item 1 of the scope of application, characterized in that the content part of the buffer-type inlet pipe is provided with a width direction in the area of the suction filtration of the dispersion liquid It can be divided into many areas, and the dispersion can be introduced into each area. At the same time, this paper size can be used in China National Standard (CNS) A4 washing grid (210X297mm) (please read the notes on the back and fill in this page ) 、 1T 丨 -37-315346 A8 B8 C8 D8 6. Scope of patent application (please read the precautions on the back before filling in this page) The structure that makes the above dispersion collide at least once against the wall surface opposite to the direction of the streamline, and There is a structure in which the flow of the dispersion liquid meets in front of each area and behind the slit-like opening, and one or more plates are provided at intervals in the flow direction of the dispersion liquid. 1 8 · The wet equipment of the fiber-reinforced thermoplastic resin sheet as described in item 7 of the patent application range m-S / mm is characterized in that the cross-sectional area of the outermost area of the above-mentioned area of the buffer inlet pipe It is smaller than other areas. 1 9. The wet-type manufacturing equipment for fiber-reinforced thermoplastic resin sheets as described in item ι of the patent application park, characterized in that, in the liquid-filled head box, the above-mentioned certain depth refers to the shaking of the dispersion liquid flowing into the head box Will not reach the depth of the above mesh belt. 2 0.—A wet-manufacturing method of fiber-reinforced thermoplastic resin sheet, which supplies a dispersion liquid containing reinforcing fibers and thermoplastic resin from a manifold device through an inlet pipe to a moving endless mesh belt, while attracting and filtering The wet manufacturing method of the woven dimension-reinforced thermoplastic resin sheet of the sheet-shaped film is characterized in that the Central Standards Bureau of the Ministry of Economic Affairs prints the dispersion liquid to be divided in the manifold device for the industrial and consumer cooperatives, and introduces it into the next wall. The inlet of the inlet pipe is divided into a small flow path that is evenly divided into many areas, so that the dispersion liquid hits the wall surface of the small flow path and turns to reduce the dynamic pressure, and then the dispersion liquid merges and then disperses through a slit The liquid flow outlet adjusts the wave-like swing of the dispersion liquid, and at the same time flattens the front of the liquid flow, and is supplied to the mesh belt. 21.-A wet manufacturing method of susceptible dimension-reinforced thermoplastic resin sheet, which will contain the dispersion of reinforcing dimensional dimension and thermoplastic resin, from the manifold to this standard is applicable to China National Standards (CNS) A4 specifications (210X297 mm i -38-At Ο _______ D8 k, the patent application scope is placed through the inlet pipe and supplied to the endless mesh belt on the move, and the thin-film reinforced thermoplastic resin thinning method of filtering and copying the sheet-like film is characterized by the Increase the flow velocity in the inlet pipe at the two ends in the direction, and then swing through the slit-shaped dispersion liquid outlet to adjust the shape, and at the same time flatten the front of the liquid flow, and supply the mesh 2 Wetness is a thin-layer reinforced thermoplastic resin thin-making method in which a dispersion containing reinforcing resin and thermoplastic resin is placed through an inlet pipe and fed to an endless mesh belt on the move, and a sheet-like film is copied by filtration. The head box dispersion liquid in the suction filtration field where the dispersion liquid is placed stays on the mesh belt, so that the swings discharged by the inlet pipe do not reach the mesh belt. On the side of the wet-brake dispersion liquid that attracts the disc on the side. The manufacturing method is to install the wet-type interior that attracts the disc from the manifold, so that the dispersion has (please read the note on the back first) Item and then fill out this page), 1T The Ministry of Economic Affairs, Central Standardization Bureau, Beigong Consumer Cooperative printed this paper, using the Chinese National Standard (CNS) Α4 specification (210Χ297 mm) 39
TW85110153A 1995-02-22 1996-08-20 TW315346B (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP7033512A JPH08224792A (en) 1995-02-22 1995-02-22 Method and apparatus for wet manufacture of fiber reinforced thermoplastic resin sheet
JP7038530A JP2907321B2 (en) 1995-02-27 1995-02-27 Wet manufacturing equipment for fiber reinforced thermoplastic resin sheet
JP7038531A JP2915316B2 (en) 1995-02-27 1995-02-27 Wet manufacturing equipment for fiber reinforced thermoplastic resin sheet
JP7038532A JPH08232187A (en) 1995-02-27 1995-02-27 Production of and production unit for fiber-reinforced thermoplastic resin sheet
JP7298577A JPH09136969A (en) 1995-11-16 1995-11-16 Wet production of fiber-reinforced tehrmoplastic resin sheet and equipment therefor

Publications (1)

Publication Number Publication Date
TW315346B true TW315346B (en) 1997-09-11

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Application Number Title Priority Date Filing Date
TW85110153A TW315346B (en) 1995-02-22 1996-08-20

Country Status (1)

Country Link
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