TWI314896B - A plastic dyeing apparatus and a method thereof - Google Patents
A plastic dyeing apparatus and a method thereof Download PDFInfo
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- TWI314896B TWI314896B TW096118158A TW96118158A TWI314896B TW I314896 B TWI314896 B TW I314896B TW 096118158 A TW096118158 A TW 096118158A TW 96118158 A TW96118158 A TW 96118158A TW I314896 B TWI314896 B TW I314896B
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- stretching
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/919—Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
1314896 九、發明說明: 【發明所屬之技術領域】 、本發明係關於-種塑膠染色設備及其方法,尤指一種 L用於H、、加色粉以進行染色之塑膠染色設備及其方法。 【先前技術】 攸石化工業發展以來’由於塑膠材料具有良好的物 易加工、絕緣性強等優點,塑膠材料已 應用於各產蜚吝。* ^ 土座興 ^ 業產口口中,包括民生用品、資訊電子、工 父=運輪業等各項產業,涵蓋食、衣、住、行、育、樂久 種设施,由此可見塑膠材料對大眾生活之影變力。、口 15 因此,在塑膠材料的製作過程中,常經由單螺桿押出 雙螺桿押出機或混合器將塑膠材料與色粉混合而提供 =的材料以符合上述各種應用需求。;1314896 IX. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a plastic dyeing apparatus and method thereof, and more particularly to a plastic dyeing apparatus and method for dyeing L, H, and coloring powder for dyeing. [Prior Art] Since the development of the petrochemical industry, plastic materials have been used in various calves due to their good physical processing and strong insulation. * ^ 土座兴^ In the mouth of the industry, including the products of people's livelihood, information electronics, fathers and workers, including the food, clothing, housing, transportation, education, and long-term planting facilities, it can be seen that the plastic materials are The shadow of the public life is changing. Therefore, in the production process of plastic materials, the plastic material and the toner are often mixed by a single-screw extrusion twin-screw extruder or a mixer to provide a material to meet the above various application requirements. ;
桿押出機或混合器之混合機制主要是使塑膠;I :广在其内產生剪切流動,而將色粉與塑膠材料攪拌 混合達到改變塑膠材料顏色之目的。 爾拌 耗能ί:混主的混合攪拌方式需要大幅消 ί味=:混練時間冗長會影響生產效率等因素而限制 ::時間的活,則需要以增加色粉的添加量的方式The mixing mechanism of the rod extruder or the mixer is mainly to make the plastic; I: the shear flow is widely generated therein, and the toner is mixed with the plastic material to change the color of the plastic material. Mixing energy consumption ί: The mixing mode of the mixing master needs to be greatly reduced. =: The length of the mixing time will affect the production efficiency and other factors. Limits: Time to live, you need to increase the amount of toner added.
的展色性。換言之’在限制混練時間的要长下I 色粉添加量時,則會造成塑膠材:染: 俊邑相飽和度不足產生色差之缺失。 20 !314896 因此,具有良好展色性而可減少色粉添加量之塑膠染 色設備及其方法實為目前塑膠產業迫切需求的技術,值得 積極研究開發。 【發明内容】 、本發明係提供一種塑膠染色設備及其方法,以增加色 值在土膠中之展色性’使得本發明染色之塑膠顏色達到盘 田技術同—色相時’依據本發明染色之塑膠所需之色;分 用量較少,而降低色粉用量。 “之色心 10 15 本發明提供—種塑膠染色方法’包括:提㈣至⑽重 二提供01至1〇重量份之-黏合劑;提㈣ > 里之色粉,以及使用一拉伸流動混合裝置混人 遠色粉、《膠及該黏合劑。 H“ 上述塑膠染色方法可更句括 劑,此…更包括楗供〇」至5重量份之分散 聚合物。^ 何型態之分散劑,較佳為1狀酿胺 或-ΐ=Γ為各種型態之黏合劑,較佳為-聚合物 物’更佳為-馬來酸酐接枝聚合物。 更佳為二氧化鈦“為無機類色粉’ 鎳黃,-顏料、;二群;黃、'紅、:紅、鈦 鈷綠、氧化鈷綠、 綠 ^鈷藍、鈦化青藍、 料。 欽化月綠、雲母真珠光澤顏料或勞光顏 20 ^14896 聚4=塑谬可為任何種類之塑勝,較佳為聚乙稀、 烯内烯腈—丁二烯-苯乙烯、聚碳酸酯、聚 口夕兀酯、聚對苯二甲酸丁酯、聚 匕 之-或其任意組合。 &次乙烯-醋酸乙烯醋 另外本發明之塑膠染色方法除了包含上叶.牛w夕 外,亦可視需要增加提供其他添加劑;驟之 增白劑、著色劑、固色劑、遮色劑:^ 劑或其他聚合物等添加劑之步驟=职紫外光安定 10 15 例,端色粉之間的混合比例可為任意比 所需染色之色相深淺調整色粉之用量。 粉分散於—塑膝 二木色°又備’適用於將一色 裝置,彳i #說 裝置以及一拉伸流動混合 合合裝置連接於押出裝置,且拉伸流動混 σ我置扣合色粉與塑膠。 何::r裝置,較佳為單螺 出裝置:,其將《與色粉力心=機或其他習知之押 置,::為拉::動厂混合裝置可為任何形式之拉㈣^ 為二縮/拉伸區域。壓縮輸^ 主要Μ乍二公、之内徑作寬窄縮放,塑勝與色粉在其中 主要疋作拉伸流動而增加 色粉之混h 4破斷機會’因此增加塑膠與 私度而達到高展色性。拉伸流動混Μ置之德 可連接-塑型裝置,如 “動混口裝置之後 之後亦可連接-冷料置,^,以使塑膠形成預定尺寸, ^置如.一水槽,以將塑膠降溫。 20 1314896 因此’本發明之塑膠染色設備及其方法使用上述拉伸 /;IL動混合裝置及上述塑膠配方,並將上述塑膠配方之塑 膠、黏合劑或分散劑及色粉提供至拉伸流動混合裝置之一 魘% /拉伸區域’透過壓縮/拉伸區域之内徑係呈縮放變化以 促進色粉與塑膠之混合,使色粉與塑膠在其中達到均勻分 放,而增加色粉之展色性’並可減少色粉使用量。 【實施方式】 10 15 4 —併參考圖1及圖2 ’圖1顯示本實施例之塑膠染色設 備1之系統架構圖,圖2顯示本實施例之塑膠染色設備丨之 視圖。 如圖1及圖2中所示,塑膠染色設備丨包括一押出裝置 U、—拉伸流動混合裝置丨2、一塑型裝置13及一冷卻裝置 1壯4,其中,拉伸流動混合裝置12連接於押出裝置丨丨,塑型 =置!3連接於拉伸流動混合裝置12,而冷卻裝置μ則連接 、塑型裝置13。在本實施例中,#出裝置⑽為―單螺桿 :出機,塑型裝置13係為一模頭’而冷卻裝置⑷系為一水 -塑膠、-黏合劑及-分散劑乾料係被提供至押出裝 以由押出襄置U將上述乾料加熱炫融, 中所使用的塑膠係為丙烯腈-丁二烯 月匕、机人… 埽-本乙烯樹脂(ABS樹 :)’黏合劑可增加不同材質顆粒間之相容性 駄酐接枝聚合物,而分散劑則促進分散 =·:、、‘、、、 醯胺聚合物。 =二又,,、為蠟狀 20 .1314896 另请參考下列表丨以了解本實施例中押出裝置1 1之溫 度設定條件。 表1 Z1 -------- Z2 Z3 Z4 ---- Z5 Z6 DIE 190 220 240 250 260 ' 250 245 表1為單螺桿押出機之螺桿各區段(Z1、Z2 ' Z3、Z4、 Z5、Z6及DIE)之溫度條件,上述押出裝置u之螺桿轉速係 没定在200r.p.m。 螺桿區段The color development. In other words, when the amount of I toner added is limited by the time of mixing, the plastic material will be caused: dyeing: The lack of saturation of the Junhao phase causes the lack of chromatic aberration. 20 !314896 Therefore, plastic dyeing equipment and methods which have good color development and can reduce the amount of toner added are practical technologies that are urgently needed in the plastics industry, and are worthy of active research and development. SUMMARY OF THE INVENTION The present invention provides a plastic dyeing apparatus and method thereof for increasing the color rendering property of the color value in the soil glue, so that the color of the dyed plastic of the present invention reaches the same state as the hue technique. The color required for the plastic; the amount used is less, and the amount of toner is reduced. "Color core 10 15 The present invention provides a method for dyeing plastics" comprising: (4) to (10) heavy two providing 01 to 1 part by weight of a binder; (4) > a toner in the powder, and using a stretching flow The mixing device is mixed with far-color powder, "glue and the adhesive. H" The above-mentioned plastic dyeing method can be further described, and this includes more than 5 parts by weight of the dispersion polymer. Preferably, the dispersant of the type is preferably a type of amine or - ΐ = Γ is a binder of various types, preferably a polymer - more preferably a maleic anhydride graft polymer. More preferably, titanium dioxide is "inorganic toner" nickel yellow, - pigment, two groups; yellow, 'red, red, titanium cobalt green, cobalt oxide green, green cobalt blue, titanium blue, material.绿月绿, mica pearly pigment or Laoguangyan 20 ^14896 Poly 4 = plastic enamel can be any kind of plastic, preferably polythene, enelenonitrile-butadiene-styrene, polycarbonate , yoghurt ester, polybutylene terephthalate, polyfluorene- or any combination thereof. &-ethylene-vinyl acetate vinegar. In addition to the plastic dyeing method of the present invention, in addition to the upper leaf. Additional additives may be added as needed; steps such as brighteners, colorants, fixing agents, opaque agents, or other polymers, etc. = steps of UV stabilization 10 15 cases, mixing between end toners The ratio can be any amount of toner adjusted to the depth of the hue required to be dyed. The powder is dispersed in the plastic knee and the wood color is also suitable for the one-color device, the 彳i # say device and a stretch flow mixing device Connected to the extrusion device, and stretched and mixed σ I put the color powder and plastic. He::r The device, preferably a single screw-out device: which will be placed with the toner core = machine or other conventional means, :: for pulling:: the factory mixing device can be any form of pulling (four) ^ for the second contraction / Stretching area. Compressed transmission ^ Mainly Μ乍 two, the inner diameter of the width is narrow and narrow, plastic and toner in which the main action is to stretch the flow and increase the mixing of the toner h 4 breaking opportunity 'thus increasing plastic and private To achieve high color development. The stretchable flow mixing device can be connected to a plastic device, such as "the mixing device can be connected after the cold mixing device, ^, so that the plastic is formed into a predetermined size. Such as a sink to cool the plastic. 20 1314896 Therefore, the plastic dyeing apparatus and method of the present invention use the above-mentioned stretching/IL mixing device and the above plastic formulation, and provide the plastic, adhesive or dispersing agent and toner of the above plastic formulation to the stretching flow mixing One of the devices 魇%/stretching area's inner diameter of the compression/stretching area is scaled to promote the mixing of the toner and the plastic, so that the toner and the plastic are evenly distributed therein, and the toner is expanded. Chromaticity' and can reduce the amount of toner used. [Embodiment] 10 15 4 - and referring to Fig. 1 and Fig. 2' Fig. 1 shows a system architecture diagram of the plastic dyeing apparatus 1 of the present embodiment, and Fig. 2 shows a view of the plastic dyeing apparatus of the present embodiment. As shown in FIGS. 1 and 2, the plastic dyeing apparatus 丨 includes an extruding device U, a stretching flow mixing device 丨2, a molding device 13, and a cooling device 1, wherein the stretching flow mixing device 12 Connected to the extrusion device 塑, molding = set! 3 is connected to the stretching flow mixing device 12, and the cooling device μ is connected to the molding device 13. In the present embodiment, the #出装置 (10) is a "single screw: the machine, the molding device 13 is a die" and the cooling device (4) is a water-plastic, - adhesive and - dispersant dry material Provided to the squeezing device to heat and smear the above dry material by the squeezing device U, the plastic used in the acrylonitrile-butadiene ruthenium, the machine... 埽-this vinyl resin (ABS tree:) 'adhesive agent The phthalic anhydride graft polymer can be added to increase the compatibility between different material particles, and the dispersant can promote the dispersion =·:,, ',,, and guanamine polymer. = two, again, is waxy 20 .1314896 Please also refer to the following list to understand the temperature setting conditions of the extruding device 1 1 in this embodiment. Table 1 Z1 -------- Z2 Z3 Z4 ---- Z5 Z6 DIE 190 220 240 250 260 ' 250 245 Table 1 is the screw section of the single screw extruder (Z1, Z2 'Z3, Z4, For the temperature conditions of Z5, Z6 and DIE), the screw rotation speed of the above-mentioned extrusion device u is not set at 200 r.pm. Screw section
經加熱熔融之塑膠材料組成物與色粉係分別被提供至 拉伸*動混合裝置12中,在本實施例巾,色粉係使用藍色 色粉與二氧化鈦。上述拉伸流動混合裝置12包括一壓縮,拉 伸區域121,其中之内徑係呈縮放變化,塑膠材料組成物與 叙在壓、.宿/拉伸區域丨2丨内徑較窄處破斷塑膠材料組成物 與色,之炼滴以使其均勾分散,而在壓縮/拉伸區域⑵内 牷較寬處拉伸流動以達到攪拌效果。The heat-melted plastic material composition and the toner system are respectively supplied to the stretching/moving mixing device 12, and in the present embodiment, the toner is a blue toner and titanium dioxide. The above-mentioned stretching flow mixing device 12 comprises a compressed, stretched region 121 in which the inner diameter is scaled, and the plastic material composition is broken at a narrower inner diameter of the plastic material, the sinking/stretching region 丨2丨. The composition of the plastic material and the color, the smelting drops are evenly dispersed, and in the compression/stretching region (2), the 牷 拉伸 wide stretches the flow to achieve the stirring effect.
另。月參考下列表2以了解本實施例中拉伸流動混合裝 置12之溫度設定條件。 表2 溫度區段 Z1 Z2 Z3 溫度(C ) 245 245 245 —1 表2之溫度區段(Z:l、Z2及Z3)代表拉伸流動混合裝置12 各個位置之溫度。 20 1314896 經染色之塑膠材料組成物係被提供至塑型裝置1 3,以 由塑型表置1 3定義塑勝材料組成物之外觀尺寸,如:塑膠 材料組成物之直徑大小,再將成形之塑膠材料組成物放置 於冷卻裝置14中降溫。 請參考表3,其顯示本實施例之塑膠材料組成物與色粉 之間的配方比例以及声罢插。A/士 及邑差值。色差值之測定係使用上 Z後之塑勝材料組成物加工製成塑膠粒子, 機射出標準試片測試之,而A m ^ K之而色差值之計算公式係為· L代表色差值’ L、—為色空間之座標軸, 之負向色度’ _之正向係為紅色方向,成 貝门係為綠色方向,b軸之正 向係為藍色方向。 係為汽色方向’ b軸之負 表3another. Refer to Table 2 below for the temperature setting conditions of the stretch flow mixing device 12 in this embodiment. Table 2 Temperature Zone Z1 Z2 Z3 Temperature (C) 245 245 245 —1 The temperature zones (Z: 1, Z2, and Z3) of Table 2 represent the temperatures at various locations of the draw flow mixing device 12. 20 1314896 The dyed plastic material composition is supplied to the molding device 13 to define the outer dimensions of the plastic composition, such as the diameter of the plastic material composition, and then form the shape of the plastic material composition. The plastic material composition is placed in the cooling device 14 to cool down. Please refer to Table 3, which shows the formulation ratio between the plastic material composition of the present embodiment and the toner, and the sound insertion. A/士 and 邑 difference. The color difference is determined by using the plastic composition of the Z after the processing to form a plastic particle, which is tested by a standard test piece, and the calculation formula of the color difference of A m ^ K is · L represents the color difference The value 'L,—is the coordinate axis of the color space, the positive direction of the negative chromaticity ' _ is the red direction, the bead system is the green direction, and the b-axis is the blue direction. It is the direction of the vapor color and the negative of the b-axis. Table 3
<:S 10 1314896<:S 10 1314896
~x~i--ί_ I I ---- 0.01 揭 口 在 樣m,代號E及F為本實施例之塑膠材料組成物樣品。由表3 之a、qd樣品之色差值數據可以得知,結合單:桿㈣ 機與拉伸流動混合裝置進行塑膠染色後,確實造成本實施 例之C樣品色粉分散性提升,故產生較大之色差值^ 叫,若欲維持A#_之飽和度,則色料減為。22,如 貫施例D。此外由表3之樣品之色粉用量數據可以得 知,加入黏合劑與分散劑確實在幾近相同色相之要求下達 10 15 到減少色粉用量,其約節省6%之色粉。由表3之八及£樣品 之數據可以得知,使用本實施例之塑膠材料組成物配方盘 塑膠染色設備進行染色後之塑膠材料組成物展色性顯著增 加:故而產生高達L95之色差值。由表3之aaf樣品之色二 用置數據可以得知,使用本實施例之㈣材料組成物配方 與塑膠染色設備進行染色後,使色粉用量減少約20%。 另月併,考圖3 A、3 B及3 C,其顯示本發明另一較佳 實施例之拉伸流動混合裝置12内的壓縮/拉伸區域i2i示意 =。如圖中所示,壓縮/拉伸區域121内徑規律地作不同數 1E的縮放變化。隨著縮放變化數量增加,則增加塑膠與色 粉在其内溶滴破斷與拉伸流動的機率,而達到良好之分散 及分佈性。 疋故’由上述中可以得知,本發明之塑膠染色設備及 其方法提供塑膠、黏合劑與色粉至一拉伸流動混合裝置中 20 1314896 =于:謂染色,以使色粉與_在其中逹 9加色粉之展色性,並可減少色粉使用量。 放’而 =_係為了方便說明而舉例而已, 張之榷利乾圍自應以申請專利範圍斤 於上述實施例。 "'、革而非僅限 【圖式簡單說明】 # m係本發明-較佳實施例之塑膠染色設備系統架構圖。 圖2係本發明-較佳實施例之塑膠染色設備剖視圖。 10目3A 3B、及3C係本發明另一較佳實施例之拉伸流動混合 裝置内的壓縮/拉伸區域示意圖。 【主要元件符號說明】 塑膠染色設備1押出裝置11 拉伸流動混合裝置12 塑型裝置1 3 冷卻裝置14 壓縮/拉伸區域12 1~x~i--ί_ I I ---- 0.01 揭口 In the sample m, codes E and F are samples of the plastic material composition of the present embodiment. It can be known from the color difference data of the samples a and qd in Table 3 that the plastic dyeing of the C sample in the present embodiment is improved by the combination of the single: rod (four) machine and the stretching flow mixing device, so that the toner dispersion of the sample C in the present embodiment is improved, so that The larger color difference ^ is called, and if you want to maintain the saturation of A#_, the color material is reduced to. 22. Example D. In addition, it can be seen from the toner usage data of the samples of Table 3 that the addition of the binder and the dispersant does require nearly 10 15 of the same hue to reduce the amount of toner, which saves about 6% of the toner. It can be known from the data of the sample of Table 8 and the sample of the sample that the plastic material composition after dyeing using the plastic material composition disc of the present embodiment has a significant increase in color development: thus, a color difference of up to L95 is generated. . From the color data of the aaf sample of Table 3, it can be known that the coloring amount of the toner is reduced by about 20% by using the (4) material composition formula of the present embodiment and dyeing with a plastic dyeing apparatus. Another month, reference is made to Figs. 3A, 3B and 3C, which show the compression/stretching region i2i in the stretch flow mixing device 12 of another preferred embodiment of the present invention. As shown in the figure, the inner diameter of the compression/stretching region 121 is regularly varied by a different number 1E. As the number of scaling changes increases, the probability of breakage and stretch flow of the plastic droplets within the plastic and toner is increased, resulting in good dispersion and distribution. As can be seen from the above, the plastic dyeing apparatus and method of the present invention provide plastic, adhesive and toner to a stretching flow mixing device 20 1314896 =: dyeing, so that the toner and _ Among them, the color development of 逹9 plus color powder can reduce the amount of toner used. Putting 'and '_ is an example for convenience of explanation, and Zhang Zhili's application for patents is in the above-mentioned embodiment. "', leather rather than limited [Simplified illustration] #m is the system architecture diagram of the plastic dyeing equipment of the present invention-best embodiment. Figure 2 is a cross-sectional view of a plastic dyeing apparatus of the preferred embodiment of the present invention. 10 mesh 3A 3B, and 3C are schematic views of the compression/stretching regions in the stretch flow mixing device of another preferred embodiment of the present invention. [Description of main component symbols] Plastic dyeing equipment 1 Extruding device 11 Stretching flow mixing device 12 Molding device 1 3 Cooling device 14 Compression/stretching area 12 1
15 12 (.S )15 12 (.S )
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