If you unroll a spool of BOPP film and hold it up to the light, you are looking at a material that has been stretched, heated, cooled, and transformed through seven distinct stages. The film in your hands is not the same plastic that went into the extruder — it is a biaxially oriented polymer with mechanical properties that bear no resemblance to the raw polypropylene pellets it started as. Understanding those seven steps is the key to understanding why BOPP behaves the way it does.
The journey begins with resin. Polypropylene homopolymer pellets arrive at the film plant in 25 kg bags or one-ton supersacks. These pellets are small translucent beads, typically 3 to 4 mm in diameter, with a melting point of approximately 165°C. For most BOPP film grades, the core layer is homopolymer PP, but the outer layers — the skin layers — are often copolymer PP (random copolymer with ethylene) to provide heat sealability or improved optics. Additional additives are blended in at this stage: antiblock agents (silica or calcium carbonate) to prevent film-to-film adhesion, slip agents (erucamide or oleamide) to reduce friction coefficient, and antistatic agents to dissipate surface charge. This additive package determines how the finished film will behave on a packaging machine or printing press.
Step one is resin feeding and drying. The pellets are conveyed from storage silos to the extruder hopper using pneumatic transport. Before entering the extruder, the resin passes through a dehumidifying dryer that removes surface moisture. Moisture in PP resin is a serious problem: when the resin melts in the extruder, trapped water turns to steam, which creates bubbles in the melt film and results in optical defects. The dryer brings the resin moisture content below 200 ppm before it enters the barrel.
Step two is melt extrusion. The dried pellets drop into the feed throat of a co-extrusion system. A modern BOPP line typically uses a three-layer or five-layer co-extrusion die. Each layer has its own extruder — a large barrel with a rotating screw that compacts, melts, and pumps the resin forward. The barrel is heated by external band heaters in zones, typically 200°C to 240°C from feed to die. The molten polymer from each extruder converges in a flat T-die (also called a coat-hanger die), where the layers are stacked and extruded through a narrow slot as a continuous, flat melt curtain. The die gap is typically 1.0 to 2.0 mm — far thicker than the final film because the stretching steps will thin it dramatically.
Step three is chill roll casting. The molten curtain drops onto a large, rotating, water-cooled chrome roller called the chill roll. The surface temperature of this roller is 15°C to 30°C. The sudden contact with the cold surface quenches the melt — it solidifies almost instantly into a thick, amorphous sheet called the cast sheet or primary web. This rapid cooling is critical: it prevents the formation of large spherulitic crystals that would scatter light and reduce clarity. The cast sheet at this stage is typically 300 to 800 microns thick — roughly twenty to forty times thicker than the finished film.
Step four is machine direction orientation (MDO). The cast sheet passes through a series of heated rollers arranged in a long stretch. The rollers accelerate progressively — each successive roller runs faster than the previous one. The temperature is set at 120°C to 145°C, within the range where the polymer is soft enough to stretch but not molten. As the sheet is drawn between the slow and fast roller groups, it elongates in the machine direction (the direction of travel). The stretch ratio is typically 4.5:1 to 5.5:1, meaning the sheet becomes roughly five times longer and five times thinner. This orientation aligns the polymer chains along the machine direction, dramatically increasing tensile strength and stiffness in that direction. But the film is now anisotropic — strong in one direction, weak in the other. That imbalance must be corrected in the next step.
Step five is transverse direction orientation (TDO). The now-lengthened sheet enters a tenter frame — a large oven with two parallel chain tracks running the full length of the machine. Metal clips grip both edges of the film and pull it into the oven. Inside the oven, the chain tracks diverge — they spread apart at a controlled rate. The film, held at both edges, is stretched sideways as the tracks widen. The oven temperature is 150°C to 170°C, and the transverse stretch ratio is typically 7:1 to 9:1. This sideways stretching aligns the polymer chains in the cross-machine direction, balancing the orientation that was created in the MDO step. After TDO, the film is biaxially oriented — the chains are now aligned in both directions, giving the film uniform strength, clarity, and dimensional stability.
As a manufacturer running biaxial orientation lines daily, we can tell you that the stretch ratios in both directions are not arbitrary — they are precisely tuned to the specific film grade being produced. A packaging film optimized for stiffness may use a 5.0 x 8.0 ratio, while a high-clarity lamination film may use 4.5 x 9.0. Getting these ratios wrong produces film that is either hazy, weak in one direction, or prone to shrinkage.
Step six is heat setting, also called thermofixation. After the tenter oven, the film passes through a second oven zone where the temperature is held at 130°C to 145°C — just below the melting point. The film is held at constant width (the clips still grip the edges) during this stage. The controlled temperature allows the polymer chains to relax into their stretched positions and partially crystallize. This locks in the orientation and dramatically reduces the film's tendency to shrink when exposed to heat later. Without heat setting, the oriented film would try to return to its original unstretched dimensions at any elevated temperature — which would make it useless for packaging applications that involve heat sealing or hot filling.
Step seven is cooling, edge trimming, and winding. The film exits the heat-setting oven and passes over cooling rollers that bring it down to room temperature. The thick edges — where the tenter clips gripped the film — are trimmed off with rotary knives. These edge trimmings are recycled: they are reground and fed back into the extruder as regrind material, typically at 5 to 15 percent of the total resin feed. Finally, the film is wound onto a cardboard core to form a master roll, which may be one to three meters wide and contain several thousand meters of film.
After winding, the master roll is transferred to a slitting area where it is cut into narrower rolls matching customer specifications. It may also undergo surface treatment (corona treatment to raise surface energy for printing or lamination) either inline during production or offline in a separate step. The finished rolls are then packaged, labeled with batch numbers and specifications, and shipped to converters worldwide.
The seven-step process transforms a simple thermoplastic into one of the most versatile packaging materials in the world. Each step serves a purpose that cannot be skipped or shortcut without degrading the film's performance. Understanding this process helps converters and printers diagnose problems — a haze issue may originate in the chill roll step, a shrinkage problem in the heat-setting step, a weakness in the stretch ratios. The film is not just stretched plastic. It is an engineered material, built one step at a time.
Frequently Asked Questions
Why is BOPP film stretched in two directions instead of one?
Stretching in only one direction (machine direction) aligns polymer chains in that direction, making the film strong longitudinally but weak and easy to tear across the web. Biaxial stretching (both machine and transverse directions) creates balanced orientation, giving the film uniform strength, clarity, and dimensional stability in all directions. Without transverse stretching, BOPP would split easily along the machine direction — a problem known as 'fibrillation.'
What is the stretch ratio and why does it matter?
Stretch ratio is the factor by which the film is elongated during orientation. Typical BOPP stretch ratios are 4.5-5.5:1 in the machine direction and 7-9:1 in the transverse direction. Higher ratios increase tensile strength and clarity but reduce thickness and can make the film brittle. The ratio is tuned for each film grade: a stiff packaging film may use 5.0 x 8.0, while a high-clarity lamination film may use 4.5 x 9.0. Incorrect ratios cause haze, directional weakness, or shrinkage.
What happens if the heat setting step is skipped?
Without heat setting, the oriented polymer chains remain in a stressed state and will attempt to return to their original, unstretched configuration when exposed to heat. This means the film will shrink dramatically at temperatures as low as 80-100°C, making it useless for heat-seal applications, hot filling, or any process involving elevated temperatures. Heat setting partially crystallizes the polymer, locking the orientation in place.
Why are the edge trimmings recycled back into the process?
The tenter clips that grip the film edges during transverse stretching leave thick, un-stretched edges that must be trimmed off. These trimmings represent 5-15% of total production volume. Recycling them as regrind reduces raw material waste and lowers cost. The regrind is blended with virgin resin at a controlled ratio. Excessive regrind can reduce optical clarity and introduce gels, so the ratio is carefully monitored.
How does co-extrusion create multi-layer BOPP film?
A co-extrusion die receives molten polymer from multiple extruders simultaneously. Each extruder feeds a different resin formulation — for example, homopolymer PP for the core, copolymer PP for heat-sealable skin layers, and PP with additives for the outer surface. The die stacks these melt streams into a multi-layer curtain before they solidify. A 5-layer structure might be: sealable copolymer / tie layer / homopolymer core / tie layer / treated skin. Each layer contributes specific properties to the finished film.
What is the typical production speed of a BOPP film line?
Modern BOPP lines run at 250 to 450 meters per minute of cast sheet, though the finished film speed is higher due to stretching. A single line can produce 3,000 to 6,000 metric tons of film per year. Line width ranges from 4.5 to 8.3 meters for the finished film. Startup and grade changeover can take several hours, which is why BOPP lines are typically run continuously with minimal product changes.
This article draws on the hands-on production experience of the technical team at Shandong Shunzhan New Materials Co., Ltd., where we have been manufacturing BOPP and PET functional films for over two decades. If you found this article helpful and have a specific film selection or processing question, we are happy to share what we know. Reach out for a technical consultation or sample evaluation.
从粒子到卷:BOPP薄膜如何通过七步制造
如果你展开一卷BOPP薄膜对着光看,你看到的是一种经过拉伸、加热、冷却和转化的材料,经历了七个不同阶段。你手中的薄膜和进入挤出机的塑料完全不同 — 它是一种双向拉伸的聚合物,机械性能与原始聚丙烯颗粒毫无相似之处。理解这七个步骤是理解BOPP为何如此表现的关键。
旅程从树脂开始。聚丙烯均聚物颗粒以25公斤袋或一吨超级袋的形式到达薄膜工厂。这些颗粒是半透明的小珠,通常直径3到4毫米,熔点约165°C。对于大多数BOPP薄膜等级,芯层是均聚PP,但外层 — 皮层 — 通常是共聚PP(乙烯无规共聚物),以提供热封性或改善光学性能。添加剂在这一阶段混合:抗粘连剂(二氧化硅或碳酸钙)防止膜间粘连,爽滑剂(芥酸酰胺或油酸酰胺)降低摩擦系数,抗静电剂消散表面电荷。这套添加剂组合决定了成品薄膜在包装机或印刷机上的表现。
第一步是树脂供料和干燥。颗粒通过气力输送从储料仓送到挤出机料斗。在进入挤出机之前,树脂通过除湿干燥机去除表面水分。PP树脂中的水分是个严重问题:当树脂在挤出机中熔化时,困住的水分变成蒸汽,在熔融薄膜中产生气泡,导致光学缺陷。干燥机将树脂含水量降到200 ppm以下后才能进入机筒。
第二步是熔融挤出。干燥后的颗粒落入共挤出系统的进料口。现代BOPP线通常使用三层或五层共挤出模头。每一层都有自己的挤出机 — 一个带旋转螺杆的大机筒,将树脂压实、熔化并向前泵送。机筒通过外部带式加热器分区加热,通常从进料到模头为200°C到240°C。来自各挤出机的熔融聚合物在扁平T型模头(也称衣架型模头)中汇合,各层叠合后通过一个狭窄缝隙挤出一道连续的扁平熔体帘。模头间隙通常为1.0到2.0毫米 — 远厚于最终薄膜,因为后续拉伸步骤会大幅减薄。
第三步是冷却辊铸片。熔体帘落在一个大型旋转的水冷镀铬辊上,称为冷却辊。该辊表面温度为15°C到30°C。与冷表面的突然接触使熔体淬火 — 几乎瞬间固化成厚厚的无定形片材,称为铸片或初级坯膜。这种快速冷却至关重要:它防止形成会散射光线的大的球晶,降低透明度。此时的铸片通常厚300到800微米 — 大约比成品薄膜厚二十到四十倍。
第四步是纵向拉伸(MDO)。铸片通过一系列排列成长排的加热辊筒。辊筒逐级加速 — 每个后续辊比前一个转得更快。温度设定在120°C到145°C,处于聚合物足够柔软可以拉伸但不会熔化的范围内。当片材在慢速辊组和快速辊组之间被拉伸时,它在机器方向(行进方向)上伸长。拉伸比通常为4.5:1到5.5:1,意味着片材变长约五倍、变薄约五倍。这种取向使聚合物链沿机器方向排列,大幅提高该方向的拉伸强度和刚性。但此时薄膜是各向异性的 — 一个方向强,另一个方向弱。这种不平衡必须在下一步纠正。
第五步是横向拉伸(TDO)。变长的片材进入拉幅机 — 一个大型烘箱,有两条平行的链轨贯穿机器全长。金属夹子夹住薄膜两侧边缘拉入烘箱。在烘箱内,链轨分叉 — 以受控速率向外展开。薄膜被两侧夹住,随着轨道变宽而被横向拉伸。烘箱温度为150°C到170°C,横向拉伸比通常为7:1到9:1。这种侧向拉伸使聚合物链在垂直于机器方向排列,平衡MDO步骤中产生的取向。经过TDO后,薄膜实现了双向取向 — 链在两个方向上都已排列,赋予薄膜均匀的强度、透明度和尺寸稳定性。
作为一家每天运行双向拉伸生产线的制造商,我们可以告诉你两个方向的拉伸比都不是任意的 — 它们是根据正在生产的特定薄膜等级精确调校的。以刚性为优化目标的包装膜可能使用5.0 x 8.0的比率,而高透明度覆膜膜可能使用4.5 x 9.0。比率不对会产出发雾、单方向弱或容易收缩的薄膜。
第六步是热定型,也称热固化。离开拉幅机烘箱后,薄膜通过第二个烘箱区,温度保持在130°C到145°C — 刚低于熔点。在此阶段薄膜保持恒定宽度(夹子仍夹住边缘)。受控温度使聚合物链在拉伸位置松弛并部分结晶。这锁定了取向并大幅降低薄膜后续暴露在热量下时的收缩倾向。没有热定型,取向薄膜在任何高温下都会试图恢复到原始未拉伸尺寸 — 这将使它无法用于涉及热封或热灌装的包装应用。
第七步是冷却、修边和收卷。薄膜离开热定型烘箱,经过冷却辊降至室温。厚的边缘 — 拉幅机夹子夹住薄膜的地方 — 被旋转刀片切掉。这些边角料被回收:重新粉碎后作为回料送回挤出机,通常占树脂总进料量的5到15%。最后,薄膜卷绕到纸芯上形成母卷,可能宽一到三米,包含数千米薄膜。
收卷后,母卷被转移到分切区,切成符合客户规格的窄卷。它还可能接受表面处理(电晕处理以提高印刷或覆膜的表面能),可以在生产线上在线进行或在单独步骤中离线进行。成品卷然后被包装、标注批号和规格、运往世界各地的加工商。
七步过程将简单的热塑性塑料转化为世界上最通用的包装材料之一。每一步都有不可跳过或走捷径而不降低薄膜性能的作用。理解这个过程帮助加工商和印刷商诊断问题 — 雾度问题可能源于冷却辊步骤,收缩问题源于热定型步骤,弱点源于拉伸比。薄膜不仅仅是拉伸的塑料。它是一种工程材料,一步一步构建而成。
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