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What Are the Advantages and Disadvantages of Adding POE to EVA?

Sep 07,2026     |     Published in:Advanced Foaming Solutions for OEM Manufacturing

EVA添加POE有哪些優缺點?

What Are the Advantages and Disadvantages of Adding POE to EVA?

PART 2

再加入SEBS改善物性,為何雙螺桿分散才是關鍵?

When SEBS Is Added to Improve Properties, Why Is Twin-Screw Dispersion the Key?

核心觀點|EVAPOE能快速降低硬度、改善回彈與低溫柔韌,但也可能犧牲結晶支撐、尺寸穩定、黏著與交聯效率。SEBS可補強熔體彈性、韌性與泡孔壁,但前提是形成細小、均勻且具有界面黏著的分散相;若仍以簡單乾混投入,SEBS的高黏度反而容易形成凝膠粒與弱界面。

Core insight | EVA/POE can rapidly reduce hardness and improve resilience and low-temperature flexibility, but it may also sacrifice crystalline support, dimensional stability, adhesion, and crosslinking efficiency. SEBS can reinforce melt elasticity, toughness, and cell walls, provided that it forms a fine, uniform dispersed phase with strong interfacial adhesion. If it is still introduced by simple dry blending, the high viscosity of SEBS instead tends to create gel particles and weak interfaces.

 

雙螺桿的四個核心優勢

Four Core Advantages of a Twin-Screw Extruder

1. 高界面更新率:兩支螺桿互相嚙合,反覆分流、合流與拉伸熔體。

High interfacial renewal rate: The two intermeshing screws repeatedly divide, recombine, and stretch the melt.

2. 可分區設計剪切:輸送元件負責前進,捏合塊提供可控分散,避免全程高剪切。

Zoned shear design: Conveying elements move the material forward, while kneading blocks provide controlled dispersion without imposing high shear throughout the entire machine.

3. 精準供料與側餵:可將高黏SEBS、油品、相容劑或填料在適當位置加入。

Precise feeding and side feeding: High-viscosity SEBS, oils, compatibilizers, or fillers can be introduced at appropriate locations.

4. 真空排氣與穩定造粒:移除水分與揮發物,生成均勻母粒供後續低溫加入發泡系統。

Vacuum venting and stable pelletization: Moisture and volatiles are removed to produce a uniform masterbatch for later low-temperature addition to the foaming system.

 

五、雙螺桿不是剪切越高越好:要控制比能量與熔體溫度

V. More Shear Is Not Always Better in Twin-Screw Processing: Control Specific Energy and Melt Temperature

雙螺桿的價值不是「把轉速開到最高」,而是用可重複的比機械能(SME)、停留時間與熔體溫度建立形態。SME可作為每公斤物料實際承受機械能的工程指標;過低無法打散SEBS,過高則可能造成EVA熱史增加、分子鏈斷裂、色變或後續發泡窗口縮小。

The value of a twin-screw extruder is not to run at the highest possible speed, but to establish morphology through reproducible specific mechanical energy (SME), residence time, and melt temperature. SME is an engineering measure of the mechanical energy actually applied per kilogram of material. If it is too low, SEBS cannot be dispersed; if it is too high, EVA may accumulate excessive thermal history, undergo chain scission or discoloration, and lose part of its downstream foaming window.

製程變數

Process Variable

過低時

When Too Low

過高時

When Too High

建議監控

Recommended Monitoring

螺桿轉速

Screw Speed

分散不足、產量低

Insufficient dispersion and low throughput

剪切發熱、降解、停留變短

Shear heating, degradation, and shorter residence time

轉速、扭矩、SME、熔體溫度

Speed, torque, SME, and melt temperature

捏合塊角度/數量

Kneading-Block Angle/Number

SEBS團聚殘留

Residual SEBS agglomerates

壓力與溫升過大

Excessive pressure and temperature rise

機頭壓力、粒子切片、濾網壓差

Die pressure, pellet cross-sections, and screen pressure differential

喂料量

Feed Rate

停留過長、易熱劣化

Overlong residence time and susceptibility to thermal degradation

填充過高、混煉不足

Excessive fill and insufficient mixing

扭矩百分比、產量、比能量

Torque percentage, throughput, and specific energy

溫度設定

Temperature Setpoints

塑化不完全

Incomplete plasticization

EVA/助劑熱史過大

Excessive thermal history for EVA/additives

各區實測熔體溫度,不只看設定

Actual melt temperature in each zone, not just the setpoint

真空排氣

Vacuum Venting

水分與揮發物殘留

Residual moisture and volatiles

過強可能抽走低分子助劑

Excessive vacuum may strip low-molecular-weight additives.

真空度、揮發分、粒子氣泡

Vacuum level, volatile content, and bubbles in pellets

安全的兩段法|第一段只製作EVAPOESEBS聚合物母粒,必要時加入相容劑;第二段再以低溫密煉或適合設備加入DCP、發泡劑與活化系統。避免活性過氧化物與發泡劑在高剪切雙螺桿中承受不必要熱史。

Safe two-stage method | In the first stage, make only an EVA/POE/SEBS polymer masterbatch, adding a compatibilizer if needed. In the second stage, add DCP, the blowing agent, and the activation system in a low-temperature internal mixer or other suitable equipment. This avoids exposing active peroxide and blowing agents to unnecessary thermal history in a high-shear twin-screw extruder.

六、相容劑何時需要?SEBS並不一定自動停留在界面

VI. When Is a Compatibilizer Needed? SEBS Does Not Necessarily Migrate to and Remain at the Interface

SEBSEB中段與POE相容性通常較佳,但EVAVA極性提高後,界面張力仍可能上升。若顯微形態顯示大顆粒、撕裂沿界面失效或貼合性明顯下降,可評估EVA-g-MAHSEBS-g-MAHEAA等相容策略。相容劑的功能是降低界面張力、抑制聚併或形成界面反應;添加過量則可能提高黏度、吸濕、影響交聯或改變發泡。

The EB midblock of SEBS is generally more compatible with POE, but interfacial tension may still rise as the VA-derived polarity of EVA increases. If microscopy shows large domains, tearing fails along interfaces, or lamination performance declines markedly, compatibilization strategies such as EVA-g-MAH, SEBS-g-MAH, or EAA can be evaluated. A compatibilizer lowers interfacial tension, suppresses coalescence, or creates interfacial reactions; excessive addition, however, may raise viscosity, absorb moisture, affect crosslinking, or alter foaming.


七、分散品質如何直接影響發泡?

VII. How Does Dispersion Quality Directly Affect Foaming?

3|粗大SEBS團聚體會形成應力集中與泡孔不均;細小分散相才可能穩定泡孔壁。

Figure 3 | Coarse SEBS agglomerates create stress concentrations and nonuniform cells; only a finely dispersed phase can potentially stabilize cell walls.

1. 成核不均:粗粒、污染物或界面空隙會造成局部過度成核與粗孔並存。

Nonuniform nucleation: Coarse particles, contaminants, or interfacial voids cause excessive local nucleation alongside coarse cells.

2. 泡孔壁薄弱:大相域橫跨泡孔壁時,界面可能成為破孔與撕裂起點。

Weak cell walls: When a large domain spans a cell wall, its interface may become the starting point for cell rupture and tearing.

3. 交聯不均:DCP與聚合物接觸歷史不同,使局部凝膠率與熔體強度波動。

Nonuniform crosslinking: Differences in the contact history between DCP and the polymers cause local fluctuations in gel content and melt strength.

4. 局部熱點:高黏團聚體提高剪切發熱,造成色差、焦燒或發泡劑提前反應。

Local hot spots: High-viscosity agglomerates increase shear heating, causing color variation, scorch, or premature blowing-agent reaction.

5. 表面與尺寸失控:粗孔、破孔及相界面回縮會放大表面粗糙與後收縮。

Loss of surface and dimensional control: Coarse cells, ruptured cells, and interfacial shrink-back magnify surface roughness and post-shrinkage.


建議的分散驗證方法

Recommended Methods for Verifying Dispersion

層級

Level

方法

Method

可判讀資訊

Information Obtained

快速製程

Rapid Process Checks

扭矩、SME、熔體溫度、濾網壓差

Torque, SME, melt temperature, and screen pressure differential

批次能量、熱史與團聚趨勢

Batch energy, thermal history, and agglomeration trends

粒子/片材

Pellets/Sheets

光學顯微鏡、染色切片、表面掃描

Optical microscopy, stained cross-sections, and surface scanning

黑點、未熔粒與相尺寸分布

Black specks, unmelted particles, and domain-size distribution

高階形態

Advanced Morphology

SEMAFM;選擇性蝕刻

SEM/AFM; selective etching

分散相尺寸、界面與連續相轉換

Dispersed-phase size, interfaces, and continuous-phase transition

熱分析

Thermal Analysis

DSCDMA

結晶變化、TgPS微區與阻尼窗口

Changes in crystallinity, Tg, PS microdomains, and the damping window

交聯流變

Crosslinking Rheology

MDR、動態流變、凝膠率、溶脹

MDR, dynamic rheology, gel content, and swelling

交聯產氣窗口與網路完整性

Crosslinking-gas-generation window and network integrity

發泡結果

Foaming Results

密度、泡孔尺寸/分布、撕裂、回彈、壓縮永久變形

Density, cell size/distribution, tear strength, resilience, and compression set

形態是否真正轉化為成品效益

Whether morphology truly translates into finished-product benefits

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