Injection Molding Process Parameters

Injection Molding Process Parameters

Chapter 27 Injection Molding Process Parameters In this chapter, we will present the main injection-molding parameters for a number of thermoplastics...

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Chapter 27

Injection Molding Process Parameters In this chapter, we will present the main injection-molding parameters for a number of thermoplastics. When setting an injection-molding machine with a new resin, you should always use the recommended process data from the raw material producer if available. If you do not have them, look on the producer’s website or search for them on the Internet. NOTE: The values shown in Table 27.1 are typical for an unmodified standard grade of the polymer in question and serve only as a rough guide. Contact your plastic raw material supplier for accurate information about your specific grade! The Melt temperature is one of the most important parameters. When processing semi-crystalline plastics, you should always consider the risk that you may get unmelted granules in the melt. To eliminate this risk, you should use the cylinder temperature profile that depends on the capacity utilization of the cylinder (see Section 26.8). You should also be aware that additives such as flame retardants or impact modifiers often require a lower temperature than the standard grade. Glass fiber reinforced grades should have, as a rule, the same temperature settings as unreinforced grades. The Mold temperature is also one of the most important parameters for achieving the best quality. For semi-crystalline plastics you need a certain temperature to ensure that the material’s crystal structure will be correct and thus provide the best strength and dimensional stability (less post-shrinkage). See Section 26.9. Drying is needed for plastics that are either hygroscopic (absorb moisture) or sensitive for hydrolysis (degraded chemically by moisture). See more in Section 26.7. We recommend that molders use dehumidifying (dry air) dryers in their production. Therefore we publish both the temperature and drying time needed to be below the maximum allowed moisture content for the material, provided that the dry air dryer is working with a sufficiently low dew point. Note also that if you dry the material longer than the indicated time in the table you should reduce the temperature 10–20 °C because some materials can oxidize or degrade thermally. Material where “Does not normally need to be dried” is given in the table may still need to be dried if condensation will occur on the surface of the granules. If this is the case, a drying temperature of 80 °C and a drying time of 1–2 hours usually works well. The reason that the maximum Peripheral speed is published in the tables is that many molders in good faith are dosing up the next shot with too high of a screw speed and thus unnecessarily degrading the polymer chains in the cylinder by high shear and friction, resulting in poorer quality. In Section 26.13 (Figure 26.40) you will find a formula where you can calculate the maximum allowed peripheral speed to maximum allowed rotation speed depending on the screw diameter. If you cannot find the recommended maximum peripheral speed for your resin, you should take into account that high-viscosity grades sometimes require 30% lower

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Chapter 27 — Injection Molding Process Parameters rotation speed compared to a less viscous standard grade. For example, impact-modified acetal with a melt index of 1–2 g/10 min has a recommended maximum peripheral speed of 0.2 m/s, compared to 0.3 m/s for a standard grade with melt index of 5–10 g/10 min. For glass fiber reinforced grades you will usually find the recommended maximum peripheral speed to be 30–50% of the speed for the unreinforced grade. Also, impact modified, flame retardant grades used to be more sensitive to shear than standard grades. Having sufficiently high Hold pressure is especially important for semi-crystalline plastics. Usually it is recommended to have as high a pressure as possible without getting flashes in the parting line or having ejection problems. We provide hold pressures because many molders sometimes in good faith set far too low a hold pressure, resulting in poorer quality. Other important parameters such as hold pressure time, hold pressure switch, back pressure, injection speed, and decompression are more dependent on the part design and machine conditions. We therefore cannot give any general values of these parameters, but refer you instead to Chapter 26. Table 27.1 Typical processing data for unmodified standard grades of common thermoplastics.

Semi-crystalline commodities Material

Type

Melt temperature Nominal

Unit Polyethylene

PEHD

Range

Mold temp.

Drying Temp. Time

Max moisture

Dew point

%

°C

°C

°C

°C

°C

200

200–280

25–60

Does not normally need to be dried

Hours

Hold pressure

Max peripheral speed

MPa

m/s

25–35

1.3

Polyethylene

PELD

200

180–240

20–60

Does not normally need to be dried

25–35

0.9

Polyethylene

PELLD

200

180–240

20–60

Does not normally need to be dried

25–35

0.9

Polyethylene

PEMD

200

200–260

25–60

Does not normally need to be dried

25–35

1.1

Polypropylene

PP

240

220–280

20–60

Does not normally need to be dried

35–45

1.1

Mold temp.

Drying Temp. Time

Max moisture

Dew point

Hold pressure

Max peripheral speed

%

°C

Amorphous commodities Material

Type

Melt temperature Nominal

Unit Polystyrene

PS

HIPS

PS/SB

SAN

Range

°C

°C

°C

°C

230

210–280

10–70

Does not normally need to be dried

Hours

MPa

m/s

45–50

0.9

230

220–270

30–70

Does not normally need to be dried

45–50

0.6

240

220–290

40–80

Does not normally need to be dried

45–50

0.6

ABS

240

220–280

40–80

80

3

0.1

− 18

45–50

0.5

ASA

250

220–280

40–80

90

3–4

0.1

− 18

40–45

0.5

PVC

Soft

170

160–220

30–50

Does not normally need to be dried

40–45

0.5

PVC

Hard

190

180–215

30–60

Does not normally need to be dried

50–55

0.2

230

190–260

30–80

8

60–80

0.6

PMMA

298

4

0.05

−18

27 Injection Molding Process Parameters

Semi-crystalline engineering polymers Material

Type

Unit

Melt temperature Nominal

Range

Mold temp.

Drying

°C

°C

°C

°C

Temp. Time

Max moisture

Dew point

%

°C

Hours

Hold pressure

Max peripheral speed

MPa

m/s

Acetal

POM Homo

215

210–220

90–120

Does not normally need to be dried*

60–80

0.3

Acetal

POM Copo

205

200–220

60–120

Does not normally need to be dried*

60–80

0.4

Polyamide 6

PA6

270

260–280

50–90

80

55–60

0.8

2–4

0.2

− 18

Polyamide 66

PA66

290

280–300

50–90

80

2–4

0.2

− 18

55–60

0.8

Polyester

PBT

250

240–260

30–130

120

2–4

0.04

− 29

50–55

0.4

Polyester

PET+ GF

285

280–300

80–120

120

4

0.02

− 40

50–55

0.2

Mold temp.

Drying

Hold pressure

Max peripheral speed

Amorphous engineering polymers Material

Type

Melt temperature Nominal

Unit Polycarbonate

PC

Range

Temp. Time

Max moisture

Dew point

°C

°C

°C

°C

Hours

%

°C

MPa

m/s

290

280–330

80–120

120

2–4

0.02

− 29

60–80

0.4

Polycarbonate

PC/ABS

250

230–280

70–100

110

2–4

0.02

− 29

40–45

0.3

Polycarbonate

PC/PBT

260

255–270

40–80

120

2–4

0.02

− 29

60–80

0.4

Polycarbonate

PC/ASA

Mod. PPO

250

240–280

40–80

110

4

0.1

− 18

40–45

0.3

290

280–310

80–120

110

3–4

0.01

− 29

35–70

0.3

Mold temp.

Drying

Hold pressure

Max peripheral speed

Semi-crystalline advanced thermoplastics Material

Type

Melt temperature Nominal

Unit Fluoroplastic Aromatic polyamide

FEP/ PFA

Range

Temp. Time

Max moisture

Dew point

%

°C

°C

°C

°C

°C

350

300–380

150

Does not normally need to be dried**

Hours

MPa

m/s

Low***

****

PA6T/66 325

320–330

 85–105

100

6–8

0.1

− 18

35–140

0.2

PA6T/XT 325

320–330

140–160

100

6–8

0.1

− 18

35–140

0.2

LCP

355

350–360

 60–120

150

3

0.01

− 29

20–60

Max

PPS

330

300–345

 70–180

150

3–6

0.04

− 29

45–50

0.2

PEEK

370

360–430

160–200

160

2–3

0.1

− 18

50–65

0.2

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Chapter 27 — Injection Molding Process Parameters

Amorphous advanced thermoplastics Material

Type

Unit

Melt temperature Nominal

Range

Mold temp.

°C

°C

°C

Drying Temp.

Time

Max Dew moisture point

°C

Hours

%

°C

Hold pressure

Max peripheral speed

MPa

m/s

Polyetherimide PEI

380

370–400

140–180

150

4–6

0.02

− 29

70–75

0.5

Polysulfone

340

330–360

120–160

150

4

0.02

− 29

50–70

0.4

PSU

PPSU

370

350–390

140–180

150

4

0.02

− 29

50–70

0.4

PES

360

340–390

140–180

140

4

0.02

− 29

60–80

0.2

   * If the granules have been exposed to moisture or condensation you should dry approximately 2 hours at 100 °C   ** If the granules have been exposed to moisture or condensation you should dry 3–4 hours at 150 °C  *** Hold pressure should be as low as possible **** Stainless special screws are required

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