Polycondensation By Reactors Of Liquid Polymers And Solvent (2 Different Lines)
1st line composed of:
1 autoclave h.press. (A1) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for polyuretan (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 autoclave h.press. (B1) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for solvent (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 autoclave h.press. (C1) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for melamin (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 reactor h.press. (R1) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for reaction 3 components (polyuretan + solvent + melamin) (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
2nd line composed of:
1 autoclave h.press. (A2) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for polyuretan (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 autoclave h.press. (B2) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for solvent (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 autoclave h.press. (C2) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for melamin (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
1 reactor h.press. (R2) with power motor (80cv) vertical mixer high speed, by electronic control inverter, for reaction 3 components (polyuretan + solvent + melamin) (temperature & pressure control by microprocessor and computer centralized) processing in nitrogen
Columns Stills For Solvent And Polyuretan And Polymer Recovery
4 vertical columns stills for recovering of solvent, polyuretan and polymer, with vertical distiller multystadios, and big plant with pumps and big tanks for storage various waste components of raw materials
Dry processing
Vertical Extrusion And Dosing Pumps For Spinning Elastomer (Spandex) Multifilaments Yarns, Range Count Yarn (From 10 Denier To 380 Denier); Years: 1988, 1991, 1994, 1998, 2000, 2002
6 lines x 18 vertical columns (height: 15m each) x 2 winders positions from 16 bobbins each = total 216 comoli automatic revolving winders (2 positions) x 16 bobbins = 3456 ends
Each line, each vertical column is composed of: 2 vertical extruders, 2 dosing pumps, 4 godets for draw system x 2 winders positions, 1 spin box from 16 spinnerettes x 1 automatic revolving winder from 16 bobbins + 2 spin box from 16 spinnerettes x 2 automatic revolving winder from 16 bobbins
Bobbins max. weight: 0.350/0.400kg
Wet Processing
Compact vertical extrusion and dosing pumps, immersion in coagulation water tank, for spinning elastomer (spandex) multifilaments yarns, range count yarn (from 380 denier to 1680 denier): years: 1988, 1991, 1993
3 lines x 36 compact vertical columns (height: 2m) x 36 winders positions from 4 bobbins each = total 108 comoli automatic winders x 4 bobbins = 432 ends
Each line, each vertical column is composed of: 2 extruders/pumps, 36 dosing pumps, 36 spin box from 4 spinnerettes each, immersion in 36 coagulation water tank, 4 godets for draw system x 1 winders positions x 36 positions winders
Bobbins max. weight: 0.650/0.800kg
1 chips pilot compact vertical line
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