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uria formal dehide plant
uria formal dehide plant
uria formal dehide plant
uria formal dehide plant
uria formal dehide plant
uria formal dehide plant
uria formal dehide plant
uria formal dehide plant

uria formal dehide plant

Price 20000000 INR/ Set

MOQ : 1 Number

uria formal dehide plant Specification

  • Condition
  • New
  • Power
  • 440 Volt (v)
  • General Use
  • ADHESIBE FOR LAMINATION
  • Material
  • Stainless Steel
  • Capacity
  • 5 Ton/day
  • Weight (kg)
  • 100000 Kilograms (kg)
  • Computerized
  • Yes
  • Automatic
  • Yes
  • PLC Control
  • Yes
  • Mixer Type
  • Agitator
  • Shaft
  • Single Shaft
  • Drive Type
  • Mechanical
  • Voltage
  • 440 Volt (v)
  • Dimension (L*W*H)
  • 120X 120 X40 Foot (ft)
  • Feature
  • High Speed, Low Energy Consumption, Automatic Alarming, Digital Time
  • Color
  • Green
  • Warranty
  • 2 YEAR
 

uria formal dehide plant Trade Information

  • Minimum Order Quantity
  • 1 Number
  • FOB Port
  • KOLKATA
  • Payment Terms
  • Cheque, Telegraphic Transfer (T/T)
  • Supply Ability
  • 1 Number Per Year
  • Delivery Time
  • 180 Days
  • Packaging Details
  • WOODEN CRATE
  • Main Export Market(s)
  • Asia, Australia, Central America, North America, South America, Eastern Europe, Western Europe, Middle East, Africa
  • Main Domestic Market
  • All India
  • Certifications
  • ISO9001 2014
 

About uria formal dehide plant

(4PR) unsaturated polyester Resins are the basis raw materials forthe manufacture of general purpose (GP) products which has applications inalmost every field of operation such as transport, construction, civil, marine,chemicals, electrical, engineering as well as domestic applications.

                                                  CommercialUPR resins are composed of the following essential ingredients a Linearpolyester resin, a cross linking monomer and inhibitor to retard cross linkinguntil the resin is to be used by the fabricator.  The linear polyester is typically thecondensation product of an unsaturated dibasic acid as the source of ethylenicunsaturation and a glycol; the usual cross linking monomer are styrene, vinyltolerance, methyl methacrylate, conventional inhibitors are hydroquinone,t-butyl catechol.  The basis resin can bepolymerized to infusible materials by the action of free radicals such as peroxides.

                         Processof manufacture                           :               There is a two step batchprocess, i) Condensatioin reaction between a dibasic acid and a diol in aninert gas atmosphere until a low acid number is reached.  The resulting linear co-polymer is cooked andblended with a monomer usually at 1200-1500- (6000C-6500C)and an inhibitor to impart storage stability.

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