Unsaturated Polyester Resin Plant

Abster Equipment offers our customers a wide array of Polyester Resin Plant for the manufacture of Polyester resin like General Purpose resin, ortho resin, Marble resin, Gel coats alkyd resins. These are highly durable and have efficient rendition capacity owing to the top-notch stuff and the most advanced technologies employed in their production. These plants are available at a very reasonable price.

Unsaturated Polyester Resin Plant

Our Unsaturated Polyester Resin Plant is developed and supplied as per our clients’ requirements. The basic system consists of a reaction kettle, vertical column, sub-cooler, and horizontally inclined condenser with separator and dilution blender. The batch time is approximately 16 to 20 hours and therefore, suitable mechanical seal arrangement for better results and to prevent any leakage is provided.

Working principle

Unsaturated polyester resin manufacturing plant is a excellent machine used to produce unsaturated polyester resin, phenolic resin, epoxy resin, ABS resin, paint. The full line is composed of Vertical distillation columns, horizontal condenser, storage devices, oil spill tank.

Application

It is a excellent machine used to produce unsaturated polyester resin, phenolic resin, epoxy resin, ABS resin, paint.

1. esterification reactor

2 Vertical frictional column

3 Vertical condenser

4 horizontal condenser

5 storage device

Introduction

Firstly, Unsaturated Polyester Resin Production Line is excellent equipment used to produce unsaturated polyester resin, phenol resin, epoxy resin, ABS resin, and related chemicals. With this machine, the purity of finished products will be more than 99.8%.

Secondly, this resin kettle is a complete production, it realizes automatic manufacturing. It is composed of the following parts:

1. Etherification reactor

2. Vertical fractional column

3. Vertical condenser

4. horizontal condenser

5. water storage tank

6. Dilution tank

Thirdly, as for the kind of reaction “Etherification” and about the “refining the final product”

l You should use activated Carbon & tetra butyl titan ate as the catalytic agent to synthesize DIOP.

l The best process condition: Molar ratio of Ethanol anhydride should be: 2.8:1.

l Etherification temperature: 210 ℃

l Etherification time: 2.5 hours

l Catalyst Amount:0.5%

Under such a condition, Etherification conversion rate of DOP is more than 99.8%. These catalysts exhibited excellent activity, it can be reused, and there is no pollution.

Pilot/Small/Laboratory Unsaturated Polyester Resin Plant

*Model selection reference of reaction kettle

Composition Instructions
Specification (L) 5-200
Design Pressure (Mpa) Atmospheric Pressure or under pressure
Material Carbon steel, stainless steel, enamel, graphite
Heating Forms Electrical heating with medium in jacket, external half coil steam heating, external half conduction oil heating, hot water infrared heating etc.
Cooling Forms Refrigeration medium in the internal pipe jacket
Blending Power Model selection is made according to material viscosity, liquid-solid ratio, liquid specific gravity, solid specific gravity, solid granularity, rotation speed, paddle type, with or without baffle or internal coil.
Stirring blade Forms Anchor type, frame type, flat paddle type, pitched paddle type, ribbon type, turbo type, pusher type and multiple compound type
Seal Mechanical seal or stuff packing seal
Inner Surface Treatment Polished or no polished
Discharge Valve Flanged ball valve, open downward discharge valve and others
Technological Pipe Hole Manhole, sight glass, distillation mouth, imported materials, pressure gauge port, temperature, mouth, mouth filling N2,

*Technical Parameter

            Model

Parameter

Reactor Volume(L) Mixing speed (rpm) Heat exchange surface (m2) Separator(L) Total power(including heating power)(KW)
RV-10 10 0-84 0.5 5 6.37
RV-30 30 0.5 12 12.37
RV-50 50 1 15 18.55
RV-100 100 2 25 19.65
RV-150 150 2.5 30 26.2
RV-200 200 3 50 33.5
Note: In case of inconformity of the data in the table due to technical improvement or customization, the real object shall prevail.
This equipment is including: Reaction vessel, mixing system, vacuum system, condenser, separator, conduction oil preheating system, platform.
1.  Heating and cooling method: 1. Heating and cooling by jacket. 2. Heating by jacket and cooling by inner pipe coil.
2.  Type of electrical device: 1. Ex-proof type. 2. Normal type
3.   Electric cabinet control mode: 1. Touch-screen control. 2. Button control 

 

Ourt Other Product: UPR resin Manufacturing Plant