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Pyrolysis Machine Converting Waste Plastic into Oil

ADITYA RECYCLING
Bangalore
www.adityahitechmachines.com

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The Project Converting Waste Plastics into Oil
Model => Batch Type ECP-2011

ADITYA RECYCLING
Bangalore
www.adityahitechmachines.com

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The Value of Business!

Depletion of Fossil Energy

Intensified Regulation of
Greenhouse Gas Emissions

Rapid Increase of the need to
Improve Nvironmental Pollution

Protection of the Earth,
the Nation,
the Environment

Creation of
New Energy
The plan to Overcome
New Regulations
High efficiency (average80%)
High quality (light oil level)

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Alternatives for the Future!

Bio Energy

Solar Energy

Wind Power Generation Energy

Nuclear Energy

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Creation of Renewable
energy!

Vinyl Waste

Waste Fishing Net,
Fishing Gear

Cracked Oil from Household Waste Vinyl

Used Waste Lubricating Oil

Wasted Tires

Cracked Oil from Wasted Tire
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The Relative Value of Oil Conversion Projects

# TOE : Tonnage of Oil Equivalent

Refinery Equipment

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Use and Value of Produced Oil from Pyrolysis

Waste Plastics, Waste Oil Conversion to Fuel Oil

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Leader of environment-friendly
technology, Ecocreation !!
Ecocreation is an environment-friendly
company that cares about future
environment of the earth and is a global
leading company that opens a new era
of low carbon green growth by reducing
CO2 emission for invigoration of
resource circulation and prevention of
global warming through production of
environment-friendly products.

Simple Process,
Low Investment

The Best Stability,
Safety

The Best Oil
Conversion
Profitability
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Hybrid Cracking Emulsion Technology
Nitrogen,
Atmospheric Pressure Condition
Pyrolysis Emulsion
( 380~480℃ Heating Fluid )
Reforming R.P.F( Solid Polymer )
Reforming Waste Plastic

PP(Poly-Propylene), PE( Poly-Ethylene )
폐기물
PS(Poly-Styrene), PPT( Polyphenylene Terephthalate )

Pyrolysis Refined Oil

Apply liquefaction,
Separation TTechnology Based Catalyst

Oil
Typical yields : Polymer Waste
Kerosene, Diesel more than 80%, Naphtha around 15%, Gas around 3%,
CHAR (Coke) around 3%

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Plant Size by 12,000mm(W) X 10,000(L) X 7,000(H)
Space required for installation => Variable for capacities
Notice => Waterproof / Protection against wind must in roof
Period required for installation by within 10 days site installation
Process

The first pyrolysis of waste and secondary
catalytic cracking with catalyst

Operation Type

Batch type

Input Plastics

PP, PE, PS

Yield

Approx. 75 ~ 80 %
(It can be different according to the waste
plastics type)

Electric Capacity Three-Phases (220V or 380V)

Produced Oil
Component

Naphtha, Kerosene & Diesel Fraction

Operating Cost

Low operating cost due to the use of
recycled oil and waste gas from self
production

Safety

Less risk of explosion and fire due to
nitrogen substitution

It is not necessary to separate, shred and
clean the waste plastics.
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Power Start ON

Gas Collector ON

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The Main Process Flow Diagram 1

Input

(Waste Plastic)

(Refining/Storage)

(Compress)

(Separation/Cooling)

(Compressed Stuff)

(Contact Catalytic Reforming Cracking)

(Pyrolysis)
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Molten Material,

Process Flow Diagram 2

Pressing Heat Supply

Air emissions

Reactor , Process fuel
Environmental Process
Dust Collection,
Adsorption of odor

Material
Screening
Compression
Input liquid cracking catalyst

Utilization of Process fuel

Vapor catalytic cracking catalyst column
The primary classification, NAPTHA, GAS

input Material
and Melting

Primary fusion
decomposition

Catalyst
Column
secondary
catalytic
cracking

Primary classification process

Primary cooling process

Decomposition of chlorine compounds, Input inhibitory catalyst
Secondary Classification

Input coking inhibitor

Storage / Ship

Secondary classification NAPTHA, GAS

Input GUM inhibitor,
Neutralization reagent

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Process Chamber Placement Pictures

Machine under
manufacturing
(Currently available
daily capacity by
1 ton, 2 tons and
3 tons)

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1. Production Process
Section

System Configuration / Characteristics

Remarks

Heating Furnace( Heater )

Indirectly Heated =>
Combustion Gas Transfer Heat to the Reactor
High Efficiency =>
Utilize Waste Gas, Apply Waste Heat Recovery System
Automation =>
Autoignition, Automatic Temperature Control Burner System
Safety / Cooling =>
Explosion Prevention, Forced Quick Exhaust Cooling

Using Liquid
Gas Fuel( Option )

Pyrolysis Reactor
Completed the iIspection of B.T.

Special Material of Explosion Proof,
Anti-Corrosion( SUS )
High Efficiency Catalyst Layer Built-In,
External Apply Coking prevention Technology
Apply Anti-Corrosion( H2S / HCl ) Technology

Pyrolysis Reactor

Splitter / Condenser

Apply Splitter,
Condenser Integrated Structure Facility
Adoption of 3( Three-Phase )( Solid,Gaseous,Liquid)
Fractionator

Heat Exchanger

Application System ofAanti-Corrosion Material and
Neutralizing Agent

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2. Process Support
Section

System Configuration / Method

Option

Cooling Equipment System

Apply Water-Cooling Type Cooling System
=> Apply Cooling Water anti-Corrosion System
=> Apply Cooling Water Scale Prevention System
Cooling Air-Cooled Furnace
=> Apply Cooling Heating Medium Reactor by
Cooling Heat Recovery

Separate
Chemical

Nitrogen Injection Safety System

Nitrogen Injection Around Process Operation
=> For Cooling
=> The Inhibition of Oxidization
=> Self-Nitrogen Generator can be Adopted

Anti-Corrosion
Chemical Injection System

Apply Special Corrosion Inhibitor
( Apply to the Target of Process Cooling Classification System )
=> Prevention of Hydrochloric Acid Corrosion
=> Prevention of Organic Acid Corrosion

Heat Recovery System

Recovery
Utilization of Exhaust Waste Heat from Heating Furnace Chimney
=> Recycling of OFF Gas by Economizer System
=> Separate Heating Furnace by Operate Reactor

Option
Equipment

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3. Safety and Environmental Equipment
Section

System Configuration / Method

Remarks

Reactor Explosion Proof Safety
System

Satisfy National Safety Standards Material & Facility
Required Government Agencies Verify
Adopt Pressure Relief System in an Emergency
Adopt National Standard Explosion Proof Equipment
Explosion Proof Electrical System

Apply Pipe
interlocking Device
Against Vibration
Apply Reactor
Interlocking Device

Emergency Response System in case
of Power Failure

Apply Emergency Private Power Station System
Apply Process Generated Gas Continuous
Processing System
Incineration of OFF-Gas
Apply Flare Stack

Option of Small
Diesel Generator

Oil Spill Response System

Apply Preparing Process for Oil Spill
Loss Prevention System
=> Compliance with Government Standard

Precipitator Deodorizing
Adsorption Removal

Post Processing of Emission Combustion Gas
from Incinerator by Heating Furnace
=> Precipitator, Odor Adsorption Column
=> Precautionary Investment Prepared for Emergency

Process Waste Treatment System

Solid Waste Consignment Process for General Landfill
Development of a Separate Solid and Sale

Facility more than
3 Tons

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Characteristic of our Development Process
Section
Our Company Process

Material
Separation
Polymer Resin of
PP, PE, PS, ABS, etc
Complex of
Single Substance or
Mixture

Other Company Process
Solid Waste RPF

Process Characteristic

Remarks

Excellent Yield
=> Kerosene, Diesel Grade
Excellent Separation Process
High Quality Oil Production
=> Minimize of Wax Component
=> Excellent Low Temperature Fluidity

In the case of
Catalytic Cracking of
Mixture,
the Process Efficiency of
Solid Liquid Mixtures
Is Twice.

Low yield
=> The Yield of Naphtha is about
60% at least
Fixed Separation Decline
Low Quality Oil Production
=> Contain Large Amounts of Wax
Very Poor Low Temperature Fluidity

Process Operating
Time Is Long
Cause Energy Mass
Consumption form or
Product Quality
Becomes Degraded
It is inevitable that
Light Naphtha Occurs
in Bulk because of
Reflux reaction to
Reduce Wax

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Characteristic of our Development Process

Section

Process Operating Condition

Relative Comparison of
Operating Hour
( Based 5 Tons Reactor)

Our Company Process

Normal Pressure Indirect
Heating Type
=> 380~480℃
=> Normal Pressure 0.5 Kgf
( Gassing Pressure Standard )

In case of Solid Liquid
Mixture Process
Around 10 hours
( Shorten Operating Hour )

Other Company Process

Normal Pressure
High Pressure Indirect
Heating Type
=> 400~500℃

In case of Solid Single
Material Process
=> 20 hours
=> Prolonged Operating
Hours According to
Reflux Reaction

Normal Pressure
High Pressure Indirect
Heating Type
450~700℃

In case of Solid Single
Material Process
15 hours

Main Products
Boiling Point Range
130~385℃ of
Fuel Oil and Similar to
Kerosene and Diesel

Fuel Oil Containing
Large Amounts of
Waste Naphtha,
Gas and Wax
=> Room Temperature
Low Temperature
Fluidity is very Bad
because of
Wax Containing

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Characteristic of our Development Process

Section
Our Company Process

Reactor

Horizontal STOP Reactor
Semi Automatic
Medium Sized Reactor

Other Company Process Rotary Fluid Reactor

Process Characteristics

Remarks

It is possible to Input more than 80% of
the Material
=> Equipped with Catalyst Column
Remove Wax and Foreign Material
Apply Technology
=> Apply self Development Isomerization
Catalyst
=> Excellent Thermal Efficiency
=> Coking Prevention and
Easy Operation Management

Isomerization
Catalyst
As the Catalyst which
Changes the Structure
of Paraffin with
It Changes
the Structure of
Wax and Makes
It very good Fluidity
Material

Limited less than 50% of Raw Material
Charging Quantity by Based on Liquid
Law Material
=> Thermal Efficiency is Disadvantage
Heat Loss is Great
=> Coking Management is Difficult
=> Front Coking Phenomenon Occurs
At 360°C
=> Concern about Mechanical Durability
Problems According to Reactor Fluid

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Our Competitive Technology
Process Risk
Reactor Coking

Distiller Tube Clogged
(Wax / Saponification substance)

Other Company
Existing Technology
Extended Maintenance time
=> Heat Transfer Decline
=> No Chemicals to Remove

Impurities Occur
Wax Occurs Frequently
Piping Blockage

Applied Independently Developed
Inhibitors for Impurities Occur
=> Expected Patent Application
=> Wax Cracking Catalyst Development
=> Expected Patent Application
Dramatically Improve Fuel Quality

Remarks

Independently Developed
Application of Anti Coking and
so Expected a Patent Application
Dramatically Improved Process

Poor Quality in Winter
Product Quality Degradation
Caused by Wax

Product Quality Degradation
due to Facility Hydrochloric Acid
Corrosionby PVC and Salt

Our Technology

Exposure to Corrosive
Hydrochloric Acid,
Difficult for Screening
Material
-Shorten Equipment Life
-VCM Monomer Occurs and
Fuel Quality Degradation

As the
Highest Level
of Technology
at Home and
Abroad,
No other
Companies
Commercial
Pracactes

-Applied VCM Monomer
Dechlorination Catalyst Development
( Expected Patent Application)
-Suppress Interference Reaction by Salt
(The same patented item)

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Our Competitive Technology

 Select Fuel Additive Based On the Same Refineries

 Applied Technology
=> Fully Improved Combustion Efficiency

=> Other Functionality

 Possible to Provide Leading High
 Performance Reforming Catalyst

 Facilities due to having Independent Catalyst Development Efforts
 Engineering Technique

=> Contribute to Improving Future Productivity

► Profitability
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Pyrolysis Yield according to Material

Material Section

Pure PE, PP, PS Standard
=> Except of PVC

Pyrolysis Yield

• Gas => 2~3%
• Naphtha => Around 15%
• Kerosene & Diesel Fuel
=> More than 80%
• Coke( ASH ) => Below 1~3%

Remarks

• Distillation Appearance
( Boiling Point )
=> 130 ℃ ~ 385℃
=> In the case of RPF
=> Yield Change Depending
on the Foreign Content

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Our Technical Characteristics
The Best Catalyst Control Technology of the World
Liquid Catalytic Cracking, Vapor Catalytic Cracking, Decomposition of Chlorine Compounds,
Neutralization Catalyst Technology, Apply Suppression Technology of Wax, Gum, Coking
Secured Economic
Minimize
Investment

Secured Stability

Cost of Equipment Superior Economic
Compared to other Company Gas uses
Its Own Fuel

Maximize the Stability of Pyrolysis
Furnace due to the Secure of Low
Pyrolysis Temperature
Decomposition of Chlorine
Compounds Input Neutralization Catalyst
Minimize the Occurrence of Chlorine
Gas Causing Equipment Corrosion to
Adoption of Anti-Corrosion
Minimize Simplify Production Process
Facility to Minimize

Minimize
Operation
Cost

Maximize Thermal efficiency
of Approx. 8 %
No limited material is Single Operation
of High Molecule and Waste Oil

Maximize
Profitability

HDPE Standard Diesel Level can be
Produced more than 75% of Pyrolysis Oil
Minimize 2nd Waste Material
=> Dangerous Substances like Gas,
Naphtha, etc
=> Generated Gas and Naphtha are used
for its Own Fuel.

Minimize Disposal Dangerous Material
Stability due to Low temperature Pyrolysis
Stable Operation due to Minimize
the Occurrence of Wax and Regular
Maintenance and Stable Shut down in
case of Abnormal Condition and
Easy Process Maintenance

Facility

Stability

Operation
Stability

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Our Process Operating Characteristics - Case 2

 Material => Waste Plastics 100%( RPF RDF, Recycling Chip )
 Operating Hour is Variable Depending on the Characteristics of Materials
=> Operating Hour is Very Variable Depending on Foreign Content and

Content of the Pure Polymer
 It is very General to Operate One Time a Day

( Normal Operating 12 hours )
=> In the case of much Foreign Content

=> ASH Removal Time Occurs by Increasing after Reaction
 Recommended Maximum One Time a Day

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Comparison of Produced Oil based on our Technology

RPF PYROYSIS OIL @ ASTM D86
당사 개질 RDF 촉매

기존 상용 촉매

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Hybrid Cracking Process Product Quality
Classification (Red is Standard)

Diesel (Oil Company’s Diesel)

Flash Point(℃)

Above 40
(Above 30℃ of Pyrolysis Oil )

Pour Point(℃)

Below 0(Apr. ~ Sep.),
Below -17.5 (Oct. ~ Mar.)

Waste Lubricating Oil
Cracking Oil (NO Catalyst)

Our Pyrolysis Oil of Waste Plastics

30~60 : Variable According to Process
-30

-10

Residual Carbon, Wt%

Below 0.15

0.17

0.05

ASH, Wt%

Below 0.05

0.001

0.001

Distillation 90%, ℃

Below 360

395

350

2.0~5.8

5.2

2

SULFUR, Wt%

Below 0.2

0.08

0.005

Moisture & Precipitate, VOL%

Below 0.5

0.07

0.05

Cetane index

Above 45

-

40~55

Lubricative, HRRR W.S.D

400 MAX

Red Orange B&C

300

Above 0.815~below 0.855

0.82~0.84

Pb

Below 1 ppm

None

None

Cr

Below 1 ppm

None

None

Cd)

Below 1 ppm

None

None

As)

Below 1 ppm

None

None

Centistoke @ 40℃, cSt

@15℃ DENSITY, g/㎤

Contents of
Heavy Metals

0.79~0.81

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Technology Outline( Catalyst Performance )

Minimize of Heavy Oil Fraction

Maximize of Kerosene & Diesel Grade

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High Molecule PP,PE,PVC

Decomposition &
isomerization ,
Reaction of dechlorination

Pour point Below -25℃
Becomes High Quality Fuel
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Technology Outline
Infrared Analysis of Kerosene & Diesel at General Gas Station

High Quality Hydrocarbon

High Quality Hydrocarbon

Aromatics

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Technology Outline
Infrared Analysis Comparison of Our Catalyst Pyrolysis Oil
High Quality Hydrocarbon

HDPE 촉매 분해유
FT-IR CHART

Hydrocarbon Double Bond Substance

High Quality Hydrocarbon

Aromatics

Fully meets as Petroleum fuel based on Analysis of the chemical structure

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Infrared Analysis Comparison of R.P.F Catalyst Cracking Oil

RPF(PE ,PS 등) 촉매 분해유
FT-IR CHART
Hydro Carbon Aromatic

High Quality Hydro Carbon

Hydro Carbon Double Bond Substance

High Quality Hydro Carbon

Unrefined Moisture

Plasticizer Line C-O Combination

Fully meets as petroleum fuel based on analysis of the chemical structure
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Economic Evaluation of Refined Oil Production
Raw Material => Waste Plastic / RPF 100% Handling
Throughput => 3 Tons / day X 20days / Month Operation
Leased Plant Standard
Output => Gross 75% Recovery Rate /2500 Liter( Reflected by a Reduction in Fuel use Itself )

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Economic Evaluation of Refined Oil Production

Standard Price => Selling Price of Gas Station Jan. 2012

Reasonable Price Range (Based Kerosene KRW 1400)

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[ The Purpose of Emulsified Recycle Business ]
1. Reduce Emission Amount of Co2
{ Reduce by Approx. ¼ Compared to Incineration Treatment }
2. Reduce Incineration Treatment or Reclaiming Disposal Cost
3. Create a New Business and Profit by Selling Recycled Oil
4. Thorough Information Management of Wastes

[ The Purpose of Product ]
▶ Fuel for Diesel
=> Industrial fuel, Agricultural Boiler, Incinerator,
Diesel engine generator, Vessel& heavy machinery fuel, etc
▶ Residue is Available as a Heating Fuel for Cement Furnace Fuel,
Heating Fuel of Iron Works and Foundry{ Cokes 4500Kcal }

[ Recommend Type of Business ]
Main Agent of Administration( City )
Recycling Resources Enterprise
=> Recycle Center, Plastics Recycling Resources Enterprise,
Mineral Resources Enterprise Waste Disposal Enterprise
=> General Waste, Industrial Waste, Agricultural Waste
Plastics Industry
Product processing industry, Film printing industry
Chemical Industry
Polymer Ingredient Manufacturing Industry
Chemicals Industry

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Q&A about Catalytic Cracker of Waste Plastics
Q.1. What is the Characteristic of this Device?
A
① Low Operation Cost due to Pyrolysis using the Fuel of Recycled Oil and
Waste Gas.
② This Device Realized Low Cost Compared to Former Emulsification Device
Q.2. What is the Processing Capacity of this Device?
A
① Processing Capacity
=> 1.000kg, 2.000kg, 3.000kg, 4.000kg, 5.000kg / Day

Q.3. What is the Processing Progress of this Device?
A
① Input a Batch of Waste Plastics in the Preprocessing Stage.
② Heat the Raw Materials of Waste Plastics and Gasify Inside a Furnace.
③ Obtained Cracked Gas is Reformed into Gasoline Grade and
Diesel Grade by a Catalyst Column and save in each Cracked Oil Tank
Q.4. What is different from General Method until now?
A
① Existing Emulsification Device Safety Matter Operation Cost and
our Emulsification device needs a Gaseous Reforming Catalyst and
there is No Risks of Explosion and Fire because of using Nitrogen and
Low Operation Cost by using the Fuel of our Own Produced Recycled Oil and Gas

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Q&A about Catalytic Cracker of Waste Plastics

Q.5. What is the Influence on Safety and Environment?
A
① Block the Emission of Harmful Gas with
the Installation of Gas Washer and Storage Tank
② Not necessary of Measures and like a Silencer and
etc Specially even though there are Operation Sounds
like Motor Sounds and Cooling Pump Sounds, etc
③ Not necessary of Measures
because we perceive almost No Vibrations even though
we are near to the Device
④ It is possible for draining and
Waterproofing Entirely without Polluting
because Drainage is only for Circulating Cooling Water

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Vitalization of Regional
Economy through Regional
Energy Supply

Change of
Environmental Friendly
Awareness by Region

Creation for Clean Streets
And Clear Regional Society
Environment

Name of Parts
Fuel Gas Storage Tank
Burner
Damper
Catalyst Reforming Column

Spiral Heat Exchanger

2EA

Noxious Gas
Neutralizing Tank

1EA

1EA

1EA

1EA

Cooling Tower

1EA

Fuel Heater

2EA

1EA

Nitrogen Generator

1EA

Overpressure Gas Tank

1EA

Gas Vein Pump

1EA

Naphtha Tank

1EA

Micro Pressure Gauge

Diesel Grade Storage Tank

1EA

Micro Thermometer

Gasoline Grade Storage Tank

1EA

Valves & Pipes

Collect Wax Column
Naphtha Separation Tank

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Relay Part
Maximum Load => 2.2 kw( Based on 1 Ton )
Average Electric Consumption => 1 ~ 2 kw / hr
Average Daily Operating Hours => 10 ~ 12 hours/day

Electricity is used to Operate Burner Pump & Lamp and to Measure the Gauge

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Relay Part

Main Control Panel

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Relay Part

Main Control Panel

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Relay Part

Main Control Panel

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Main Device Status

Indirect Heating Furnace & Burner

Indirect Heating Furnace & Burner

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Main Device Status

Melting Pyrolysis Reactor

Melting Pyrolysis Reactor
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Main Device Status
DUFJ

Various Tank

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Various Tank

Main Device Status
Power Start ON

Gas Collector ON

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Main Device Status

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Main Device Status

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Main Device Status

( Sight Glass )

Sight Glass

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Other Major Device

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Other Major Device

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Other Major Device

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Gas Compressor

Despite being compact in size and
light in weight vertical Air Cooled Oil Free
Reciprocating Compressor is as Highly
reliable as any industrial version used
in utility supply plants and the product
is used to Supply High Pressure Gas
as required by increasing and
the Pressure of a Low Pressure Gas
operation speed of Compressor
It should not operate at 820rpm or Higher
or at 200 rpm or Lower

Nitrogen Generator
Electricity
 Single Phase
 AC 220V
 50 / 60Hz

Specification
Flow 98% by the purity of the Nitrogen Generated( Nm3/hr )

Discharge Pressure of the Nitrogen Generated( kg/㎠g )
Inflow Air Volume( nm3/hr )
Inflow air Generated( kg/㎠g )
Voltage ( V, AC )
Frequency(Hz)

Number of Phase
Current( Ampere )
Discharge Port Diameter of the Nitrogen Generated( PT )

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Burner
Technical and Functional Features
•
•
•
•
•

Diesel Burner / Oil Burner, OFF GAS Incineration Burner
Single Stage Operation( ON / OFF )
Compatible with Any type of Combustion Chamber
High Pressure Mechanical Atomization of Fuel using Nozzle
Ability to Obtain Optimal Combustion Values by Regulating Combustion Air
and Blast Pipe
• Maintenance Facilitated by the fact that the Atomization unit can be removed
without having to remove the Burner from the Boiler
• Manual Air Flow Adjustment

Technical Data

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No.

ITEM

1

Inner Volume

2

Name of the Fluid to be used

3

Design

4

Opera
tion

5

UNIT

CONTENT

No.

1.0

1

Inner Volume

Air

M³

2
3

Design

4

Opera
tion

Mpa G

0.97

Temperature

℃

60

Pressure

Mpa G

0.88

Temperature

℃

AMB.

Inner Diameter of fuselage

mm

I.D 898.4 x 1264h

5

6

Corrosion Tolerance

mm

1.0

7

Radiation Inspection(S/H)

NO / N.A

8

Welding
Efficienc
y

9

Post Heat Treatment

10

Used
Materi
al

11

Permis
sible
Stress

Flat End Plate

%
%

UNIT

Name of the Fluid to be used

Pressure

Fuselage

ITEM

NO

Fuselage and Flat End Plate

SS400

Anchor Bolt

0.97

Temperature

℃

60

Pressure

Mpa G

0.882

Temperature

℃

AMB.

Inner Diameter of fuselage

mm

I.D 1130 x 1584h

6

Corrosion Tolerance

mm

1.0

7

Radiation Inspection(S/H)

8

Welding
Efficienc
y

9

Post Heat Treatment

10

Used
Materi
al

SS400

Fuselage and Flat End Plate

N/㎟

100

Support

N/㎟

100

Anchor Bolt

N/㎟

Air
Mpa G

SS400

Support

2.0

Pressure

70
85

M³

CONTENT

61

11

Permis
sible
Stress

NO / N.A

Fuselage

%

70

Flat End Plate

%

85
NO

Fuselage and Flat End Plate

SS400

Support

SS400

Anchor Bolt

SS400

Fuselage and Flat End Plate

N/㎟

100

Support

N/㎟

100

Anchor Bolt

N/㎟

61

12

Water-Pressure Test Pressure

Mpa G

1.261

12

Water-Pressure Test Pressure

Mpa G

1.261

13

Wind Load/Earthquake Load

㎧

45/ZONE 2A(1.15)

13

Wind Load/Earthquake Load

㎧

45/ZONE 2A(1.15)

Kg

383

In installation

Kg

739

14

Weigh
t

14

Weigh
t

In operation

Kg

739

In Water-Pressure

Kg

2794

In installation

Kg

383

In Water-Pressure
15

In operation

Kg

1393

Installation Place

OUTDOOR

15

Installation Place

OUTDOOR

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Patent Status

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Certificate of
Test for
Pyrolysis Oil

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Thanks So Much to You
New Technology by Ecocreation Industries
keeps running forward for more Clear and Cleaner World

ADITYA RECYCLING
Bangalore
www.adityahitechmachines.com

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Waste Plastic to Oil

  • 1. Green Energy creator Pyrolysis Machine Converting Waste Plastic into Oil ADITYA RECYCLING Bangalore www.adityahitechmachines.com Green Energy Leader
  • 2. Green Energy creator The Project Converting Waste Plastics into Oil Model => Batch Type ECP-2011 ADITYA RECYCLING Bangalore www.adityahitechmachines.com Green Energy Leader
  • 3. Green Energy creator The Value of Business! Depletion of Fossil Energy Intensified Regulation of Greenhouse Gas Emissions Rapid Increase of the need to Improve Nvironmental Pollution Protection of the Earth, the Nation, the Environment Creation of New Energy The plan to Overcome New Regulations High efficiency (average80%) High quality (light oil level) Green Energy Leader
  • 4. Green Energy creator Alternatives for the Future! Bio Energy Solar Energy Wind Power Generation Energy Nuclear Energy Green Energy Leader
  • 5. Green Energy creator Creation of Renewable energy! Vinyl Waste Waste Fishing Net, Fishing Gear Cracked Oil from Household Waste Vinyl Used Waste Lubricating Oil Wasted Tires Cracked Oil from Wasted Tire Green Energy Leader
  • 6. Green Energy creator The Relative Value of Oil Conversion Projects # TOE : Tonnage of Oil Equivalent Refinery Equipment Green Energy Leader
  • 7. Green Energy creator Use and Value of Produced Oil from Pyrolysis Waste Plastics, Waste Oil Conversion to Fuel Oil Green Energy Leader
  • 8. Green Energy creator Leader of environment-friendly technology, Ecocreation !! Ecocreation is an environment-friendly company that cares about future environment of the earth and is a global leading company that opens a new era of low carbon green growth by reducing CO2 emission for invigoration of resource circulation and prevention of global warming through production of environment-friendly products. Simple Process, Low Investment The Best Stability, Safety The Best Oil Conversion Profitability Green Energy Leader
  • 9. Green Energy creator Hybrid Cracking Emulsion Technology Nitrogen, Atmospheric Pressure Condition Pyrolysis Emulsion ( 380~480℃ Heating Fluid ) Reforming R.P.F( Solid Polymer ) Reforming Waste Plastic PP(Poly-Propylene), PE( Poly-Ethylene ) 폐기물 PS(Poly-Styrene), PPT( Polyphenylene Terephthalate ) Pyrolysis Refined Oil Apply liquefaction, Separation TTechnology Based Catalyst Oil Typical yields : Polymer Waste Kerosene, Diesel more than 80%, Naphtha around 15%, Gas around 3%, CHAR (Coke) around 3% Green Energy Leader
  • 10. Green Energy creator Plant Size by 12,000mm(W) X 10,000(L) X 7,000(H) Space required for installation => Variable for capacities Notice => Waterproof / Protection against wind must in roof Period required for installation by within 10 days site installation Process The first pyrolysis of waste and secondary catalytic cracking with catalyst Operation Type Batch type Input Plastics PP, PE, PS Yield Approx. 75 ~ 80 % (It can be different according to the waste plastics type) Electric Capacity Three-Phases (220V or 380V) Produced Oil Component Naphtha, Kerosene & Diesel Fraction Operating Cost Low operating cost due to the use of recycled oil and waste gas from self production Safety Less risk of explosion and fire due to nitrogen substitution It is not necessary to separate, shred and clean the waste plastics. Green Energy Leader
  • 11. Green Energy creator Power Start ON Gas Collector ON Green Energy Leader
  • 12. Green Energy creator The Main Process Flow Diagram 1 Input (Waste Plastic) (Refining/Storage) (Compress) (Separation/Cooling) (Compressed Stuff) (Contact Catalytic Reforming Cracking) (Pyrolysis) Green Energy Leader
  • 13. Green Energy creator Molten Material, Process Flow Diagram 2 Pressing Heat Supply Air emissions Reactor , Process fuel Environmental Process Dust Collection, Adsorption of odor Material Screening Compression Input liquid cracking catalyst Utilization of Process fuel Vapor catalytic cracking catalyst column The primary classification, NAPTHA, GAS input Material and Melting Primary fusion decomposition Catalyst Column secondary catalytic cracking Primary classification process Primary cooling process Decomposition of chlorine compounds, Input inhibitory catalyst Secondary Classification Input coking inhibitor Storage / Ship Secondary classification NAPTHA, GAS Input GUM inhibitor, Neutralization reagent Green Energy Leader
  • 14. Green Energy creator Process Chamber Placement Pictures Machine under manufacturing (Currently available daily capacity by 1 ton, 2 tons and 3 tons) Green Energy Leader
  • 15. Green Energy creator 1. Production Process Section System Configuration / Characteristics Remarks Heating Furnace( Heater ) Indirectly Heated => Combustion Gas Transfer Heat to the Reactor High Efficiency => Utilize Waste Gas, Apply Waste Heat Recovery System Automation => Autoignition, Automatic Temperature Control Burner System Safety / Cooling => Explosion Prevention, Forced Quick Exhaust Cooling Using Liquid Gas Fuel( Option ) Pyrolysis Reactor Completed the iIspection of B.T. Special Material of Explosion Proof, Anti-Corrosion( SUS ) High Efficiency Catalyst Layer Built-In, External Apply Coking prevention Technology Apply Anti-Corrosion( H2S / HCl ) Technology Pyrolysis Reactor Splitter / Condenser Apply Splitter, Condenser Integrated Structure Facility Adoption of 3( Three-Phase )( Solid,Gaseous,Liquid) Fractionator Heat Exchanger Application System ofAanti-Corrosion Material and Neutralizing Agent Green Energy Leader
  • 16. Green Energy creator 2. Process Support Section System Configuration / Method Option Cooling Equipment System Apply Water-Cooling Type Cooling System => Apply Cooling Water anti-Corrosion System => Apply Cooling Water Scale Prevention System Cooling Air-Cooled Furnace => Apply Cooling Heating Medium Reactor by Cooling Heat Recovery Separate Chemical Nitrogen Injection Safety System Nitrogen Injection Around Process Operation => For Cooling => The Inhibition of Oxidization => Self-Nitrogen Generator can be Adopted Anti-Corrosion Chemical Injection System Apply Special Corrosion Inhibitor ( Apply to the Target of Process Cooling Classification System ) => Prevention of Hydrochloric Acid Corrosion => Prevention of Organic Acid Corrosion Heat Recovery System Recovery Utilization of Exhaust Waste Heat from Heating Furnace Chimney => Recycling of OFF Gas by Economizer System => Separate Heating Furnace by Operate Reactor Option Equipment Green Energy Leader
  • 17. Green Energy creator 3. Safety and Environmental Equipment Section System Configuration / Method Remarks Reactor Explosion Proof Safety System Satisfy National Safety Standards Material & Facility Required Government Agencies Verify Adopt Pressure Relief System in an Emergency Adopt National Standard Explosion Proof Equipment Explosion Proof Electrical System Apply Pipe interlocking Device Against Vibration Apply Reactor Interlocking Device Emergency Response System in case of Power Failure Apply Emergency Private Power Station System Apply Process Generated Gas Continuous Processing System Incineration of OFF-Gas Apply Flare Stack Option of Small Diesel Generator Oil Spill Response System Apply Preparing Process for Oil Spill Loss Prevention System => Compliance with Government Standard Precipitator Deodorizing Adsorption Removal Post Processing of Emission Combustion Gas from Incinerator by Heating Furnace => Precipitator, Odor Adsorption Column => Precautionary Investment Prepared for Emergency Process Waste Treatment System Solid Waste Consignment Process for General Landfill Development of a Separate Solid and Sale Facility more than 3 Tons Green Energy Leader
  • 18. Green Energy creator Characteristic of our Development Process Section Our Company Process Material Separation Polymer Resin of PP, PE, PS, ABS, etc Complex of Single Substance or Mixture Other Company Process Solid Waste RPF Process Characteristic Remarks Excellent Yield => Kerosene, Diesel Grade Excellent Separation Process High Quality Oil Production => Minimize of Wax Component => Excellent Low Temperature Fluidity In the case of Catalytic Cracking of Mixture, the Process Efficiency of Solid Liquid Mixtures Is Twice. Low yield => The Yield of Naphtha is about 60% at least Fixed Separation Decline Low Quality Oil Production => Contain Large Amounts of Wax Very Poor Low Temperature Fluidity Process Operating Time Is Long Cause Energy Mass Consumption form or Product Quality Becomes Degraded It is inevitable that Light Naphtha Occurs in Bulk because of Reflux reaction to Reduce Wax Green Energy Leader
  • 19. Green Energy creator Characteristic of our Development Process Section Process Operating Condition Relative Comparison of Operating Hour ( Based 5 Tons Reactor) Our Company Process Normal Pressure Indirect Heating Type => 380~480℃ => Normal Pressure 0.5 Kgf ( Gassing Pressure Standard ) In case of Solid Liquid Mixture Process Around 10 hours ( Shorten Operating Hour ) Other Company Process Normal Pressure High Pressure Indirect Heating Type => 400~500℃ In case of Solid Single Material Process => 20 hours => Prolonged Operating Hours According to Reflux Reaction Normal Pressure High Pressure Indirect Heating Type 450~700℃ In case of Solid Single Material Process 15 hours Main Products Boiling Point Range 130~385℃ of Fuel Oil and Similar to Kerosene and Diesel Fuel Oil Containing Large Amounts of Waste Naphtha, Gas and Wax => Room Temperature Low Temperature Fluidity is very Bad because of Wax Containing Green Energy Leader
  • 20. Green Energy creator Characteristic of our Development Process Section Our Company Process Reactor Horizontal STOP Reactor Semi Automatic Medium Sized Reactor Other Company Process Rotary Fluid Reactor Process Characteristics Remarks It is possible to Input more than 80% of the Material => Equipped with Catalyst Column Remove Wax and Foreign Material Apply Technology => Apply self Development Isomerization Catalyst => Excellent Thermal Efficiency => Coking Prevention and Easy Operation Management Isomerization Catalyst As the Catalyst which Changes the Structure of Paraffin with It Changes the Structure of Wax and Makes It very good Fluidity Material Limited less than 50% of Raw Material Charging Quantity by Based on Liquid Law Material => Thermal Efficiency is Disadvantage Heat Loss is Great => Coking Management is Difficult => Front Coking Phenomenon Occurs At 360°C => Concern about Mechanical Durability Problems According to Reactor Fluid Green Energy Leader
  • 21. Green Energy creator Our Competitive Technology Process Risk Reactor Coking Distiller Tube Clogged (Wax / Saponification substance) Other Company Existing Technology Extended Maintenance time => Heat Transfer Decline => No Chemicals to Remove Impurities Occur Wax Occurs Frequently Piping Blockage Applied Independently Developed Inhibitors for Impurities Occur => Expected Patent Application => Wax Cracking Catalyst Development => Expected Patent Application Dramatically Improve Fuel Quality Remarks Independently Developed Application of Anti Coking and so Expected a Patent Application Dramatically Improved Process Poor Quality in Winter Product Quality Degradation Caused by Wax Product Quality Degradation due to Facility Hydrochloric Acid Corrosionby PVC and Salt Our Technology Exposure to Corrosive Hydrochloric Acid, Difficult for Screening Material -Shorten Equipment Life -VCM Monomer Occurs and Fuel Quality Degradation As the Highest Level of Technology at Home and Abroad, No other Companies Commercial Pracactes -Applied VCM Monomer Dechlorination Catalyst Development ( Expected Patent Application) -Suppress Interference Reaction by Salt (The same patented item) Green Energy Leader
  • 22. Green Energy creator Our Competitive Technology  Select Fuel Additive Based On the Same Refineries  Applied Technology => Fully Improved Combustion Efficiency => Other Functionality  Possible to Provide Leading High  Performance Reforming Catalyst  Facilities due to having Independent Catalyst Development Efforts  Engineering Technique => Contribute to Improving Future Productivity ► Profitability Green Energy Leader
  • 23. Green Energy creator Pyrolysis Yield according to Material Material Section Pure PE, PP, PS Standard => Except of PVC Pyrolysis Yield • Gas => 2~3% • Naphtha => Around 15% • Kerosene & Diesel Fuel => More than 80% • Coke( ASH ) => Below 1~3% Remarks • Distillation Appearance ( Boiling Point ) => 130 ℃ ~ 385℃ => In the case of RPF => Yield Change Depending on the Foreign Content Green Energy Leader
  • 24. Green Energy creator Our Technical Characteristics The Best Catalyst Control Technology of the World Liquid Catalytic Cracking, Vapor Catalytic Cracking, Decomposition of Chlorine Compounds, Neutralization Catalyst Technology, Apply Suppression Technology of Wax, Gum, Coking Secured Economic Minimize Investment Secured Stability Cost of Equipment Superior Economic Compared to other Company Gas uses Its Own Fuel Maximize the Stability of Pyrolysis Furnace due to the Secure of Low Pyrolysis Temperature Decomposition of Chlorine Compounds Input Neutralization Catalyst Minimize the Occurrence of Chlorine Gas Causing Equipment Corrosion to Adoption of Anti-Corrosion Minimize Simplify Production Process Facility to Minimize Minimize Operation Cost Maximize Thermal efficiency of Approx. 8 % No limited material is Single Operation of High Molecule and Waste Oil Maximize Profitability HDPE Standard Diesel Level can be Produced more than 75% of Pyrolysis Oil Minimize 2nd Waste Material => Dangerous Substances like Gas, Naphtha, etc => Generated Gas and Naphtha are used for its Own Fuel. Minimize Disposal Dangerous Material Stability due to Low temperature Pyrolysis Stable Operation due to Minimize the Occurrence of Wax and Regular Maintenance and Stable Shut down in case of Abnormal Condition and Easy Process Maintenance Facility Stability Operation Stability Green Energy Leader
  • 25. Green Energy creator Our Process Operating Characteristics - Case 2  Material => Waste Plastics 100%( RPF RDF, Recycling Chip )  Operating Hour is Variable Depending on the Characteristics of Materials => Operating Hour is Very Variable Depending on Foreign Content and Content of the Pure Polymer  It is very General to Operate One Time a Day ( Normal Operating 12 hours ) => In the case of much Foreign Content => ASH Removal Time Occurs by Increasing after Reaction  Recommended Maximum One Time a Day Green Energy Leader
  • 26. Green Energy creator Comparison of Produced Oil based on our Technology RPF PYROYSIS OIL @ ASTM D86 당사 개질 RDF 촉매 기존 상용 촉매 Green Energy Leader
  • 27. Green Energy creator Hybrid Cracking Process Product Quality Classification (Red is Standard) Diesel (Oil Company’s Diesel) Flash Point(℃) Above 40 (Above 30℃ of Pyrolysis Oil ) Pour Point(℃) Below 0(Apr. ~ Sep.), Below -17.5 (Oct. ~ Mar.) Waste Lubricating Oil Cracking Oil (NO Catalyst) Our Pyrolysis Oil of Waste Plastics 30~60 : Variable According to Process -30 -10 Residual Carbon, Wt% Below 0.15 0.17 0.05 ASH, Wt% Below 0.05 0.001 0.001 Distillation 90%, ℃ Below 360 395 350 2.0~5.8 5.2 2 SULFUR, Wt% Below 0.2 0.08 0.005 Moisture & Precipitate, VOL% Below 0.5 0.07 0.05 Cetane index Above 45 - 40~55 Lubricative, HRRR W.S.D 400 MAX Red Orange B&C 300 Above 0.815~below 0.855 0.82~0.84 Pb Below 1 ppm None None Cr Below 1 ppm None None Cd) Below 1 ppm None None As) Below 1 ppm None None Centistoke @ 40℃, cSt @15℃ DENSITY, g/㎤ Contents of Heavy Metals 0.79~0.81 Green Energy Leader
  • 28. Green Energy creator Technology Outline( Catalyst Performance ) Minimize of Heavy Oil Fraction Maximize of Kerosene & Diesel Grade Green Energy Leader
  • 29. Green Energy creator High Molecule PP,PE,PVC Decomposition & isomerization , Reaction of dechlorination Pour point Below -25℃ Becomes High Quality Fuel Green Energy Leader
  • 30. Green Energy creator Technology Outline Infrared Analysis of Kerosene & Diesel at General Gas Station High Quality Hydrocarbon High Quality Hydrocarbon Aromatics Green Energy Leader
  • 31. Green Energy creator Technology Outline Infrared Analysis Comparison of Our Catalyst Pyrolysis Oil High Quality Hydrocarbon HDPE 촉매 분해유 FT-IR CHART Hydrocarbon Double Bond Substance High Quality Hydrocarbon Aromatics Fully meets as Petroleum fuel based on Analysis of the chemical structure Green Energy Leader
  • 32. Green Energy creator Infrared Analysis Comparison of R.P.F Catalyst Cracking Oil RPF(PE ,PS 등) 촉매 분해유 FT-IR CHART Hydro Carbon Aromatic High Quality Hydro Carbon Hydro Carbon Double Bond Substance High Quality Hydro Carbon Unrefined Moisture Plasticizer Line C-O Combination Fully meets as petroleum fuel based on analysis of the chemical structure Green Energy Leader
  • 33. Green Energy creator Economic Evaluation of Refined Oil Production Raw Material => Waste Plastic / RPF 100% Handling Throughput => 3 Tons / day X 20days / Month Operation Leased Plant Standard Output => Gross 75% Recovery Rate /2500 Liter( Reflected by a Reduction in Fuel use Itself ) Green Energy Leader
  • 34. Green Energy creator Economic Evaluation of Refined Oil Production Standard Price => Selling Price of Gas Station Jan. 2012 Reasonable Price Range (Based Kerosene KRW 1400) Green Energy Leader
  • 35. Green Energy creator [ The Purpose of Emulsified Recycle Business ] 1. Reduce Emission Amount of Co2 { Reduce by Approx. ¼ Compared to Incineration Treatment } 2. Reduce Incineration Treatment or Reclaiming Disposal Cost 3. Create a New Business and Profit by Selling Recycled Oil 4. Thorough Information Management of Wastes [ The Purpose of Product ] ▶ Fuel for Diesel => Industrial fuel, Agricultural Boiler, Incinerator, Diesel engine generator, Vessel& heavy machinery fuel, etc ▶ Residue is Available as a Heating Fuel for Cement Furnace Fuel, Heating Fuel of Iron Works and Foundry{ Cokes 4500Kcal } [ Recommend Type of Business ] Main Agent of Administration( City ) Recycling Resources Enterprise => Recycle Center, Plastics Recycling Resources Enterprise, Mineral Resources Enterprise Waste Disposal Enterprise => General Waste, Industrial Waste, Agricultural Waste Plastics Industry Product processing industry, Film printing industry Chemical Industry Polymer Ingredient Manufacturing Industry Chemicals Industry Green Energy Leader
  • 36. Green Energy creator Q&A about Catalytic Cracker of Waste Plastics Q.1. What is the Characteristic of this Device? A ① Low Operation Cost due to Pyrolysis using the Fuel of Recycled Oil and Waste Gas. ② This Device Realized Low Cost Compared to Former Emulsification Device Q.2. What is the Processing Capacity of this Device? A ① Processing Capacity => 1.000kg, 2.000kg, 3.000kg, 4.000kg, 5.000kg / Day Q.3. What is the Processing Progress of this Device? A ① Input a Batch of Waste Plastics in the Preprocessing Stage. ② Heat the Raw Materials of Waste Plastics and Gasify Inside a Furnace. ③ Obtained Cracked Gas is Reformed into Gasoline Grade and Diesel Grade by a Catalyst Column and save in each Cracked Oil Tank Q.4. What is different from General Method until now? A ① Existing Emulsification Device Safety Matter Operation Cost and our Emulsification device needs a Gaseous Reforming Catalyst and there is No Risks of Explosion and Fire because of using Nitrogen and Low Operation Cost by using the Fuel of our Own Produced Recycled Oil and Gas Green Energy Leader
  • 37. Green Energy creator Q&A about Catalytic Cracker of Waste Plastics Q.5. What is the Influence on Safety and Environment? A ① Block the Emission of Harmful Gas with the Installation of Gas Washer and Storage Tank ② Not necessary of Measures and like a Silencer and etc Specially even though there are Operation Sounds like Motor Sounds and Cooling Pump Sounds, etc ③ Not necessary of Measures because we perceive almost No Vibrations even though we are near to the Device ④ It is possible for draining and Waterproofing Entirely without Polluting because Drainage is only for Circulating Cooling Water Green Energy Leader
  • 38. Green Energy creator Vitalization of Regional Economy through Regional Energy Supply Change of Environmental Friendly Awareness by Region Creation for Clean Streets And Clear Regional Society Environment Name of Parts Fuel Gas Storage Tank Burner Damper Catalyst Reforming Column Spiral Heat Exchanger 2EA Noxious Gas Neutralizing Tank 1EA 1EA 1EA 1EA Cooling Tower 1EA Fuel Heater 2EA 1EA Nitrogen Generator 1EA Overpressure Gas Tank 1EA Gas Vein Pump 1EA Naphtha Tank 1EA Micro Pressure Gauge Diesel Grade Storage Tank 1EA Micro Thermometer Gasoline Grade Storage Tank 1EA Valves & Pipes Collect Wax Column Naphtha Separation Tank Green Energy Leader
  • 39. Green Energy creator Relay Part Maximum Load => 2.2 kw( Based on 1 Ton ) Average Electric Consumption => 1 ~ 2 kw / hr Average Daily Operating Hours => 10 ~ 12 hours/day Electricity is used to Operate Burner Pump & Lamp and to Measure the Gauge Green Energy Leader
  • 40. Green Energy creator Relay Part Main Control Panel Green Energy Leader
  • 41. Green Energy creator Relay Part Main Control Panel Green Energy Leader
  • 42. Green Energy creator Relay Part Main Control Panel Green Energy Leader
  • 43. Green Energy creator Main Device Status Indirect Heating Furnace & Burner Indirect Heating Furnace & Burner Green Energy Leader
  • 44. Green Energy creator Main Device Status Melting Pyrolysis Reactor Melting Pyrolysis Reactor Green Energy Leader
  • 45. Green Energy creator Main Device Status DUFJ Various Tank Green Energy Leader
  • 46. Green Energy creator Various Tank Main Device Status Power Start ON Gas Collector ON Green Energy Leader
  • 47. Green Energy creator Main Device Status Green Energy Leader
  • 48. Green Energy creator Main Device Status Green Energy Leader
  • 49. Green Energy creator Main Device Status ( Sight Glass ) Sight Glass Green Energy Leader
  • 50. Green Energy creator Other Major Device Green Energy Leader
  • 51. Green Energy creator Other Major Device Green Energy Leader
  • 52. Green Energy creator Other Major Device Green Energy Leader
  • 53. Green Energy creator Gas Compressor Despite being compact in size and light in weight vertical Air Cooled Oil Free Reciprocating Compressor is as Highly reliable as any industrial version used in utility supply plants and the product is used to Supply High Pressure Gas as required by increasing and the Pressure of a Low Pressure Gas operation speed of Compressor It should not operate at 820rpm or Higher or at 200 rpm or Lower Nitrogen Generator Electricity  Single Phase  AC 220V  50 / 60Hz Specification Flow 98% by the purity of the Nitrogen Generated( Nm3/hr ) Discharge Pressure of the Nitrogen Generated( kg/㎠g ) Inflow Air Volume( nm3/hr ) Inflow air Generated( kg/㎠g ) Voltage ( V, AC ) Frequency(Hz) Number of Phase Current( Ampere ) Discharge Port Diameter of the Nitrogen Generated( PT ) Green Energy Leader
  • 54. Green Energy creator Burner Technical and Functional Features • • • • • Diesel Burner / Oil Burner, OFF GAS Incineration Burner Single Stage Operation( ON / OFF ) Compatible with Any type of Combustion Chamber High Pressure Mechanical Atomization of Fuel using Nozzle Ability to Obtain Optimal Combustion Values by Regulating Combustion Air and Blast Pipe • Maintenance Facilitated by the fact that the Atomization unit can be removed without having to remove the Burner from the Boiler • Manual Air Flow Adjustment Technical Data Green Energy Leader
  • 55. Green Energy creator No. ITEM 1 Inner Volume 2 Name of the Fluid to be used 3 Design 4 Opera tion 5 UNIT CONTENT No. 1.0 1 Inner Volume Air M³ 2 3 Design 4 Opera tion Mpa G 0.97 Temperature ℃ 60 Pressure Mpa G 0.88 Temperature ℃ AMB. Inner Diameter of fuselage mm I.D 898.4 x 1264h 5 6 Corrosion Tolerance mm 1.0 7 Radiation Inspection(S/H) NO / N.A 8 Welding Efficienc y 9 Post Heat Treatment 10 Used Materi al 11 Permis sible Stress Flat End Plate % % UNIT Name of the Fluid to be used Pressure Fuselage ITEM NO Fuselage and Flat End Plate SS400 Anchor Bolt 0.97 Temperature ℃ 60 Pressure Mpa G 0.882 Temperature ℃ AMB. Inner Diameter of fuselage mm I.D 1130 x 1584h 6 Corrosion Tolerance mm 1.0 7 Radiation Inspection(S/H) 8 Welding Efficienc y 9 Post Heat Treatment 10 Used Materi al SS400 Fuselage and Flat End Plate N/㎟ 100 Support N/㎟ 100 Anchor Bolt N/㎟ Air Mpa G SS400 Support 2.0 Pressure 70 85 M³ CONTENT 61 11 Permis sible Stress NO / N.A Fuselage % 70 Flat End Plate % 85 NO Fuselage and Flat End Plate SS400 Support SS400 Anchor Bolt SS400 Fuselage and Flat End Plate N/㎟ 100 Support N/㎟ 100 Anchor Bolt N/㎟ 61 12 Water-Pressure Test Pressure Mpa G 1.261 12 Water-Pressure Test Pressure Mpa G 1.261 13 Wind Load/Earthquake Load ㎧ 45/ZONE 2A(1.15) 13 Wind Load/Earthquake Load ㎧ 45/ZONE 2A(1.15) Kg 383 In installation Kg 739 14 Weigh t 14 Weigh t In operation Kg 739 In Water-Pressure Kg 2794 In installation Kg 383 In Water-Pressure 15 In operation Kg 1393 Installation Place OUTDOOR 15 Installation Place OUTDOOR Green Energy Leader
  • 56. Green Energy creator Patent Status Green Energy Leader
  • 57. Green Energy creator Certificate of Test for Pyrolysis Oil Green Energy Leader
  • 58. Green Energy creator Thanks So Much to You New Technology by Ecocreation Industries keeps running forward for more Clear and Cleaner World ADITYA RECYCLING Bangalore www.adityahitechmachines.com Green Energy Leader