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SLMAC(SHORT PATH DISTILLATION)
WASTE & USED LUBE OIL REFINING
PROCESS ALMOST ZERO CLAY
TECHNOLOGY
ABOUT US
Arslan Enginery™ Private Limited Company is an esteemed company based in India. We offer
technical solutions and projects related primarily to hydrocarbon processing. We are engaged
in setting up Turn Key projects overseas, Designing, Engineering & Supply and Installation &
Commissioning of trouble free projects. We wish to create a pollution minimized atmosphere
by following our mission of protecting the nature with innovative ideas for Recycling Waste
Lube Oil, Petroleum Jelly plants, Blending plants, and Diesel plants.
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Arslan Enginery™ offers tailor made designs & technology. Our Turnkey project provisions
include:
Engineering
Procurement
Commissioning
Our Plant Design Team is working on latest 3D base software to develop the best plant
and project for much higher quality experience.
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SLMAC
WASTE/USED LUBE OIL REFINING PROCESS
ZERO CLAY TECHNOLOGY
(DE METALIZE + DE ASH + DE CARBON)
SLMAC is an indigenous used lube oil products. Some of its astute characteristics are:
• SLMAC uses No Hazardous or Banned chemicals.
• SLMAC removes Halogens, heavy metals, Sulfur and oxidized products and bring them
within permissible limits.
• SLMAC yields high quality base stock with better Color and Oxidation Stability with
ALMOST ZERO CLAY.
• SLMAC Save Complete process Energy Consumption by 30%, as compared to other
Processes.
• SLMAC Prevents equipment fouling, corrosion, and coking of process equipment such
as heat exchangers and vacuum system.
• SLMAC process separates bottom from feedstock which can be used as asphalt
extender, rubber process oil, base for black printing ink, axle grease manufacturing
and as rust proofing compound.
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WASTE LUBE OIL
(WLO)
Lube oil is a fraction of crude oil distillate which is generally taken for granted by us. But,
vehicle numbers are at a high and are still rocketing.
The Lube Oil’s quality during its tenure is deterred mainly by contaminants such as
Cotton Waste, Bolt, Nuts, metals (in ppm), free and emulsified water. These contaminants
in the used lube oil may be treated and converted to a cleaner and usable form by not
involving any chemical treatment via our method.
Various Sources of Used Oil Include:
Car & locomotive Gear boxes and engines.
Generators.
Hydraulic cylinders of Heavy & Light machinery.
Electrical Transformers.
Any Lube oil application machinery of industry.
Chief oil contaminants may be categorized under various headings such as:
o COMBUSTION PRODUCTS
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WATER SOOT AND CARBON
LEAD
FUEL
o ABRASIVES
ROAD DUST
WEAR METALS
o CHEMICAL PRODUCTS
OXIDATION PRODUCTS
DEPLETED ADDITIVE REMNANTS
WASTE LUBE OIL (WLO) CHARACTERISTICS
SR. NO. PARAMETER MAXIMUM PERMISSIBLE LIMIT
1 Color 8 Hazen Units
2 Water 5 to 15 %
3 Density 0.85 to 0.95
4 Kinematic Viscosity CST at 100 °C 10 to 32
5 Dilutents 15% by volume
6 Neutralization Number 3.5 mg KOH/grams
7 Saponification Value 18 mg KOH/grams
8 Total Halogens 4000 ppm
9 Polychlorinated Biphenyls (PCB’s) Below Detection Limit
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10 Lead 100 ppm
11 Arsenic 5 ppm
12 Cadmium + Chromium + Nickel 500 ppm
13 Polyaromatic Hydrocarbons 6 %
SPECIFICATION OF USED OIL IDEAL FOR DMAC RE - REFINING
SR.NO. PARAMETERS MAX PERMISSIBLE LIMIT
1. COLOUR 8 hazen units.
2. Water 3-5% max.
3. Density 0.85 to 0.92
4. Kinematic viscosity CST at 100° Celsius 10 To 32
5. Diluents ( additives) 15% by vol
6. Neutralization Number 3.5 mg KOH/grams.
7. Saponification value 18 mg KOH/grams.
8. Total halogens 4000 PPM
9. Polychlorinated biphenyls (PCB’s) Below detection limits.
10. Lead 100 PPM
11. Arsenic 5 PPM
12. Cadmium+chromium+ Nickle 500 PPM
13. Polyaromatics Hydrocarbons (PAH) 6%
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SCHEMATICS AND
PROCESS FLOW DIAGRAMS
a. PROCESS PROFILE
A proposal for processing used lube oil, mineral oils and industrial oils, using high vacuum molecular distillation technology is presented here.
The various steps involved in the projects are given below:
Step # 1: The used & mineral oils are pre-treated with two types of polymer, which will flocculate the carbon sludge substantially
and separated by centrifuging/filtering Step#2: The used & mineral oil from the previous step is passed through
phase separators, coalescer filters to remove free and emulsified water.
Step# 3: These used and mineral oils are passed through a thin film
evaporator, under medium vacuum and temperature, to
remove, diesel, dissolved water if any and some lighter fractions
Step# 4: The undistilled used and mineral oils are passed through a molecular distillation Plant, under higher vacuum and temperature, to distill off lighter oil (approximately equal to SAE
20 in viscosity).
Step#5: The undistilled used and mineral oils subjected to high vacuum, high temperature in an induction heated molecular distillation plant. The distilled oil will have a viscosity of about SAE 40 at
ambient.
Step #6: The distilled oils are bleached with very less quantity of active
clay to get very light colored base oils, to be blended with
additives to get finished oils for the automotive and industrial
applications.
Step# 7: The final residue is semi solid at ambient and can be processed
for manufacturing asphalt or briquettes, finished to make off-
speck heavy fuel oil or to make greases for slow moving
machineries.
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Step# 8: The used clay can be reclaimed, re-activated 3-4 times, by using solvent extraction and high temperature activation
process. The entire project can be installed in 6 modular structures and
capacities of the plant can be increased later by adding modules
b. PROCESS DISCRIPTIONS
The following process stage has to be followed to obtain quality base oil as per ministry of
petroleum and environments:
1) Pre-treatment: Stripping, Centrifuging
2) Decantation & Dehydration
3) Thin film molecular distillation using high vacuum
4) Bleaching & Neutralization
5) Filtration
6) Blending
7) Waste water treatment plant & Oxidizer to re-use waste & to become
environment friendly.
1) Pre-treatment:
The used Lubricating oils usually contains aromatics,Carbons,heavy particals gets
settle,steam stripped & the filtered & clarified using centrifuge.
2) Decantation & Dehydration:
The used Lubricating oils usually contains aromatics etc., and free water which can be
separated by way of decantation and heating at high temperature to remove emulsified
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water and gas oil i.e., mixed lighter fractionators fuel oils under vacuum heated by thermic
fluid heater.
3) Thin film molecular distillation:
After decantation and dehydration the used oil will be transferred for high vacuum
distillation and taken the distillate out as a distilled oil. And residue will be separated -
stored & supplied for further use.
4) Bleaching & Neutralization:
After distillation, the treated oil may need very les quantity i.e. not more than 2% activated
fuller’s earth by volume and it has to be neutralized before taking in for blending of various
grade of lubricants. For filtration the spent clay which has been added for neutralization has
to be removed through plate and frame filter press as well as centrifuge and thus we
obtained the base oil for blending.
5) Blending:
The base oil has to be degraded for application of industrial lubricating oil after adding required additives.
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FLOW DIAGRAMS: 1.PRETREATMENT SECTION:
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2.DEHYDRATION SECTION:
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3.WIPED FILM EVAPORATORSECTION:
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4.BLEACHING & NEUTRALIZATION SECTION:
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5.WASTE WATER TREATMENT PLANT –
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6.THERMAL EXHAUST & AIR POLLUTION CONTROL SYSTEM
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POSSIBLE RCOVERIES FROM USED OIL
COMPONENT PERCENTAGE (%)
Water & VOC 5
Diesel (Fuel) 7
Losses 1
Asphalt 15
SN 150 15
SN 500 57
Total 100
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OVERALL MASS BALANCE
LIST OF EQUIPMENT IN THE
SCOPE OF ARSLAN ENGINERY (INDIVIDUAL PROCESSES)
PRE TREATMENT AND DEHYDRATION
SR. NO.
DESCRIPTION QTY (*)
1 USED LUBE OIL TRANSFER TO PHE PUMP (CENTRIFUGAL PUMP)
2 PLATE HEAT EXCHANGER
3 PURIFIER (WITH MOTOR)
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4 PURIFIED OIL TRANSFER PUMP
5 DMAC OIL PROCESSING KETTLE
6 DMAC OIL TRANSFER TO DMAC OIL SETTLING TANKS
7 DEMAC DEHYDRATION CONDENSOR
8 DMAC RECEIVER
9 DMAC RECEIVED OIL TRANSFER TO MIXING TANK
10 DMAC RECEIVED WATER TRANSFER TO DRAIN LINE
11 GEAR BOX FOR DMAC KETTLES
12 MOTOR FOR DAMAC KETTLE
13 CLARIFIER (WITH MOTOR)
14 DMAC OIL TRANSFER FROM STOARAGE TANKS TO CLARIFIER
15 MECHANICAL BOOSTER
16 DRY VACUUM PUMP
17 CHILLER
18 OIL ENTRAP SECTION
19 OIL POT
20 HEAT EXCHANGER
21 DISTILLATION/FRACTIONATION TOWER
22 USED LUBE OIL TRANSFER TO PHE PUMP ( CENTRIFUGAL PUMP )
23 DISTILLATION CONDENSOR
24 LIGHT BASE OIL RECEIVER
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25 LIGHT BASE OIL TRANSFER TO SLUDGE MIXING TANK
(CENTRIFUGAL PUMP )
26 DISTILLATE OIL TRANSFER TO FEED BUFFER TANK
(CENTRIFUGAL PUMP )
27 MECHANICAL BOOSTER
28 DRY VACUUM PUMP
29 CHILLER CONDENSOR
30 OIL ENTRAP SECTION
31 OIL POT
THIN FILM EVAPORATION
SR. NO. DESCRIPTION QTY (*)
1 FEED BUFFER TANK
2 WIPED FILM EVAPORATOR
3 PRIMARY CONDENSER
4 SECONDARY CONDENSER
5 WFE RESIDUE RECEIVER
6 RESIDUE TRANSFER PUMP
7 BASE OIL RECEIVER(SN 150,SN 300/500)
8 DISTILLED LUBE OIL TRANSFER TO PROCESS TANK
9 MULTIBAG POLISHING FILTER(5 Micron)
10 BASE OIL RECEIVER
11 ELECTRO STATIC TRAP
12 VAPOUR TRAP
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13 MECHANICAL BOOSTER
14 MECHANICAL BOOSTER
15 DRY VACUUM PUMP
16 CHILLER CONDENSOR
17 OIL ENTRAP SECTION
18 OIL POT
19 CHILLER PLANT FOR WFE
20 CHILLED WATER TRANSFER TO WFE SYSTEM
(CENTRIFUGAL PUMP )
21 CHILLER POT
22 VAPOUR TRAP
UTILITY SECTION
SR. NO. DESCRIPTION QTY (*)
1 CHILLER
2 COOLING TOWER
3 COOLING WATER RECIRCULATION (CENTRIFUGAL PUMP)
4 BOILER UNITS
5 EXPANTION TANK
6 DE-AERATION TANK
7 HOT OIL DRAIN TANK
8 THERMIC FLUID HEATER-295 DEGREES
9 THERMIC FLUID HEATER-320 DEGREES
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10 THERMAL EXHAUST OXIDIZER
11 FUEL OIL SERVICE TANK
12 CIRCULATION PUMP
13 FUEL PUMP
14 OIL FILTER
15 PUMP
16 STEAM GENERATOR
WASTE WATER TREATMENT
SR. NO. DESCRIPTION QTY (*)
1 OIL WATER SKIMMER
2 SKIMMED WATER TRANSFER TO MIXING TANK
(CENTRIFUGAL PUMP)
3 MIXING TANK
4 SETTLING TANK
5 FILTRER BED
6 FILTERED WATER TO MIXED BED (CENTRIFUGAL PUMP)
7 MIXED BED FILTER
8 WATER TRANSFER FROM MIXED BED TO CARBON FILTER
(CENTRIFUGAL PUMP)
9 CARBON FILTER
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LIST OF INSTRUMENTS
SR. NO. DESCRIPTION QTY (*)
1 CONTROL VALVE- MOTORISD
2 LEVEL INDICATOR
3 PRESSURE INDICATOR
4 TEMPERATURE INDICATOR
5 FLOW METER
6 LEVEL TRANSMITTERS
7 PRESSURE/VACUUM TRANSMITTERS
8 TEMPERATURE TRANSMITTERS
9 LEVEL SWITCHES
10 VACUUM SWITCHES
11 PLC CONTROL PANEL-AUTOMATION
12 SUB PANNEL
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SUMMARY OF UTILITIES CONSUMPTION
UTILITY UNIT
Electricity kW hr-1
Energy Required Kcal
Cooling/chilling Kcal
Steam LP Kg
Water m3
Aditive-ARSLAN 44 Kg
Water treatment chemicals
Kg
Hot Oil Mg
PRODUCT LIST
NAME
Volatile
Diesel
SN 150
SN 500
Residue
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ANNUAL TOTAL PRODUCT COST ESTIMATION
ITEM COST(*)
Raw Material
Operating Labor
Utilities
Maintenance & Repairs – ARSLAN ROYALTY
Cost of Finance
Total
TOTAL PROFIT ANNUALLY
RE – REFINED LUBE OIL FROM OUR ARSLAN ENGINERY™ - DMAC
PARAMETERS RE-REFINED
LIGHT (SN-70) RE-REFINED
LBO (SN-150) RE-REFINED
HBO (SN-500)
BOTTOM RESIDUE
(ASPHALT)
Density at 15° C 0.85-0.87 0.86-0.89 0.89-0.94 0.95-0.97
Viscosity 100° CST 2.5 – 3.5 5 - 6 11 - 12 30 - 32
Viscosity 40 C CST 10 - 14 30 - 34 90 - 105 180 – 200
Viscosity index 98 - 102 98 - 102 95 - 98 95 to 110
Color ASTM 0.5 – 1.5 1.5 – 2.5 2.5 to 3.5 8 hazel
Tan, mg KOH/gm 0.01 0.01 0.05 max 0.05 max
Flash Point COC >140 >180 >210 >300
Pour Point -4 C -4 C -6 C -
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Sulphur % wt 0.5 -1.0 0.7 – 1.2 1.0 – 1.5 1.5 – 1.6
Aniline Point 90 - 95 95 - 100 100 - 105 105 - 110
METALS (PPM)
METAL
Ba <2 <2
Ca <1 <1
Pb <2 <2
Zn <1 <1
Ph <5 <5
Cr <0.5 <0.5
Fe <0.5 <0.5
ENVIRONMENT FRIENDLY AND HAZARD FREE TECHNOLOGIES
Environmental impact has become a primary concern for all involved firms. Hence our process makes sure that all waste products have a minimal impact on the environment. Every byproduct of the process is dealt in the following manner:
• WASTE RESIDUAL OIL from the Vacuum Distillation – Asphalt which is 10 to 15% of the feed can be blended in to Heavy fuel oil, which
further can be combusted with specially designed fuel burners. – Asphalt can replace expensive Masticating Agents, such as Pine Tar in Various
Industrial Rubber Application. – Asphaltic residues with inherent Metals and Carbon can also be used in the form
of ‘Flap Oil’, for mixing with Rubber. – Asphaltic residues from our processes can also be used as an additive in tarmac,
applied for Road Building. • EXTERNAL WATER supply is not required. Any water generated during the distillation
process (1200 to 1500 lts) is reutilized in the cooling towers only or for gardening purposes.
• AIR EMISSIONS emitted by the vacuum system are also oxidized under controlled temperature and environment at 390°C before exhausting to the atmosphere. The other gases exhausted are in the form of combustion OF FUEL for heating , and thermal oxidization of VOC and are as per the following :
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APPROXIMATE COMPOSITION OF LUBE OIL
COMPONENT PERCENTAGE (%)
Water 6
VOC 2.3
Diesel (Fuel) 6
Losses 1.8
Asphalt 11.8
SN 150 32
SN 500 40.2
Total 100.1
OVERALL MASS BALANCE
FEED (RAW MAERIAL)
PRODUCT MASS FLOW
(kg hr-1) *
Waste Oil Volatile
Hydrogen Waste H2O
Steam Diesel
SN150
SN 500
Residue
Waste Gas
H2S in Amine Solution
Waste Water from
Steam Strip
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UTILITIES
UTILITY UNIT
Electricity kW hr-1
Energy Required Kcal
Steam LP Kg
Water m3
Catalyst Kg
Amine Solvent Kg
Hot Oil Mg
ANNUAL TOTAL PRODUCT COST ESTIMATION
ITEM COST (*)
Raw Material
Operating Labor
Operating Supervision
Utilities
Maintenance & Repairs
Laboratory Charges
Other (Advertisement & Logistics)
Total
TOTAL PROFIT ANNUALLY
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ADDITIONAL PROJECT POSSIBILITIES WITH RESPECT TO THE SAME COMPLEX
-The Term (*) Means that number (value) will be added depending on capacity of plant required.
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Some Images of Successfully Constructed Plants.
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ARSLAN ENGINERY Pvt.Ltd. Plot- 25/1, Additional-MIDC ,AMBERNATH Pin Numb-421501 MUMBAI,MAHARASHTRA- INDIA
Contact Number - +91-8983227333 , (Tel) +91-251-6555300 Email- [email protected] , [email protected]
Web - www.arslanenginery.com , www.indiamart.com/arslanenginery Skype – infoarslan