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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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Page 1: (SHORT PATH DISTILLATION) - f01.s.alicdn.comf01.s.alicdn.com/kf/UL8gPMKXaXcXXc_PVbXu.pdf · SLMAC (SHORT PATH DISTILLATION) WASTE & USED LUBE OIL REFINING PROCESS ALMOST ZERO CLAY

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