تارا فایل

پاورپوینت انگلیسی اسلاید صنعت پتروشیمی




Shahid Bahonar University of Kerman
College of Science
Department of Chemistry

Title
Petrochemical industry

Author
A.mohammadi
M.khaje hasani

Supervisor
Z.rashidi ranjbar

October 2015

Development of Chemical industries

The end of 18th century The beginning of the chemical industry
reason
Saponification
Development factories
Textile
Everyday needs

Population growth

Industry

Car
Glass
Color
Petrochemical
Types of industry
.
.
.

Mother's Industries

Definition:

Comprehensive industries that are linked with a wide range of technologies.
Parts used are great.
…………..

as an example
Steel
Car
and etc

Petrochemical industry

1
Petrochemical Industries Development

After the First World War (1914)
The beginning of the petrochemical industry (1920)
The Second World War (1939)
Modern times

After the First World War (1914)

1. Machine Manufacturing Factories

2. The Unavailability of Petroleum Products

Thermal Cracking

Thermal Cracking

Heavy oil production lighter products
Production propylene

The beginning of the petrochemical industry (1920)

American
First Petroleum Company

Problem
Aviation Fuel

Thermal Cracking
Catalytic Cracking
1. Production of high octane benzine
Results
propylene
2. unsaturated hydrocarbons
Butylene

The Second World War (1939)

The dramatic development

Rubber
Explosives
Medication
DDT

The development of the petrochemical industry

Oil companies 400th 80 million ton

Petrochemical Products

Fertilizers
Polymers
Pesticide
Detergents
Solvents
Foods
Pharmaceutical
Explosives

Crude oil sources

Salty water

Depth Earth

Gass
Depth 7000 m
Discovered reserves

Depth 15000 m

characteristics of crude petroleum
A. Physical properties
*Color
Heavy hydrocarbons

Light hydrocarbons

(Fluorescent green)

*smell
Sulfur oil
Disagreeable

Pennsylvania
Garlic

Texas
Camphor

Specific Gravity
*Lighter than water
*0.8 to 1 range

SG = W'V‘/WV
(A specified temperature 60 F )

W‘ =Weight Oil
V‘ = Volume Oil
W = Weight Water
V = Volume Water

American Petroleum Institute – Api

SG = 141.5 / (Api + 131.5)

Viscosity

*unit viscosity in system cgs
*unit viscosity in system british

1 C Poise = 2.42 B.V.U

Temperature
Viscosity
The amount of dissolved gas

0.6 to 600 range

Volatility

1. Light hydrocarbons

Before 250 C Distillation

2. Heavy hydrocarbons

After 250 C Distillation

B .Chemical Properties

*composition

Hydrocarbons

Pennsylvania %98

California %50

*Saturated hydrocarbons
CnH2n+2
Methane, Hexane,Ethane,Hexadecan
paraffin series

*Unsaturated hydrocarbons
CnH2n
Ethylene, propylene,Butylene
Olefin Ethylene series

*Unsaturated hydrocarbons
Cyclopropane,Cyclopantane
Naphthene series

*Aromatic hydrocarbons
C2Hn2-6
Aromatic Series

*Hydrocarbons diolefin
C2H2n-2
Diolefin series

*Hydrocarbons cyclic
C2H2n-4
C2H2n-6
.
.
.

Classification

paraffin series

Naphthene series
Oils

Intermediate

Paraffin Series

Saturated Hydrocarbons

To C4 Gas
C4 To C8 liquid
C8 To Up Solid

Pennsylvani & Poland

Naphthene series

CnH2n

Cyclopropane, Methylcyclopentane,Cyclohexane

Liquid

Venezuela, Caucasus

Oxygenated Compounds

Sulfur Compounds

Nitrogen Compounds

Metal salts> :PPm<
Iron, Lead, Nickel, Vanadium, Potassium
Gas:
Helium

Refining process

Natural Gas
Product oil well
Crude Oil Useless
Reasons
Volatile gases Explosion
Heavy oil Useless
Sulfur compounds Acid

Separation Devices

Distillation

Extraction

Absorption

Molecular sieves

Crystallization

Distillation of crude oil in refineries

Before distillation
Remove salts

MgCl + H2O MgClOH + HCl

Corrosion

Desalting of crude oil

Distiller
Two-phase
step one
Distillation at normal pressure

Separation of light weight components

Step two
Distillation at Vacuum

Separation of heavy weight components

Products

light – distillation

Intermediate – distillation

Heavy – distillation

light – distillation
Benzine
Specific Gravity < 0.8
Distillation < 150 ℃
Petroleum ether
Distillation again
Benzin super
*consisting of C₅ and C₆ hydrocarbons & boiling in the range 35‒60 ℃ & used as a laboratory solvent.

*Octane number 95

Intermediate – distillation

Kerosene
Gas oil
Specific Gravity 0.8 to 0.83 range
Distillation 150 – 250 ℃ range

Jet Fuel
Distillation again
Gas oil & Kerosene

Heavy – distillation

Mazote black oil
engine oil
Specific Gravity > 0.83
Distillation > 250 ℃

Remaining Primary distillation column

*Vacuum distillation & cracking lighter products

Vaccum – towers

Residius:

*Temperature 600 to 700 ℃ range
* Pressure 20 to 40 mmHg
Furnace
Vacuum tower
lighter products

*رسوخ فناوری نانو در صنعت نفت*

کاربرد نانو حسگرها برای جلوگیری از زمین لرزه در حفر چاه های نفت
کاربرد نانو سنسورها در حفر چاه های نفت
کاربرد نانوساختارها، نانوکامپوزیت ها، نانولوله های کربنی در ساخت مته حفاری
کاربرد نانو افزودنی ها برای افزایش توان هیدرولیکی پمپ ها و تحکیم جداره چاه نفت
کاربرد نانو کاتالیست ها برای تولید محصولات نفتی سبک
کاربرد نانو عایق ها برای جلوگیری از خوردگی و ….

Thanks


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