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Petrochemical feed stocks
Presented by:
Sarah Al-HoutyOhoud Al-Mutairy
Dlal Al-MoullaHessah Al-Ameer
Introduction
The basic petrochemical manufactured by :
1- Aromatics ( Benzene , toluene , xylene ,and ethyl benzene ) 2- Un saturates (Olefins ,Diolefins ) 3 – Saturates (Paraffin and cyclo paraffin )
Uses of Petrochemical: 1- Plastic production 2- Synthetic fibers 3- Rubber (SBR ) 4-Solvents 5- Polymers
Aromatics Production *Aromatics are obtained mainly from the catalytic reforming of heavy naphtha .
* Solvent liquid – liquid extraction method used to separate aromatics from anther hydrocarbons .
* Finally the aromatics are separated to produce ( Benzene , toluene , xylene which separated to m- o -p –xylenes , and ethyl benzene )
Solvent extraction of Aromatics :The points important for solvent
selection : 1- Good thermal stability . 2- Raid phase separation .3-Non corrosively . 4 - High capacity ( Solubility of Aromatic ) . 5- High selectivity for aromatics versus
non aromatics.
Solvent extraction of Aromatics :
There are Two major solvent that used to extract aromatics :
1 -Sulfolane .
2 -Ethylene glycol .
Comparison of Solvent Systems For Aromatics
Recovery
Extractive splitter
Extract recovery column
Extraction equipment
2-101.5Wash water wt%
1.442Relative Volatility
33S/L
Tetra-ethylene
Sulofane
General L-L extraction flow sheet
Solvent extraction of Aromatics :
Aromatics Separation :* Benzene and Toluene can be recovered from the extract product stream of the extraction unit by distillation.
* The separation by distillation become more difficult Because the boiling points of C8 aromatics are so close together.
* Solution: by using a combination of distillation and crystallization or adsorption.
o-Xylene
m-Xylene
p-Xylene
Ethyl benzene
Toluene
Benzene
aromatics
291.1
282.4
281
277.1
231.2
176.2
Fo
Boiling point
144.4
139.1
138.4
136.2
110.6
80.1
Co
Sequence of Aromatics recovery operation :
For a good desired separation efficiency the reflux ratio must be high. Disadvantage: it needs more energy so the cost will be higher.
Solution : Alkylation Benzene with ethylene to produce ethyl Benzene.
Processing sequence to produce C8 aromatics :
Benzene :
*The primary source of benzene is from the reforming unit, but substantial amount of benzene are also produced by hydrodealkylation of toluene
*Process flow for a hydrodealkylation unit (HAD):
1-Feed can be to toluene or admixture of to toluene and xylenes.
2-The feed is heated to 1175 f (630 c) at 600psig (4140kpa).
3-The feed charged to an open non catalytic reactor (L/D= reflux ration < 20) where thermal dealkylation of to toluene and xylenes take place during residence time of 25-30 seconds.
4-The hydrogenation step in the dealkylation reaction is highly exothermic [Q 22,000 Btu/lb-mol]So the temperature is controlled by injection of quench hydrogen at several point along the reactor.
Results :
-The hydealkylation reaction results in the conversion of benzene.
-Also small amount of polymer is formed, primarily diphenyl.
-To prevent catastrophic corrosion of the furnace tubes small amount of hydrogen sulfide is added.
-To minimize polymerformation.
Un saturate Production :
*Steam cracking of gas oil naphthas is most important process for producing a wide range of unsaturated hydrocarbons for petrochemical use.
1 -alkane (single bond) dehydrogenation(-H2) alkene (double bond)
Come from 1-ethylene.
LBG or flue gas 2-propalene.
( C2, C3, C4 )3-Butadiene.
2 -Steam – cracking : is the thermal cracking and reforming of hydrocarbons with steam at :
a- low pressure. b- High temperature.
c- Very short residence times (generally < seconds).
Process of Un saturated
- The hydrocarbon is mixed with steam in the steam/ hydrocarbon weight ratio of (0.2 to 0.8) and fed into a steam – cracking furnance.
- The residence times in the cracking Zone range from (0.3 to 0.8) seconds
- There is a coil with : outlet temperature between 1400 and 1500F , and out let pressure in the rang 10 to 20 psig .
- The coil outlet steam is quickly quenched to about 600F to stop the cracking and polymerization reactions, by transfer –line heat exchanger with a low – pressure drop .
-The quenched furnace outlet stream is sent a primary fractionators where it is separated into:a- gas steam.b- Liquid steams according to boiling point range.
-The gases are separated into to individual component as desired by compression and high – pressure fractionation .
- Paraffin obtained from the dewaxing of lubricating oil base stocks are frequently steam – creaked to produce a wide range of linear olefins.
Steam –Cracking Condition :
8-1060-80C3 conversion wt%
0.12-0.150.3-0.9Steam /HC
15-3045Pressure psig
1100-12001100-1650Coil outlet temp F
Wax Naphtha
*If we use wax stream it must be de oiled before being used as a stream –cracker feed stock.
*By choosing feed stock with an initial boiling point greater thane the end point of the desired product it will :
a) Increase the yield of the desired olefins.
b) Makes it possible to separate the product olefins from the feed paraffines by distillation
*Results: atypical product stream conditions above 80% mono olefins with only a small percentage less than 11 carbon.
*Linear mono olefins: it is also produced by several catalyst processes:_The overall process consists of:
a) Vapor- phase catalytic dehydrogenation unit b) Followed by an extraction unit.
-The linear olefins will extract from paraffin hydrocarbons by adsorption on a bed of solid adsorbent material
-They use a hydrocarbon as desorbed, it boiling at lower temperature thane olefin product
So the separation of olefin product from adsorbent will be easy.
-Then the adsorbant hydrocarbon is recycled in the extraction section.
*The results:-The olefin product contains about 96 wt% linear olefins of which about 98%are mono-olefins.
Saturated Paraffin’s
1-Normal paraffin’s:
They are recovered from petroleum fractions by vapor phase adsorption on molecular sieves.
2-Cycloparaffin’s:
They are prepared by hydrogenation of the corresponding aromatic compounds.
Normal paraffin’s:
It uses molecular sieves which are materials containing tiny pores of a precise and uniform size that is used as an adsorbent for gases and liquids.
Molecular sieves are often utilized in the petroleum industry.
5 Å pore diameter sieves are
used.
1-The adsorption takes place in vapor phase at pressure of (5-10 psig) and temperature of (300-350oC).
2-AMMONIA is used as a adsorbent.
3-The sieves loses its capacity because of contamination , so it is regenerated by controlled burn-off.
N-paraffin recovery by adsorption :
Cyclo paraffin’s
*Example(1): Cyclohexane is prepared by hydrogenation of benzene.
*The hydrogenation of benzene is carried out on:
*Platinum.
*Raney Nickel supported on alumina or silica alumina.
*The hydrogenation reaction is highly exothermic.
*The reaction temperature is controlled by recycling and injecting the cyclohexane to
the reactor.
*Example (2):Tetralin and Decalin are prepared by hydrogenation
of Naphthalene.
*The same as hydrogenation of cyclohexane .
*The catalyst is Cobalt-molybdenum.
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