Title: Distillation D86 True Boiling Point
1Distillation (D-86) True Boiling Point
Asst. Prof. Dr. Pakamas Chetpattananondh In House
Practical Training (IHPT)
Department of Chemical Engineering, Faculty of
Engineering, PSU
2Vaporization of pure component
212 F
70 F
3Does "Boiling" Mean "Hot"?
- Boiling occurs when the vapor pressure inside the
bubble equals atmospheric pressure. - What would happen if the atmospheric pressure
would drop? - The simple example of this is the case of a
camper who is on the top of a 10,000 ft mountain.
While water boils at 100 degrees C at sea level
(where the atmospheric pressure is 760mm Hg) the
atmospheric pressure at 10,000 ft altitude is
about 530 mm Hg. - Because the boiling point of water is about 90
degrees C at this altitude, not only will our
camper find that his food will cook a little
slower than normal, any attempt to boil water to
kill germs and pathogens may be unsuccessful
since the water isn't getting hot enough.
4Vaporization of mixtures
Pure ethanol BP 173 F
5Batch distiallation
6Continuous distillation
7Volatility
- A fuels ability to vaporize or change from
liquid to vapor is referred to as its volatility. - The volatility characteristics of a spark
ignition (SI) engine fuel are of prime
importance. - Fuels that do not vaporize readily may cause hard
starting of cold engines and poor vehicle
driveability during warm-up and acceleration. - Conversely, fuels that vaporize too readily at
higher operating temperatures will cause too much
vapor to form causing a decrease in fuel flow to
the engine (known as vapor lock).
8Volatility
9Volatility
- The main parameters to establish volatility
limits are Vapor/Liquid Ratio (V/L), Vapor
Pressure (RVP), and Distillation Curve. - The vapor/liquid ratio uses a test to determine
the temperature required to create a V/L ratio of
20. - More volatile fuels require lower temperatures to
achieve this ratio while less volatile fuels
require higher temperatures to create the same
ratio. - The V/L ratio assists in defining a fuel's
tendency to contribute to vapor lock. - The V/L ratio and RVP are measurements of a
fuel's "front end volatility", or more volatile
components which vaporize first. - The distillation test is used to determine fuel
volatility over the entire boiling range of
gasoline.
10Classification methods of petroleum fractions by
boiling point
- ASTM-D86
- Distillation method for light petroleum products
- ASTM D-1160
- Distillation method for heavier fractions
(gt500F) carried out in vacuum
- ASTM-D2892
- True Boiling Point (TBP)
11How is D-86 important ?
- D 86 is used to determine fuel volatility across
the entire boiling range of fuel.
- A Front End (020 evaporated)
- B Mid-range (20-90 evaporated)
- C Tail End (90-100 evaporated)
12How is D-86 important ?
- The 10 evaporated temperature must be low enough
to provide easy cold starting but high enough to
minimize vapor lock as well as hot driveability
problems. - The 50 evaporated temperature must be low enough
to provide good warm up and cold weather
driveabiity without being so low as to contribute
to hot driveability and vapor locking problems. - The 90 and end point evaporation temperatures
must be low enough to minimize crankcase and
combustion chamber deposits as well as spark plug
fouling and dilution of engine oil.
13Flexible Volatility Index (FVI) This is a
parameter calculated from the RVP and the
measured value of E70, and is an indicator of the
hot running performance (the tendency for vapour
lock). FVI RVP (0.7 x E70)
14Using distillation curve
In New Zealand E 70?C at 25-45 E 100?C at 45-67
DI for UL 91 is about 495 DI 550 cause
driveability problem in cold
DI 1.5 x T10 3 x T50 T90
15True boiling point
- ASTM D-2892 is used for samples with a wide
boiling range such as crude petroleum up to a
final cut temperature of 400C (752F)
atmospheric equivalent temperature (AET). - Theoretical plate 14-18 (15)
- Distillation pot, volume 15 L
- Volumetric of feed 5 10 L
- Reflux ratio 51
- Temperature of distillation 350?C (AET)
- Weight loss 4
16True boiling point
- It is often useful to extend the boiling point
data to higher temperatures than are possible in
the fractionating distillation method and for
this purpose a vacuum distillation in a simple
still with no fractionating column (ASTM D-1160)
can be carried out. - This distillation, which is done under
fractionating conditions equivalent to one
theoretical plate, allows the boiling point data
to be extended to about 600C (1112F) with many
crude oils. - This method gives useful comparative and
reproducible results that are often accurate
enough for refinery purposes, provided
significant cracking does not occur. - Usually seven fractions provide the basis for a
reasonably thorough evaluation of the
distillation properties of the feedstock
17True boiling point
- 1. Gas, boiling range lt15.5C (60F)
- 2. Gasoline (light naphtha), boiling range
l5.5149C (60300F) - 3. Kerosene (medium naphtha), boiling range
149232C (300450F) - 4. Gas oil, boiling range 232343C (450650F)
- 5. Light vacuum gas oil, boiling range 343371C
(650700F) - 6. Heavy vacuum gas oil, boiling range 371566C
(7001050F) - 7. Residuum, boiling range gt566C (1050F)
18Typical Refinery Products
From Schmidt, G.K. and Forster, E.J., Modern
Refining for Todays Fuels and Lubricants, SAE
Paper 861176, 1986.
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21Crude Assay
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23For vacuum residues a typical true boiling point
(TBP) cut point is 538?C, but it may be lower or
higher depending on the crude. The TBP cut point
will define the concentration of Conradson carbon
residue (CCR), sulfur, and metals in the feed and
thereby affect yields and product quality.
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27Thanks for your attention