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Project Phase 1 Seminar
BT19CME045 Prabuddha Gope
BT19CME051 Himanshu Yadav
BT19CME085 Kartik Prasad
Project Guide: Dr. A.S. Chaurasia
Department of Chemical Engineering
Date: 19/09/2022
Co-gasification
of Rice Straw
and LDPE
Objectives
To study the changes in the gasification process by the addition
of polymer to biomass
To study gas composition and tar,char weights
Biomass
Gasification
At high temperatures and in the
presence of air, biomass is converted
into useful gases such as methane
and hydrogen. This is a fast and
efficient method for the conversion of
biomass into a high calorific value
fuel.
Gasification
Reaction Scheme
Khonde R, Chaurasia A, Rice husk gasification in a two-stage fixed-bed gasifier: Production of
hydrogen rich syngas and kinetics, InternationalJournal of Hydrogen Energy (2016), http://dx.doi.org/10.1016/j.ijhydene.2016.03.138
Reaction conditions
● The temperature for the pyrolysis
section is maintained at 500 oC and
the temperature of the gasification
section is maintained at 800 oC. These
values are reported as optimum values
in previous studies using this reactor.
● The combination of nitrogen for
pyrolysis section and air for the
gasification section is chosen as they
give the highest yield of hydrogen.
Khonde R, Chaurasia A, Rice husk gasification in a two-stage fixed-bed gasifier: Production of
hydrogen rich syngas and kinetics, InternationalJournal of Hydrogen Energy (2016), http://dx.doi.org/10.1016/j.ijhydene.2016.03.138
Co - gasification of biomass with plastic
● Co-gasification of biomass with plastic
(waste plastic) has several
advantages over traditional
gasification.
● The first advantage is that the supply
of biomass is seasonal, a facility that
can also use waste plastic as
feedstock has an advantage.
● Using waste plastic also leads to a
product gas that is richer in hydrogen
as the following graph published by F.
Pinto et al. shows.
F. Pinto et al./ Fuel 81(2002) 291-297
Choice of plastic
● LDPE makes up a major chunk of
plastic waste in municipal solid waste.
● It was also readily available (as waste
bubble wrap) in our lab.
● C. Cao et al. ( reported the gasification
efficiency of different polymers as
PE > PC = PP > ABS
Table source : International Journal of Design Sciences and
Technology,Volume 22 Number 2(201 6) ISSN 1 630-7267
Experimental
Procedure
01
LAB PROCEDURE
Assembly
Pyrolysis
section
Attache 3
Throat
section
Attache 2
Gasification
section
Attache 1
Step 1:Feed preparation
1. We prepare the feed
Rice straw→Cut it into small pieces
Grind it in a mixer
Sieve it
Oven dry it
Polymer(LDPE) → Cut it into small squares of approx 1
cm2
1. Weighing
We store our feed in batches of 25g rice straw and
variable amount of plastic in each batch in air tight bags
Step 2:Assemble
1. PYROLYSIS CHAMBER
● The pyrolysis chamber is made leak proof (viz-a-
viz,feed leak) using three meshes [two square meshes
pushed in; one circular mesh below the above two(for
the periphery)].
● Now the feed is fed to the chamber from above
● We proceed to break ice and put it into the drum where
tar is condensed (¼ by height of the drum) & seal it.
● A mesh is put between the gasket and the given
structure
● Now, the gasification chamber is affixed first(using nuts
& bolts on the given structure.
Cont.
2.THROAT
After,[1] we affix the throat on the gasification chamber.
3.PYROLYSIS CHAMBER
The pyrolysis chamber is affixed over the throat(,also a mesh
is put between the two chambers)
4.
The instrument for intermittent feeding is affixed over the
pyrolysis chamber
5.VALVE
The valve along with its pipe is attached to the drum,for
collecting gas in the tedlar bag.
Step 3:Wiring & Heating
1.Wiring
The wires are colour coded i.e. our seniors have left some
markings.
The red wires go in the hole marked ‘R’;The black wires, ‘B’
marked hole;The green wires (*2) are for earthing [wound at
the back of the assembly(,on the support)]
2.Heating
After the wiring is done,we switch on the heating controller for
the gasification section, & after it reaches 300 °C (,in about 20
min),we switch on the heating controller for the pyrolysis
section.
LS
US
Step 4:Gas collection
1.Flow rates
When the temp. Of the pyrolysis section reaches 300 °C we
start the air flow (0.5 LPH ) and nitrogen flow (0.2 LPH).
Now we also connect a tedlar bag to the pipe attached to the
valve on the drum for gas collection.
The heating of the system is concluded when the upper
section reaches 500 and the lower section reaches 800.
Note:The throat is connected to the upper section for its own
heating.
Step 5: Tar & Char collection
1.Tar
● After the reactor is cooled,we start disassembling the stages .
● In the U-tube type of structure attached to the bottom of the the drum head,we put approx
40 ml chloroform and shake the structure well.
● The tar chloroform solution is poured into another beaker;again,we add chloroform for
2nd washing.
● Later,the chloroform is evaporated from the mixture using suitable equipment.
2.Char
The leftover char in the pyrolysis chamber is collected in an airtight bag and is weighed.
Cont.
Run 1: 2.5g LDPE
+
25g rice straw
[11.33 g char]
Run 2: 1.25g LDPE
+
25g rice straw
[11.25 g char(1g
trapped in the mesh)]
Run 3: 3.75g LDPE
+
25g rice straw
[11.68 g char]
Run 4: 5g LDPE
+
25g rice straw
[16.16 g char]
**-1 g from wt.[wt. Of plastic bag].
**+0.5 g (approx) char got wasted.
Cont.
**-23.16g from each(to account wt.
Of container).
Run 1: 2.5g LDPE
+
25g rice straw
[13.23 g Tar]
Run 2: 1.25g LDPE
+
25g rice straw
[15.81 g Tar]
Run 3: 3.75g LDPE
+
25g rice straw
[23.62 g Tar]
Run 4: 5g LDPE
+
25g rice straw
[26.19 g Tar]
Issues faced
Current situation
1 2 3 4
Problems
Reactor
leakage
Dearth of N2 Gasket leak
Small space
in the reactor
We are going good
Cont.
Reactor malfunction Reactor malfunction Gasket leak
Preliminary
Results
03
A sample gas chromatogram
Weight of Tar vs Weight of LDPE added
Thank You
Sem 7_FYP BT19CME_85_51_45.pptx

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Sem 7_FYP BT19CME_85_51_45.pptx

  • 1. Project Phase 1 Seminar BT19CME045 Prabuddha Gope BT19CME051 Himanshu Yadav BT19CME085 Kartik Prasad Project Guide: Dr. A.S. Chaurasia Department of Chemical Engineering Date: 19/09/2022
  • 3. Objectives To study the changes in the gasification process by the addition of polymer to biomass To study gas composition and tar,char weights
  • 4. Biomass Gasification At high temperatures and in the presence of air, biomass is converted into useful gases such as methane and hydrogen. This is a fast and efficient method for the conversion of biomass into a high calorific value fuel.
  • 5. Gasification Reaction Scheme Khonde R, Chaurasia A, Rice husk gasification in a two-stage fixed-bed gasifier: Production of hydrogen rich syngas and kinetics, InternationalJournal of Hydrogen Energy (2016), http://dx.doi.org/10.1016/j.ijhydene.2016.03.138
  • 6. Reaction conditions ● The temperature for the pyrolysis section is maintained at 500 oC and the temperature of the gasification section is maintained at 800 oC. These values are reported as optimum values in previous studies using this reactor. ● The combination of nitrogen for pyrolysis section and air for the gasification section is chosen as they give the highest yield of hydrogen. Khonde R, Chaurasia A, Rice husk gasification in a two-stage fixed-bed gasifier: Production of hydrogen rich syngas and kinetics, InternationalJournal of Hydrogen Energy (2016), http://dx.doi.org/10.1016/j.ijhydene.2016.03.138
  • 7. Co - gasification of biomass with plastic ● Co-gasification of biomass with plastic (waste plastic) has several advantages over traditional gasification. ● The first advantage is that the supply of biomass is seasonal, a facility that can also use waste plastic as feedstock has an advantage. ● Using waste plastic also leads to a product gas that is richer in hydrogen as the following graph published by F. Pinto et al. shows. F. Pinto et al./ Fuel 81(2002) 291-297
  • 8. Choice of plastic ● LDPE makes up a major chunk of plastic waste in municipal solid waste. ● It was also readily available (as waste bubble wrap) in our lab. ● C. Cao et al. ( reported the gasification efficiency of different polymers as PE > PC = PP > ABS Table source : International Journal of Design Sciences and Technology,Volume 22 Number 2(201 6) ISSN 1 630-7267
  • 11. Step 1:Feed preparation 1. We prepare the feed Rice straw→Cut it into small pieces Grind it in a mixer Sieve it Oven dry it Polymer(LDPE) → Cut it into small squares of approx 1 cm2 1. Weighing We store our feed in batches of 25g rice straw and variable amount of plastic in each batch in air tight bags
  • 12. Step 2:Assemble 1. PYROLYSIS CHAMBER ● The pyrolysis chamber is made leak proof (viz-a- viz,feed leak) using three meshes [two square meshes pushed in; one circular mesh below the above two(for the periphery)]. ● Now the feed is fed to the chamber from above ● We proceed to break ice and put it into the drum where tar is condensed (¼ by height of the drum) & seal it. ● A mesh is put between the gasket and the given structure ● Now, the gasification chamber is affixed first(using nuts & bolts on the given structure.
  • 13. Cont. 2.THROAT After,[1] we affix the throat on the gasification chamber. 3.PYROLYSIS CHAMBER The pyrolysis chamber is affixed over the throat(,also a mesh is put between the two chambers) 4. The instrument for intermittent feeding is affixed over the pyrolysis chamber 5.VALVE The valve along with its pipe is attached to the drum,for collecting gas in the tedlar bag.
  • 14. Step 3:Wiring & Heating 1.Wiring The wires are colour coded i.e. our seniors have left some markings. The red wires go in the hole marked ‘R’;The black wires, ‘B’ marked hole;The green wires (*2) are for earthing [wound at the back of the assembly(,on the support)] 2.Heating After the wiring is done,we switch on the heating controller for the gasification section, & after it reaches 300 °C (,in about 20 min),we switch on the heating controller for the pyrolysis section. LS US
  • 15. Step 4:Gas collection 1.Flow rates When the temp. Of the pyrolysis section reaches 300 °C we start the air flow (0.5 LPH ) and nitrogen flow (0.2 LPH). Now we also connect a tedlar bag to the pipe attached to the valve on the drum for gas collection. The heating of the system is concluded when the upper section reaches 500 and the lower section reaches 800. Note:The throat is connected to the upper section for its own heating.
  • 16. Step 5: Tar & Char collection 1.Tar ● After the reactor is cooled,we start disassembling the stages . ● In the U-tube type of structure attached to the bottom of the the drum head,we put approx 40 ml chloroform and shake the structure well. ● The tar chloroform solution is poured into another beaker;again,we add chloroform for 2nd washing. ● Later,the chloroform is evaporated from the mixture using suitable equipment. 2.Char The leftover char in the pyrolysis chamber is collected in an airtight bag and is weighed.
  • 17. Cont. Run 1: 2.5g LDPE + 25g rice straw [11.33 g char] Run 2: 1.25g LDPE + 25g rice straw [11.25 g char(1g trapped in the mesh)] Run 3: 3.75g LDPE + 25g rice straw [11.68 g char] Run 4: 5g LDPE + 25g rice straw [16.16 g char] **-1 g from wt.[wt. Of plastic bag]. **+0.5 g (approx) char got wasted.
  • 18. Cont. **-23.16g from each(to account wt. Of container). Run 1: 2.5g LDPE + 25g rice straw [13.23 g Tar] Run 2: 1.25g LDPE + 25g rice straw [15.81 g Tar] Run 3: 3.75g LDPE + 25g rice straw [23.62 g Tar] Run 4: 5g LDPE + 25g rice straw [26.19 g Tar]
  • 19. Issues faced Current situation 1 2 3 4 Problems Reactor leakage Dearth of N2 Gasket leak Small space in the reactor We are going good
  • 20. Cont. Reactor malfunction Reactor malfunction Gasket leak
  • 22. A sample gas chromatogram
  • 23. Weight of Tar vs Weight of LDPE added

Editor's Notes

  1. Find out the definition of gasification efficiency
  2. COMMENT:NOT SURE WHETHER LPH OR LPM
  3. First peak Second peak Third peak Fourth peak
  4. First peak Second peak Third peak Fourth peak