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INDUSTRIAL PRODUCTION OF
QUINIZARIN
Quinizarin is an orange or red-brown crystalline powder
Solvent Orange 86
REACTION
H2SO4
H3BO3
Phthalic
anhydride
p-chlorophenol Quinizarin
RAW MATERIALS AND COST
CHEMICAL QUANTITY COST (Rs)
Phthalic anhydride 950 kg 428 /kg
p-chlorophenol 750 kg 1376 /kg
Boric acid 350 kg 359 /kg
Sulfuric acid 2170 L 251 /L
Toluene 2000 L 350 /L
CHEMICAL TABLE
Chemicals Weight(g) Molecular
Weight(g)
Moles Molar
ratio
Weight
ratio
P-chlorophenol 7.5 128 0.058 1 1
Phthalic
anhydride
9.5 148 0.064 1.103 1.27
Sulfuric acid 40 98 0.41 7.069 5.33
Boric acid 3.5 61.83 0.06 1.034 0.47
PROCESS
 Sulfuric acid (2170 L) is added to the
reactor
 Boric acid (350 kg) is taken in a 5000 L
reactor the temperature is raised to about
110oC and incubated for about 45-60
minutes.
 Then phthalic anhydride (950 kg) is added
and the heat released by the reaction
temperature was raised to about 130oC.
PROCESS
Phthalic
anhydride
p-chlorophenol
o After the addition of pthalic anhydride,
o p-chlorophenol (750 kg) is added repeatedly in
batches for over 4 hours.
PROCESS
 The temperature control throughout the
addition is maintained at about 130-150oC.
 After adding p-chlorophenol, the
temperature is raised to 200-205oC and the
mixture is incubated for around 5 hours.
PROCESS
o The reaction product is then placed in a
pre-hydrolysis water (12000 L) and the
temperature is maintained at 100oC.
 Now, toluene (2000 L) is added to the
hydrolysis vessel with stirring over 30
minutes.
PROCESS
 The mixture is allowed to stand and then again hot
water (1000 L) is added for washing.
 The toluene extract is fed to a distillation kettle
where the distilled toluene is recycled.
 After the evaporation of toluene, high vaccum pump
is turned on,
 the mixture is added to another kettle sublimation
and 1,4-dihydroxy anthraquinone is obtained.
 Quinizarin obtained is 1250 kg
 The yield is 89.28%. The purity is 98%.
PA SULFURIC
ACID
REACTOR 1
H3BO3 PCP
REACTOR 2
WATER
WASTE
ACID
TOLUENE
DIS
TIL
LAT
ION
QUINIZARIN
REFERENCES
 CN1289756A
 Novel synthetic approach for 1,4-
dihydroxyanthraquinone and the development
of its lithiated salts as anode materials for
aqueous rechargeable lithium-ion batteries

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Industrial production of quinizarin

  • 1. INDUSTRIAL PRODUCTION OF QUINIZARIN Quinizarin is an orange or red-brown crystalline powder Solvent Orange 86
  • 3. RAW MATERIALS AND COST CHEMICAL QUANTITY COST (Rs) Phthalic anhydride 950 kg 428 /kg p-chlorophenol 750 kg 1376 /kg Boric acid 350 kg 359 /kg Sulfuric acid 2170 L 251 /L Toluene 2000 L 350 /L
  • 4. CHEMICAL TABLE Chemicals Weight(g) Molecular Weight(g) Moles Molar ratio Weight ratio P-chlorophenol 7.5 128 0.058 1 1 Phthalic anhydride 9.5 148 0.064 1.103 1.27 Sulfuric acid 40 98 0.41 7.069 5.33 Boric acid 3.5 61.83 0.06 1.034 0.47
  • 5. PROCESS  Sulfuric acid (2170 L) is added to the reactor  Boric acid (350 kg) is taken in a 5000 L reactor the temperature is raised to about 110oC and incubated for about 45-60 minutes.  Then phthalic anhydride (950 kg) is added and the heat released by the reaction temperature was raised to about 130oC.
  • 6. PROCESS Phthalic anhydride p-chlorophenol o After the addition of pthalic anhydride, o p-chlorophenol (750 kg) is added repeatedly in batches for over 4 hours.
  • 7. PROCESS  The temperature control throughout the addition is maintained at about 130-150oC.  After adding p-chlorophenol, the temperature is raised to 200-205oC and the mixture is incubated for around 5 hours.
  • 8. PROCESS o The reaction product is then placed in a pre-hydrolysis water (12000 L) and the temperature is maintained at 100oC.  Now, toluene (2000 L) is added to the hydrolysis vessel with stirring over 30 minutes.
  • 9. PROCESS  The mixture is allowed to stand and then again hot water (1000 L) is added for washing.  The toluene extract is fed to a distillation kettle where the distilled toluene is recycled.  After the evaporation of toluene, high vaccum pump is turned on,  the mixture is added to another kettle sublimation and 1,4-dihydroxy anthraquinone is obtained.  Quinizarin obtained is 1250 kg  The yield is 89.28%. The purity is 98%.
  • 10. PA SULFURIC ACID REACTOR 1 H3BO3 PCP REACTOR 2 WATER WASTE ACID TOLUENE DIS TIL LAT ION QUINIZARIN
  • 11. REFERENCES  CN1289756A  Novel synthetic approach for 1,4- dihydroxyanthraquinone and the development of its lithiated salts as anode materials for aqueous rechargeable lithium-ion batteries