Lecture Outline - Sulfuric Acid - PowerPoint PPT Presentation

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Lecture Outline - Sulfuric Acid

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Lecture Outline - Sulfuric Acid - History of Manufacture Development - Manufacture - Oleum Production - Heat Integration Issues / By-products - Markets – PowerPoint PPT presentation

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Title: Lecture Outline - Sulfuric Acid


1
Lecture Outline - Sulfuric Acid
- History of Manufacture Development -
Manufacture - Oleum Production - Heat Integration
Issues / By-products - Markets - Usage in
Caprolactam Manufacture
2
History of Manufacture of Sulfuric Acid
  • One of the oldest industrially applied processes.
    Discovered by a Persian alchemist in the tenth
    century.
  • Saltpeter and sulfur were mixed in a glass
    container and burned in a moist atmosphere. Acid
    was collected from the condensed vapors.
  • In England, 1746, the lead chamber reactor was
    invented. This invention allowed for higher
    production rates (lt78).
  • In England, 1831, a patent was filed that
    described the oxidation of sulfur dioxide over a
    platinum catalyst, the Contact Process. This new
    process increased yields of reaction from 70 to
    above 95.
  • In 1913, BASF was granted a patent for the use of
    vanadium pentoxide as a catalyst for the Contact
    Process
  • By the 1930s, vanadium pentoxide was becoming
    the dominate catalyst used because of
    insensitivities to poisons and lower cost.
  • In 1960 a patent application was filed by Bayer
    using the so called double-catalyst process
    (double absorption).

3
Manufacture
4
Oxidation of Sulfur
Process - Air drying tower with acid - Sulfur is
injected into burner - Reaction Temperature
2000F - Exothermic reaction must be cooled -
Steam recovered
  • Primary Generation of SO2
  • 79 Combustion of Sulfur
  • 9 Recovery from Metallurgic Processes
  • - 5 Regeneration of Spent Acids

5
Oxidation of Sulfur Dioxide
Contact Process -Vanadium pentoxide
catalyst - Exothermic Reaction - Multiple Steps
with cooling in between - Double
absorption - Heat integration
6
Oxidation of Sulfur Dioxide
  • Because of the large effect temperature plays on
    the reaction, multiple catalyst layers are used,
    with cooling between each step.
  • Additionally, as the partial pressure of SO3
    increases, further reaction is limited.
  • This is overcome by removing the SO3 after the
    third stage to drive the reaction to completion.

7
Oxidation of Sulfur Dioxide
  • Kinetic Effects
  • - Oxidation of sulfur dioxide is slow and
    reversible
  • - The reaction requires a catalyst and 426.7C
    temperatures
  • The reaction is exothermic and sensitive to
    excessive heat
  • Equilibrium Constant (The degree at which the
    reaction proceeds is temp. dependent)
  • log Kp 4.956 - 4.678
  • T
  • T absolute temp. in kelvin
  • Kp equilibrium constant as a function of
    partial pressure of gases
  • Kp ( PSO3 )
  • PSO2 PO2

0.5
8
Oxidation of Sulfur Dioxide
  • Temperature Profile

510 C
75 C
430 C
200 C
125 C
9
Oxidation of Sulfur Dioxide
  • Temperature Profile

10
Oxidation of Sulfur Dioxide
Typical Catalyst Distribution
11
Overall Production Scheme
12
Oleum Production
  • Sulfuric acid with additional SO3 absorbed
  • 20 Oleum contains 20 SO3 by weight in the oleum
  • Common strengths of oleum are 20, 30, 40, 65
    percent.
  • To produce 20 and 30 percent oleum, only requires
    an additional absorption tower.
  • Oleum is used in reactions where water is
    excluded
  • SO3 H2SO4 H2S2O7
    (disulfuric acid)

13
Reaction By-products / Heat Integration
  • By-products
  • 57 to 64 of the energy input generates steam
  • Steam energy is used to drive the turbine that
    supplies power to the main air blower
  • Additional steam remaining is tolled internally
    for other plant operations
  • SO2/SO3 is vented in small amounts and is
    federally regulated.
  • Heat Integration
  • Steam is used to pre-heat and vapor from the
    absorption towers used to cool
  • Minimizes the cost of manufacturing to maximize
    the profit.

14
Production Considerations
  • Metal corrosion is a big issue in the manufacture
    of sulfuric acid.
  • Special alloy metals must be used to guard
    against excessive corrosion.
  • Nickel, chromium, molybdenum, copper, an silicon
    are the most important elements that enhance
    corrosion resistance of alloys.
  • Important variables for corrosion
  • Concentration of the acid
  • Temperature of service
  • Speed of flow in pipes and
  • equipment
  • Alloy element make-up

15
World Production of Sulfuric Acid
16
World Supply / Demand for Sulfuric
Acid(thousands of metric tons, 100 H2SO4)
17
Markets for Sulfuric Acid
  • The fertilizer market is the largest U.S. single
    use for sulfuric acid and consumes 50-65 percent
    of all produced.
  • Second is the organic chemical industry.
    Production of plastics and synthetic fibers are
    examples.
  • Production of TiO2 consumes large quantities of
    sulfuric acid. TiO2 is a white pigment used in
    paints and plastics.
  • In the metal industry, sulfuric acid is used for
    pickling ferrous and non-ferrous materials and in
    the recovery of copper, nickel, and zinc from
    low-grade ores.
  • Finally, the petroleum industry uses acid as a
    catalyst for various reactions.

18
Acid Strengths Associated End Uses
19
Usage in Caprolactam Manufacture
Production and consumption figures for
caprolactam manufacture
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