CASALE: 95 YEARS OF HISTORY 1921: First ammonia technology 1980s: - - PowerPoint PPT Presentation

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CASALE: 95 YEARS OF HISTORY 1921: First ammonia technology 1980s: - - PowerPoint PPT Presentation

CASALE: 95 YEARS OF HISTORY 1921: First ammonia technology 1980s: Urea and Methanol technologies 2013: Melamine technology 2014: Nitrate, Phosphate, Complex fertilizer AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL


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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

CASALE: 95 YEARS OF HISTORY

1921: First ammonia technology 1980s: Urea and Methanol technologies 2013: Melamine technology 2014: Nitrate, Phosphate, Complex fertilizer

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

TECHNOLOGICAL PORTFOLIO

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

New Plants

Small – World Scale – Mega High energy efficiency Integrated productions TAILORED ENGINEERING SOLUTIONS

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

Plant Revamping

Capacity Increase (up to +100%) Energy Saving (5% - 30%) TAILORED ENGINEERING SOLUTIONS

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

EXPERIENCE – Revamping

Start ups in the last 5y: 61

  • Energy Saving

4’110’000 Gcal/Y

  • CO2 saving

946’000 T/Y

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

Project Customer Care Conceptual Design

COMPLETE RANGE OF SERVICES

Casale life-cycle approach

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

Brazil China Egypt India Indonesia Iran North America Pakistan Russia

A GLOBAL PRESENCE

Network of representatives

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

NURTURING INNOVATIONS: the key to a successful future

R&D : driver to deliver our client better solutions

Developing new technologies Improving existing ones

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

Casale cooperates with leading institutions

NURTURING INNOVATIONS: the key to a successful future

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS TODAY

  • 56 new synthesis loop (40 in operation) in the last 25 years
  • Capacities from 200 MTD to 2000 MTD
  • More then 220 converters installed since 85
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS TODAY Iron granules catalyst

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS TODAY

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

CATALYST BEDS INTERCHANGERS AMMONIA SYNTHESIS TODAY

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

CASALE car (1935)

  • NH3 fuelled
  • Driven from Terni to Trieste,

560 km (350 miles) AMMONIA FUTURE AS SEEN YESTERDAY

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS TOMORROW Desired Improvements:

  • Lower catalyst light off temperature
  • Alternative NH3 product separation
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

  • Lower catalyst light off temperature
  • higher conversion per pass
  • lower circulation
  • Less power for circulating

compressor

  • Smaller equipment
  • Easier NH3 condensation
  • Lower pressure

AMMONIA SYNTHESIS TOMORROW

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

  • Lower pressure
  • Lower energy consumption, if coupled with lower light off temperature
  • Simpler syngas compressor, if any
  • Lighter, cheaper equipment

AMMONIA SYNTHESIS TOMORROW

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

  • Alternative NH3 product separation
  • No need for refridge compressor
  • Simpler synthesis loop
  • Lower consumption

AMMONIA SYNTHESIS TOMORROW

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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES Requisites:

  • Simple
  • Easy to operate
  • Robust
  • Lowest cost
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES Constraints:

  • Variable load
  • Small size
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES Desired Improvements :

  • Lower catalyst light off temperature
  • Alternative NH3 product separation
  • Insensitiveness to plant load variability
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES

  • Lower catalyst light off temperature:
  • higher conversion per pass
  • lower circulation
  • Less power for circulating compressor
  • Smaller equipment
  • Easier NH3 condensation
  • Easier operation
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES

  • Lower operating pressure:
  • Simpler syngas compressor, if any
  • Lower energy consumption, if coupled with lower light off temperature
  • Lighter, cheaper equipment
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES

  • Insensitiveness to plant load variability:
  • Easier operation
  • Less mechanical stresses, higher reliability
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES

  • Alternative NH3 product separation:
  • No need for refridge compressor
  • Simpler synthesis loop
  • Lower consumption
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AMMONIA NITRATES AND PHOSPHATES UREA MELAMINE METHANOL SYNGAS

AMMONIA SYNTHESIS FROM RENEWABLES

  • Small size:
  • Simplified converter design

v Quench instead of interchanger v Accessibility for maintenance

  • Simplified loop design
  • Loop pressure and syngas compressor selection critical
  • Automation
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THANK YOU