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United Arab Emirates University Chemical and Petroleum Engineering

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Title: United Arab Emirates University Chemical and Petroleum Engineering


1
United Arab Emirates UniversityChemical and
Petroleum Engineering
Desalination of seawater using exhaust CO2
  • Presented By
  • Ahmad Hussain AlHossany
  • Adeeb Omar Bamatraf
  • Mohamad Jamal El-Cadi
  • Saleh Mohammed Mohammed
  • Advisor Co-advisors
  • Dr. Ali Al-Marzouqi Dr. Omar Chaalal

2
Water Desalination
  • The Na of seawater is 14,000 ppm.
  • Brackish Water with Na of 1000 4000 ppm is
    suitable for irrigation (depending on crops).
  • Saline type agriculture is under research to use
    saline water up to Na of 10,000 ppm.
  • Water demands include
  • Domestic use
  • Agriculture use
  • Industrial use

3
Main Desalination Technologies
Multi-Stage Flash (MSF)
4
Gas Flaring in the UAE
Total Gas Flaring in the UAE 83 MMSCFD
MMSCFD
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OBJECTIVE
Propose a practical process, at low cost, for
producing large quantities of brackish water,
using CO2 from combustion exhaust, which
otherwise would be contaminating the environment.

7
Advantages of the proposed process
  • Low energy consumption low cost.
  • Raw materials available at low cost.
  • Produce brackish water for irrigation purposes.
  • Produce valuable by-products.
  • Solves two environmental problems
  • Reduce CO2 emissions to the atmosphere.
  • Treatment of reject brine or formation water.

8
Theory
  • - The absorbed CO2 reacts with ammonia in the
    ammoniated brine to form carbamic acid.
  • CO2 NH3 NH2COOH (carbamic acid )
    (1)
  • - Carbamic acid reacts with ammonia to form
    ammonium carbamate.
  • NH3 NH2COOH NH4 NH2COO-
    (2)
  • - The overall reaction is given as (Primary Rxn.)
  • CO2 2NH3 NH2COO-
    NH4 (3)
  • - The carbonate slowly converts into bicarbonate
    (Secondary Rxn.)
  • NH2COO- H2O NH3 HOCOO-
    (4)
  • Main Reaction
  • NaCl (aq) NH3 (aq) H2O (l) CO2(g)
    NaHCO3 (s) NH4Cl(aq)

9
EXPERIMENTAL WORK
  • Aim
  • To investigate the optimum conditions that give
  • the best quality of irrigation water.
  • - Temperature
  • - Pressure
  • - Concentration of NaCl
  • - Concentration of Ammonia
  • - CO2 flow rate
  • - Mixing
  • - Time

10
Experimental Setup
11
PRECIPITATE
12
Experimental Work
Trial NH4OH (ml) Seawater (ml) Total (ml)
1 7 193 200
2 15 185 200
3 30 170 200
4 50 150 200
5 100 100 200
6 150 50 200
Experiments were conducted at 25 oC
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Process Flow Diagram
20
Evaporation required for different feed types
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HEALTH, SAFETY ENVIRONMENTAL REGULATIONS
Safety of the employees - Complete training
on each piece of equipment - Wear personal
protective equipment The operating conditions
(i.e. P, T, and concentration of chemicals) will
always be within OSHA regulations and limits
24
Conclusion
  • Effects of different parameters were
    investigated.
  • Optimum Conditions
  • T 20 oC
  • P 2 atm
  • CO2 Flow Rate to reactor 2 L/min
  • NH3/NaCl Ratio 1
  • Time of reaction 2 hrs

25
Conclusion
  • Proposed process has a low energy consumption
    since exhaust gases are available at high
    temperature.
  • Most of the raw materials are readily available
    at low cost.
  • Proposed process solves two environmental
    problems
  • Reduce CO2 emissions to the atmosphere.
  • Treatment of reject brine or formation water.

26
  • Thank You for Your Attention

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