AMMONIUM CHLORIDE RECOVERY FROM WASTEWATER
Polyvinyl Chloride (PVC) is one of the most common polymers for daily use. However, PVC needs thermal stabilizer such as methyl tin ethylhexyl thioglycolate (MTET) to prevents degradation at high temperature which causes functional damage. In the production of the stabilizer, ammonium chloride (N...
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Format: | Final Project |
Language: | Indonesia |
Subjects: | |
Online Access: | https://digilib.itb.ac.id/gdl/view/61461 |
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Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | Polyvinyl Chloride (PVC) is one of the most common polymers for daily use. However,
PVC needs thermal stabilizer such as methyl tin ethylhexyl thioglycolate (MTET) to
prevents degradation at high temperature which causes functional damage. In the
production of the stabilizer, ammonium chloride (NH4Cl) is produced in the wastewater
since there is neutralization of HCl using base, NH4OH. NH4Cl is a multipurpose
inorganic compound, for example, dry cells electrolyte, fertilizer, pharmaceuticals, etc.
Thus, NH4Cl in wastewater should be recycled to reduce the wastewater treatment cost,
to increase NH4Cl added-value, and to recycle water used in the process.
The main objective of this study is to develop the process of NH4Cl recovery from thermal
stabilizers wastewater by undertaking evaporation-crystallization process. The recovery
process will be carried out by thermal vapor recompression (TVR) system for saving
energy. This research involves developing process flow diagram and evaluating TVR
system using Aspen Plus V.10 and ANSYS 2021 R1. The recovery process involves
evaporation and crystallization at various pressure of the evaporation and steam jet ejector
system as major unit for TVR. Two parameters including NH4Cl yield and steam
consumption per produced NH4Cl crystal from each system are compared. NH4Cl yield
for recovery process by conventional method without recycle, with recycle, and TVR
method are 0.54, 1, and 1 respectively. While steam consumption are 7.30 kg steam/kg
crystal, 5.21 kg steam/kg crystal, and 4.66 kg steam/kg crystal respectively. Based on the
simulations’ results, the most efficient method for NH4Cl recovery process is TVR
system. |
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