Pollution Prevention and Control Technologies for Plating
Operations
Section 3 - Chemical Recovery
3.4 ION EXCHANGE
3.4.2 Development and Commercialization
Ion exchange is a versatile separation process with potential
for broad application in the metal finishing industry. The ion
exchange process has been commercially available for many years,
but early use was primarily for water deionization or softening.
Widespread interest in the process for metal finishing pollution
prevention and control is a more recent application that has grown
rapidly over the past 10 to 20 years.
Although the ion exchange process was first recognized in 1850,
and defined as a reversible process in 1858, the first practical
application of the process did not occur until 1905 when the inorganic
sodium aluminosilicate cation exchanger was synthesized and used
to soften water. In the early 1930's a cation material was developed
from sulfonated coals, which extended the operable pH range of
the process. In 1935, condensate polymers were first used as structural
substrates for various functional groups, thereby creating both
anion and cation exchange materials. The early anion product was
not the strong base anion exchanger available today. Instead,
it acted as an acid adsorbent capable of removing only free acids
from the process stream. The cation and anion forms were used
in series for the first time and deionization was accomplished;
however it was limited in application. Strong base anion exchange
materials were developed in the 1940's that extended the use of
the process. In 1945 synthetic organic polymers were developed
using styrene and divinylbenzene as the monomers. These were later
prepared in bead form (earlier, only granular products were available).
This gave rise to the modern "gel" type ion exchange
materials. Improvements during the 1950's focused on reducing
the fouling of resins by organic substances (ref. 383). One of
the earliest applications of ion exchange to metal finishing mentioned
in the literature was a hard chromium bath maintenance system
operated by the Rock Island Arsenal in 1952 (ref. 368). The use
of ion exchange as a pollution control and chemical recovery tool
progressed steadily as pollution control regulations became more
widespread and more stringent. As with many technologies, ion
exchange use for pollution control in the metal finishing industry
increased very rapidly in the late 1970's and early 1980's with
the implementation of the Federal effluent guidelines. The most
recent developments have focused on expanding the range of applications
(e.g., cyanide plating and electroless plating baths) with new
resins, equipment and techniques.
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