C2764 - Galvanising Services Ltd - Auckland Region
Summary
Galvanising Services has virtually eliminated the liquid effluent discharged
to trade waste by implementing a Cleaner Production programme. The mechanical
cleaning process has reduced acid consumption by 50%. Annual savings from
projects implemented to date are approximately $40,000 with a maximum payback
period of 1.5 years.
Business Profile
Galvanising Services galvanises steel products and nail components to provide
an anti-corrosive layer. The main processes are metal cleaning and hot dip
galvanising. The business employs 20 staff.
Type of Project
Self-regulating flow valves, recycling and filtration of rinse water from cleaning
baths, replacement of caustic cleaning and acid pickling by mechanical rumbling,
continuous preflux filtration, use of inhibitors, fume suppressants and surface
wetting agents, removal and recycling of zinc dross and dust, temperature
control and insulation of prefluxing bath, negotiating reduced power rates
for bulk power consumption.
Reasons for Project
The company participated in the cleaner production project due to its social
responsibility towards the environment and also to comply with trade waste
regulations.
The Project
| Details |
Negotiating
reduced power rates for bulk power consumption Details Galvanising
Services replaced the power meters from two separate production
units by one power meter. This enabled the business to negotiate
lower power tariffs due to bulk consumption. The business
also took advantage of discount rates for nights and weekends. |
| Economics |
The total investment
for upgrading the power distribution system was $3,400. Savings
from reduced energy consumption are $4,320 per year. The
payback period is approximately 10 months. |
| Benefits |
Reduced energy costs.
Improved power distribution system. |
METAL CLEANING PROCESSES
Self regulating flow valves
| Details |
The
objective of rinse water conservation is to use only as much
water as is needed. Self regulating flow controls valves
have been installed in the rinse tanks water inlet. The valves
set the water flow at a constant rate (0.06 L/sec) independent
of the back pressure in the mains. The flow control valves
are low cost, easy to install and maintain, and reliable.
The company saves 2000 m3 of water per year. |
| Economics |
Annual water costs
are reduced by $1,700. |
| Benefits |
Reduced water consumption
and costs. |
Recycling and filtration of rinse water from cleaning baths
| Details |
Wastewater from rinsing tanks needs to be treated to remove
zinc prior to discharge into the sewer. Galvanising Services
previously treated the wastewater with caustic soda in
a neutralisation tank. As a result the zinc hydroxides
precipitated and the clean liquid was discharged as trade
waste. As there was little control over the neutralisation
reaction, however, suspended salts were discharged with
the wastewater.
In the new situation, spent diluted acid and rinse water
are recycled as shown in the figure below. Spent weak acid
is disposed of through a waste contractor. The spent dilute
acid is filtered and then reused in the weak acid tank.
Fresh acid is added to obtain the correct concentration.
Fresh dilute acid is made using concentrated acid and filtered
rinse water. Thus spent dilute acid and rinse water are
recycled rather than dicharged as trade waste. The suspended
iron particles are trapped in the filter. Water consumption
has reduced by approximately 3,500 L per month. Quantities
of wastewater and sludge discharged and associated cost
were reduced. As the zinc levels in trade waste are reduced,
the business now complies with trade waste bylaws.
|
| Economics |
Reduced
water costs of $2,400 per year. |
| Benefits |
Reduced water consumption.
Compliance with environmental regulations through reduced
zinc levels in wastewater. Reduced wastewater quantities
and costs. Reduced quantities of sludge. |
Replacement of acid cleaning by mechanical rumbling
| Details |
In the
nail galvanising plant at Galvanising Services, the acid
cleaning process has been replaced with abrasive cleaning
by mechanical rumbling. Nails and sawdust are mixed in a
rumbling barrel. The barrel rotation exposes the surface
of the nails to the sawdust which absorbs the drawing soaps
and the manufacturing oils. The impact of nail on nail removes
any corrosion and the activation of the extractor removes
both the contaminated sawdust and any corrosion dust. The
process gives reliable surface finish so there is no need
for pickling with hydrochloric acid, and the component can
be directly processed in the prefluxing tank and the galvanising
zinc pot. As a result consumption of 42,000 l/year of hydrochloric
acid is eliminated. |
| Economics |
Capital costs for
the purchase and installation of the system are $45,000.
The operating costs of the mechanical rumbler are nominal.
Total estimated savings from elimination of the acid pickle
and rinsing process are $30,000 and include: - reduced acid
consumption $20,000/year; - reduced spent acid disposal $8,000/year;
- reduced treatment $2,000/year. The payback period is 18
months. |
| Benefits |
Reduced costs for
acid consumption, disposal and treatment. Reduced water consumption
and costs. Reduction of zinc ash and drost generation. Compliance
with environmental legislation. Improved health and safety
conditions resulting in improved staff morale. |
Removal and recycling of zinc dross and dust
| Details |
Details
Zinc dross is a pasty solid comprising of 96% zinc and 4%
iron and is produced by dragout form iron-containing pickle
salts, the fluxin solution, products that are being galvanised,
and iron and steel products reacting with molten zinc. Zinc
ash is a mixture of zinc oxide and entrained zinc, which
is often in excess of 80% of the total weight. Zinc ash is
produced when zinc is in contact with air. Galvanising Services
has reduced the formation of zinc dross and zinc ash by 18
tonnes per year by: improving work practices through good
housekeeping; filtration of the fluxing solution; replacing
acid pickling by mechanical rumbling (see previous case study). |
| Economics |
Savings of reduced
zinc dross and ash formation is $45,000 per year. |
| Benefits |
Reduced zinc costs.
Reduced zinc dross and zinc ash waste. Reduced emissions.
Improved health and safety conditions for staff. |
Continuous preflux filtration
| Details |
Details
Iron levels in the zinc ammonium chloride preflux tank must
be maintained at minimum levels of 1% as excess iron has
a detrimental effect on the amount of waste produced. The
majority of the iron is introduced to the preflux through
dragout from the acid tanks. Because of the high iron content
during pickling, rinsing is necessary before prefluxing.
A continuous preflux filtration system has therefore been
installed over the preflux to remove iron from the process. |
| Economics |
As the preflux filtration
system was already available only installation costs were
made. Zinc ammonium chloride savings have not been determined. |
| Benefits |
Reduced zinc ammonium
chloride consumption. |
METAL FINISHING PROCESSES
Use of inhibitors and fume suppressants
| Details |
Details Hydrogen chloride (HCl) is used to pickle clean
steel (Fe) objects prior to galvanising and to strip old
layers of zinc (Zn) from already galvanised objects. When
hydrogen chloride is in contact with steel or steel oxides,
it reacts as follows: Fe+ 2 HCl FeCl2 + H2(g)
FeO + 2 HCl FeCl2 + H2O
Fe2O3 + 6 HCl 2 FeCl3 + 3 H2O
Fe3O4 + 8 HCl 2 FeCl3 + FeCl2 + 4H2O
Similar reactions take place between hydrogen chloride
and zinc:
Zn + 2 HCl ZnCl2 + H2(g) ZnO + 2 HCl ZnCl2 + H2O
These reactions cause three problems for metal cleaning
businesses: the reactions with steel and zinc generate
iron chloride and zinc chloride which end up in the wastewater
stream; hydrogen chloride emissions are produced near the
bath surface through contact with the air. The vapours
are a health hazard for production staff; during the reactions
hydrogen gas (H2) is formed which is trapped in the solution.
The gas is potentially explosive.
Galvanising Services has added inhibitors, fume suppressants
and wetting agents to the pickling baths to solve these
problems:
inhibitors (steel pickling bath): the first reaction between hydrogen
chloride and steel is suppressed by up to 94-98%. This reduces the formation
of hydrogen gas and the production of iron chlorides;
fume suppressants (both baths): these
chemicals form a "foam" layer on the bath surface,
preventing the emission of hydrogen chloride
vapours;
wetting agents (both baths): these chemicals
improve the contact between workpieces and
chemicals in the bath. As a result the pickling
process is improved. |
| Economics |
Economics $600 is
spent each year on inhibitors. This is a slight increase
in costs but this is outweighed by the benefits. |
| Benefits |
Reduced metal corrosion.
Reduced hydrogen chloride emissions. Improved health and
safety conditions for staff and compliance with health and
safety regulations. Improved wastewater quality and reduced
trade waste costs. |
For additional information contact:
Mr A. Lonsdale Cooper,
Galvanising Services Ltd,
PO Box 13181,
Onehunga,
Auckland
Ph 09-6366003
Fax 09-6365967
For further information about Cleaner Production in the
Metal Industry see:
Opus International Consultants (September 1997): Cleaner
Production Guide for the Metal Industry- Minimising waste,
reducing costs and caring for the environment.
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