ENVIRONMENTAL
IMPROVEMENT RESULTING FROM OXYCOMBUSTION TECHNOLOGY USE IN THE GLASS INDUSTRY LOCATED IN SACCA SERENELLA (MURANO ISLAND, VENICE)
Introduction
One of the main environmental impacts due to this type of
manufacturing activity are the emissions of pollutants
in the atmosphere.
The production cycle of artistic glass is based on
different operational phases; with regard to the environmental impact one of
the most important steps is the blending of the vitreous solutions and by the
following processing of formed glass.
Fusion of glass is responsible for about the 60% of energy
consumption and 90% of solid and gaseous emissions deriving from the whole production
cycle.
The aim of the project is the replacement of traditional
techniques of glass fusion with techniques that lead to a lesser environmental
impact and a lesser consumption of energy.
The furnaces for glass fusion are presently stoked by methane
and the combustion is air/methane driven. Since a long time, experimental tests
have been underway in order to evaluate the possibility of introducing
different fusion techniques that could have relevant benefits also vis-à-vis
energy consumption. Among them, the “oxycombustion”
technique is one of the most promising.
Oxycombustion use in the glass industries
located in Sacca Serenella
(Murano Island, Venice) is foreseen as part of an
experimental test that aims to reduce the environmental impact of the artistic
glass production sector with regard to both, atmospheric emissions (i.e. carbon
dioxide) and energy consumption.
The initiative has the support of the City of Venice, Artambiente (Craftsmen Association), SAPIO Spa (Private
Company that produces oxygen), Confartigianato di Venezia and is to be enacted
by glass craftsmen and the Glass Experimental Station (Laboratory for emissions
analyses).
Environmental problems deriving from artistic glass
production
Emissions in the atmosphere are caused by the raw
materials themselves, the temperatures reached during the fusion phase and the
combustion system.
Specifically they are made up of:
-
by-products
of methane combustion during the production cycle (carbon dioxide, and NOX
due to air oxidisation);
-
by-products
of the decomposition of the raw materials used to form the vitreous mixture (NOX
due to nitrates decomposition, CO2 to carbonates);
-
by-products of evaporation phenomena and possible re-condensation of
volatile substances present into the vitreous mixture (PM, Heavy metals,
chlorides and gaseous fluorides).
Oxycombustion replaces traditional methane/air
combustion with a methane/oxygen driven combustion. In this way, the calorific
value of the fuel increases because the presence of nitrogen, that at high
rates in regular air combustion(about 80%), is almost completely removed. The
result is a flame with higher temperatures so that a better diffusion of heat
to the furnace and to the glass is obtained.
There are five glass industries involved in this
experimental oxycombustion test..
They have a similar production cycle and a typology of product.
SAPIO Spa is charged with the detailed designs of all
structural intervention necessary to run the experimental test both inside and
outside the glassworks. Artambiente has to identify
the glassworks that will be involved. The City of Venice Administration finances and establishes
structural installations necessary for the experimental test as part of its
urbanization intervention in Sacca Serenella. Upon the completion of the structural
installations, the testing will last at least two years.
It is also expected to make use of the oxygen production
potential in Porto Marghera industrial area and to
link Murano through an underwater pipeline. Time
needed for the pipeline completion is 12-18 months (upon receipt of the
requisite authorisation release). To facilitate local distribution an arrival
terminal for the pipeline will be built, from where a local distribution
network will originate.
Potential energy consumption
reduction
A relevant reduction of combustion consumption is due to
experimental tests run on furnaces for artistic glass. Their combustion scheme
has been modified from the methane/air to methane/oxygen mixture system.
The following table sums up specific consumptions checked
during many tests:
|
Air / methane
|
Oxygen
/ methane
|
Final consumption (MJ/kg glass)
|
72,7
|
38,71
|
Primary consumption2
(MJ/kg glass)
|
72,7
|
42,2
|
1 The value is given as the sum of
energy spent for combustion and oxygen production equal to 2,3MJ/Kg of glass (2,1 mc O2/kg glass; 0,3 kWh/mc O2)
2 A conventional factor of 2200
Kcal/KWh has been used.
At the moment in the Murano Island district a methane consumption of
4,4 million cubic metre has been recorded.
In terms of primary energy, consumption corresponding to
the considerable introduction of the oxycombustion
technique is reported into the following scheme:
|
Air / methane
|
Oxygen / methane
|
Primary Consumption (TJ)
|
1.520
|
882
|
Primary Consumption (tep)
|
36.309
|
21.076
|
Saving (%)
|
|
-42
|
Fuels consumption (basically natural gas) for house
heating is about 148.000 tep.
Potential reduction
of atmospheric emissions
The following scheme sums up the
change of CO2 global emissions corresponding to alternative
configurations, both for unit of glass worked and as resulting from a
considerable introduction of the oxycombustion
technique.
Global CO2 eq.
emissions
|
Air / methane
|
Oxygen /
methane
|
Specific (kg/kg glass)
|
4,9
|
2,9
|
Total (kilotons)
|
102
|
66
|
Total reduction of equivalent CO2 results
in about 45.000 tons.
Other benefits
The main benefits derived from oxycombustion,
besides the lower energy consumption and the reduction in emissions of
greenhouse gases can be summed up in the following points:
1. reduction of nitrogen oxide
emissions (lack of nitrogen to oxidize);
2. reduction of solid and gaseous
emissions during production cycle (less frequent phenomena of
evaporation/re-condensation)
3. reduction of smoke volume to be
shifted by fan;
4. reduction of noise emissions (no air
compressor is needed).
Inclusive costs
Costs corresponding to production
of the distribution system is estimated to be about €10 million. This is broken down as
follows:
-
€4
million to build the oxygen pipe;
-
€4
million to build the network of local distribution;
-
€2
million to adapt the fusion furnaces.
Current and new technology working costs are also
estimated as follows:
-
€8,2
million to buy methane in the current
methane/air blend;
-
€6,8 million to buy methane and oxygen in the new
methane/oxygen blend. |