Title: Cement Kilns Overview
1Cement Kilns - Overview
- Prepared for the CEC North American Strategy for
Catalyzing Cooperation on Dioxins, Furans and HCB - Source Control Workshop
- April 17-18, 2008
- Leon, Guanajuato, Mexico
2Cement Kilns - Overview
- Cement is manufactured by burning limestone in
high temperature kilns to produce clinker, which
is then ground and blended with additives to
produce cement - Cement is the glue used to make concrete, a key
construction material used for infrastructure - Feed materials can include limestone, chalk,
sand, shale, marl, etc. - Fuels include coal, petroleum coke, oil, gas and
alternative fuels such as - tires, tire derived fuel (TDF), spent solvents,
hazardous wastes, etc. - Use of alternative fuels can offset fuel costs,
as generally more cost-effective - The combustion process in the kiln has the
potential to result in the formation and
subsequent release of dioxins/furans and HCB. - Cement kilns firing hazardous waste are noted as
having relatively high potential for the
formation and release of dioxins/furans, HCB, and
unintentional PCBs (UNEP Stockholm Convention on
POPs)
3Cement typical dry kiln system(Source
CEMBUREAU. Best Available Techniques for the
Cement Industry, December 1999
http//www.cembureau.be)
4General Measures 1
- For new plants and major upgrades, dry kiln
system with multi-stage preheating and
precalcination is considered state-of-the-art. - Cement plants typically use dust (particulate
matter) control measures. BAT for dust control
include - Electrostatic precipitators with appropriate
monitoring/ control equipment to minimize the
number of CO trips - Fabric filters with bag leak detectors
- Achievable performance 20 to 30 mg/m3
- May also have measures to prevent or reduce
emissions of - NOx low-NOx burners, selective non-catalytic
reduction (SNCR), selective catalytic reduction
(SCR) - SO2 absorbent injection, dry scrubber, wet
scrubber, activated carbon, switching to low
sulphur fuels and/or feeds.
1 European Commission, Reference Document on Best
Available Techniques in the Cement and Lime
Manufacturing Industries, December 2001,
http//eippcb.jrc.es/pages/FActivities.htm
5Primary Measures 1
- Examples
- Process optimization
- rapid cooling of off-gases to below 200OC
- Characterize and monitor parameters that
corresponde to good operation - Maintain stable operating conditions
- Minimize fuel and energy use with use of
preheating nad precalcination - Pretreatment of wastes to enable a more
homogeneous feed and stable combustion conditions - Avoid use of waste derived fuel during start-up
and shutdown - Waste should be fed through the main burner, or
secondary burner for preheater/precalciner kilns.
- For secondary burners, combustion zone
temperature should be maintained at gt850OC for a
residence time of 2 sec.
1 Part II Source Category (b) Cement kilns
firing hazardous waste, Revised Draft Guidelines
On Best Available Techniques And Provisional
Guidance On Best Environmental Practices Relevant
To Article 5 And Annex C Of The Stockholm
Convention On Persistent Organic Pollutants,
December 2006, http//www.pops.int/documents/guida
nce/batbep/batbepguide_en.pdf
6Secondary Measures 1
- Improvement of dust abatement, ESP or fabric
filter - Achievable performance of 20 to 30 mg/m3
- Activated carbon injection (combined with use of
fabric filters) - Activated carbon filter
- Selective catalytic reduction (SCR)
- Note, may required increased fuel use for
reheating of off-gases - Achievable performance based on BAT for control
of D/F should be lt 0.1 ng ITEQ/Nm3 with reference
conditions of 273 K, 101.3 kPa, 11 O2, dry gas
basis.
1 Part II Source Category (b) Cement kilns
firing hazardous waste, Revised Draft Guidelines
On Best Available Techniques And Provisional
Guidance On Best Environmental Practices Relevant
To Article 5 And Annex C Of The Stockholm
Convention On Persistent Organic Pollutants,
December 2006, http//www.pops.int/documents/guida
nce/batbep/batbepguide_en.pdf