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ECC - - Ethylene Cracking Heaters Brochure
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By controlling flame shape on both the hearth
burner and radiant wall burners, enhanced tai-
loring of the heat flux profile should be achieved.
Lengthening the de-coking cycle will bring sub-
stantial economic benefits to operators of ethylene
cracking furnaces. The period of a de-coking cy-
cle varies depending on the process and technol-
ogy. Under the worst-case scenario, de-coking
must be performed after as little as less than 20
days, while under the best-case scenario, de-cok-
ing occurs every six months. Improvements in
de-coking cycles represents less downtime and
more revenue. Additionally, by improving flame
luminosity, ECC may provide far greater control
(a new degree of freedom) for operators to sig-
nificantly increase heat flux transfer to the process
tubes while still maintaining optimal uniformity.
The ECC™ Solution
Limitations in the ability to optimize burner per-
formance (i.e., meeting NOx objectives while
optimizing flame geometry) create challenges in
delivering uniform heat flux profiles. Most heat-
ers experience higher heat flux profiles near the
bottom of the furnace with fluxes gradually de-
creasing with furnace height. Delivering a more
uniform heat flux profile is desirable because it
has the potential to 1) improve energy exchange
and 2) lengthen the de-coking cycle.
The Problem
Ethylene Cracking Heaters
Ethylene is an important chemical widely used in
the production of plastics for products such as PVC,
packaging, and window frames, among others.
The product is obtained by the pyrolysis of naph-
tha, ethane or propane. Currently there are 45
ethylene plants in the United States, 90% of which
use gaseous feedstock. Due to expanded world
demand, it has also experienced rapid growth.
An ethylene cracking furnace is a tall and narrow
box -- typically 40ft+ high -- with vertical process
tubes on one side and a combustion wall’ on the
other. They use burners of two types: The first,
‘hearth’ burners are rectangular, floor mounted,
vertical-firing against the combustion wall to radi-
ate heat into the tubes on the opposite wall. The
second, ‘radiant wall’ burners are installed in one
to four rows at various furnace heights and fire
radially onto the combustion wall to heat up the
refractory surface and radiate energy to the pro-
cess tubes. These two burner types are designed
and installed to try to maintain a uniform heat flux
profile to the process tubes.
Ethylene Cracking Plant
www.ClearSign.com
Contact Us
Phone: (206) 673-4848
Fax: (206) 299-3553
Email: info@clearsigncombustion.com
12870 Interurban Avenue South Seattle, WA 98168 ©2013 ClearSign Combustion Corporation. All rights reserved.
Petrochemical ProcessingImproved Heat Flux Uniformity
Improved Ethylene Heat Flux Profile - De-Coking
Cycle Increase
Ethylene/Poly plants in US 45 Facilities
Polypropylene Spot Price $0.63 per lb.
Ethylene Spot Price $0.75 per lb.
Plant Capacity (liquid feed) 120,000 lb/hr
Number of Furnaces 6
Yield Efficiency (est.) 45% per year
Product Revenue $336MM per year
Product Profit $219MM
Margin 62.5%
ECC™ .75% Capacity Increase $1.6MM Incr. Annual Profit
ECC™ 2% Capacity Increase $4.4MM Incr. Annual Profit
This benefit will impact two areas:
Summary of ECC™ Annual Economic Impact on
Ethylene Processing
Low Est. High Est.
Extending De-Coking Cycles $1.6MM $4.4MM
Increased Capacity $2.2MM $4.4MM
Total $3.8MM $8.8MM
Although de-coking cycles vary depending on feed-
stock, technology and operating practices, we could
make a conservative assumption that an ethylene
heater retrofitted with ECC could enhance the de-cok-
ing cycle from every four months to every six months.
Sometimes increasing capacity in an ethylene heater
does not provide any benefit because downstream
equipment (e.g., distillation towers, compressors) may
not be able to accommodate the increase. However,
in cases where a capacity increase can be handled
plant-wide, we can calculate the economic benefit as-
sociated with a 1-2% capacity increase.
Increasing Capacity Increasing De-Coking Cycles
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