Title: Plasma Electrodynamics
1Electron Scrubbing of Flue Gases to Remove
Unwanted By-Products
- History of electron beam dry scrubbing(EBDS)
system - EBDS Process Description
- e-Scrub Requirements
- SOx and NOx removal requirements
- EBDS cost estimates and technology comparison
- HPTA technology vs. conventional electron-beam
guns - HPTA Technology Development
- DOD technology overview
- HPTA technology overview
- Power-conditioning subsystem description
- Electron-beam gun design
- e-Scrub Project Description
2What is EBDS ?
- A single-step method for the simultaneous
removal of SOx and NOx from flue emissions - Appropriate for use by boilers burning
high-sulfur coal or incinerators burning
municipal solid waste (MSW) - Removal efficiencies of approximately 90 for
both SO2 and NOx at high overall process energy
efficiency and low-energy consumption - In coal burning facilities, the flue gas with
small amount of ammonia is irradiated with an
electron beam, causing reactions that convert the
SO2 and NOx to ammonium sulfate or ammonium
sulfate-nitrate (salts) - --gt salts collected by the conventional methods
such as moving-gravel-bed filters or wet
electrostatic participators(ESP) may be sold as
fertilizer - For flue gases from MSW incinerators, the EBDS
process uses either sodium or calcium hydroxide
for the reagent
3History of EBDS System
Need update !
4Alternative Technologies of EBDS
- Wet limestone slurry scrubbing for removing SO2
(de-SOx) plus selective catalytic reduction (SCR)
for removing NOx (de-NOx) - Advanced limestone wet scrubbing combined with
advanced SCR - ( Low energy electron scrubbing by corona
discharges ) - Advantages of EBDS
- Increased efficiency as the sulfur contents of
coal increases - Highly efficient removal of both SO2 and Nox
from flue gas in a single process. - Easily controlled and has excellent
load-following capability - Stack gas heat is not required
- The pollutants and by-products are converted
into a marketable agricultural fertilizer
5Obstacles and Promising Design of EBDS
- Obstacles of conventional electron-beam
generators - Too small a module power (factor of 5-10)
- Too large a module size (factor of 2)
- Too great a module cost (factor of 3-4)
- New design
- DOD in 1992 developed a design for a
high-average-power electron-beam generator based
on high-power transformer accelerator (HPTA)
technology - 1993 initiation of e-Scrub program
- develop a cost-effective, high-average-power
electron-beam generator using HPTA technology - integrate EBDS technology with the new
electron-beam generator in a power plant - ultimately provide for a complete technology
transfer to the private sector
6Simplified Flow Schematic of the EBDS Process
exhaust
Electrostatic participators
salts
Lower Tg add humidity
fertilizer
7Reaction Mechanisms of EBDS Process
Genuario and Brown (1993)
8EBDS Process Characteristics
- SO2 removal efficiency gt 95
- comparable to that of an advanced wet scrubbing
process - depends on gas relative humidity, NH3
stoichiometry ,and electron-beam dose (energy
absorbed per mass of flue gas, 1Mrad10kGy4.13Btu
/lb) - mostly by a thermal reaction with the NH3 and
water vapor, remainder by the radiation-induced
oxidation of SO2 to SO3 via reaction with OH - Ammonium sulfate by-product likely forms from a
heterogeneous reaction between gaseous ammonia
and nucleating sulfuric acid droplets - NOx removal efficiency
- primarily dependent on electron-beam-initiated
chemistry via the formation of specific oxidative
radical species such as OH and HO2 - Ammonium nitrate by-product directly formed
homogeneously from gaseous nitric acid and
ammonia - non-linearity with the electron-beam dose
- positive impact of increased initial SO2
concentration
9EBDS Process Summary
10SOx and NOx Removal Requirements
To meet already strict SO2 removal requirements
as well as the looming potential for very strict
NOx reduction, a combination of low-NOx burner
(LNB) and EBDS to achieve 85-91 NOx and over 90
SOx removal levels is envisioned.
11EBDS Cost Estimates
12EBDS Cost Estimates
FGD (wet limestone flue-gas desulfurization) SCR
(selective catalytic reduction) for de-NOx
13Cost Comparison with fertilizer by-product value
14Cost Comparison with electron gun cost
15Cost Comparison with e-Scrubber by-product value
16Cost Comparison
17DOD Technology Overview
18(No Transcript)
19Power-Conditioning Subsystem Description
20Electron-Beam Gun Design
21E-Scrub Project Description