Þrefallt notið góðs af landi fyllt og Ponded Flúðahæl

1.7+ billion tons of fly ash are primarily found in landfills or ponded impoundments…and 40 million tons of fly ash continue to be disposed of annually. …interest in recovering this disposed material has increased, að hluta til vegna eftirspurnar eftir hágæða Fly Ash fyrir steypu og sementframleiðslu á tímabili með minni framleiðslu sem kol-rekinn máttur kynslóð hefur minnkað í Evrópu og Norður-Ameríku. Áhyggjur af langtímaumhverfisáhrifum slíkra urðunarstaðanna eru einnig tafarlaus tól til að finna gagnleg forrit fyrir þetta geymda Ash.

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Þrefallt notið góðs af landi fyllt og Ponded Flúðahæl

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Triboraffastan rétthafa á

Land Filled and Ponded Fly Ash

By Lewis Baker, Abhishek Gupta, Stephen Gasiorowski, and Frank Hrach

The American Coal Ash Association (ACAA) annual survey of production and use of coal fly ash reports that between 1966 og 2011, Yfir 2.3 billion short tons of fly ash have been produced by coal-fired utility boilers.1 Of this amount approximately 625 million tons have been beneficially used, mostly for cement and concrete production. þó, the remaining 1.7+ billion tons are primarily found in landfills or filled ponded impoundments. While utilization rates for freshly generated fly ash have increased considerably over recent years, with current rates near 45%, um það bil 40 million tons of fly ash continue to be disposed of annually. While utilization rates in Europe have been much higher than in the US, considerable volumes of fly ash have also been stored in landfills and impoundments in some European countries.

Nýverið, áhugi á að endurheimta þetta losaði efni hefur aukist, að hluta til vegna eftirspurnar eftir hágæða Fly Ash fyrir steypu og sementframleiðslu á tímabili með minni framleiðslu sem kol-rekinn máttur kynslóð hefur minnkað í Evrópu og Norður-Ameríku. Áhyggjur af langtímaumhverfisáhrifum slíkra urðunarstaðanna eru einnig tafarlaus tól til að finna gagnleg forrit fyrir þetta geymda Ash.

LAND FYLLT ASH GÆÐI OG NAUÐSYNLEGUR VIÐTAKENDUR

While some of this stored fly ash may be suitable for beneficial use as initially excavated, the vast majority will require some processing to meet quality standards for cement or concrete production. Since the material has been typically wetted to enable handling and compaction while avoiding airborne dust generation, drying and deagglomeration is a necessary requirement for use in concrete since concrete producers will want to continue the practice of batching fly ash as a dry, fine powder. þó, assuring the chemical composition of the ash meets specifications, most notably the carbon content measured as loss-on-ignition (LOI), is a greater challenge. As fly ash utilization has increased in the last 20+ Ára, most “in-spec” ash has been beneficially used, and the off-quality ash disposed. Thus, LOI reduction will be a requirement for utilizing the vast majority of fly ash recoverable from utility impoundments.

LOI REDUCTION BY TRIBOELECTRIC SEPARATION

While other researchers have used combustion techniques and flotation processes for LOI reduction of recovered landfilled and ponded fly ash, ST Equipment & Tækni (STET) has found that its unique triboelectrostatic belt separation system, lengi notað fyrir viðtakendur nýmynduðum fljúgandi Ash, is also effective on recovered ash after suitable drying and deagglomeration.

STET researchers have tested the triboelectrostatic separation behavior of dried landfilled ash from several fly ash landfills in the Americas and Europe. Þessi endurheimti Ash aðskilin mjög álíka að nýmynduðum ösku með einum óvæntan mismun: í agnahleðslu var snúið úr því að ferskari aska með kolefnislífhleðslu neikvæð í tengslum við steinullarmagnið.2 Aðrar rannsóknir á rafstöðuskilrúmum á Fly Ash kolefni hafa einnig fylgt þessu fyrirbæri.3,4,5 The polarity of the STET triboelectrostatic separator can easily be adjusted to allow rejection of negatively charged carbon from dried landfilled fly ash sources. No special modifications to the separator design or controls are necessary to accommodate this phenomena.

YFIRLIT YFIR TÆKNI – FLJÚGANDI KOLEFNISATÓMINN AÐSKILNAÐUR

Í STET Carbon Skilrúm (Mynd 1), efni er fóðraður í þunna bilið milli tveggja samsíða planar rafskaut. Þær agnir sem eru mjög hlaðnar með interagnið snertileysi. Hið jákvæða innheimt kolefni og neikvæð innheimt steinefni (í nýmynduðum ösku sem ekki hefur verið bleytt og þurrkuð) eru dregnar saman á móti rafskaut. Agnirnar eru síðan sópaðar upp af samfelldu hreyfanlegum beltum og settar í gagnstæðar áttir. Beltið flytur agnir sem eru samliggjandi við hverja rafall í átt að gagnstæðum endum skiltisins. Hár beltahraði gerir einnig mjög mikil gegnumsnúningshraði, allt að 36 tonnum á klukkustund á einni skilvindu. Litla bilið, háspennulínur í háaleit, Teljari núverandi flæðis, vigorous particle-particle agitation and self-cleaning action of the belt on the electrodes are the critical features

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of the STET separator. Með því að stýra ýmsum ferlistikum, eins og beltahraði, straumur punktur, og straumhraði, STET ferlið framleiðir lágt LOI fljúga ösku á kolefnisinnihaldi minna en 1.5 að 4.5% from feed fly ashes ranging in LOI from 4% að yfir 25%.

Mynd. 1 STET Separator processing dried, landfilled fly ash

The separator design is relatively simple and compact. Vél hönnuð til vinnslu 40 tons per hour is approximately 30 Ft. (9 m.) Langur, 5 Ft. (1.5 m.) wide, og 9 Ft., M (2.75 m.) Hár. Beltið og tengd rollinum eru einu Hreyfðu hlutar. Rafskaut eru kyrrstætt og samsett úr viðeigandi varanlegum efnum. The belt is made of non-conductive plastic. The separator’s power consumption is about 1 kílóvattstund á tonn af efni sem unnið er með mest af krafti sem neytt er af tveimur mótorum sem aka beltinu.

Ferlið er algjörlega þurrt, requires no additional materials other than the fly ash and produces no waste water or air emissions. The recovered materials consist of fly ash reduced in carbon content to levels suitable for use as a pozzolanic admixture in concrete, and a high carbon fraction useful as fuel. Nýting beggja afurðastrauma veitir 100% lausn til að fljúga aska förgun vandamál.

PROASH® RECOVERED FROM LAND FILLS

Four sources of ash were obtained from landfills: sample A from a power plant located in the United Kingdom and samples B, C, and D from the United States. All these samples consisted of ash from the combustion of bituminous coal by large utility boilers. Due to the intermingling of material in the landfills, no further information is available concerning specific coal source or combustion conditions.

The samples as received by STET contained between 15% og 27% water as is typical for landfilled material. The samples also contained varying amounts of large >1/8 inch (~3 mm) material. Að undirbúa sýnunum fyrir kolefnisaðskilnað, mikið rusl var fjarlægt með skimun og sýnin síðan þurrkuð og deagglomerated áður en Kolsýringur. Several methods for drying/deagglomeration have been evaluated at the pilot-scale in order to optimize the overall process. STET has selected an industrially proven, feed processing system that offers simultaneous drying and deagglomeration necessary for effective electrostatic separation. Almennt ferli flæðablað er sett fram á mynd 2.

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Mynd 2: Process Flow Diagram

Eiginleikar tilbúinna Sýna voru vel innan marka fljúga Ash fengin beint frá venjulegum gagnsemi Kötlum. Viðeigandi Eiginleikar fyrir bæði aðgreiningarstrauma og afurðir eru teknar saman í töflu 2 ásamt endurheimtu vöru.

KOLEFNISSAÐSKILNAÐINN

Carbon reduction trials using the STET triboelectric belt separator resulted in very good recovery of low LOI products from all four landfill fly ash sources. The reverse charging of the carbon as discussed above did not degrade the separation in any way as compared to processing fresh ash.

The properties of the low LOI fly ash recovered using the STET process for both freshly collected ash from the boiler and ash recovered from the landfill is summarized in Table 1. The results show that the product quality for ProAsh® produced from landfilled material is equivalent to product produced from fresh fly ash sources.

Table 1: Properties of feed and recovered ProAsh®.

Feed Sample to Separator

LOI

ProAsh LOI®

ProAsh® Fineness, % +325 mesh

ProAsh® Mass Yield

Fresh A

10.2 %

3.6 %

23 %

84 %

Landfill A

11.1 %

3.6 %

20 %

80 %

Fresh B

5.3 %

2.0 %

13 %

86 %

Landfill B

7.1 %

2.0 %

15 %

65 %

Fresh C

4.7%

2.6%

16%

82%

Landfill C

5.7%

2.5%

23%

72 %

Landfill D

10.8 %

3.0 %

25 %

80 %

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PERFORMANCE IN CONCRETE

The properties of the ProAsh® generated from the reclaimed landfill material were compared to that of ProAsh® produced from fresh fly ash generated by the utility boilers from the same location. The processed reclaimed ash meets all the specifications of ASTM C618 and AASHTO M250 standards. The following table summarizes the chemistry for samples from two of the sources showing the insignificant difference between the fresh and reclaimed material.

Table 2: Ash efnafræði Low LOI Ash.

Material Source

SiO2

Al2O3

Fe2O3

CaO

MgO

K2O

Na2O

SO3

Fresh B

51.60

24.70

9.9

2.22

0.85

2.19

0.28

0.09

Landfilled B

50.40

25.00

9.3

3.04

0.85

2.41

0.21

0.11

Fresh C

47.7

23.4

10.8

5.6

1.0

1.9

1.1

0.03

Landfilled C

48.5

26.5

11.5

1.8

0.86

2.39

0.18

0.02

Styrkja þróun á 20% substitution of the low LOI fly ash in a mortar containing 600 lb cementitious/ yd3 (Sjá töflu 3 below) showed the ProAsh® product derived from landfilled ash yielded mortars with strength comparable to mortars produced using ProAsh® from fresh fly ash produced at the same location. The end product of the beneficiated reclaimed ash would support high end uses in the concrete industry consistent with the highly valuable position ProAsh® enjoys in the markets it currently serves.

Table 3: Compressive strength of mortar cylinders.

7 day Compressive Strength, % of fresh ash control

28 day Compressive Strength, % of fresh ash control

Fresh B

100

100

Landfilled B

107

113

Fresh C

100

100

Landfilled C

97

99

PROCESS ECONOMICS

The availability of low cost natural gas in the USA greatly enhances the economics of drying processes, including the drying of wetted fly ash from landfills. Table 4 summarizes the fuel costs for operations in the USA for 15% og 20% raki innihald. Dæmigerðar óhagstæðar þurrkarar eru innifaldir í útreiknuðum gildum. Kostnaður miðast við massa efnis eftir þurrkun. The incremental costs for drying fly ash for STET triboelectrostatic separation processing are relatively low.

Table 4: Þurrkun kostar á grundvelli þurrkaðra massa.

Rakt efni

Heat Requirement KWhr/T wet basis

Þurrkkostnaður / T dry basis (Nat Gas cost $3.45 / Mmbtu)

15 %

165

$ 2.28

20 %

217

$ 3.19

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Even with the addition of feed drying costs, the STET separation process offers a low cost, industrially proven, process for LOI reduction of landfilled fly ash. The STET process for reclaimed fly ash is one-third to one-half of the capital cost compared to combustion based systems. The STET process for reclaimed fly ash also has significantly lower emissions to the environment compared to combustion or flotation based systems. Since the only additional air emission source to the standard STET process installation is a natural gas-fired dryer, permitting would be relatively simple.

RECOVERED FUEL VALUE OF HIGH-CARBON FLY ASH

In addition to the low carbon product for use in concrete, brand named ProAsh®, the STET separation process also recovers otherwise wasted unburned carbon in the form of carbon-rich fly ash, branded EcoTherm. EcoThermhas significant fuel value and can easily be returned to the electric power plant using the STET EcoThermReturn system to reduce the coal use at the plant. When EcoThermis burned in the utility boiler, the energy from combustion is converted to high pressure / high temperature steam and then to electricity at the same efficiency as coal, typically 35%. The conversion of the recovered thermal energy to electricity in ST Equipment & Technology LLC EcoThermReturn system is two to three times higher than that of the competitive technology where the energy is recovered as low-grade heat in the form of hot water which is circulated to the boiler feed water system. EcoThermis also used as a source of alumina in cement kilns, displacing the more expensive bauxite which is usually transported long distances. Utilizing the high carbon EcoThermhæhæ annað hvort á orkuverksmiðju eða sementsbundið Kiln, hámarkar orkuendurheimt frá afhentu grófu, draga úr þörfinni til minja og flytja viðbótareldsneyti til aðstæðna.

STET’s Talen Energy Brandon Shores, SMEPA R. D. Morrow, NBP Belledune, RWEnpower Didcot, EDF Energy West Burton, RWEnpower Aberthaw, and the Korea South-East Power fly ash plants all include EcoTherm™ Skilakerfi.

STET ASH PROCESSING FACILITIES

STET’s separation process has been used commercial since 1995 for fly ash beneficiation and has generated over 20 million tons of high quality fly ash for concrete production. Controlled low LOI fly ProAsh®, is currently produced with STET’s technology at eleven power stations throughout the U.S., Canada, the U.K., poland, and Republic of Korea. ProAsh® fly ash has been approved for use by over twenty state highway authorities, sem og margar aðrar tilgreiningar stofnana. ProAsh® has also been certified under Canadian Standards Association and EN 450:2005 gæðastöðlum í Evrópu. Ash processing facilities using STET technology are listed in Table 5.

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Table 5. Fly Ash Processing facilities using STET separation technology

Gagnsemi / Power Station

Staðsetning

Start of Commercial operations

Facility Details

Duke Energy – Roxboro-stöðin

Norður-Karólína Bandaríkin

Sept. 1997

2

Skiltákn

Talen orka – Brandon Shores Station

Maryland Bandaríkin

apríl 1999

2

Skiltákn 35,000 ton storage dome. EcothermReturn 2008

ScotAsh (Lafarge / ScottishPower Joint Venture) – Longannet-stöðin

Skotland Bretland

október. 2002

1

Skiltákn

Jacksonville Electric AuthoritySt. John’s River Power Park, FL

Flórída Bandaríkin

maí 2003

2

Separators Coal/Petcoke blends Ammonia Removal

South Mississippi Electric Power Authority R.D. Morrow Station

Mississippi Bandaríkin

Jan. 2005

1

Separator EcothermReturn

New Brunswick Power Company Belledune Station

New Brunswick, Canada

apríl 2005

1

Separator Coal/Petcoke Blends EcothermReturn

RWE npower Didcot Station

England Bretland

ágúst 2005

1

Separator EcothermReturn

Talen Energy Brunner Island Station

Pennsylvanía Bandaríkin

desember 2006

2

Skiltákn 40,000 Ton storage dome

Tampa Electric Co. Big Bend Station

Flórída Bandaríkin

apríl 2008

3

Skiltákn, tvöfaldur passi 25,000 Ton storage dome Ammonia Removal

RWE npower Aberthaw Station (Lafarge Cement UK)

Wales Bretland

September 2008

1

Separator Ammonia Removal EcothermReturn

EDF Energy West Burton Station (Lafarge Cement UK, Cemex)

England Bretland

október 2008

1

Separator EcothermReturn

ZGP (Lafarge Sement Pólland / Ciech Janikosoda JV)

poland

mars 2010

1

Skiltákn

Korea South-East Power Yeongheung Units 5&6

Suður-Kórea

September 2014

1

Separator EcothermReturn

PGNiG Termika-Siekierki

poland

Áætluð 2016

1

Skiltákn

ZAK -Energo Ash

poland

Áætluð 2016

1

Skiltákn

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CONCLUSIONS

After suitable scalping of large material, drying, and deagglomeration, fly ash recovered from utility plant landfills can be reduced in carbon content using the commercialized STET triboelectric belt separator. The quality of the fly ash product, ProAsh® using the STET system on reclaimed landfill material is equivalent to ProAsh® produced from fresh feed fly ash. The ProAsh® product is very well suited and proven in concrete production. The recovery and beneficiation of landfilled ash will provide a continuing supply of high quality ash for concrete producers in spite of the reduced production of “fresh” ash as coal-fired utilities reduce generation. Additionally, power plants that need to remove ash from landfills to meet changing environmental regulations will be able to utilize the process to alter a waste product liability into a valuable raw material for concrete producers. The STET separation process with feed pre-processing equipment for drying and deagglomerating landfilled fly ash is an attractive option for ash beneficiation with significantly lower cost and lower emissions compared to other combustion and flotation based systems.

TILVÍSANIR

[1]American Coal Ash Coal Combustion products and Use Statistics: http://www.acaa- usa.org/Publications/Production-Use-Reports.

[2]ST internal report, ágúst 1995.

[3]Li,T.X,. Schaefer, J.L., Ban, H., Neathery, J.K., and Stencel, J.M. Dry Beneficiation Processing of Combustion Fly Ash, Proceedings of the DOE Conference on Unburned Carbon on Utility Fly Ash, maí 19 20, Pittsburgh, PA, 1998.

[4]Baltrus, J.P., Diehl, J.R., Soong, Y., Sands, W. Triboelectrostatic separation of fly ash and charge reversal, Fuel 81, (2002) pp.757-762.

[5]Cangialosi, F., Notarnicola, M., Liberti, L, Stencel, J. The role of weathering on fly ash charge distribution during triboelectrostatic beneficiation, Journal of Hazardous Materials, 164 (2009) pp.683-688.

AUTHORS

Lewis Baker is the European Technical Support Manager for ST Equipment & tækni (STET) based in the United Kingdom

Abhishek Gupta is a Process Engineer based at the Separation Technologies pilot plant and lab facility, STET Technical Center, 101 Hampton Ave, Prjóninn MA 02494 +1-781-972-2300

Dr. Stephen Gasiorowski, Ph.D. is a Senior Research Scientist for ST Equipment & tækni (STET) based in the New Hampshire.

Frank Hrach is Vice President of Process Engineering based at the Separation Technologies pilot plant and lab facility, STET Technical Center, 101 Hampton Ave, Prjóninn MA 02494 +1-781-972-2300