Top Banner
Biomass specialisation course Review of Gasification Plants Jesús Arauzo, Alberto Gonzalo, José L. Sánchez ([email protected]) Chem.&Environ. Eng. Dpt. C.P.S.
53
Welcome message from author
This document is posted to help you gain knowledge. Please leave a comment to let me know what you think about it! Share it to your friends and learn new things together.
Transcript
Page 1: gasifiers

Biomass specialisation course

Review of Gasification Plants

Jesús Arauzo, Alberto Gonzalo, José L. Sánchez ([email protected])

Chem.&Environ. Eng. Dpt.

C.P.S.

www.cps.unizar.es/~proter

Page 2: gasifiers

Gasification Plants

Configuration of a gasification plant depends on:- Fuel to be used- Type of reactor:

- fixed/moving bed- fluidized bed- entrained flow- combination

- Operation pressure (near atmospheric or pressurired)- Method to deliver the heat needed for reaction- End use of producer gas gas cleanup

There are so many different configurations possible, that it is difficult to find two similar plants in the world

Page 3: gasifiers

Gasification Plants

Review of some of the most representative plants/projects,sorted by the kind of reactor used:

- Fixed bed gasifiersUpdraftDowndraft

- Fluidized bed gasifiersBubbling FBCirculating FB

- Entrained bed gasifiers- “Special” Plants with a combination of reactors:

Compact Power processCarbo V process

Page 4: gasifiers

Gasification PlantsFixed Bed

FB UPDRAFT GASIFICATION

Babcock & Wilcox Vølund ApS

Put into operation in 1993, in the city ofHarboøre, to supply heat to 560 homesand municipal buildings.Fuelled by wood chips.Initially the producer gas was burnt in aboiler.After several years of research on gascleaning, in 2000 two 750 kWe Jenbachergas engines were set in operation

Page 5: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

OIL/TAR FUELLED DISTRICT HEATING BOILER

Page 6: gasifiers

UPDRAFT WOOD GASIFIER

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

Page 7: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

FUEL AND ASH HANDLING SYSTEM

Page 8: gasifiers

PRODUCER GAS FIRED DISTRICT HEATING BOILER

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

Page 9: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

GAS CLEANING SYSTEM

Page 10: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

HEAVY TAR SEPARATION SYSTEM

Page 11: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

GAS ENGINES

Page 12: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

TARWATC (FINAL WATER CLEAN UP)

Page 13: gasifiers

Gasification PlantsFixed Bed

Babcock & Wilcox Vølund ApS

Page 14: gasifiers

Gasification PlantsFixed Bed

FB DOWNDRAFT GASIFICATION

Combined Cycle Heat and Power PlantProject TU Bergakademie Freiberg

PPS Pipeline Systems GmbH

The technology is result of the research at the TU Bergakademie Freiberg in

cooperation with the Institute forInternational Forestry and WoodManagement at the TU Dresden

Page 15: gasifiers

Gasification PlantsFixed Bed

Project TU Bergakademie Freiberg - PPS Pipeline Systems GmbH

Based on a IGCC conceptProducer gas is burned in a combustionchamberCombustion flue gas is used in a hightemperature heat exchanger to heatfresh air, which is used to move thegas turbineThus, gas cleaning and the technicalrisk for gas turbine operation are mi-nimised

Page 16: gasifiers

Gasification PlantsFixed Bed

Project TU Bergakademie Freiberg - PPS Pipeline Systems GmbH

Page 17: gasifiers

Gasification PlantsFixed Bed

Project TU Bergakademie Freiberg - PPS Pipeline Systems GmbH

Clean wood consumed: 2500 kg/hHeating value of wood: 13.6 MJ/kgHeating value of producer gas: 5 MJ/kgCombustion chamber temperature: 980ºCHot air temperature: 800ºCGas turbine power generation: 1.3 MWSteam turbine power generation: 0.7-1 MWHeat output: 4.5 MW

Page 18: gasifiers

Gasification PlantsFluidized Bed

BUBBLING FLUIDIZED BED GASIFICATION

Plastics Gasification Plant Poligas Ambiente

Biosyn Technolgy developed byKemestrie (spinoff company of theUniversity of Sherbrook, Canada)The plant is located in Ribesalbes (Castellón).Gasifies 15000 ton/year of plastic residues from the ceramic industry

Page 19: gasifiers

Gasification PlantsFluidized Bed

Plastics Gasification Plant Poligas Ambiente

Gasifier feed rate: 3000 kg/hRaw material: PE and PP residuesStart-up finished at the end of 2002Gasifying medium: O2-enriched air (40% O2)Fuel gas composition:

30-55% N2

16-30% CO2

12-30% CO2-10% H2

Gas HHV: 12 MJ/Nm3

8.4 MWe are generated by 11 760-kWe Jenbacher EnginesSolid residues are vitrified with natural gas

Page 20: gasifiers

Gasification PlantsFluidized Bed

Plastics Gasification Plant Poligas Ambiente

Page 21: gasifiers

Gasification PlantsFluidized Bed

Plastics Gasification Plant Poligas Ambiente

Page 22: gasifiers

Gasification PlantsFluidized Bed

CIRCULATING FLUIDIZED BED GASIFICATION

Atmospheric air CGB gasification for heat production:Lahti Gasifier at Kymijärvi CHP Power Plant

Pressurised air IGCC producing hot fuel gas:Sydkraft Project at Värmano

Atmospheric air IGCC producing cold fuel gas:ARable Biomass Renewable Energy (ARBRE)

Dual bed atmospheric steam IGCC:FERCO-Silvagas plant at Vermont

Page 23: gasifiers

Gasification PlantsFluidized Bed

Atmospheric air gasification in CFB for heat production:Lahti Gasifier at Kymijärvi CHP Power Plant

The plant is located near the city of Lahti (Finland)The 350 MW power plant runs on pulverized coal combustionThe 60 MWth gasifier was added in 1998, suppliedby Foster Wheeler Energia OyFuelled by: waste wood, packaging wastes,tyres, forest residues, replacing 15% offossil fuelProducer gas is fed into the coal boiler,to produce heat and steamInvestment of 14 M€

Page 24: gasifiers

Gasification PlantsFluidized Bed

Lahti Gasifier at Kymijärvi CHP Power Plant

Page 25: gasifiers

Gasification PlantsFluidized Bed

Lahti Gasifier at Kymijärvi CHP Power Plant

Gas composition (at 50% feed moisture):CO2 – 12.9%H2 – 5.9%N2 – 40.2%CO – 4.6%CxHy – 3.4%H2O – 33%LHV – 2.2 MJ/Nm3

Page 26: gasifiers

Pressurised air IGCC producing hot fuel gas: Sydkraft Project at Värmano

Gasification PlantsFluidized Bed

The plant was built between 1991 and 1993.Demonstration programme concluded in October 1999First IGCC installation which worked at near commercial scaleThe plant run on gasifying operationfor more than 8500 hours and thegas turbine run on producer gasfor more that 3600 hoursFuels tested include:

barkWood chipsSalixStrawRDF

Page 27: gasifiers

Sydkraft Project at Värmano

Gasification PlantsFluidized Bed

- The gasification technology hasbeen developed in cooperationbetween Sydkraft AB and FosterWheeler Energy International- The gas turbine was supplied by Alstom Power, with an electricaloutput of 4.2 MWe. A steam turbine produces 1.8 MWe- Thermal output 9 MWth- Biomass feed rate: 4300 kg/h- Air flow rate: 6500 kg/h- Pressure of operation: 18-22 bar- Hot gas cleaning system to avoidtar condensation

Page 28: gasifiers

Sydkraft Project at Värmano

Gasification PlantsFluidized Bed

Page 29: gasifiers

Feeding a mixture of bark, logging residues & waste woodat 5-25% moisture content:LHV of 18,9 MJ/kg.Carbon conversion in the gasifier: 97-98%.Gas LHV: 4.2-4.6 MJ/kg (does not include benzene and tar content)Gas composition (% in volume):

 H2 - 11 %

CO - 16 %CO2 -12  %

CH4 -5 %

H2O - 12 %

N2 - 44 %

1300-1700 ppm NH3 , 9000 mg/m3 benzene, 3500 mg/m3 light tar,

500 mg/m3 heavy tarAsh from the cyclone: 15-20% de unburned carbon and 65-75% bed materialAsh from the bed: 0,2-0,5 % UC and 75-80% BM.

Sydkraft Project at Värmano

Gasification PlantsFluidized Bed

Page 30: gasifiers

Atmospheric air IGCC producing cool fuel gas: ARBRE Project

Gasification PlantsFluidized Bed

The gasifier is an atmospheric pressure, air-blown circulating fluidizedbed system, developed by TPS of Sweden Construction began in 1998Feed material: wood (from conventional forestry and short-rotationplantation sites)Electrical output of 8 MWe,overall electrical eficiencyof 31%Cool clean producer gasis compressed to feed thegas turbine

Page 31: gasifiers

ARBRE ProjectGasification PlantsFluidized Bed

Page 32: gasifiers

Gasification PlantsFluidized Bed

Dual circulating fluid bed steam gasification:FERCO-SilvaGas™ Process Plant at Vermont

The SilvaGas process was developed by Batelle´s ColumbusLaboratories in 1970’s-80’sFuture Energy Corporation (FERCO) comercialices and has furtherdepeloped the technologyAfter more than 20000 hours of gasifying experience in a Process Research Unit (PRU) of 10 ton per day, FERCO constructed a 200 ton/d plant, located at BurlingtonElectric’s McNeil Power Station in VermontIn a first phase, producer gas was burned inthe station boiler .In a second phase, gas is cleaned and com-pressed in a gas turbine

Page 33: gasifiers

Gasification PlantsFluidized Bed

FERCO-SilvaGas™ Process Plant at Vermont

Gasification is carried out in two CFB:

Steam is the fluiding/gasifying agent of the CFB where biomass is fedSolids (sand +char) entrained fromthis bed are transported to the 2ndCFB where the char is combustedwith air, producing the heat tocarry out gasification.

Hot sand from this bed is transportedto the 1st CFB, acting as the heatCarrier.

The advantage of the process isproducing a medium heating valuegas, as the product gas is not dilutedwith nitrogen from the air

Page 34: gasifiers

Gasification PlantsFluidized Bed

FERCO-SilvaGas™ Process Plant at Vermont

Page 35: gasifiers

Gasifier temperature: 800-850ºCGas heating value: 11-14 MJ/Nm3

Gas composition:

Gasification PlantsFluidized Bed

FERCO-SilvaGas™ Process Plant at Vermont

Gas cleaning includes a catalytic FB cracking, scrubbing andfinal refining in a wet ESP.

Page 36: gasifiers

Gasification PlantsEntrained Bed

ENTRAINED BED GASIFICATIONSVZ Schwarze Pumpe waste gasification plant

Originally, SVZ produced town gas from lignite.Since 1995 SVZ gasifies different residues (plastics, contaminatedwood, sewage sludge, shredded materials from automovile recycling,MSW, waste oil, tar, …) with a total capacity of 560000 ton/y

Three types of reactors:Entrained flowUD with solid dischargeBGL (UD with moltendischarge of ash)

Page 37: gasifiers

Gasification PlantsEntrained Bed

SVZ Schwarze Pumpe waste gasification plant

Page 38: gasifiers

Gasification PlantsEntrained Bed

SVZ Schwarze Pumpe waste gasification plant

Feed material: liquid wastes

Reaction temperature: 1600-1800ºC

Capacity: 15 ton/h

Gasifying agent: O2 and steam

CO and H2 are the main gas products

Page 39: gasifiers

Gasification PlantsEntrained Bed

SVZ Schwarze Pumpe waste gasification plant

Feed material: solid wastes

Reaction temperature: 800-1300ºC

Operation pressure: 25 bar

Capacity: 12 ton/h

Gasifying agent: O2 and steam

CO and H2 are the main gas products

Page 40: gasifiers

Gasification PlantsEntrained Bed

SVZ Schwarze Pumpe waste gasification plant

Feed material: solid and liquid wastes

Reaction temperature: 1600ºC

Operation pressure: 25 bar

Capacity: 35 ton/h

Gasifying agent: O2 and steam

CO and H2 are the main gas products

Page 41: gasifiers

Synthesis gas is used for methanol (120000 ton/y) and powerproduction (75 MWe gas/steam turbine)

Gasification PlantsEntrained Bed

SVZ Schwarze Pumpe waste gasification plant

Page 42: gasifiers

Gasification Plants

Special plants, with a combination of different reactors:

Carbo V process: pyrolysis + thermal cracking + char gasification

Ebara-Ube process: FB + Entrained flow

Compact Power process: pyrolysis + UD char gasification + combustion

Page 43: gasifiers

Gasification PlantsCarbo V process

CARBO V PROCESS

CHOREN Industries

A 1 MWth pilot unit was constructed at the Freiberg (Germany), commissioned in 1998. The process has been tested with a variety of feed materials over a period of 3 years and ran for a total of 5,000 hours.

The feed material includes: coal, sewage sludge, wood, ...

Page 44: gasifiers

Carbo V process Gasification Plants

The Carbo-V Process is a three-stage gasification process incorporating the following steps:

- Low temperature gasification. working between 400ºC-600ºC.- High temperature gasification. Temperatures between 1300ºC and 1500ºC.- Endothermic entrained bed gasification. The temperature drops from more than 1,300 °C to 800 °C in a matter of seconds as a result of endothermic reactions.

Page 45: gasifiers

Carbo V process Gasification Plants

The capacity of the pilot unit in Freiberg is 1 MWth.

A 150 kW gas engine from the Caterpillar company was installed in 2001 and was operated and optimized for a total of more than 600 hours.

Page 46: gasifiers

Carbo V process Gasification Plants

Page 47: gasifiers

Special Plants

ENTRAINED FLOW GASIFICATION

Gasification Plants

EBARA-UBE Process

Placed in Yamaguchi (south of Japan).Completion date: 30 November 1999. Since this date the plant has been working for 3500 hours.

Page 48: gasifiers

Gasification Plants

The EBARA-UBE is a process of two-stage gasification under pressure.- Preparation of plastic: The plastics are compressed and molted (50 to 100 mm diameter, 100 to 200 mm length).- Low temperature gasification: 600ºC-800ºC.- High temperature partial oxidization of gas from low temperature gasifier.

Special Plants

Page 49: gasifiers

Gasification Plants

Raw material: Waste plasticsPCS: 9000 kcal/kg.Plant capacity: 30 Ton/d (as waste plastic). They are building a 240 Ton/day plant. Product: 3500 Nm3/h of gas,Equivalent to 26 ton/d NH3 Hydrogen in gas is 49.9 vol%.By-product: Ammonium Cloride 1Ton/day.Gas composition:

H2 – 49.9 %CO – 33.6 %CO2 – 15.2%H2S – 2.3 %

Special Plants

Page 50: gasifiers

Gasification PlantsSpecial Plants

Page 51: gasifiers

Compact Power Process Gasification Plants

COMPACT POWER PROCESS

Compact Power is a British company which has developeda three-stage process to valorize difficult wastes (as clinical wastes

The stages are:Rotary kiln pyrolysisUpdraft gasificationHigh temperature combustion

Valorization is performedthrough a steam cycle

Page 52: gasifiers

Compact Power Process Gasification Plants

COMPACT POWER PROCESS

Page 53: gasifiers

Biomass specialisation course

Review of Gasification Plants

Jesús Arauzo, Alberto Gonzalo, José L. Sánchez ([email protected])

Chem.&Environ. Eng. Dpt.

C.P.S.

www.cps.unizar.es/~proter