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Technology of thermal processing of organic- containing raw materials. Unit with solid heat carrier (UTT). Prof. E.P. Volkov, Director of Power Engineering Institute (ENIN) Moscow, Russia Moscow, Russia

Prof. E.P. Volkov, Director of Power Engineering Institute (ENIN) Moscow, Russia

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Prof. E.P. Volkov, Director of Power Engineering Institute (ENIN) Moscow, Russia. Technology of thermal processing of organic-containing raw materials. Unit with solid heat carrier (UTT). Narva. Baltic Sea. Russia. Russian technology of pyrolys is — development and maintenance. - PowerPoint PPT Presentation

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Page 1: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Technology of thermal

processing of organic-containing

raw materials.

Unit with solid heat carrier

(UTT).

Prof. E.P. Volkov,

Director of Power Engineering Institute (ENIN)

Moscow, RussiaMoscow, Russia

Page 2: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Russian technology of pyrolysis — development and maintenance

Technology of oil shale pyrolysis

was successfully mastered

and introduced in industrial scales

at the unit UTT-500processing 500 t of oil shale per day

and that at the unit

UTT-3000 processing 3000 t per day.

Baltic Sea

Russia

Two units UTT-3000 were put into operation in 1987 at the Power plant at city Narva, Estonia (in the time of former USSR). It demonstrate successful experience of thermal processing of Baltic oil shales as well as of waste automobile tires, solid and liquid organic waste in a mixture with oil shale.

The result is the obtaining of high calorific liquid and gaseous fuels as well as the very valuable chemical products.

Narva

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Page 3: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Unit UTT-3000 in city Narva for thermal processing of oil shales

Two units UTT-3000

in Narva take up to now

the leading place in the world

as to the quality

of oils and gas

obtained from oil shale,

ecological indicators and

economic efficiency.

General view

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Page 4: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Schematic diagram of thermal processing of Baltic oil shale. Unit UTT-3000

1 – aero-fountain air spray drier, 2 – dry shale cyclone, 3 – mixer,

4 – drum reactor, 5 – dust separator, 6 – aero-fountain furnace, 7 – flow separator,

8 – heat carrier cyclone, 9 – ash cyclone,

10 – recovery boiler, 11 – ash heat exchanger, 12 - filter

shale oil heavy, middle and light

fractions

7

5

4

13gas

6

steam-gas mixture

airwater

10

ash

11

9

to atmosphere

2

3

oil shale

1

12

steam8

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Page 5: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Unit UTT-3000 for thermal processing of oil shales

The main advantage of pyrolysis by means of units UTT is

a possibility of oil shale processing of any fractional composition and quality

Only the oils shales with calorific value lower than 2.9 MJ/kg

require the supply of additional fuel for processing that is

necessary for supporting the pyrolysis process.

For reference:

Heat of combustion of Baltic oil shales for

Estonia and Leningradskaya region

of Russia is

8,37 MJ/kg

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Page 6: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Baltic oil shales

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Page 7: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Unit UTT-3000 in city Narva for thermal processing of oil shales

Is in operation since 1989 more than 14 years

View of

the section

for thermal

decomposition

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Page 8: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Rotating

drum reactor

Unit UTT-3000 in city Narva for thermal processing of oil shales

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Page 9: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Unit UTT-3000 has the following advantages:

The heat of combustion gas obtained after pyrolysis in units UTT is in 2.5-3.0 times more than in the plants of other countries. So, the calorific value of pyrolysis gas after the processing of oil shale of Leningradskoye deposits is 42,2 MJ/kg.

The gas obtained in the units UTTs represents the marketable product - a fuel for gas turbines, while in other technologies the considerable part of gas is used in the cycle itself for combustion in the reactor.

The utilization of ash instead of gas for pyrolysis increases the efficiency of inits up to 84-89%, while the efficiency doesn’t exceed 65% for the majority of plants of other types.

The total efficiency of cleaning of gas-vapor mixture in cyclones achieves 99,5%. Owing to it, the content of dust doesn’t exceed 1.0-1.5% even in the heavy fractions of oil shale.

The inits UTT-3000 process the waste automobile tires in a mixture with oil shale. The processing of grounds saturated by oil products (for example, because of accidents during transportation) is also technically possible and was confirmed in practice.

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Page 10: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Scheme of steam-gas unit with recovery boiler

1 - compressor of gas turbine

2 - combustion chamber for gaz afterUTT

3 - Combustion chamber for GF ( gasoil fraction )

4 - gas turbine

5 - electric generator

6 - recovery boiler

7 - steam turbine

8 - electric generator

9 - condenser

10 – condensate pump

11 - deaerator

12 – feed pump

13 – drum separator of high pressure

14 – circulating high-pressure pump

15 – drum separator of low pressure

16 – circulating low-pressure pump

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Page 11: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Main characteristics of oil shale fractions obtained in the units UTT.

Oil shales of Leningradskoye deposit

Elementary composition in maximum, % Fractions of

shale oil

Density, kg/m3

(for 20°C) sulfur water ash

Mechanical admixtures

Heat value, MJ/kg

% evapora-

tion in the end of boiling

Total shale oil 950- 1000

0.8 0.3 0.1 0.15 38 64

Heavy oil 1050- 1100

0.6 1.0 0.8 1.0 36.5 60

Middle oil 1010 0.8 0.3 0.1 0,15 37.4 70

Diesel oil (fuel for gas turbine)

925 0.8 0.1 0.015 0,02 38.4 85

Petroleum fraction

810- 825

1.0 0.1 abs abs 41.2 90

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Page 12: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Calculated indices gas turbine cogeneration plant (steam-gas plant - SGP ) on the basis of CHP and UTT.

Compane-producing the gas turbine plants (GTP)

Index Westinhouse ABB Siemens GE LMZ

Type of’ gas turbine plants (GTP)

W251 GT 8C V64.3 GE6101 GTE-45

Number of GTP in SGP

2 2 2 4 2

Power of CHP as a complex, MW

182.2 190.0 205.5 185.0 154.3

Power of SGP with gas after UTT, MW

73.4 77.4 85.2 2Ч37.5 59.4

Power of GTP on the gas after UTT, MW

48.5 52.1 61.65 2Ч25.9 40.4

Efficiiency, % 47.3 48.9 49.4 42.4 42.1

*LMZ – Leningradsky Metal Works, Russia

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Page 13: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Marketable products, which can be obtained in the energy-technological complex on the basis of heat power plant (CHP)

UTT-3000 with steam gas (gas turbine cogeneration) plant (variant of gas turbines of company ABB)

Marketable products, million ton per year

Electric energy 969 million kWh/year

Total cost of marketable products is 72.77 million $ / year

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26,161,5

171,5

100

Diesel oil Petroleum fraction

Liquid boiler fuel (mixture of heavy and middle fractions of shail oil) Liquid boiler fuel, obtained by processing waste automobile tires

Page 14: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Characteristics of gas obtained in UTT from the oil shales Leningradskoye deposit

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Page 15: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Financial and commercial efficiency of energy-technological complex on the basis of UTT-3000

(variant de ABB gas turbines).Oil shales of Leningradskoye deposit

Conditions of crediting Rate of interest …….…9%

Postponement of payment.......................…15 ans

Privileged postponement........…….. 3 ans

Conditions of financing

%

Capacity: 2500 thousand ton of oil sahle per yearOutput of products: 250 thousand of shale oil from the processes oil shale plus 100 thous. tonn of oil from processed rubber products

Capital investments…….189 million $

Duration of construction…....3 years

Price of oil shale………5 $/tTarif on electricity….....3 cent/kWh

Rate of profit…..……………………………………………19.42%Discounted net profit……….……………………………100.0 millions $Payback peiod after putting into operation..……………5 years

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Page 16: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Main applications of products obtained from shale oil and gas during the pyrolysis of oil shales

Thiophene

Benzene

Toluene

Albichtene

Ichtyol

Plactisizer

Souftener

Technical sulfur

Sodium thiosulfate

etc. pharmacology

medicine

agriculture

chemistry

veterinary medicine

Electric industry et optics

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Page 17: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Applications

Examples :

Dyes

obtained from thiophene — for dyeing the cotton, wool, rayon

etc.Medical ichtyol

— for desinfection in the treatment of skin and mucous

membranes

Technical sulfur — for wood pulp and

paper industry

Albichtene — as an antiseptics in production of articles for tropical zones

Sodium ichtyol — for production of

creoline used in veterinary medicine

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Page 18: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Kerogene composition for oil shales of different deposits

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DepositComposition of kerogene

of oil shail

C H O SPribaltyiskoye (Estonia) 77.3 9.8 11.2 1.7

Leningradskoye (Russia) 77.7 9.8 11.3 1.2

Kashpirskoye (Russia) 61.1 7.3 23.8 7.8

Kenderlikskoye (Uzbekistan) 73.8 8.4 17.8  

Boltyshskoye (Ukraine) 68.0 9.3 18.3 1.9

Timakhdi (Morocco) 70.5 9.3 12.4 7.8

Green-River (USA) 80.9 11.4 6.9 0.8

Nerke (Sweden) 69.5 7.7 16.8 6.0

Lotiani (Scotland) 63.0 10.1 26.2 0.7

Render (Australia) 63.1 7.9 28.3 0.7

Irati (Brazil) 68.1 10.3 17.9 3.7

Rotem (Israel) 65.0 7.0 15.4 10.7

Page 19: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Yield of semicoking products from the oil shales

of different deposits

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Page 20: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Advancing the Russian UTT technology

of oil shale processing

to a number of countries

to involve national oil shale deposits in power industries

Israeli electric company and company OSE (city Edelsburg).

Deposit Rotem.

Ministry of Natural Resources of Jordan.

Deposit El-Ladjun.

Ministry of Natural Resources of Morocco. Deposits Timakhdit, Tarfaya.

The negotiations with foreign companies were positive,

the protocols of intents were concluded. 20

Page 21: Prof.  E.P. Volkov,     Director of Power Engineering Institute (ENIN) Moscow,    Russia

Potential partners

Lurgi-Rurgas, Germany

Tosco, USA

Petrosix, Brasil

Tasiuk, Australia

Factory of shale oil,

Estonia

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