Subject: BUN-INDIA 4th ISSUE NEWSLETTER

Dear Members
We are happy to announce that 4th issue of our
newsletter , we are releasing. We are seding here with the softcopy
of the same. Hardcopy hasbeen sent to all the members
of our mailing list.Its available on the internet at
http://144.16.73.100/~mukunda/home.html



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                  BIOMASS USERS NETWORK - INDIA
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============================================================================



Volume 1.4                     			 June'97

						BUN-INDIA
				Biomass Users Network India

Chairman
=========
Prof. H S Mukunda
Combustion, Gasification & Propulsion Lab.
Dept. of Aerospace Engineering
Indian Institute of Science
Bangalore  560 012, India 
Tel +91-80-3348536
Fax +91-80-3444692
E-mail:  mukunda@aero.iisc.ernet.in
Internet: 
http://144.16.73.100/~mukunda/home.html ~mukunda/ home.html

Contents
============

? Foreword
? Business Meet on Biomass Gasifiers
? Decomposed    Coirpith    as    nutriant 
  source Bioenergy Research Group
? Report on the international conference on 
  Gasification and Pyrolysis of biomass 
  held at Stuttgart, Germany 
? Biomass gasifier for plywood drier installed 
  at M/s. Pratik panels limited Raipur
? Biomass Research Group- Swiss Federal 
  Institute of Technology
? The Styrian experience
? Biomass Gasifier Programme in High Focus Area

FOREWORD
========
We are happy to place the fourth issue of the news 
letter. As in the past, the newsletter is a mix of 
some success stories, policy initiatives and 
further research and development efforts. The 
number of copies printed has trebled over the 
four issues. Communications over e-mail 
needing education and demonstration projects 
from several countries including Africa have 
been received. Sustained efforts in 
demonstration in several countries are an 
important necessity before biomass utilisation 
for electricity generation becomes a large scale 
phenomenon over the globe. 


Prof.  H S Mukunda

---------------------------------------------------------------

Business Meet On Biomass Gasifiers
Dr. N . P Singh , Director Biomass
MNES, Lodhi Road, New Delhi

Ministry of Non-Conventional Energy Sources (MNES), 
Govt. of India, jointly with West Bengal Renewable 
Energy Development Agency (WBREDA)  organized  a  
one  day  Business Meet on use of Biomass  Gasifiers  
in  the  rice  mill,  plywood  &  tea  drying industries on  
19.6.1997  at  Calcutta.  The Meet was attended by 
about 150 participants from Union and  State  Govts.,  
Research Institutes, gasifier manufactures, 
representatives of rice mills, plywood & tea drying 
industries & Financial Institutions.
Prof. Sankar Sen, Minister Incharge of Power, Science & 
Technology and Non-Conventional Energy Sources, 
Govt. of West Bengal in his inaugural address stressed 
the need for utilization of Renewable  Energy 
Technologies such as Solar, Wind & Biomass, 
developed  &  found  viable,  not  only  in  those  areas   
where conventional  energies  are  not available but also 
at all places where such resources  are  available. He 
urged  participating industries  to  utilize  the  biomass  
generated their production processes more efficiently 
and in  a  more  environment  friendly manner through 
gasifiers.
Mr. Ashok Parthasarthi, Secretary, MNES, in his  
keynote address  highlighted  the  progress  made  in the 
development and commercialization of Biomass  
Gasification  and  other  renewable energy technologies   
like  solar,  wind  &  small  hydro.    Mr. Parthasarathi 
mentioned that our gasification and other renewable 
energy technologies  and  systems  are  now   of   
international standards and many countries namely 
Cuba, Indonesia, Male, Brazil Nepal, Sri  Lanka and 
Bangladesh have  shown interest in import of our  
renewable  energy  technologies  and  systems,  he 
added.
Mr. Parthasarthi indicated  that  over the last decade 
some 30 MW aggregate capacity of gasifiers have been 
set up.  The need for gasifiers was  to  large  and  the  
present  fiscal  and financial  package  is sufficiently 
attractive for the country to expand installed gasifier 
capacity to 300 MW by the last year  of the 9th   Plan.    
During  the  meet,  15  papers  on  technology 
development, technology  transfer,  commercialization,  
financing and govt.    colleges  in  the  are  of biomass 
gasification were presented and discussed. 
The representatives from rice mills, plywood & tea drying 
industries shown keen interest  in  adopting  gasifiers  for  
the generation of both process heat and power in their 
industries.

---------------------------------------------------------------
Decomposed    Coirpith    As    Nutriant   Source
S .  GlorySwarupa, Soil  Chemist,  Regional  Coffee  
Research Station, Chundale  677 123 , 
 Wynad  District,  Kerala.

In  India  around   7.5  metric  tonnes  of  Coirpith  is  
produced  annually.  It  is  treated  as  waste  and  
dumped  in  mounds  and it  oozes  tannins  during  
monsoon  causing  environmental  pollution. To  make 
Coirpith  nutrient rich in  available  form  and  to reuse  it  
in  farms , one  tonne  of  Coirpith  is  sandwiched  with  
1.5 kgs  of  Pleurotus Sajor - Caju  spawn  and  5 kg of 
urea  in  alternative  layers  in  a open yard , measuring 
of 5 mtrs  length  & 3 mtrs width . The  heap  is sprinkled  
with  water  regularly  to  maintain  200 %   moisture . 
The  raw  Coirpith turns  black  compost  after  30 days . 
Analysis  of  this compost  it  contains 0.058 %  
Phospharous and 1.17 %  Potassium  besides many  
micronutrients. It has enormous water holding  capacity  
also. Cost of production  of  one  tonne Coirpith  
compost  work  out  to Rs. 360.00 which  is  less  than  
half  of the  cost  of  one  tonne  of FYM  which is 
Rs.640.00  ( as on 1995 ) Thus, the  farmers  in  the  
Coconut  growing  tracts  can  make  use  of  this  
method  to  minimise  the  cost  of   nutrient  
management . 


Report On The International Conference On 
Gasification And Pyrolysis Of Biomass
held at Stuttgart, Germany,  9 to 11 April 1997
Prof. H S Mukunda, CGPL, IISc, Bangalore, India

The conference organized by Dr. A. V. Bridgewater of 
Aston University, UK and Dr. Ing. M. Kaltschmitt of IER, 
Uni. Stuttgart, Germany at Haus der Wirtschaft, Stuttgart 
was  attended by about 100 scientists predominantly 
from Germany, Switzerland, Netherlands, Sweden, 
Finland, UK, Canada, India and a few other countries 
was a focused meeting with all active scientists from 
these countries presenting their current work. The three 
day meeting started with .a brief inauguration with a. 
lead lecture by Mr. Daskelaros of the European 
Commission, Brussels. The arrangements for the 
meeting provided for a number of  informal 
conversations during lunch since all the arrangements 
were located in the same area. Dr. Kaltschmitt presented 
an overview of the biomass energy potential in Europe - 
through the assessment of bioresources, the 
technologies and the benefits in terms of reduction in 
CO2 emission. He presented various values in support of 
these points. Prof. Beenackers presented the 
conventional as well as the unconventional aspects of 
the bioresidue gasification technologies for heat by and 
large and some for electricity. Prof. Bridgewater covered 
the recent studies on fast pyrolysis activities in Europe. 
There were problems related to quality upgradation and 
use in engines and these were under research and 
development.
Dr. Dumbleton of ETSU, UK discussed the methods of 
large scale handling of bioresidues from forests and use 
for many purposes including chemical conversion.
In a very interesting presentation, Dr. Hans Hartmann 
and Iris Lewandowski  of Uni. Of Munich and 
Hohenheim, Germany,  brought up the properties of 
bioresidues - both physical and chemical - concentration 
of Cl, N, S, K and heavy metals as well as ash and water 
content. Several interesting aspects on the influence of 
growing phase, supply phase of biomass for energetic 
uses were described, largely for European bioresidues, 
like Miscanthus. They indicated that the growth rate of 
Miscanthus could be as high as 25 dry 
tonnes/hectare/year. Dr. Hiddink of Netherlands 
described the availability of organic wastes from 
agriculture and agrofood industry in Netherlands. His 
classification included flour mill wastes, straw, beet 
molasses soy meal, waste frying fat with total solids 
more than 80 %,  wastes from wood fruit trees, fish and 
meat industry with solids content of 50 to 80 %, roadside 
grass, domestic organic waste, waste from green 
houses and sugar, potato, onion, and other industries. 
While in several cases with high moisture content with 
not much of Lignin, one can use biomethanation 
technique, in cases where the solids content is high and 
moisture low, one should use gasification.
The next day, the tenth of April, was largely devoted to 
technologies. The session got started with a 
presentation by Mr. Haavisto of Finland on fixed bed 
gasifiers for heat production.  He described updraft 
gasifiers built after research and development in Finland 
for power levels up to 15 MWth and described that they 
were very reliable. In fact their availability was as high as 
95 %. These could be used with moisture content up to  
40 % (dry basis). They can accept a wide ranging fuels 
except powders like sawdust, bark and green chips. It is 
of course not clear why bark cannot be used as a  fuel in 
the system. Further research is intended towards using 
the system for refuse derived fuel (RDF) pellets and 
efforts to be put in towards clean up of tar from the 
systems. The next two co-ordinated presentations were 
by Prof. Mukunda of India and Mr. Buhler of Switzerland. 
Prof. Mukunda addressed the scientific basis, 
technological details as well as field experience of open 
top twin air entry downdraft gasifiers for solid woody 
biofuels (including agro-residues). The duel results from 
joint Indo-Swiss tests both in India and Switzerland were 
presented and it was indicated that these are perhaps 
the only results from gasifier tests have been made with 
third party analysis and the results published in open 
literature. He brought out results of engine tests and 
indicated that in the Indian context where diesel engines 
are more extensively available, their efforts to convert 
commercial naturally aspirated engines to spark ignition 
mode has resulted in successful runs with about 65 % of 
the rated diesel power and at compression ratios of 17, 
typical of compression ignition engines. There was a 
vigorous discussion on this subject with a comment that 
despite the possibility of running the engine smoothly at 
compression ratio of  17, maximum power that may be 
extracted from the engine would be around a 
compression ratio of 14/15. Mr. Buhler in his 
presentation described several European gasifiers and 
the Swiss efforts in going through a formal rigorous test 
programme on gasifiers to establish smooth running and 
good gas quality.  He further emphasized that the 
programme of tests on a gas engine for power 
generation purposes based on IISc-DASAG gasifier is 
currently on and only when these tests are satisfactorily 
completed would they proceed with further expansion of 
the activities of bioresidue based power generation.  He 
emphasized a phased programme like this is the only 
appropriate route for future growth. Eric Rensfelt of 
Sweden gave a scintillating presentation of the 
atmospheric gasification programme at TPS Terminska.  
Systematically going through the various technical 
features of the system, he brought out aspects of 
circulating fluid bed system, the Dolomite tar cracking 
system and the cooling and cleaning systems before the 
gas is taken through a compressor into the combustion 
chamber of a gas turbine engine.  The gas turbine 
engine of General Electric Company was tested with a 
simulated gas  and has been found to work satisfactorily. 
The next presentation of the competing technology - 
pressurized circulating fluid bed gasification system at 
Vernamo by Mr. Stahl of Skydkraft of Sweden was very 
interesting with many details of the high pressure 
gasification system. The fuel feed system involving air 
lock valves to stand up to 25 atmospheres of pressure, 
the candle filter (of Schumacher, GmbH, Germany)  to 
reduce the particulate content to less than  a few PPM 
and the performance details on a gas turbine engine 
(Ruston - Typhoon engine of European gas turbine 
Company) which has already run in an integrated mode 
for the last 150 hours were the highlights of his 
presentation. 
The next four presentations were on liquid fuels from 
biomass.  The presentation by Dr. C. Rossi of ENEL, 
Italy and Dr. Graham of Ensyn technologies, Canada 
was on the plant to be established at Bastardo near 
Perugia in Italy. The plant was in the last stages of 
acceptance tests and would be producing liquid fuel at 
10 tonnes/day using woody biostock at 15 tonnes/day. 
There was considerable hope that these liquid fuels 
would be available for tests in different laboratories. Mr. 
Prins of BTG, Enchede in Netherlands described the 
rotating cone technology for fast pyrolysis. The process 
appeared involved and was the subject of considerable 
discussion. Dr.C Roy of Canada described a patented 
process called pyrocycling. The only new element of the 
process appeared to be the vacuum pyrolysis of bio-
feedstock. There were several aspects which appeared 
optimistic and questions regarding the process needed 
answers. The paper by Mr. Baldauf on the upgrading of 
pyrolysis liquids was thorough and described the 
intricate science and the experience, but the process 
was stated to be not economically  attractive. Similar  
was  the paper by M. Kaiser on the upgrading of liquid 
fuels to near-petroleum class - excellent in detail, but 
economically unattractive now.  The next paper by 
Kurkela and Simell, presented by Simell summarized the 
work of VTT Energy in Finland (a pioneer in bio-fuel 
related work) on tar removal from gasification gas. Most 
of the work in Finland is related to updraft gasifiers or 
circulating fluid bed gasifiers, both meant for direct 
combustion applications using uncooled gas. The paper 
addressed some methods of cracking the tar in the gas 
with fairly high levels of tar. Calcium based bed additives 
into the feedstock, catalytic decomposition using 
monolithic nickel reactor and a secondary granular bed 
catalyst reactor with calcium based materials were the 
methods suggested. Some data on operating conditions 
- around 900o C were also provided. Prof. H. E. Stassen 
of BTG, Enschede, Netherlands described some 
classical aspects of the properties of producer gas for 
engine applications. The importance of flame speed was 
also mentioned. Though measured data on flame 
speeds of producer gas are available, they do not seem 
to have been  taken note of  by many researchers.
Turbines for electricity generation from producer gas 
was discussed by  Dr. Haselbacher. Many points 
discussed here were the part of actual design as 
described by Drs. Rensfelt and Stahl.  The next paper by 
Meier and Scholze on a  characterization of the 
properties of liquid fuels from different sources - Ensyn, 
BTG, NREL, and Fenosa, these being either small or 
large size manufacturers - was very informative  and  
very  thoroughly  presented  by    Dr. Meier. The basic 
idea was to establish the methods that could be used to 
characterize the liquids. It was brought out that the liquid 
fuels have aliphatic and phenolics, hydroxyls, carboxyl, 
carbonyl, alkenyl, vinyl groups and some products due to 
reaction of phenolics and formaldehyde as well as 
polymerised acetals.  The next paper by Radlein of 
Canada on the production of chemicals from bio-oil was 
very interesting. He introduced the concept of bio-
refinery comparable to petroleum oil refinery. All kinds of 
biofeedstock can enter the refinery, be subject to 
different processes and a number of chemicals could 
come out of the refinery. Biolime that could be used for 
NOX/SOX reduction,  Alcohols, Fuel enhancers when bio-
oil is treated with alcohols,  flavours (currently largely 
used) and others were mentioned. The profundity of the 
idea is that a single refinery can make several 
chemicals,  fuel being the low cost item amongst them. 
Such a strategy might help produce mildly upgraded  
fuel oils for automotive applications at lower costs these 
being achieved by cross subsidy. Combustion of liquid 
fuels in furnaces was described by S. Gust of Finland. 
Problems encountered were blocking and clogging of 
nozzles and crust formation on the burner head. It was 
suggested that careful control of fuel lines was 
imperative for proper operation of the system.
The next two presentations were on the technical 
aspects of the use of liquid fuels in reciprocating and gas 
turbine engines. J. Leech of UK presented the research 
studies done by him on the use of these liquid fuels in 
one cylinder of a multi-cylinder engine. In these tests the 
pyrolytic oil was mixed with 20 % methanol and tried out 
in a diesel engine. From the experience indicated, the 
engine does not run on the pyrolytic oil alone. The 
pressure-time curves indicated to non-smooth 
functioning of the system and this needed further 
research. 
The next paper by Dr. Patnaik of Orenda Research 
Corporation, Canada presented the experience on the 
use of pyrolytic oil in a 2.5 MW class - GT2500 gas 
turbine engine. The results of several systematic studies 
aimed at determining the suitability of the fuel for gas 
turbine applications were presented and it appears that 
major problems on operating the engine with the fuel 
have been sorted out. This is one major positive result 
on the use of pyrolytic oils for power generation. The 
primary feature in all this case is continuos combustion 
compared to periodic ignition and combustion in the 
case of reciprocating engines.
Apart from oral presentations described above, there 
were thirty poster presentations. These were the results 
from on-going studies or just-completed studies on 
biomass related issues. While about 65 % of them were 
directly related to the topics of oral presentations, some 
were new - Fluidised bed gasification of urban waste 
wood,  steam gasification of biomass chars, new 
systems for tar sampling and characterization  (the solid 
phase adsorption technique), tar characterization in 
cyclone and downdraft wood gasifiers, cogasification of 
coal with biomass, and  computer models of gasification 
process. 
There was a final session on panel discussion on 
gasification, liquid fuels and other imperatives. Chaired 
by Prof. Beenackers, the discussion was vigorous and 
even  those who listened from a distance could get a 
picture of the general trends. The impression that could 
be gleaned was Europe was more favourably inclined to 
the use of biomass gasification for power generation and 
liquid fuels still needed to overcome the cost factor 
before they became attractive. The role that liquid fuels 
from biomass should play in automotive applications is 
still being given lower priority in terms of research and 
this needs to be amended in times to come. On the 
whole the meeting well conducted served its purpose 
more than adequately.  A volume containing the papers 
will appear soon and readers can look forward to a treat 
of valuable material.

--------------------------------------------------------------
Biomass Gasifier For Plywood Drier Installed At 
M/S. Pratik Panels Limited Raipur
Mr. B V Ravikumar, Cosmo Products, Raipur

A 2,50,000 kcal/h capacity biomass gasifier has been 
retrofitted to steam based drier at M/s. Pratik Panels 
Limited, Raipur. In the present installation the producer 
gas generated in a gasifier is burnt in combustion cum 
mixing chamber and diluted with recirculating/fresh air to 
get hot air of desired temperature.  When drier is run on 
gas produced by gasifier temperatures higher than those 
attainable by boiler are achieved.  (By suitably selecting 
the capacity of gasifier, hot air temperatures upto 200 ?C 
are achievable).  Therefore, the qualitative performance 
of drier as well as production increases.
Earlier, M/s. Pratik Panels Limited were running the drier 
by steam and could not get the temperatures beyond 70 
?C.  At that time, they thought of installing a thermic fluid 
heater.  Instead of thermic fluid heater, they installed a 
2,50,000 kcal/h capacity gasifier system.  Now that the 
drier is run on producer gas produced by gasifier, 
desired temperature upon 120 ?C are achieved.  
The main advantage to them is reduction in drying time.  
Earlier the drier was the bottleneck equipment in the 
factory.  Now, the productivity of the entire factory has 
increased yielding considerable economic benefits.  The 
fuel consumption has also come down by 15-20 %.
----------------------------------------------------------------------
Bioenergy Research Group
Swiss Federal Institute Of Technology
Scientific Staff: Dr. Thomas Nussbaumer (Group 
Leader), Hanspeter Kaufmann, Philipp Morf, Roger 
Salzmann, Serge Biollaz, Christian Bruch

Activities: The aim of the Bioenergy Research is to 
improve technologies for heat and power production 
from biofuels, especially wood. Research projects are 
carried out in cooperation with industry and aim for low 
emissions and high efficiencies. The topics of the 
research are combustion and gasification processes, 
including reactor design, process control and gas 
cleaning. 

Activity1: Low Nox Wood Combustion : 

The NOX emissions from biomass combustion originate 
mainly from the fuel bound nitrogen. In this project the 
possibilites of air staging and fuel staging for wood 
furnaces are investigated in laboratory facilities and in 
full scale automatic wood furnaces of 200 - 600 kWth. 
Furthermore, process control technologies by use of 
temperature and lambda sensors are developed to 
guarantee optimum operation conditions for complete 
burnout and low NOX emissions. To control the 
temperature in the reduction chamber, air staging is 
combined with external flue gas recirculation. The aim of 
the low NOX furnace design and its operation is to form 
molecular N2 from the fuel nitrogen inspite of NO in a 
reduction chamber before entering the combustion 
chamber. In the reduction chamber, intermediate N-
species as N, NH and NH2 from the fuel nitrogen can act 
as oxidizing agent for NO in different reactions, e.g. in 
the reaction scheme: NO + NH2 ? N2 + H2O. The 
investigations show that an NOX reduction of app. 50% 
can be reached for native wood with low nitrogen 
content (0.1 - 0.2 wt.-%), while for wood residues and 
chip boards with high nitrogen content (1 - 3 %) up to 
75% reduction can be reached. However the NOX 
reduction is strongly influenced by the reaction 
conditions in the reduction chamber, especially the 
primary excess air ratio (?P), the temperature (T) and the 
residence time (t). For maximum NOX reduction the 
parameters in the reduction chamber have to be 
controlled as follows: ?P = 0.7 - 0.8, T = 1'150-1'250øC 
and t >0.3 s.
Financial support: Swiss Federal Office for Science 
and Education  as part of the EU-Project JOR3-CT96-
0059 "Reduction of Nitrogen Oxide Emissions from 
Wood Chip Grate Furnaces"
Activity 2: 
Determination of Mixing Qualities in Furnaces with 
Injection of Tracer Gas and Measuring the 
Residence Time Distribution: The burn out efficiency 
(CO, HC, soot) and the formation of NOX in combustion 
processes is strongly influenced by the mixing quality 
between combustible gases and combustion air. The 
aim of the present project is to develop an experimental 
tool to measure and describe the mixing quality in 
furnaces by injection of a tracer and measuring the step 
response of the tracer at the outlet of the reactor. 
>From this information, the residence time distribution of 
the gases and the mean residence time in the 
combustion chamber can be determined. Helium is used 
as tracer and a fast thermal conductivity detector is used 
to measure the step response.


reduction is strongly influenced by the reaction 
conditions in the reduction chamber, especially the 
primary excess air ratio (?P), the temperature (T) and the 
residence time (t). For maximum NOX reduction the 
parameters in the reduction chamber have to be 
controlled as follows: ?P = 0.7 - 0.8, T = 1'150-1'250øC 
and t >0.3 s.

Financial support: Swiss Federal Office for Science 
and Education  as part of the EU-Project JOR3-CT96-
0059 "Reduction of Nitrogen Oxide Emissions from 
Wood Chip Grate Furnaces"
Furthermore temperature and O2 content are measured 
continously. In future work, a mathematical model of the 
combustion kinetics by respect of the residence time 
distribution will be developped to optimize the 
combustion chamber and the injection of combustion air.  
In wood furnaces, the method will be used to optimize 
the combustion chamber for a complete burnout of CO, 
hydrocarbons and soot. Furthermore the model will be 
used to minimize NOX formation from fuel nitrogen by 
optimizing the reduction of fuel nitrogen to N2 in an 
understoichiometric atmosphere in the reduction 
chamber.
However, the method can also be used for other solid 
fuels as waste or coal and it can also be applied in liquid 
and gaseous fuel combustion, where for example the 
recirculation rate in low NOX-burners can be determined.
Financial support: Swiss Federal Office for Energy


Activity 3: Biomass Gasification for Power 

Production : Fixed bed gasifiers with internal 
combustion engines offer the possibility for decentralized 
heat and power production from biomass in small scale 
units (50 - 500 kWe) with relatively high electrical 
efficiency (up to app. 25% in comparison to app. 10% for 
steam turbines and steam engines in the same power 
range). However tar and particles in the low calorific 
producer gas from gasifiers can cause damages in 
internal combustion engines and lead to short service 
periods. Although this problem is well known from earlier 
applications, only few data are available on the 
concentration and compositionof tar and particles in the 
producer gas. Since the sampling and analysis 
techniques are not standardized, a comparison between 
different results from the literature is not possible. 
Further more, there are only few experiences with 
application of nowadays scrubber and filter techniques 
for the gas cleaning from downdraft gasifiers, which 
promise the lowest.



-----------------------------------------------------------
The Styrian Experience 
Source:  Woodfuel Technologies and development

Styria, a province in the south-east of Austria, is a 
European region which appears to have set a fine 
example in promoting the use of bioresidue based 
renewable energy. It has seen the largest development 
in the use of wood fuel for district heating and has so far 
established around 87 wood-fuelled heating network in 
about ten years. Having realised the importance of 
renewables, the Stryrian government set up a detailed 
plan in 1984 to harness this energy by initiating a close 
dialogue with the local farmers, who are also the 
foresters.The scheme was initialised by setting up pilot 
projects to show the feasibility of the system in terms of 
supply  logistics and combustion material etc. After 
successfully overcoming stiff opposition from the fossil 
fuels, today the wood-fuelled heating has become the 
largest heating network amounting to a total installed 
capacity of 121 MW thermal. The wood consumption for 
these systems amounts to 55 tonnes of oven-dry wood 
per hour, of which 60% constitutes the bark. The wood 
for these plants is obtained from local forests and this 
has in no way led to their degradation. The afforestation 
stands high at  54% of the total land area. Initially the 
government encouraged by providing subsidies which 
was partly responsible for a faster growth rate of the 
heating network.  Now having created a public 
awareness on this environment friendly method of 
harnessing the energy, the need for searching for 
potential clients is no longer required, those interested 
come on their own is the  impression of the people 
behind the scheme.

--------------------------------------------------------------

Biomass Gasifier Programme in High Focus Areas
Dr. K C Kandelwal, Advisor, MNES, Lodi Road,
 New Delhi

After successful demonstration of different applications 
of  biomass gasifiers in the states of Arunachal 
Pradesh and Assam and an evincing interest shown by 
Manipur and Mizoram States also in the Review 
Meeting on Renewable Energy held at North - Eastern 
Region Stares on 17 April,1997, the Ministry of Non - 
Conventional Energy Sources (MNES) has taken new 
initiatives for installation of gasifiers in all North - 
Eastern Region States. A list of gasifiers installed in 
Arunachal Pradesh and Assam is given at Table 1. 
Besides, the Biomass Gasifier Demonstration 
Programme will be implemented in other High Focus 
Areas, namely Sikkim, Jammu and Kashmir, Andaman 
and Nicobar Islands, Lakshadweep tribal areas , 
Fastern and Western Ghats, villages in and around 
National Parks and Forest Reserves, estuarmine areas  
such as Sunderban and major inhabitant riverine 
islands such as Majuli in Assam.


Table 1. A List Of Biomass Gasifiers Installed In Arunachal 
Pradesh And Assam

Location					System Rating	 			Mode of
							application
---------------------------------------------------------------------------

Vivekananda Kendra Vidyalaya 	2,50,000  kcal / hr  	 Thermal 
Vahajan , Arunachal Pradesh

M/s Nokte Timber Company 			40  kW			 	Electrical
 Post - Demoli Dist. Tirap 
Arunachal Pradesh

M/s Donyl Polo Saw Mill Jirdo		40  kW			 	Electrical
Post Basar, Dist.West Kameng, 
Arunachal Pradesh

Assam Riha Samabat		 			10 kW				Electrical
Samity Ltd. Guwahati , Assam

Assam Police Radio Organisation	 	3 kW & 5 HP			Electrical &
(APRO), Guwahati , Assam				 				Mechanical
------------------------------------------------------------------------


The amount of Central incentives has been increased for 
installation of gasifiers in all North Eastern Region 
States, Sikkim, Jammu and Kashmir, Andaman and 
Nicobar Islands and Lakshadweep. Details of the revised 
rates of  incentives are given in Table 2.


Table 2 :Revised rates of Central financial assistance on 
Biomass Gasifiers for 1997-98
--------------------------------------------------------------------------

Mode of  		Rating
application				Amount of Central assistance in Rupees[India]

						North-Eastern , 	  		Union Territories
						Region StatesSikkim
						Jammu,Kashmir Andaman,
						Nicobar Islands, 
						LakshadweepOther States
----------------------------------------------------------------------------

Mechanical:	   	 5 HP		14,500						 9,000
				10 HP		10,500						12,000

Electrical:		 3  kW		18,000						15,000		
				 5  kW		28,000						24,000		
				10  kW		45,000						39,000
				20  kW		70,000						60,000
				40  kW    1,35,000				      1,14,000
			   100  kw    3,10,000					  2,64,000
			   200  kW    4,30,000					  3,60,000
			   300  kW    5,60,000			   		  4,68,000
			   500  kW    8,10,000					  6,87,000

Thermal:	7,500 kcal/hr	 9,000						 7,500
		   12,500 kcal/hr	13,000						10,500	
		   25,000 kcal/hr	20,000						17,000
		   50,000 kcal/hr	34,000						28,000
		   1,00,000 kcal/h	55,000						45,000
----------------------------------------------------------------------------

1 US$ = Rs. 36.00:  The subsidies constitute about 25 to 30% of the cost of the 
Gasification System.

Recent Conferences, Presentations And Training Programs
=============================================================
? Seminar on Recent Developments in fluidized bed biomass 
gasification organized by Centre for new & renewable 
sources of energy, Anna University, Madras. 

? National seminar on Power generation from Industrial, 
Urban and Municipal wastes organized by Mahathma 
Gandhi Institute of Integrated Rural Energy Planning & 
Development, New Delhi.

? Conference on Gasification and Pyrolysis of Biomass - 
State of the art and future prospect and presented a paper 
on "Fixed bed gasification for electricity generation" at 
Stuttgart, Germany between 9-11 April 97

? International workshop  on Plantation & other Industries at 
Indian Institute (IIT), Madras, between 9-11 April. 

? Presentation on "Technologies For Biomass Utilization" at 
National Bioenergy board, MNES, NewDelhi on 30th May 97.

? Renewable energy training workshop for MNES officers at 
Pondichery between 2nd June to 7th June 97.

? Business meet on Use of Biomass for Gasification in 
ricemills, plywood and tea industries held at Calcutta on 
19th June 97.

? Technical Training programme for engineering 
Consultants on Biomass Power and Co-generation at Anna 
University, Madras between 30-4 July  97.

Do u Know This
==================

Comparison Of Biomethanation Properties Of Various Feed 
Stocks

Substrate 	Residence    T *C  	%COD		% VS			Comments
				time			Destroyed	destroyed
------------------------------------------------------------------------
Poultry waste  	15  		32  	78  		68  

Piggary waste   15  		35 		58  		60  		14 % protein  
ratio
Bovine dung 	15  		32  	11  		27  		10 % TS 	
feed
Municipal  		15  		35  	45  		36  		12 % 5 	
refuse sewage 	
solids added
Dairy  manure 	25  		35  	30 			29  
+ barley straw


News print  	90  		35  	- 			28  
---------------------------------------------------------------------------

Services

? Abstracts relating to published papers on bio-resource can now be made 
available at no cost. This could be obtained by sending a request letter along 
with one or two relevant key words.
? Services relating to search for Patents can now are availed from Bun-India  on 
chargeable basis.

Editorial

The BUN-NEWSLETTER is published by the BUN-INDIA 
Combustion, Gasification & Propulsion Laboratory, Indian Institute of Science, 
Bangalore 560 012, India. 

For further information or correspondence please Contact:
			 
Mrs. Gayathri V
Combustion Gasification & Propulsion Laboratory [CGPL]
Indian Institute of Science, Bangalore 560 012, India
E-mail: gayathri@aero.iisc.ernet.in or
gayathri@cgpl.iisc.ernet.in
Fax: +91-80-3444692, 3341683
Tel : +91-80-3348536, 3092338


 




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