Elaborated:
Ph. D. Attila Meggyes

Budapest, 6-th August 1996.

1./ Introduction.

Mr Allan Inovius President of the CCB /Complete Combustion BureauSweden/Hungary AB/ asked us for the studding effect CCR NOCO-reactordeveloped and invented by them on the efficiency and exhaust gasemission of small size boiler.

2.1 Data of the boiler under measurement and the measureddata.

The measured boiler:
	CCR NOCO EUROPE BOILER Number 1 Maker: FÛTÔBER; Nagybátony.
Oil burner:
	OIL N 10 B Maker: GB GANZ; Budapest
CCR NOCO-reactor:
	Type 240/2
Nozzle of oil atomiser:
	0.5 G/h 60° H

Annex I. contains the measuring points on thedevice and the result of them.

3./ Results of calculations.

The calculated characters based on the measured results:

Indirect efficiency:

_ind.= 93,35 %

	Exhaust gas losses	= 5,35 %
	Losses of radiation and heat transfer	= 1,3 %
	Losses of unburned fuel	= 0 %

Direct efficiency:

_dir.= 92,7 %

	Heat flux of the input fuel	= 17479,3 W
	Heat flux of the input air	= 163,351 W
	Effective head flux of water	= 16347,9 W

Emission values related to 3% 0₂

NOx	= 91,32 ppm
NO	= 88,31 ppm
CO	= 22,38 ppm
Soot	Å 0 mg/m3
CO2 = CO2max. = 15,8 1,17 = 13,51 %

NO/NO_x ratio andNO₂/NO_x ratio

Excess air coefficients

The above values are calculated on average.

4./ Summary, conclusions

Following statements can be taken for the small size boilerprovided with CCR NOCO-reactor based on the measured result and thecalculation.

1./ Both direct and the indirect boiler efficiencies are veryadvantages /more then 92 %/ that can be realised primary by the lowexhaust gas temperature.

2./ The CO emission and the soot emission are also of veryadvantages.

3./ The air excess change /O₂ content/ is of loweradvantages in the area of fluctuation. At a given adjustment theO₂ emission was between 2,92/3,4 V%.

4./ We propose -to achieve lower air excess /without COrespectively soot emission increase/ and the decrease the air excessfluctuation- further development for the adaptation of the burnerwith CCR NOCO-reactor respectively the complementation of CCR NOCO-reactorwith deflector.

Ph.D. Attila Meggyes Candidate of Sciences Dip. N°: 8116/79 Associate professor Technical University of Budapest

I. Annex.

	Ambient air:
		temperature:	ta	= 22,98 °C
		pressure:	pa	= 101*103 Pa
		humidity:		= 70 %
	Water:
		inlet temp.:	twi	= 21,2 °C
		outlet temp.:	tWO	= 54,25 °C
		mass flow:	mv	= 0,1173 kg/sec
	Fuel:
		pressure:	pf	= 7 bar
		temperature:	tf	= 20,5 °C
		mass flow:	mf	= 1,4964 kg/h
		spec. heat value:	Hi	= 42000 kJ/kg
	Exhaust gas:
		temperature:	texh	= 120,0 °C
	Measured exhaust gas components: min./max. NOx = 90,09 ppm 88,53/92,09 NO = 87,13 ppm 81,53/92,09 CO = 22,08 ppm 13,61/64,67 O2 = 3,12 V% 2,92/3,4 R = 0 mg/m3 NO2 = NOx - NO = 2,96 ppm

The above values are average values in stationary condition.
Place of the measuring points are on Fig. 1.
The boiler was not connected to chimney.

1. fig.: The test rig