In order to promote decomposition of wasted tires and wasted rubbers, wash and dry the pieces mentioned above, and then transport and insert into preheater to get recycled materials in good quality.
At same time, insert catalyst initiator into the catalyst initiator insertion hole in order to promote active decomposition.
Catalyst initiator should be continuously inserted until the first decomposition is executed. If first decomposition is executed, it will keep operating decomposition although you stop inserting catalyst initiator.
If you do not want to secure GAS generated since then, use it for heat source. GAS processed through condenser is stored at TANK as OIL.
CARBON BLACJ(C/B) and steel cores decomposed into original materials are separated through M/S, and then they are packed and stored for delivery.

1. Continuous low temperature decomposition is enabled.
2. Generated materials are restored to original materials.
3. It is quite competitive with its low operation expense and generated materials.
4. Since it uses GAS generated by itself, there is no burden for fuel expense.
5. Since it decomposes at low temperature, manufacturing expense is low and life cycle of the device is long.
6. No environmental pollution.
7. For foreign countries (United States, Thailand, Canada, Australia, EU countries and others), it is quite economical since their operation expense is higher than US$2.

Wasted Tires and Synthetic Rubbers

Waste tire cutting process at item 1 → Transport them to waste accumulator after washing and drying procedure → Insert into main decomposition chamber

Fuel insertion in item 2, preheating process → Sublimation process is performed at main decomposition chamber → Separated gas is compressed and transported to concentration device in item 2, remaining CARBON BLACH and other solid state materials and steel cores are transported to separation process in item 3

Transport to storing tank after concentrating into oil at condenser and related device of item 2. In item 3, ③ Steel core and CARBON BLACK separation process ④ Directly transport and pack after going through CARBON BLACK differential pulverizing process

Waiting for delivery at oil storing tank Steel → Store → Waiting for Delivery Waiting for delivery after packing in certain unit

Oil Delivery Steel Delivery CARBON BLACK Delivery

No.	Item	Based on Tires of 50t in a Day		Wasted Rubbers 25ton Tires 24ton
		Generated Quantity	Amount (Won)
1	OIL (Annual Production)	6,000,000ℓ	2,220,000
2	CARBON BLACK (Annual Production)	4,200ton	924,000
3	STEEL	1,470ton	132,000
4	Wasted Tire Handling Expense	825,000 EA	412,500	150 Days
5	Wasted Rubber Handling Expense	7,500ton	1,050,000	150 Days
	Total Annual Profit		4,738,500

Conversion Basis

Based on oil sales price of 1ℓ x 370 won Based on oil generation amount of 400ℓ for tires of 1t Based on CARBON BLACK generation amount of 280kg for tires of 1t, Based on sales price of 1t x 220,000 won Based on steel generation amount of 98kg for tires of 1t and sales price of 1kg x 90 won Based wasted tire handling expense for passenger cars of 500 won for each tire (based on the price in 1999) Based on 110 EA for tires of 1T (average weight of 8.9kg) Wasted rubber handling expense of \140,000/t

		MICHENAE	ATR	OXFORD	CONRAD	ONODA CEMENT	ENERGECO	T.R. ENVIRONMENTAL TECHNOLOGY
Handling Method		Dried gas	Thermal decomposition	Incineration	Thermal decomposition	Incineration	Incineration	Thermal decomposition
Location		Japan	United States	United States	United States	Japan	Italia	Korea
Quantity of Tire Handling		200T/D	50T/D	300T/D	24T/D	72T/D	60T/D	50T/D
Operating Tem.		About 500℃	540~650℃		482~537℃	1,500~2,000℃		200~250℃
Gene rated Mater ials	OIL GAS STEEL	0.35kg/kgTIRE 0.6N㎡/kgTIRE 0.3kg/kgTIRE 0.1kg/kgTIRE	0.42kg/kgTIRE 0.44N㎡/kgTIRE 0.29kg/kgTIRE 0.1kg/kgTIRE	Electricity 300KW/H	0.35kg/kgTIRE Electricity 5000KW/H 0.26kg/kgTIRE		STEAM:20T/H          (20KG) 400KG/H	Oil & gas or both in option 0.25kg/kgTIRE 0.1kg/kgTIRE
Required Site			About 9,917.4m2				About 1,983.5m2	About 1,322.3m2
Operating Expense			Requires 55 operators		Requires 6 operators		5,000KW/H of electricity and 11 operators are required	Requires 5 operators
Tire Handling Investment by TON/D		121 million won(T/D)	136 million won(T/D)	283 million won (T/D)	146 million won (T/D)		213 million won(T/D)	100 million won (T/D)
Characteristics of Process		Use whole tiresLow operation expenseLONE SELF-COOLINGSYSTEMFine heat efficacy as a vertical furnace	Requires tire cutting device (increase expense for power)Requires too much operation expense Requires upgraded facility for CARBON	User tires Requires great amount of investment for pollution preventing facility STOKERincinerator type Requires too much operation expenseIncineration process for handling tires is prohibited by domestic environmental regulations	Requires tire cutting deviceInstalls large PLANTNo sales recordGenerating power with STEAM is possible	Substitute 15% of fuel with wasted tires Use whole tires Requires no pollution preventing facility Using large tires is possible Because of efficacy value difference of soft coal alternative furnace, performance level is low	ROTARYKLIN typePrice is high and overall facility efficacy rate is low Impossible to install single large plant Not allowed by environmental regulations	Includes cutting device Low operation expense Simple facility Secondary pollution preventing device is not necessary Decomposes to original materials by applying new principles
Technical Reliability		Highly reliable	Highly reliable	Highly reliable	Technology in distribution stage	Highly reliable	Highly reliable	Decomposition to original materials

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