Products to be manufactured: Following products shall be manufactured from waste plastic 1) REFUSED DERIVED FUEL (ALTERNATIVE TO LDO) 2) Natural gas 3) Charcoal C) Market Potential: The potential buyers shall be as under: Establishment with furnaces D) Licenses for manufacture, storage and sale: License required for manufacture of RDF oil. Noc from local authority SSI registration with DIC Pollution control board consent needs to be obtained to certify that all parameters of operation are in specified limit. Fire department NOC Storage licenses above prescribed limit NOC from PESCO E) Production Capacity: All capacities quoted as per day are on 24 hour basis, three shifts per day. On an average, 70% of RDF oil is obtained, 15 % as recirculation gas and 15% as charcoal. F) Raw Materials: The raw materials include following: 1) Waste Plastic of density, sp gravity less then water Namely PP and PE. Method of testing raw material: Observations PE PP COLOR OF FLAME BLUE WITH YELLOW TIP BLUE WITH YELLOW TIP ODOR PARAFFIN ACRID OR DIESEL FUMES SPEED OF BURNING FAST SLOW SLOW < 3 INCH FAST>3 PER MIN OTHER CARACTERISTIC MELTS AND DRIPS ----------------------- 1
G) The Oil Standards: The oil directly obtained is crude oil which has less flash point of approx 38 degree centigrade. Hence to make it comparable to LDO the light volatiles are evaporated in second cracking column to make oil as comparable to LDO all its properties must match closely with standard Is specifications of LDO. The schematic diagram of the process with all its stages is given in adjoining diagram.the key indicators include flash point, viscosity, density etc. are within specified standards for LDO. The requisite standards applicable are attached for reference. AS NO SPECIFICATION IS AVAILABLE FOR RDF OIL WE ARE ENCLOSING LIGHT DEISEL OIL SPECIFICATION FOR REFERENCE. RDF OIL SPECIFICATION SHOULD MATCH CLOSE TO THIS Sl.No PARAMETER SPECIFICATION STD METHOD Typical Quality 1 RELATIVE DENSITY AT 15 REPORT IS 1448 (P:32) 855 ^C, KG/M3 2 FLASH POINT (PMC) 66 MIN IS 1448 (P:21) 74 3 VISCOSITY KINEMATIC AT 2.5 TO 15.7 MAX IS 1448 (P:25) 5.0 40 ^C, cst 4 WATER CONTENT % BY 1.0 MAX IS 1448 (P:40) <0.05 VOLUME 5 SEDIMENT % BY MASS 0.10 MAX IS 1448 (P:30) 0.04 6 ASH % BY MASS 0.02 IS 1448 (P:4) 0.01 For gas storage,we provide intermediate floating tank of suitable capacity. PLANT CAPACITY IN KG/24 HOURS GAS STORAGE TANK VOLUME GAS EQVIVALENT INTERMEDIATE STORAGE FOR FLOATING TANK 20 50 100 200 500 1000 80 LITER 200 LITER 500 LITER 800 LITER 1600 LITER 4000 LITER 57 143 357 571 1143 2857 2
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FOR CURRENT PRICES OF LDO PLEASE REFER WEBSITES BELOW WHICH PUBLISH CURRENT RATES AT REGULAR INTERVALS www.petroleumbazaar.com www.bharatpetroleum.co.in/yourcorner/petroprice.aspx?id=5 The price of crude which is primary product is available and fluctuates steadily as international market. In India the pricing sheet for LDO is as follows: STATE BASIC(Rs./KL) EX.DUTY EX EDU WORKS VAT(12.5%) RATE/KL RS/LITER (14%) Cess(3%) (Rs./KL) MAH 34840 4877.6 146 39863 4983 44846 44.84 OUR PLANT CAN USE VARIOUS INPUTS AS GIVEN BELOW AS FUEL.WE HAVE GIVEN BELOW GENERAL COST ANALYSIS BASED ON 10000 KCAL FOR CUSTOMER REFERENCE. COMPARISON OF VARIOUS FUELS LPG Electricity HSD LDO FO Kerosene Product Unit 1 KG 1 KWH 1 LITER 1 LITER 1 KG 1 LITER Calorific Value in kcal/unit 11840 860 10500 10000 9500 10420 Fuel efficiency % 80 100 62 60 50 60 Effective CV PER UNIT 9472 860 6510 6000 4750 6252 (Pune) 63 7 55 38 27 55 Costing for 10000 kcal 66.5 81.39 84.48 63.33 56.84 87.97 Savings % by using LPG 14.89 17.48 21.47 Consumption of fuel for 20 kg load at 25 kw 2.26 25 3.3 3.58 4.52 3.43 power(at 15 kw power) Cost in rs/liter at 100 % recovery of oil 7.1(4.26) 12.5(7.5) 9.07(5.44) 6.8(4.08) 6.1(3.66) 9.4(5.64) Cost in rs/liter at 70 % recovery of oil 10.14(6.08) 17.8(10.7) 12.95(7.77) 9.71(5.82) 8.71(5.22) 13.42(8.05) Cost in rs/liter at 50 % recovery of oil 14.2(8.52) 25(15) 18.14(10.88) 13.6(8.16) 12.2(7.32) 18.8(11.28) These calculations are based on 100% use of external fuel, but as the process itself generates natural gas which can be used for heating the system the consumption of gas is expected to be 60 % of the values quoted in the table. 4
PLANT COMPARISON IN VARIOUS CAPACITIES: PLANT 20 50 100 200 500 1000 CAPACITY IN KG/24 HOURS GAS 2.26 5.65 11.3 22.6 56.5 113 CONSUMPTION IN KG ELECTRICITY 2 KW 2 KW 5 KW 10KW 25 KW 25 KW REQUIRED WATER 400 LPH 400 LPH 1200 LPH 2400 LPH 6000 LPH 6000 LPH SUPPLY REQUIRED GAS STORAGE 80 LITER 200 LITER 500 LITER 800 LITER 1600 LITER 4000 LITER The above values are subject to change based on raw material and extracted output. COMPONENTS OF PRICING AS ROUGH ESTIMATE ARE AS FOLLOWS,IT IS SUBJECT TO CHANGE BASED ON RAW MATERIAL AND EXTRACTED OUTPUT: SR DESCRIPTION COST IN RS/KG % of total cost NO 1 RAW 16 66 PLASTIC+ PROCESSING COST 2 PROCESSING 3 12 COST : LABOUR 3 Profit 5 22 4 24 100 ADVANTAGE IN PROCESSING TO GENERATOR OF PLASTIC WASTE IS Saving in disposal and transport of waste plastic. If he himself is consumer of LDO he saves on sales tax, drum cost.net saving (8+4.25+3=15.25 rs/litre). 41.25-15.25=26 rs/litre will be his RDF cost. As you can see from the illustration the profitability of project is based on the oil recovery and end value added product cost. Factors affecting profitability: Oil being a commodity is subject to cyclic fluctuations, role of our plant is limited to processing costs and capital investments, the customer has to take care that he doesn t indulge in high value purchase of raw material over and above market rate to maintain profitability. 5