ppt for budget 2014.pptx

8/11/2019 PPT for budget 2014.pptx

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Eliminate Outgoing Organic andconvert organic into FUEL,

recover RDF and RECYCLABLE

2



Objective of the Project.

Estimate Cost the project.

Cost benefit of the project.

Eliminate out going organic and

convert into FUEL recover RDF and

RECYCLABLES.



Plastic (Rigid)2.27%

Plastic (Film)5.28%

Plastic (Foam &Polystyrene)

1.21%Textiles9.27% Paper (mixed)

2.77%

Diaper / Pad10.60%

Wood

2.54%

Yard1.15%

Coconut Husk,Fiber & Shell

2.35%

Sponge0.79%

Ferrous & NonFerrous0.93%

Electrical Parts0.00%

Aluminum

0.00%

Glass (mixed)2.10%

Rubber / Leather

1.55%

Battery / Hazards

0.00%

Marble / Stone /

Ceramic3.54%

Cockle & OthersShell

1.42%

Cigarettes0.00%

Food & Organic52.24%

Composition of Organic (Rotary Screen)



Simulation for removal of MSW(organic)

components to produce RDF

MSW weight Removal RDF weight RDF

Kg % Kg %

Food & organic 5.52 65 1.93 35.32

Plastic 0.93 5 0.88 16.08

Paper 0.29 5 0.28 5.09

Rubber 0.24 10 0.22 4.06

Yard 0.12 95 0.006 0.11

Textile 2.1 0 2.1 38.39

Wood 0.51 90 0 0.94

Ferrous 0.098 0 0 0

Item



Simulation for removal of MSW(organic)

components to produce RDF

Food &organic

56%

Plastic10%

Paper3%

Rubber3%

Yard

1%

Textile21%

Wood5%

Ferrous1%



Final simulation from Organic

disposable

200 tan/ day

Actual Total

Composition weight (T)

Food & organic 56% RDF 112

Plastic 10% RDF 20

Paper 3% RDF 6

Rubber 3% RDF 6

Yard 1% RDF 2

Textile 21% RDF 42

Wood 5% RDF 10

Ferrous 1% recycleable 2

Total % Recover as



Eliminate out going organic and

convert into FUEL (Process

Flow) Organic will be separated after the screening

process where all the recyclable materials will be

sorted and balance of materials return to FORUS

Shredder as FUEL.

Pure Organic will be feed into Screw Press to

remove (moisture 15.95%) an average weight

reduction of (42.88%) mean says that the actualorganic net weight after the above process is 48.02

tones(from 112T).



PROJECT NAME: ORGANIC SCREW PRESS TESTING.

TESTING DESCRIPTION :REDUCE MOISTURE FROM

ORGANIC AND CONVERT TO RDF

DATE : 11/3/13 TO 19/3/13

WEIGHT MOISTURE

Before press After Press Before After Reduction lost %

11-Mar 9.30AM 1 520 300 60.96% 47.83% 220 13.13

11-Mar 4.50PM 2 520 320 63% 44.30% 200 18.72

12-Mar 2.30PM 3 4090 2390 59.20% 44.55% 1700 14.65

13-Mar 2.50PM 4 1080 630 64.94% 50.90% 450 13.97

13-Mar 5.15PM 5 630 460 50.97% 48.51% 170 16.44

14-Mar 2.41PM 6 1010 610 64.85% 46.19% 400 18.66

14-Mar 4.30PM 7 610 440 46.19% 44.45% 170 20.42

15-Mar 3.25PM 8 1080 500 63.29% 47.17% 580 16.57

15-Mar 5.30PM 9 500 400 47.17% 46.90% 100 17.89

MOISTURE (%)WEIGHT (kg)DATE TIME BATH



Proposed Organic to RDF

Layout

To PP

R e t u r n C o n v e y o r

RecyclablesConveyo

Rotary

Screen

Rotary

Screen

Rotary

Screen

Forus

Forus

Magnetic

Separator

Screw

Press

Drier

Organic

Screen

Rotary

Screen

Fee

ding

Organic will besorted in a

organic screen

Pure organics

pass throughscrew press and

drying, and sent

to power plant via

manual feeding

Balance from

RDF sent to

recyclables return

conveyor to be

processed



Estimated Project Cost

NO DESCREPCTION QTYUNIT

PRICE

1 DRYING SYS 1LOT 1,500,000

2 SCREEN SETTING AND REPAIR 1LOT 200,000

3

SCREW PRESS (12 TON

CAPACITY) 1UNIT 800,000

4 CONVEYOR SYS 1LOT 300,000

TOTAL 2,800,000



OPERATION COST/MTH

NO COST QTY AMOUNT

1 GAS COST 120,000

2 ELE COST 200/KW/HR 93,000

3 MAN POWER 4 PAX 5800

4 PERAIR AND MAINTENANCE 5000

TOTAL OPERATION COST

(RM 223,800.00 )



COST BENEFIT ANALYSIS

NO BENEFIT MONTHLY YEARLY

1 DISPOSABLE 252,000 3,024,000

2 RECYCLEABLE RECOVER 9000 108,000

3

RDF RECOVER FROMORGANIC

241,920 2,903,040

48TON/DAY

502,920 6,035,040

TOTAL RECOVER6,035,040

48TON /2.5 PER MW * RM 420.00



TOTAL SAVING PER YEAR

NO BENEFIT

INVESTMENT

COST

MONTHLY

RECOVER

ANNUAL

RECOVER

1 TOTAL RECOVER 502,920 6,035,040

2 PROJECT COST 2,800,000 2,800,000

1st YEAR (RM 3,235,040)

2nd YEAR (RM 6,035,040 )



Thank

You

ppt for budget 2014.pptx

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