Title: Design and Evaluation of Novel Agriculture Byproducts Process Development
1Design and Evaluation of Novel Agriculture
By-products Process Development
- Mat Rasol Awang and Hassan Hamdani
MutaatBahagian Agroteknologi dan Biosains
Sivakumar Kumaresan, Dominic Foo Chwan Yee and
Ramlan Abd. Aziz, Chemical Engineering Pilot
Plant (CEPP), UTM, Skudai.
2INTRODUCTION
- Sterifeed Process Processing of oil palm Empty
fruit Bunch (EFB) into roughage feed materials. - Two by-products generated by this process
mushroom compost.
3STERIFEED
COMPOST
MUSHROOM
4Section 1 Raw Materials Preparation
Section 2 Fermentation
Section 3 Products Processing
5Pleurotus mushroom (Price US 3.06 /Kg)
Shiitake mushroom (Price US 9.86 /Kg)
EFB (Price US 0.01/Kg)
Cattle feed (Price US 78/tonne)
Compost (Price US 78 /tonne)
6White Oyster
Shiitake
7INTRODUCTION
- The economics of a processing technology depends
on its cost and revenues generated. - Two types of costs commonly used in the
estimation are a fixed cost and the other is
variable cost
8INTRODUCTION
- Economic and financial feasibility were examined
using Discounted Cash Flow Analysis (DCF) on
SuperPro Designer.
9INTRODUCTION
- SuperPro Designer is a comprehensive process
simulator for specialty chemical, biochemical,
pharmaceutical, wastes treatment processes etc.
10INTRODUCTION
- SuperPro Designer handles process simulation,
comprehensive economic evaluation, throughput
analysis, process scheduling etc. in a single
environment.
11INTRODUCTION
- SuperPro Designer capabilities enabling a quick
identification of process bottlenecks, reduce
capital and operating costs, shorten
time-to-market, perform accurate economic
analysis etc.
12OBJECTIVES
- to present the processing system layout of the
facility at MINT, built as a base case total
system - to evaluate economic and feasibility of the
process as well providing four schemes modifying
the base case to achieve its economic production
model.
13METHODS
- Build Process Flow Diagram using unit procedure
icons. - Key in actual cost capital cost of equipments,
operating cost. - Key in actual procedures and related parameters
14METHODS
- Solve the material energy (ME) balance of
Sterifeed process flow. - Determine the annual batch process.
- Scale up the process throughput by simulator
15METHODS
- Perform the economic calculations.
- Generate economic evaluation report
16METHODS (cont.)
- Capital budgeting involved Discounted Cash Flow
Analysis (DCF) Discounted Cash Flow Analysis
(DCF) and utilises investment criteria to make
accept / reject decision.
17METHODS (cont.)
- The investment criteria used are
- 1. Net Present Value (NPV)
- 2. Internal Rate of Return (IRR)
- 3. Net Benefit Cost Ratio (BCR)
- 4. Pay Back Period (PBP)
18METHODS (cont.)
- The Unit Production Cost (UPC) was computed based
on Break-even analysis. -
19Cost structure
20Unit Production Cost (UPC)
(Repayment of capital variable cost profit)
UPC
Volume of animal feed produced
21RESULTS AND DISCUSSION
Project Costs and Financing
22Economic Definition
- sales-cost of
goods sold - Gross Margin
- sales
gross profit
sales
23Economic Definition
- net
profit after taxes - Return of investment
-
total assets
24Economic Definition
- Internal rate of return is the discount rate that
equate the present value of cash inflows - Net present value (NPV) present values of cash
inflows initial investment.
25Scenario Analysis
Base case process simulation is a case of a
Scenario Analysis, one of the techniques employed
to evaluate stand-alone risk of a project.
Scenario Analysis considers both the sensitivity
of NPV to changes in key variables and the range
of likely variable values (Brigham, 1988).
26Sensitivity Analysis
Sensitivity Analysis is another technique to
measure stand-alone risk but it indicates the
change in NPV responding to a given change in an
input, other things held constant. (Brigham,
1988).
27Economic and Financial Indicators
28Economic and Financial Indicators
29Economic and Financial Indicators
30Economic and Financial Indicators
31Economic and Financial Indicators
32FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- A. TOTAL PLANT DIRECT COST (TPDC) (physical
cost) - 1. Equipment Purchase Cost 93,000
- 2. Installation
1,000 - 3. Process Piping
0 -
33FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- A. TOTAL PLANT DIRECT COST (TPDC) (physical
cost) - 4. Instrumentation 0
- 5. Insulation
0 - 6. Electricals
2000 -
34FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- A. TOTAL PLANT DIRECT COST (TPDC) (physical
cost) - 7. Buildings
10,000 - 8. Yard Improvement
4,000 - 9. Auxiliary Facilities
9,000 - ------------------------------------------------
----- - TPDC
119000
35FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- B. TOTAL PLANT INDIRECT COST (TPIC)
- 10. Engineering
7000 - 11. Construction
11000 - --------------------------------------------------
------ - TPIC
18000
36FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- C. TOTAL PLANT COST (TPDCTPIC) TPC
137000 - 12. Contractor's fee
1000 - 13. Contingency
4000 - --------------------------------
------------------------ - (1213)
5000
37FIXED CAPITAL ESTIMATE SUMMARY (2004 prices)
- D. DIRECT FIXED CAPITAL (DFC) TPC1213
143000
38LABOR REQUIREMENT AND COST SUMMARY
- Section Labor Hours Labor Cost
- Name Per Year /year
- --------------------------------------------------
--------- - Main Section 2024 7000
100.00 - --------------------------------------------------
--------- TOTAL 2024
7000 100.00 -
39RAW MATERIALS COST SUMMARY
- Raw Material Unit Cost Annual Amount
Cost - Bulk (/kg) (kg)
( /yr ) - --------------------------------------------------
----------------------------- - Lime 0.008
6666.79 56 0.23 - Rice bran 0.021
18518.87 390 1.57 - EFB 0.010
334451.61 3345 13.49 - Water 0.000
1481509.30 0 0.00 - Potato 0.042
59260.37 2495 10.07
40RAW MATERIALS COST SUMMARY
- Raw Material Unit Cost Annual Amount Cost
- Bulk (/kg) (kg)
( /yr ) - --------------------------------------------------
----------------------------- - Glucose 0.263
1185.21 312 1.26 - Liquid seed 0.010
2963.02 30 0.12 - Air 0.000
1240023.28 0 0.00 - Bag 0.028
56282.02 1576 6.36 - Box 0.066
9516.11 628 2.53 -
41RAW MATERIALS COST SUMMARY
- Raw Material Unit Cost Annual
Amount Cost - Bulk (/kg) (kg)
( /yr ) - --------------------------------------------------
----------------------------- - Discrete (/Entity) ( of
Entities) ( /yr ) - --------------------------------------------------
----------------------------- - Plastic Bottle 0.028
415446.53 11633 46.93 - Craft Paper Box 0.066
13848.22 914 3.69 - Plastic Bag 0.050
51840.00 2592 10.46 - Box 0.066
5184.00 342 1.38 - Animal Feed Bag 0.050
9512.71 476 1.92 - --------------------------------------------------
----------------------------- - TOTAL
25000 100.00
42ELECTRICITY
- Procedure Equipment Annual
Amount Cost - Name Name (
kWh ) ( /yr ) - --------------------------------------------------
------------------------ - P-1 MX-101
282 28 - P-2 SR-101
376 38 - P-12 FKLF-101
376 38 - P-14 V-106
17454 1745 - Inoculation INOC-102
141 14 - P-15 V-107
9650 965 -
43ELECTRICITY
- Procedure Equipment Annual
Amount Cost - Name Name (
kWh ) ( /yr ) - --------------------------------------------------
------------------------ - P-21 RDR-101
94 9 - P-22 RDR-102
94 9 - P-23 XD-101
705 71 - Unlisted Equipment
1823 182 - General Load
5470 547 - Additional Electricity
0 0 - --------------------------------------------------
------------------------ - SUBTOTAL
3647
44HEAT TRANSFER AGENT Steam (4.2000 /1000 kg)
- Procedure Equipment Annual
Amount Cost - Name Name ( kg
) ( /yr ) - --------------------------------------------------
------------------------ - P-11 ST-101
34217 144 - P-21 RDR-101
347207 1458 - P-22 RDR-102
148803 625 - --------------------------------------------------
------------------------ - SUBTOTAL
2227
45HEAT TRANSFER AGENT Chilled Water (0.4000
/1000 kg)
- Procedure Equipment Annual
Amount Cost - Name Name ( kg
) ( /yr ) - --------------------------------------------------
------------------------ - P-15 V-107
1104298 442 - --------------------------------------------------
------------------------ - SUBTOTAL
442
46HEAT TRANSFER AGENT Cooling Water (0.1000
/1000 kg)
- Procedure Equipment Annual
Amount Cost - Name Name ( kg
) ( /yr ) - --------------------------------------------------
------------------------ - P-11 ST-101
2224467 222 - --------------------------------------------------
------------------------ - SUBTOTAL
222
47ANNUAL OPERATING COST - SUMMARY (2004 prices)
- Cost Item /Year
- --------------------------------------------------
------------ - Raw Materials 25000
38.44 - Labor-Dependent 7000
11.09 - Facility-Dependent 25000
38.67 - Laboratory/QC/QA 1000
1.66 - Consumables 0
0.00 - Waste Treatment/Disposal 0
0.00 - Utilities
7000 10.14 -
48ANNUAL OPERATING COST - SUMMARY (2004 prices)
- Cost Item /Year
- --------------------------------------------------
------------ - Transportation 0
0.00 - Miscellaneous 0
0.00 - Advertising and Selling 0
0.00 - Running Royalties 0
0.00 - Failed Product Disposal 0
0.00 -
- TOTAL 64000
100.00
49PROFITABILITY ANALYSIS (2004 prices)
- A. DIRECT FIXED CAPITAL
143000 - B. WORKING CAPITAL
4000 - C. STARTUP COST
7000 - D. UP-FRONT RD
0 - E. UP-FRONT ROYALTIES
0 - F. TOTAL INVESTMENT (ABCDE)
15400 - G. INVESTMENT CHARGED TO THIS PROJECT 154000
50H. REVENUE STREAM FLOWRATES
- /year of Packaging Box (in Mushroom Box)
5184.0 - /year of Animal Feed Bag (in Animal feed
Bag 9512.7 - kg/year of total flow (in Compost)
74217 -
51I. PRODUCTION (UNIT) COST
-
- /Packaging Box (in Mushroom Box)
12.440
52J. SELLING/PROCESSING PRICE
- /Packaging Box (in Mushroom Box)
19.730 - /Animal Feed Bagged (in Animal feed Bag)
1.950 - /kg of total flow (in Compost)
0.078
53K. REVENUES (/year)
- Mushroom Box
102000 - Animal feed Bag
19000 - Compost
6000 - ----------------------------------------------
----------------- - Total Revenues
127000
54- L. ANNUAL OPERATING COST
64000 - M. GROSS PROFIT (K-L)
62000 - N. TAXES (40 )
25000 - O. NET PROFIT (M-N Depreciation )
51000
55Conclusion
- The above analysis indicates that on financial
ground and with the assumptions made, this
project is highly viable.