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4

In an ordinary chemical plant, electrical installation cost may be about

A. 10-15% of purchased equipment cost

B. 3-10% of fixed capital investment

C. Either (A) or (B)

D. Neither (A) nor (B)

Correct Answer :

C. Either (A) or (B)


Related Questions

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4

For a typical project, the cumulative cash flow is zero at the

A. End of the project life

B. Breakeven point

C. Start up

D. End of the design stage

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4

If an amount R is paid at the end of every year for 'n' years, then the net present value of the annuity at an interest rate of i is

A. R [{(1 + i)n - 1}/ i ]

B. R [{(1 + i)n - 1}/ i (1 + i)n]

C. R(1 + i)n

D. R/(1 + i)n

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4

The depreciation during the year 'n', in diminishing balance method of depreciation calculation, is calculated by multiplying a fixed percentage 'N' to the

A. Initial cost

B. Book value at the end of (n - 1)th year

C. Depreciation during the (n - 1)th year

D. Difference between initial cost and salvage value

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4

Gantt chart (or Bar chart) is helpful in

A. Efficient utilisation of manpower and machines

B. Preparing production schedule

C. Efficient despatching of products

D. Inventory control

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4

The economic life of a large chemical process plant as compared to a small chemical plant is

A. Only slightly more

B. Much more

C. Slightly less

D. Almost equal

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4

The 'total capital investment' for a chemical process plant comprises of the fixed capital investment and the

A. Overhead cost

B. Working capital

C. Indirect production cost

D. Direct production cost

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4

Which of the following is the costliest source of getting hydrogen on commercial scale for the manufacture of nitrogenous fertiliser?

A. Coal gasification

B. Steam reforming of naphtha

C. Electrolysis of water

D. Coke oven gas

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4

Effective and nominal interest rates are equal, when the interest is compounded

A. Annually

B. Fortnightly

C. Monthly

D. Half-yearly

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4

Utilities cost in the operation of chemical process plant comes under the

A. Plant overhead cost

B. Fixed charges

C. Direct production cost

D. General expenses

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4

'Lang factor' is defined as the ratio of the capital investment to the delivered cost of major equipments. The value of 'Lang factor' for fixed capital investment, for a solid-fluid processing chemical plant ranges from

A. 1.2 to 1.4

B. 2.5 to 2.7

C. 4.2 to 4.4

D. 6.2 to 6.4

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4

Which of the following is not a mathematical method for evaluation of profitability of a chemical process plant?

A. Cash reserve

B. Rate of return on investment

C. Payout period

D. Discounted cash flow based on full life performance

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4

__________ of depreciation calculation accounts for the interest on investment.

A. Straight line method

B. Declining balance

C. Both (A) and (B)

D. Neither (A) nor (B)

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4

Maximum production start up cost for making a chemical plant operational is about __________ percent of the fixed capital cost.

A. 1

B. 5

C. 10

D. 30

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4

In a chemical process plant, the total product cost comprises of manufacturing cost and the

A. General expenses

B. Overhead cost

C. R & D cost

D. None of these

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4

Relative cost of chemical process plants in India is about __________ percent more than the similar plants in U.S.A.

A. 15

B. 35

C. 55

D. 75

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4

Which of the following is not a component of the fixed capital for a chemical plant facility?

A. Raw materials inventory

B. Utilities plants

C. Process equipment

D. Emergency facilities

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4

'Six-tenth factor' rule is used for estimating the

A. Equipment installation cost

B. Equipment cost by scaling

C. Cost of piping

D. Utilities cost

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4

Pick out the wrong statement.

A. Net worth means paid up share capital and reserve & surplus (i.e. shareholders equity)

B. Return on equity = profit after tax/net worth

C. Working capital turnover ratio = sales/net working capital

D. Total cost of production is more than net sales realisation (NSR) at breakeven point

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4

Optimum number of effects in a multiple effect evaporator is decided by the

A. Cost benefit analysis

B. Floor area availability

C. Terminal parameters

D. Evaporation capacity required

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4

Chemical engineering plant cost index is used for finding the present cost of a particular chemical plant, if the cost of similar plant at some time in the past is known. The present cost of the plant = original cost × (index value at present/ index value at time original cost was obtained). The most major component of this cost index is

A. Fabricated equipment and machinery

B. Process instruments and control

C. Pumps and compressor

D. Electrical equipments and material

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4

Break-even point is the point of intersection of

A. Fixed cost and total cost

B. Total cost and sales revenue

C. Fixed cost and sales revenue

D. None of these

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4

Profit is equal to revenue minus

A. Book value

B. Total cost

C. Operating cost

D. None of these

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4

If 'S' is the amount available after 'n' interest periods for an initial principal 'P' with the discrete compound interest rate 'i', the present worth is given by

A. (1 + i)n/S

B. S/(1 + i)n

C. S/(1 + in)

D. S/(1 + n)i

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4

For a given fluid, as the pipe diameter increases, the pumping cost

A. Decreases

B. Increases

C. Remains the same

D. May increase or decrease, depending upon whether the fluid is Newtonian or non-Newtonian

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4

Scheduling provides information about the

A. Proper utilisation of machines

B. Means to minimise idle time for machines

C. Time of completion of job

D. Time of starting of job and also about how much work should be completed during a particular period

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4

Which of the following is not a component of the working capital for a chemical process plant?

A. Product inventory

B. In-process inventory

C. Minimum cash reserve

D. Storage facilities

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4

__________ taxes are based on gross earnings.

A. Property

B. Excise

C. Income

D. Capital gain

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4

Which of the following is a component of working capital investment?

A. Utilities plants

B. Maintenance and repair inventory

C. Process equipments

D. Depreciation

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4

'Utilities' in a chemical process plant includes compressed air, steam, water, electrical power, oxygen, acetylene, fuel gases etc. Utility costs for ordinary chemical process plants ranges roughly from __________ percent of the total product cost.

A. 1 to 5

B. 10 to 20

C. 25 to 35

D. 35 to 45

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4

'P' is the investment made on an equipment, 'S' is its salvage value and 'n is the life of the equipment in years. The depreciation for Rath year by the sum-of years digit method will be

A. (P - S)/n

B. 1 - (P/S)1/m

C. (m/n) (P - S)

D. [2 (n - m + 1)/n(n + 1)]. (P - S)