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Variable recipes : to use or not to use

Citation for published version (APA):

Rutten, W. G. M. M., & Bertrand, J. W. M. (1993). Variable recipes : to use or not to use. (TU Eindhoven. Fac. TBDK, Vakgroep LBS : working paper series; Vol. 9334). Technische Universiteit Eindhoven.

Document status and date: Published: 01/01/1993 Document Version:

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Department of Operations Planning and Control-- Working Paper Series

Variable recipes: to use or not to use

W.G.M.M. Rutten and ].W.M. Bertrand

Research Report TUE/BDKlLBS/93-34 August, 1993

Graduate School of Industrial Engineering and Management Science Eindhoven U niversi ty of Technology

P.O. Box 513, Paviljoen Fll NL-5600 MB Eindhoven The Netherlands

Phone: +31.40.473828

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Variable recipes: to use or not to use

Abstract: Process industries often obtain their raw materials from mining or agricultural industries. These raw materials usually have variations in quality which often lead to variations in the recipes used for manufacturing a product. Another reason for using variable recipes is to minimize production costs by using the cheapest materials which still lead to a satisfactory quality in the product. A third reason for using variable recipes is in case that not all materials for the standard recipe are available. This last use of variable recipes can be avoided by keeping sufficient safety stock. This means that keeping safety stock can be balanced with using variable recipes. In this paper we study this issue by means of a small scale model of the situation. We construct a simple, quantitative model of the situation under investigation and for this simple situation we derive a decision procedure that balances safety stock costs and increased production costs.

1. Introduction

During the last decade, various articles have been published on production control in process industries. Most of these articles focus on the typical characteristics of process industry as compared to the discrete manufacturing situations. In this body of literature two extreme types of process industry can be distinguished; the process/ flow industry and the batch/mix industry (Fransoo and Rutten 1993). Process/flow is defined as: a manufacturer who produces with minimal interruptions in anyone production run or between production runs of products which exhibit process char-acteristics such as liquids, fibres, powders, gases etc. Batch/mix is defined as a process business which primarily schedules short production runs of products (Connor 1986). In this paper we concentrate on the batch/mix process industry.

Process industries often obtain their raw materials from mining or agricultural industries. These raw materials have natural variations in quality. For example, crude oils from different oil fields have different sulphur contents and different proportions of naphta, destillates and fuel oils. Oil refinery designs, production plans and operating schedules must account for this variability in crude oil qualities (Taylor et al 1981). May (1984) mentioned that material variability implies that the real characteristics of the material are usually not known until the production process is started. The variability in raw materials sometimes even determines which product will be produced (Rice and Norback 1987).

Variations in raw material quality often lead to vanatlons in bills of material (recipesl

) (May 1984, Cokins 1988). For example, variation in the moisture contents,

acidity, viscosity or concentration of active ingredients in different raw materials

1 A recipe is the specification of the amount of each raw material which is required per unit of measure of the finished product.

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may cause variations in raw material proportions required to make finished product quality specifications (Taylor et al 1981). This variation in raw material quality is one reason for using variable recipes.

A second reason for using recipes that are dependent on the quality of available materials is to minimize the total materials costs to produce the finished product. Then for each production order the recipe is determined such that the finished product quality specification is met with a combination of available raw materials which produces least costs. For example, a pet food may have specifications for the minimum amount of protein, carbohydrates and fat per pound of pet food; however, the proportions of various materials may be varied depending on their current price, quality and availability. In this way recipe variability is used to minimize product costs.

A third reason for varying the recipe of a product is that not all the materials which are required for the standard recipe are available at the time of production. This option is available if the finished product can be made with different recipes, whereby a specific cost is associated with each recipe. Of course, the recipe with the minimum costs is the standard recipe, but this standard recipe can only be applied if all raw materials required are available. If not all required raw materials are at hand, an alternative recipe may be applied which uses available materials, but ends up with higher costs. From this it follows that in this situation the use of variable recipes should be avoided. Two ways to avoid the use of alternative, more expensive reCI pes are:

1. to postpone production of the finished product until all raw materials in the standard recipe are available,

2. to always have sufficient raw materials available to cope with the demand for raw materials which follows from the demand for finished products.

The first condition can be satisfied if the market accepts variable lead times which depend on materials availability. Generally however, the finished products are com-modities which are delivered to many customers and for which a short, standard leadtime must be used in the market place to maintain competitiveness. Thus postponing production often is not a realistic option. The second condition can be satisfied if either the demand for finished products can be predicted with certainty over a horizon which covers the production throughput time plus the raw materials replenishment throughput time (the stacked leadtime) or, sufficient raw materials safety stock is kept to cope with the cumulated demand uncertainty over the stacked leadtime. In a commodity market, the customers usually demand short delivery leadtimes. Therefore, unless production and replenishment lead times are very short, the only means to avoid the use of alternative recipes is to have sufficient safety stock.

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An implicit assumption in the previous discussion is that all raw materials received are exactly according to their quality specification. Often however, raw materials have to be rejected or graded differently than ordered. This supply uncertainty in the replenishment orders of specific raw materials must be added to the require-ments uncertainty to get the total uncertainty that the materials planner has to cope with.

Now the question arises under what conditions, or to what extent, raw materials safety stocks should be used to cope with uncertainty, and under what conditions, or to what extent, alternative recipes should be used. It will be clear that the answer to this question depends on:

• the uncertainty to cope with • the costs of keeping safety stock

• the increase in production costs due to the alternative recipe.

In this paper we study this issue by means of a small scale model. The purpose of our study is to construct a simple, quantitative model of the situation under investigation and to derive a decision procedure for this simple situation that balances safety stock costs and increased production costs. The remainder of this paper is as follows. First, we will consider a simple model without variation in raw materials quality and derive an equation for balancing safety stock costs and increased production costs. Next, we will extend the model to situations with variable qualities in raw materials and show that the value of the balance equation increases, which means that using variable recipes becomes more attractive. In the last section, some conclusions are given.

2.

The simple model

We consider the situation with two finished products denoted x and

y,

and two raw materials, denoted a and

b.

Product x uses per unit demand one unit of raw material

a,

and product

y

uses per unit demand one unit of raw material

b.

However, product

y

can also be made out of raw material

a

(one unit per unit demand); but then the production costs increase. Raw materials are replenished using an (S - 1, S) replenishment system, with for both materials a replenishment leadtime of four periods. The order-up-to level S for each material is based on the average and variance in demand for its main product. The demand process is modelled as follows: Each period for each product one order is generated with order size according to an (n, A) Erlang distribution function. Orders are processed in the same period in which they are generated; there are no capacity limitations, only materials availability limitations. We measure the a service level, which is defined as

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the probability of no stockout in a period. The S-level has been set such that 95% (

=a) of all orders can be produced in the ordering period, assuming use of alternative recipes. For the time being we only consider demand uncertainty and neglect supply uncertainty. If due to lack of raw materials, an order for product x cannot be completely produced, the rest of the order is backlogged and has priority in the next period when competing for materials. If due to lacking materials an order for product

y

cannot be completely produced, the (rest of the) order is produced out of material a. If there is not enough material a, the rest of the order for product

y

is also backordered.

Now it will be clear that when using the alternative recipe for product

y

two things will happen. First, in 5% of the cases for product y an out of stock situation occurs and the alternative recipe will be tried for. This will be succesfull in at most 95% of the cases (service level of material a is 95%, we neglect the interactions). This will result in an upperbound for the service level for product

y

of 0.95 + 0.05 x 0.95 =

0.9975. Also this will result in an increase in the costs of product y. Suppose that producing product

y

out of material a costs p times the costs of producing it out of material

b,

denoted by Cpo Then under the conditions indicated the average costs for product y would be: 0.95 x cp +0.05 x

P

x c

r

The increase in cost per unit then is:

(p-1) x 0.05 x c

r

Second, in approximately 5% of the cases, material a will be used for

product y and this will decrease its availability for product x. This will lead to a reduction in service level for product x. The magnitude of the reduction depends on the level of safety stock.

From the reasoning above it follows that when using recipe flexibility it is impossible to control the service levels of x and

y

only by manipulating the S-levels of a and

b.

For instance, we could decrease the Sb-Ievel such that the actual service level for product

y,

using recipe flexibility, is equal to 95%. This however will increase the number of occasions where a will be used for

y

and will decrease the availability of a for product x. Thus the service level for product x will decrease. Suppose we try to compensate that by increasing the Sa-level to the extent that the service level of x is again 95%. Then the service level for y will increase also, because the probability of succes when trying the alternative recipe increases.

In short, due to the single-direction recipe flexibility, the service level of product

y

will always be larger than the service level of product x. This phenomenon is illustrated in Table 1 which shows the actual service levels ax and ay , the (relative) number of cases where the alternative recipe is used, #ay , the mean fraction of material a in product y,

fa,

and the average material stock levels Inva and Invb, as a function of the S-level for material

b,

for two combinations of the variation coefficients in demand for x and

y.

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Table 1 Simulation results when using variable recipes. The S-Ievel a is 3661, which is the 95% service

level for product x with a leadtime of four periods. S-Ievelb is changed in order to decrease the ay • The results given are the means of 15 runs of 4.000 periods each. The number of cases where the alternative recipe is used, #ay , is lower than expected since we use an order-up-to level which is based on a backorder situation. The demand for raw material b, however, can be considered as a lost sales situation (if no b is available, a is used and thus demand for b is lost). Using a 'backorder order-up-to level' in a lost sales situation results in a higher a (Rutten et al. 1992), and therefore the resulting #ay will be lower. cr'/Ilx crilly S-Ievelb ax (%) ay (%) fa (%) #ay (%) Mean Mean

Inva Invb 400/ 400/ 3661 (95%) 94.33 99.38 2.88 3.09 1832.43 1908.82 400 400 3197 (90%) 93.67 98.67 5.46 5.82 1789.28 1495.53 2907 (85%) 93.03 97.90 7.91 8.47 1748.69 1254.10 2688 (80%) 92.35 97.00 10.27 10.95 1709.44 1082.83 2510 (75%) 91.65 96.20 12.58 13.36 1671.41 952.17 2356 (70%) 90.95 95.25 14.91 15.65 1633.42 846.25 400/ 200/ 2788 (95%) 94.76 99.68 1.34 3.09 1858.09 1018.75 400 400 2590 (90%) 94.57 99.37 2.56 5.81 1837.05 843.57 2462 (85%) 94.38 99.02 3.76 8.32 1816.52 737.96 2363 (80%) 94.20 98.64 4.96 11.02 1796.01 661.44 2281 (75%) 93.97 98.30 6.18 13.48 1775.32 602.19 2208 (70%) 93.79 97.89 7.43 15.91 1754.03 552.66

One way to tackle this control problem is to let the use of the alternative recipe depend on the cumulative measure of the service level, which is defined as the actual service level measured in the current subrun (2.000 periods). If the

cumulative service is below the target (95%) then the use of the alternative recipe is allowed for the production order considered. If not, then the alternative recipe is not used, the order is backlogged to the next period. Using this decision procedure the control of the service levels improves a lot, as is shown in Table 2.

Table 2 Simulation results with using variable recipes and tuning ~. The target a for controlling the service level of product y is 95% in all situations. The situations are i entical to the ones in Table 1. The results given are the means of 15 runs of 4.000 periods each.

cr'/Ilx crilly S-Ievelb ax (%) CXy (%) fa (%) #ay (%) Mean Mean

Inva Invb 400/ 400/ 3661 (95%) 94.87 95.65 0.51 0.48 1872.14 1889.24 400 400 3197 (90%) 94.09 94.98 3.42 3.49 1823.84 1483.63 2907 (85%) 93.36 94.91 6.46 6.62 1773.17 1248.64 2688 (80%) 92.56 94.84 9.27 9.64 1726.47 1081.40 2510 (75%) 91.81 94.75 11.92 12.54 1682.55 951.89 2356 (70%) 91.03 94.45 14.54 15.21 1639.78 846.77 400/ 200/ 2788 (95%) 94.95 95.72 0.20 0.43 1877.34 1008.18 400 400 2590 (90%) 94.71 95.04 1.51 3.04 1854.95 836.23 2462 (85%) 94.48 94.99 2.90 5.75 1831.35 732.91 2363 (80%) 94.26 94.97 4.26 8.75 1808.29 658.83 2281 (75%) 94.03 94.96 5.58 11.40 1785.78 600.56 2208 (70%) 93.83 94.93 6.93 14.06 1762.60 552.45

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There is still interaction between the service levels of the two products, but since the service level of y is under control for each order-up-to level of Sb, the order-up-to level of Sa can be determined experimentally (for instance via simulations) such that the service level ax is equal to 95%, as is shown in Table 3.

Table 3 Simulation results with using variable recipes and tuning <X

r

The S-Ievel a is increased until <Xx = 95%. The situations are identical to the ones in Table 1. The resu ts given are the means of 15 runs of 4.000 periods each.

cr/flx crl~ S-Ievelb increase <Xx (%) <Xy (%) fa (%) #ay (%) Mean Mean

S-Ievela Inva Invb

400/ 400/ 3661 (95%) 10 94.97 95.65 0.51 0.48 1881.63 1889.24 400 400 3197 (90%) 100 94.96 94.98 3.41 3.50 1918.72 1483.46 2907 (85%) 195 95.01 94.92 6.43 6.50 1958.38 1248.81 2688 (80%) 265 94.97 94.90 9.32 9.53 1975.99 1082.65 2510 (75%) 330 94.93 94.88 11.92 12.40 1993.80 954.52 2356 (70%) 415 94.98 94.87 14.60 14.97 2029.72 849.54 400/ 200/ 2788 (95%) 0 94.95 95.72 0.20 0.43 1877.34 1008.18 400 400 2590 (90%) 30 94.97 95.04 1.52 3.04 1883.35 836.31 2462 (85%) 57 94.95 94.99 2.91 5.75 1885.26 733.04 2363 (80%) 90 94.98 94.97 4.27 8.66 1893.43 659.19 2281 (75%) 110 95.00 94.97 5.58 11.34 1889.94 600.68 2208 (70%) 130 94.95 94.94 6.94 14.00 1885.61 552.69

Now suppose that we know all combinations of S~ and Sb which produce ax=ay=

95%, and compare these with the levels Sa and Sb which lead to a x=ay=95% in the situation without use of alternative recipes. Then it will be clear that: S~ - Sa <

Sb-S'b, since with the use of the alternative recipe, some of the demand uncertainty for material

a

and

b

is puzzled. As a result the total of inventory decreases with an amount: Sb-S'b+Sa-S~,

This decrease in inventory must be valued and balanced against the increase in production costs, which can be modelled as:

fax (p -

1) x

c

p per unit production

y,

where

fa

is the mean fraction of product

y

which is made of alternative material a

and

(p -

1) is the increase in production costs per unit. To obtain the annual increase in production cost we multiply this by Dy ' the annual demand for product y. Since with each combination (S~, Sb) a fraction of alternative recipe use of

fa

is involved, denoted by

fa:

the entire range of combinations can be valued as follows:

Determine from among all combinations (S~ Sb) the combination such that

ax

=

ay

=

95% for which the following expression takes a maximum value:

(Sb-Sb+Sa-S')xCj -

fa

'x (P-1) x cp xDy (1) where the costs Cj consist of capital investment cost related to the product, valued at the interest rate, plus the costs of the capital invested in inventory related infrastructure (silos etc.)

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If this maximum value is negative than it does not pay to use the alternative recipe. Then the increase in production costs is never offset by the decrease in inventory holding costs. However if this maximum value is positive then the use of alternative recipes can lead to a decrease in total costs, provided of course that the right combination of Sa and Sb is used. Figure 1 illustrates equation (1), using the numbers from Table 3. As can be seen in Figure 1, the maximum p for which it still pays to use alternative recipes under the given conditions, equals 1.0159 and therefore the maximum per unit increase in product costs

((p

-1) x cp ) in case of alternative recipe use equals 1.59%. Since the profit margins are very small in the commodity market, this value is of significant importance.

t

Value equation (1) 15,000 10,000 5,000 -5,000 -10,000 I

t

+415, 2356 1.0050 1.0100

t

t

+330, +265, 2510 2688

t

+195, 2907 5-levelb ---. + 100, increase 5-levela +10, 3197 5-levelb 3661

Figure 1 Equation (1) for the situation with cr/I-!x = crilly = 400/400, for several factors p. The different (5' a'S' b) combinations are marked on the x-axis, the y-axis gives the value of equation (1). The factor cj

is calculated as the capital investment cost related to the product, valued at an interest rate of 15%. Factor cp equals 100 and annual demand for product y is taken 100,000 (250 xI-!) units.

3. Variation in raw materials quality

In many process industries, raw materials are graded at arrival. For instance in animal food industry, soya is used in which the fraction of protein is the main ingredient to classify soya. If 'soya class II' is ordered, the arriving replenishment lot can be in class I, II or III, where a higher class stands for more protein. Thus the grading process can yield a lower, but also a higher quality than ordered. We still consider the case with two products and two raw materials, which means that grading raw materials is worked out as follows: raw material a is reordered and at delivery we detect (with probability q) if the raw material indeed is raw material a,

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or if it can be classified as raw material

b

instead. The same procedure is followed for raw material b turning out to be a.

Due to this supply uncertainty, the Sa and Sb levels have to be increased, even if we

do not use variable recipes. So first we have to find the inventory levels which are necessary to achieve the service level of 95% without using variable recipes (the (SIP

SiJ

values). Second, we will use variable recipes, and an equal procedure as shown in the previous section can be followed; we decrease the Sb-Ievel and control the service level of product

y

and we increase the Sa-level to achieve the situation where ux=uy

=95%. In Table 4, the results of this procedure are shown for one combination of variation coefficients in demand for x and y and for two values of the probability

that the material received equals the material ordered (q).

Table 4 Simulation results with grading of raw materials. We use two values for the probability that the material received equals the material ordered (q). In the situation without using variable recipes, first the results are shown if no correction on the S-Ievels is made and second the corrected situation is shown. The S-Ievels for the corrected situation are the (Sa' Sb) combination for keeping safety stock. In the situation with variable recipes, several (5' a' 5' b) combinations are given for which ax = ay = 95%. The results given are the means of 15 runs of 4,000 periods each.

cr;~x cr!~ q 5-level a S-Ievelb ax (%) ay (%) fa (%) #a Mean Mean

(%) Inva Invb

without using variable recipes, keeping safety stock

400/ 400/ 0.90 3661 3661 93.10 93.10 0.00 0.00 1943.50 1951.98

400 400 3911 3911 95.03 95.01 0.00 0.00 2178.80 2187.22

0.70 3661 3661 87.79 88.05 0.00 0.00 2244.55 2282.32 4561 4561 94.94 95.03 0.00 0.00 3071.15 3110.19 with using variable recipes

400/ 400/ 0.90 3911 3911 95.02 95.78 0.45 0.45 2164.21 2194.29 400 400 3911 3661 94.95 95.21 1.37 1.32 2135.43 1970.84 4025 3197 94.93 94.98 4.75 4.61 2164.06 1593.56 4131 2907 95.02 94.94 7.81 7.54 2192.85 1389.33 4186 2688 94.91 94.91 10.09 9.96 2189.73 1219.51 4271 2510 94.99 94.93 12.74 12.62 2210.78 1104.86 4326 2356 94.93 94.91 15.20 15.26 2208.62 1004.28 0.70 4561 4561 95.30 96.18 0.67 0.55 2983.81 3091.48 4696 3661 95.02 95.06 3.31 3.17 2840.51 2454.84 4761 3197 95.06 95.02 6.42 5.97 2764.65 2086.44 4826 2907 95.17 94.95 8.68 8.17 2720.66 1925.60 4946 2688 94.94 94.93 10.00 9.71 2735.41 1870.97 4971 2510 94.90 94.94 11.74 11.36 2701.85 1721.13 5071 2356 94.90 94.94 12.88 12.43 2703.66 1679.70

Finally, equation (1) can be used again to find the maximum per unit increase in production costs

((p-

1) x cp ) in case of alternative recipe use, for which it still pays

to use alternative recipes. Under the given conditions, the maximum equals 3.44%, as is shown in Figure 2. For q=o.90, the maximum equals 2.73%.

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20,000 10,000

t

Value 0

~,...:::::::::=---=;:::7"'"-=:::::;~~~~~

equation (1) -10,000 5-levelb ---. -20,000 I

t t

t

t

t

t

t

5071 4971 4946 4826 4761 4696 5-levela 4561 2356 2510 2688 2907 3197 3661 5-levelb 4561

Figure 2 Equation (1) for the situation with cr,/Ilx = cr/~ = 400/400 and variation in raw materials (q=0.70), for several factors p. The different (5' a'S' b) combinations are marked on the x-axis, the y-axis gives the value of equation (1). The factor c1 is calculated as the capital investment cost related to the product, valued at an interest rate of 15%. Factor cp equals 100 and annual demand for product y is taken 100,000 (250 xll) units.

4.

The analysis of the model

It will be clear that the outcome of the balancing process heavily depends on the parameters of the model used, and thus depends on the characteristics of the production process. The purpose of this paper is to determine for the simple situation considered the set of parameter values for which the use of the alternative recipe is economically justified. For that purpose we first have determined (for a range of values of combined uncertainty in demand and supply (grading of an arriving replenishment lot) in both products) the (S~ S',) values that are required to realise a service level of 95% in both products with alternative recipe use, and the

(Sa' S,) values without alternative recipe use.

Next we have determined the value of the factor

p

for which equation (1) is equal to zero. This yields the maximum per unit increase in product costs

((p

-1) x

c)

in case of alternative recipe use, for which it still pays to use alternative recipes. For higher per unit cost increase values, the variable recipes should never be used under the given conditions, and all uncertainty should be compensated by holding safety stock.

In conclusion, if the variability in raw materials increases (lower q), the use of variable recipes becomes more attractive. Even if there is no variability In raw

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materials, there still are situations in which it is favorable to use variable recipes instead of holding safety stock. We developed a decision procedure to find the balance in keeping safety stock and using variable recipes. The conclusions are of course limited to the simple model we used. Nevertheless, considering the results for this simple model, examining more complex and realistic situations can be argued.

References

COKINS G.M., 'Control systems for process industries', Manufacturing Systems,

vol. 6, no. 5, 1988, pp. 79-85.

CONNOR S.]., Process Industry Thesaurus: American Production and Inventory

Control Society, 1986.

FRANSOO ].C. and W.G.M.M. RUTTEN, :4 typology ofproduction control situations in

process industries: Research report TUE!BDKhBS!93-02, Eindhoven University

of Technology, Graduate School of Industrial Engineering and Management Science, 1993.

MAY N.P., 'The functions needed for process-oriented systems', APICS 1984 Conference proceedings, 1984, pp. 29-32.

RICE ].W. and ].P. NORBACK, 'Process industries production planning using matrix

data structures', Production and Inventory Management Journal second quarter,

1987, pp. 15-23.

RUTTEN W.G.M.M., K. VAN DONSELAAR, A.G. DE KOK and G.].K. REGTERSCHOT,

'The lost sales inventory model: Research report TUE!BDKhBS!92-04, Eindhoven

University of Technology, Graduate School of Industrial Engineering and Management Science, 1992.

TAYLOR S.G., S.M. SEWART and S.F. BOLANDER, 'Why the process industries are

different', Production and Inventory Management Journal fourth quarter, 1981,

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Integrating material coordination and capacity load smoothing in multi-product multi-phase production systems

A heuristic policy for capacity coordination in multiple products single-machine production systems with stationary stochastic demands

Diagnosis of the long-term logistics performance of production units. Part I: the interior shop Diagnosis of the long-term logistics performance of production units. Part II: the turnery Demand management as a tactical decision tool in capacitated process industries The robustness of multi-echelon service models under autocorrelated demands On the time-phased resource requirements of quotations

On the logistics of recycling

Production control in multi-purpose batch process industries: a research proposal Mix nexibility in mixed material structures

Structuring of maintenance control systems

A method for evaluating and diagnosing inventory levels

Back-<lrder lead time behavior in (s,Q)-inventory models with compound renewal demand Hierarchical planning in a single stage system

Capaciteitsmanagement in het St Annaziekenhuis te ass Capaciteitsmanagement in het Elisabethziekenhuis te Tilburg

Implementing patient now based hospital resource allocation models in hospitals

Distribution planning for a divergent 2-echelon network without intermediate stocks under service restrictions

A model for the short-term logistic shop noor performance evaluation and diagnosis Het gebruik van operationele research modellen in de logistiek

Coordinating differential customer lead times in rea It ion to the manufacturing constraints Design of maintenance control systems

Optimal lead times planning in a serial production system Balancing capacity and inventory in repair inventory systems Variable recipes: to use or not to use

Demand management in a multi-stage distribution chain Determining a maintenance budget for architectural systems

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