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Setup operations

Finally, an important characteristic identified in chemical production processes are time-consuming and costly setup operations. Thus, the representation of time is a critical issue in the modeling of chemical production processes. Three fundamental deficiencies of the representation result if continuous processes are modeled by standard bucket-oriented lot-sizing models. These are the carry-over of setup states... [Pg.242]

The first issue, a setup state carry-over between adjacent periods, is depicted in Figure 11.3. On a continuous time scale a sequence of five products (A to E) can be modeled straightforwardly. However, if the same is to be done in a bucket-oriented setting some difficulties arise. Production within a bucket is coupled with a corresponding setup operation which causes a lot of problems. [Pg.243]

In Section 11.4.5, we have already seen that the SNP optimizer is restricted to plan in the SNP horizon. If campaign production problems are solved in the context of hierarchical planning it is important that the SNP optimizer respects setup operations of PP/DS orders in the overlap of the SNP and PP/DS horizon. This... [Pg.257]

Unfortunately, the continuous time representation of PP/DS can cause PP/DS campaigns not to satisfy the restrictions of the PLSP model that there is at most one setup operation per bucket. Another reason might be that due to manual modifications of the PP/DS plan the PLSP constraints are violated. Therefore, the PLSP model in the SNP optimizer has been extended in order to work with setup situations that are inconsistent with the PLSP. Given an initial setup state situation, the SNP optimizer tries to construct a model that keeps the cross bucket setup state conservation as good as possible. For example, in buckets in which there are already more than two different products no additional products may be planned. It is only allowed to extend the campaigns. [Pg.258]

Scheme 3 Diagram of a quartz crystal microbalance (QCM) setup operating under flow injection analysis (FIA) conditions... Scheme 3 Diagram of a quartz crystal microbalance (QCM) setup operating under flow injection analysis (FIA) conditions...
Equipment procedures documentation of safety precautions and step-by-step methods for equipment setup, operation, and cleanup... [Pg.68]

The Food Alliance has both fixed standards, which specifically prohibit the use of feed additives or subtherapeutic antibiotics, growth hormones, and genetically modified stock, and scored standards, which focus on more particular practices such as feed production, pasture management, manure management, and animal pest management. The Animal Welfare Institute (AWI) has also setup operational standards called the Humane Husbandry Criteria that farmers who produce meat for companies such as Niman Ranch voluntarily implement in order to receive the AWI certification. [Pg.92]

Edvardsson, M., Rodahl, M., Kasemo, B., and H66k, F. (2005). A dual-frequency QCM-D setup operating at elevated oscillation amplitudes. Anal. Chem., 77, 4918-4926. [Pg.141]

This very comprehensive process is a component of CRl. It is conducted for critical assets and, typically, discrete manufacturing equipment. The objective is to maximize the capability of the asset to perform its primary functions. It takes a complete look at the requirements for maintenance, setup, operations, changeover and shutdown, and documents these into standard operating and maintenance procedures. The results of a typical asset-facilitation process would include the following ... [Pg.1611]

Dobson, G. The cycUc lot scheduUng problem with sequence-dependent setups. Operations Research, 40(4) 736-749, 1992. [Pg.212]

This work was financially supported by the Shanghai Natural Science Foundation (12ZR1410000), National science and technology major project of water pollution control and treatment (2012ZX07414-001). We also appreciate the assistance of Shanghai Safbon water service Co. Ltd. in the experimental setup operation. [Pg.189]

The experimental setups, operating conditions, and procedures followed for the study of the hydrodynamics and mass transfer in the two-phase small scale contactors are discussed below. In general, the experimental semp comprises five main sections fluids delivery in the mixing zone, flow visualization, pressure drop measurement, online separation, and dioxouranium(VI) ion detection (Fig. 3.2). Depending on the nature of the measurements and the application, the semp was slightly modified for each set of experiments. [Pg.53]

It is helpful to compare the areal and volumetric power density of prior art versus theoretical calculation in Fig. 5b. The maximum areal and volumetric power density of prior art are 7.72 W/m and 3,685 W/m, respectively. The areal power density is close to the theoretical prediction of 10 W/m, while the volumetric power density is approximately one order of magnitude lower than the theoretical prediction of 2.5 x lO" W/m (both of 250 pm characteristic length). This discrepancy may be due to the effective chamber volume that ultramicroelectrode is associated with. The geometrical chamber volume may not be fully utilized by ultramicroelectrode. On the other hand, performance of prior art microscale MFCs have varied significantly, which may be due to different setups, operation procedures, inoculum, etc. [Pg.2195]

Single Minute A theory and the techniques for performing setup operations... [Pg.551]

Electrospinning Simple setup operating under ambient atmosphere. Unoriented, porous fiber mats with high surface areas Without additioneil treatment poor adhesion to substrate... [Pg.402]

Electrospraying Simple setup operating under ambient atmosphere. Preparation of films with nanoscaled features Deposition parameters need to be carefully controlled... [Pg.402]

Fig. 3 A scheme of the LICRM setup operating under compressive stress, 1, Laser light source 2, movable corner reflector 3, polarizer 4 and 5, photocells 6 and 7, semi-transparent mirrors 8, stationary corner reflector 9, specimen 10, support 11, puncheon 12, clock-like scale micrometer for rough controlling deformation 13, dampers 14, figured lever providing a stress constancy 15, load 16, oil damper 17, cooling unit 18, heater 19 and 20, programmable temperature regulator 21, amplifier 22, tape recorder 23, oscillograph 24, shaper of a meander (Schmitt trigger) 25, computer with the interface board imbedded... Fig. 3 A scheme of the LICRM setup operating under compressive stress, 1, Laser light source 2, movable corner reflector 3, polarizer 4 and 5, photocells 6 and 7, semi-transparent mirrors 8, stationary corner reflector 9, specimen 10, support 11, puncheon 12, clock-like scale micrometer for rough controlling deformation 13, dampers 14, figured lever providing a stress constancy 15, load 16, oil damper 17, cooling unit 18, heater 19 and 20, programmable temperature regulator 21, amplifier 22, tape recorder 23, oscillograph 24, shaper of a meander (Schmitt trigger) 25, computer with the interface board imbedded...
A significant increase in the pulp mobility (liquification) and homogenization can be achieved by vibration [27,44]. According to the published data [44,45], in a rotational setup operating at a rate of 3000 rev/min, the viscosity of a 15% pulp slurry was about 10 Pa s with the power consumption on the order of a few watts per cm. It is of interest to estimate the fraction of consumed power that has been used in overcoming the friction forces in the contacts between fibers. [Pg.108]

The techniques for performing setup operations in imder 10 minutes, the number of minutes expressed in a single digit. The SMED philosophy is important in moving from "batch-" to "flow-oriented" supply chains. Chapter 26... [Pg.437]

Verification Case for Model Setup Operation Data... [Pg.217]


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See also in sourсe #XX -- [ Pg.242 ]




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