Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Process multiplier implementation

Further development of synthesizers was critically dependent on the technology of multiplier implementation, TI s early 2 bit by 4 bit Wallace Tree [Karen, 1993] [Waser and Flynn, 1982] was introduced in 1974. The AMD25S10 was an early improvement 4 bits by 4 bits. Monolithic Memories 74S558 multiplier was 8 bits by 8 bits. The major improvement was the 16 by 16 multiplier (the TRW MPY-16). This single chip did more for audio signal processing than almost any other device. It was used for many of the IRCAM machines and also the Alles synthesizer. [Pg.402]

Equation 8.19 can be used for analysis of both steady-state and dynamic optimization problems. In time-varying processes, actual implementation of optimum operation policies requires discretization of the dynamic trajectories [ 165]. In these cases, the vectors of state variables, end-use properties and manipulated variables include the set of discretized values along the whole dynamic trajectory. This means, for example, that NX equals the number of state variables multiplied by the number of discretized intervals (or sampling intervals). Finally, it must be clear that some of the weighting values can be equal to zero, which means that some of the available data may not be relevant for operation of the analyzed polymerization problem. [Pg.342]

Continuous processes are more efficient than batch processes, as the use of stationary phase is optimized and the amount of eluent needed for the purification is significantly reduced. The concentration of feed mixture inside the column can be much higher than it is in the case of a batch process. As a consequence, productivity is multiplied by a factor of two to five, less manpower is required, usage of stationary phase is optimized, and the amount of solvent used is reduced by a factor of two to ten. Two multicolumn continuous chromatography processes have been commercially implemented at commercial scale for pharmaceutical chiral separahons, these being the simulated moving bed (SMB) process and the Varicol process [15-17]. [Pg.251]

Computational complexity The most used parameter here is the signal processing complexity, i.e. the number of multiply-accumulate instructions necessary to process a block of input samples. If the algorithm is implemented on a general purpose computing architecture like a workstation or PC, this is the most important complexity figure. [Pg.36]

The prime in Eq. (3-62) indicates that the sum is restricted to sites that do not belong to the same molecule. Depending on the specific implementation the tensors T(1) are multiplied with appropriate /e factors for the associated atoms. The last term in Eq. (3-59), efacM, is the macroscopic electric field. This completes the most usual form of vpo1, i.e., the potential of the dipoles due to the total field at the polarizable sites is made a part of the effective Hamiltonian and Eq.(3-24) is solved self-consistently. Since the induced dipoles M in the solvent (MM) part are self-consistent for any field E, i.e., also for intermediate fields during the iterative process for solving Eq. (3-24), in this way we obtain an overall self-consistent solution, similar to, e.g., the HF or Kohn-Sham procedure. Extension to post-HF methods are straightforward because the reaction potential (RP) is formally a one-particle... [Pg.61]

Potential applications for FEM in plastics processing have multiplied in recent years due to development and implementation of additional substance-related laws and calculatory methods. [Pg.353]

So the basic conventional control structure selected has reflux-to-feed ratio. This is implemented in Aspen Dynamics using a multiplier block (R/F) with one input being the molar flow rate of feed and the other input the specified reflux-to-feed molar ratio. Since Aspen Dynamics has the rather odd limitation of only being able to directly specify the mass flow rate of the reflux, a flow controller must be installed whose process variable signal is the reflux molar flow rate, and whose output signal is the reflux mass flow rate. This flow controller is put onto cascade with its set point signal coming from the R/F multiplier. [Pg.447]

Installing additional accessories in front of the ion source can render analytes amenable to ionization and subsequent mass spectrometric analysis. On-line sample treatment is especially important when analyzing liquid-phase, complex, and/or concentrated samples. For example a thermal vaporizer was used to enable analysis of liquid samples by a process mass spectrometer designed for gas analysis [196], This system has been successfully implemented in the monitoring of an esterification reaction [197]. The obtained data were in a good agreement with those recorded by in-line mid-infrared spectrometry. The setup incorporated a magnetic sector analyzer with two detectors an electron multiplier detector... [Pg.124]

Pulse compression requires a separate matched filter be supported for each waveform used by the radar system. In practice, this filter is implemented via fast convolution as illustrated in Fig. 17.12. From Fourier transform theory, frequency-domain multiplication is equivalent to time-domain convolution. Hence, receiver digitized output data is input to a FFT, multiplied by the Fourier transform of the matched filter response, and then passed through an inverse FFT (I FFT) to output time-domain data. The matched filter reference functions transforms are generally computed off-line and stored in memory to support real-time processing. Fast convolution significantly reduces the number of operations required compared to time-domain direct convolution of returns and the appropriate matched filter function. [Pg.1837]

The different measures help to improve and further strengthen the supply chain differentiation process and to create preconditions for the smooth transition into multiply supply chains. PC Manufacturing Inc. has to fidfiU these measures in order to introduce the supply chain differentiation process. Next to the outlined methods, there are manifold ways of conducting project management in this context. These methods are meant to create an understanding of the implications of preparing and implementing the supply chain differentiation process. [Pg.304]

Damman grating to replicate the source inputs. The use of the CGH to replicate the inputs comes from the CGH property that the spots in the replay field are the Fourier transform of input illumination. Since only one channel is likely to be required at each output, those not required can be blocked using liquid crystal shutters. Such switches are based on the Stanford vector matrix multiplier (SVMM) [50] related switching devices [51]. When implemented using a CGH to fan out, and with a 2D array of inputs (rather than the 1D arrays of the SVMM) to simplify the free space optics, these are called matrix - matrix switches [52]. This kind of structure is found in a range of optical processing architectures (see Sec. 2.4). For a symmetrical switch with n inputs and n outputs, an array of nxn shutters is required. [Pg.830]

The multiplier could be implemented as a function or as part of a process that will form a component. A function would probably be the best solu-... [Pg.202]

The Booth recoding algorithm of this multiplier required a behavioural implementation as opposed to the structured approach taken with the carry-lookahead adder. A behavioural style allows the multiplier to be implemented in different ways, such as a function or a process. The former ap-... [Pg.210]

In signal processing systems a very common computation is the multiply accumulate A= A + B C. Design such a multiply accumulator, assuming a 16-bit input A and 3-bit inputs B and C. You will need to implement A as a registei> which will need a reset feature. In addition, a dock or control signal is needed to tell tiie drcuit when new values of B and C are available. [Pg.216]


See other pages where Process multiplier implementation is mentioned: [Pg.8]    [Pg.72]    [Pg.922]    [Pg.226]    [Pg.516]    [Pg.29]    [Pg.29]    [Pg.303]    [Pg.420]    [Pg.92]    [Pg.413]    [Pg.157]    [Pg.474]    [Pg.46]    [Pg.752]    [Pg.172]    [Pg.698]    [Pg.204]    [Pg.450]    [Pg.803]    [Pg.4]    [Pg.8]    [Pg.472]    [Pg.49]    [Pg.261]    [Pg.93]    [Pg.1844]    [Pg.336]    [Pg.75]    [Pg.314]    [Pg.1377]    [Pg.157]    [Pg.732]    [Pg.11]    [Pg.169]    [Pg.276]   


SEARCH



Multipliers

Multiply

Multiplying

Process implementation

© 2024 chempedia.info