Flash vacuum pyrolysis of 2-(2-vinylstyryl)furan derivatives via electrocyclization followed by dehydrogenation will give 2-(2-naphthalen-2-yl)furan analogues, on the other hand, FVP of 2-(2-vinylstyryl)furan derivatives via electrocyclization followed by [1,5]-H shift will give 3-(2-furyl)-1,2-dihydronaphthalene analogues. FVP of 2-[2-(4-methoxyphenyl)vinyl]benzo[b]thiophene gave three products: trans-4-(2-benzo[b]thiophen-2-ylvinyl)phenol, benzo[b]naphtha[1,2-d]thiophen-2-ol and 1H-6-thiacyclopenta[c]fluorene.

1. 2-[2-(2vinylphenyl)ethenyl]thiophene ( 30 ) and 2,2-(o-phenylenedivinylene)dithiophene ( 31 ) were studied under pyrolytic and photolytic conditions, photolytic of 30 gave upon bicyclic product 35, whereas photolytic of 31 gave products 37 and 39, FVP of 30 and 31 gave 34 and 37, respectively,which all include naphthalene nucleus. 2. 2-methoxystilbene ( 17 ) and 3-methoxystilbene ( 18 ) were studied under pyrolytic conditions, FVP of 17 gave single product 2-Phenylbenzo[b]furan ( 23 ), FVP of 18 gave 2-phenanthrol ( 27 ), ( 4-phenanthrol ) ( 28 ), trans-3- hydroxystilbene ( 29 ), Fluoren 9 -one ( 30 ) and a pair of isomer 1H-benz[e]indene ( 11a ) and 3H-benz[e]indene (11b).

Following the growth of IC and opto-elctronic industry in Taiwan in recent years, vacuum coaters used in the both industries has drawn a lot attention and initiated a growing investment in this sector. Conventional wisdom toward this industry had been much related to consumer products such watch cases and low-price optical lenses and decorative plastic parts. Companies facing unique industrial market characteristics and tougher competition, Competitive strategies for Taiwanese players in this sector are explored. Resources based theory and related secondary industrial data were used to form a base on which a managerial strategy and marketing perspevtives are built. As limited source of industrial information available from existing vacuum coating companies in Taiwan either inform of interview or indigenous literature, the thesis were prepared mostly based on author's industrial experiences, data provided by author's company and related academy literature related to strategy. A further field study for a generalization of competition strategy shall be required and refined for this special industry in Taiwan.

Coordinated or synchronized tasks can always be found in various manufacturing processes, e.g., machining along spatial trajectories, coordinated operations of multi-manipulators, and vacuum pumps, etc. The vacuum pump is a typical device with synchronized motion among those examples. The vacuum pump has played an important role in current semiconductor manufacturing processes. Its pumping feature is achieved by synchronized motion of two mating pump rotors. A common approach to accomplish the synchronized motion is by idle gears. Nevertheless, this design cannot meet serious requirements of vacuum systems demanded by growing manufacturing techniques. In order to provide a complete and proper control strategy for synchronized motion, and to overthrow traditional architecture of vacuum pumps by raising a better control scheme for new generation oil-less products, the paper focuses on synchronized motion control for dual motors. The first objective of here is to develop a control method for synchronized motion of two separated motors. Both system uncertainties and unknown disturbances occurring in actual implementation need to be carefully considered. An experimental setup will also be established for examinations and verifications. And then synchronized motion control of dual motors including two mating screw rotors then will be investigated. During this period, the emphasis will be on solution finding for unexpected contact collision between two rotors. An effective and efficient control strategy will be developed for synchronized motion control of dual motors. Longer operation time and better synchronization performance for two motors can therefore be anticipated.

Abstract Coordinated or synchronized tasks can always be found in various manufacturing processes, e.g., machining along spatial trajectories, coordinated operations of multi-manipulators, and vacuum pumps, etc. The vacuum pump is a typical device with synchronized motion among those examples. The vacuum pump has played an important role in current semiconductor manufacturing processes. Its pumping feature is achieved by synchronized motion of two mating pump rotors. A common approach to accomplish the synchronized motion is by idle gears. Nevertheless, this design cannot meet serious requirements of vacuum systems demanded by growing manufacturing techniques. In order to provide a complete and proper control strategy for synchronized motion, and to overthrow traditional architecture of vacuum pumps by raising a better control scheme for new generation oil-less products, the paper focuses on synchronized motion control for dual motors. The first objective of here is to develop a control method for synchronized motion of two separated motors. Both system uncertainties and unknown disturbances occurring in actual implementation need to be carefully considered. An experimental setup will also be established for examinations and verifications. And then synchronized motion control of dual motors including two mating screw rotors then will be investigated. During this period, the emphasis will be on solution finding for unexpected contact collision between two rotors. An effective and efficient control strategy will be developed for synchronized motion control of dual motors. Longer operation time and better synchronization performance for two motors can therefore be anticipated.

The first chapter describe the pyrolytic and photolytic studies of substituted styrylarenes. Flash vacuum pyrolysis (FVP) of (2-(4-methoxystyryl)-N-methylindole) (18) gave (4-vinylphenol) (81)¡B (7-methyl-7H-benzo[c]carbazole) (82)¡B (benzo[c]carbazole) (83)¡B (1,6-dihydrocyclopenta[c]carbazole) (84) and (3,6-dihydrocyclopenta- [c]carbazole) (84'). FVP of 2',3,5-trimethoxystilbene (31) gave 2-(3,5-dihydroxyphenyl)benzo[b]furan) (26) and 2-(3,5-dimethoxy- phenyl)benzo[b]furan (95). FVP of 2-methoxy-4-(methoxymethyl)-1- [2-(4-methoxyphenyl)-1-methylvinyl]benzene (33) gave [2-(4- methoxyphenyl)-3-methylbenzofuran-5-yl]methanol (104)¡B4-(3,5- dimethylbenzofuran-2-yl)phenol (105) and 2-(4-hydroxyphenyl)-3- methylbenzofuran-5-carbaldehyde (106). FVP of 2-(2-chlorostyryl)- benzo[b]furan (44) ¡B2-(2-chlorostyryl)benzo[b]thiophene (45) and 2-(2-chlorostyryl)-N-methylindole (46) gave benzo[b]naphtha[1,2-d]- furan (116)¡Bbenzo[b]naphtho[1,2-d]thiophene (117)¡B7-methyl-7H- benzo[c] carbazole (82) and benzo[c]carbazole (83). FVP of 2-chloro-N-(N-methylindol-2-ylmethylene)aniline (71) gave N-methylindole-2-carbonitrile (124)¡B 7H-indolo[2,3-c]quinoline (125) and indolo[1,2-a]quinoxaline (126). FVP of 2-methoxy -N-(N-methyl- indol-2-ylmethylene)aniline (72) gave N-methylindole-2-carbonitrile (124) ¡B 2-(N-methylindol- 2-yl)benzoxazole (132) and 2-hydroxy- benzonitrile (133). FVP of 2-methylthio-N-(phenylmethylene)aniline (73)¡B2-methylthio-N-(furylmethylene)aniline (74)¡B2-methylthio-N- (benzo[b]thiophen-2-ylmethylene)aniline (75) and 2-methylthio-N- (N-methylindol-2-ylmethylene)aniline (76) gave 2-phenylbenzothiazole (143)¡B2-furylbenzothiazole (144)¡B2-benzo[b]thiophen-2-ylbenzo- thiazole (145)¡B2-(N-methylindol-2-yl)benzothiazole (146)¡B2-(1H- indol-2-yl)benzothiazole (147) and benzothiazole (148).Such a method, via oxygen-carbon bond disconnecting, can synthesize efficiently a nature product, stemofuran A 26. Photolytic study of 2',3,5-trimethoxystilbene (31) gave 1,5,7- trimethoxyphenanthrene) (101). Photolytic studies of 2-(2-chloro- styryl)benzo[b]furan (44) ¡B2-(2-chlorostyryl)benzo[b]thiophene (45) and 2-(2-chlorostyryl)-N-methylindole (46) gave benzo[b]naphtha- [1,2-d]furan (116) and 4-chlorobenzo[b]naphtha[1,2-d]furan (120)¡Bbenzo[b]naphtho[1,2-d]thiophene (117) and 4-chlorobenzo[b]naphtha- [1,2-d]thiophene (120) ¡B7-methyl-7H- benzo[c]carbazole (82) and 4-chloro-7-methyl-7H-benzo[c]carbazole (121). Photolytic studies of 2-methylthio-N-(phenylmethylene)aniline (73)¡B2-methylthio- -N-(furylmethylene)aniline (74)¡B2-methylthio-N-(benzo[b]thiophen-2- ylmethylene)aniline (75) and 2-methylthio-N-(N-methylindol-2- ylmethylene)aniline (76) gave 2-phenylbenzothiazole (143)¡B2-furyl- benzothiazole (144)¡B2-benzo[b]thiophen-2-ylbenzo- thiazole (145)¡B2-(N-methylindol-2-yl)benzothiazole (146)¡B2-(1H-indol-2-yl)benzo- thiazole (147) and 2-(2,4-dimethoxyphenyl)benzothiazole) (60f). Such a method has the potential for preparing drugs and application on material science. (¤G)FVP of 2-inden-1-ylidenemethylthiophene (24) and 2-inden-1-ylidene- methylfuran (25) gave the cyclized products 2-(2'-thienyl)naphthalene (29) and 2-(2'-furyl)naphthalene (32).

1.trans o-methoxystilbene and its derivatives 47a-f had been studied by means of pyrolysis and photolysis. Under pyrolytic conditions, compounds 47a-f gave not only the expected products 52a,c-f, but also their corresponding isomers 53a,c-f . Furthermore, compound 47b gave naphthalene (63) as the major product by opening the furan ring at higher temperature. Under photolytic conditions, compounds 47a-f gave the expected photocyclic products 2a-f and 109a-f.2.Pyrolytic chemistry of N-(N-Methyl-3-indolyl)methyl benzamide (45) hes been studied. Pyrolysis of 45 gave 3-methyl quinoline (38), 4-methyl quinoline (39) and secondary pyrolysis product quinoline (36). 2.Pyrolytic chemistry of N-(N-Methyl-3-indolyl)methyl benzamide (45) hes been studied. Pyrolysis of 45 gave 3-methyl quinoline (38), 4-methyl quinoline (39) and secondary pyrolysis product quinoline (36).

Thesis (Ph. D.)--University of Texas at Austin, 2000. / Vita. Includes bibliographical references (leaves 87-91). Available also in a digital version from Dissertation Abstracts.

Vacuum arc remelting is a secondary melting process used to produce a variety of segregation sensitive and reactive metal alloys. The present day VAR practice for superalloys involves, typically, melting electrodes of 17'' into ingots of 20'' in diameter. Even larger diameter forging stock is desirable. However, beyond 20'' ingots of superalloys are increasingly prone to segregation defects if solidification is not adequately controlled. In the past years a new generation of model-based controllers was developed to prevent segregation in VAR by controlling melt rate, or the total amount of power flowing into the liquid pool. These controllers were seen as significant improvements in the industry of remelting processes, but these controllers were still focusing on the melting sub-process and ignoring ingot solidification. Accurate control of the liquid pool profile is expected to result in segregation-free ingots, but unfortunately a controller capable of stabilizing the solidification front in VAR is currently not available. The goal of the proposed research is to develop a cyber-enabled controller for VAR pool depth control that will enhance the capabilities of current technologies. More specifically, the objectives of this research are threefold. Firstly, a control-friendly model is proposed based on a high-fidelity ingot solidification model and is coupled to a thermal model of electrode melting. Secondly, sequential Monte Carlo estimators are proposed to replace the traditional Kalman filter, used in the previous VAR controllers. And finally, a model predictive controller (MPC) is designed based on the proposed reduced-order model. The time-critical characteristics of these methods are studied, and the feasibility of their real-time implementation is reported. / text

Vapor pressure data are vital to understanding impacts that substances, specifically pesticides, may exert on the environment. They enter into atmospheric deposition models for such chemicals which determine the fate and transport of these species in the environment. At normal application temperatures (i.e. room temperature) the vapor pressures of many of these chemicals are too low to be determined by conventional means. An isothermal Knudsen effusion technique was designed and developed in our laboratory for such measurements. The effusion mass as a function of time is measured in our technique using a thickness shear mode (TSM) acoustic wave sensor, which allows for extremely high (few nanograms) sensitivity. This sensitivity allows for much more rapid determination of low vapor pressures (10-1 to 10-5 Pa) than is possible by other Knudsen effusion techniques. Basing the effusion mass measurement on the TSM sensor as in our apparatus eliminates the typically seen dependence on vibration in conventional microbalance-based effusion techniques. Full design details of our apparatus and specifically the Knudsen cell, based on original equations derived by Knudsen, and many corrections that have been noted in the literature for cell and effusion-hole dimensions, are presented. The accuracy of our methodwas tested by a comparison of published vapor pressure data to vapor pressure data acquired in our laboratory with measurements on naphthalene and catechol.