Automated formulation of optimisation models for steel beam structures

Over 70% of the total costs of an end product are consequences of decisions that are made during the design process. A search for optimal cross-sections will often have only a marginal effect on the amount of material used if the geometry of a structure is fixed and if the cross-sectional characteristics of its elements are property designed by conventional methods. In recent years, optimalgeometry has become a central area of research in the automated design of structures. It is generally accepted that no single optimisation algorithm is suitable for all engineering design problems. An appropriate algorithm, therefore, mustbe selected individually for each optimisation situation. Modelling is the mosttime consuming phase in the optimisation of steel and metal structures. In thisresearch, the goal was to develop a method and computer program, which reduces the modelling and optimisation time for structural design. The program needed anoptimisation algorithm that is suitable for various engineering design problems. Because Finite Element modelling is commonly used in the design of steel and metal structures, the interaction between a finite element tool and optimisation tool needed a practical solution. The developed method and computer programs were tested with standard optimisation tests and practical design optimisation cases. Three generations of computer programs are developed. The programs combine anoptimisation problem modelling tool and FE-modelling program using three alternate methdos. The modelling and optimisation was demonstrated in the design of a new boom construction and steel structures of flat and ridge roofs. This thesis demonstrates that the most time consuming modelling time is significantly reduced. Modelling errors are reduced and the results are more reliable. A new selection rule for the evolution algorithm, which eliminates the need for constraint weight factors is tested with optimisation cases of the steel structures that include hundreds of constraints. It is seen that the tested algorithm can be used nearly as a black box without parameter settings and penalty factors of the constraints.

On the Reversed Brayton Cycle with High Speed Machinery

This work was carried out in the laboratory of Fluid Dynamics, at Lappeenranta University of Technology during the years 1991-1996. The research was a part of larger high speed technology development research. First, there was the idea of making high speed machinery applications with the Brayton cycle. There was a clear need to deepen theknowledge of the cycle itself and to make a new approach in the field of the research. Also, the removal of water from the humid air seemed very interesting. The goal of this work was to study methods of designing high speed machinery to the reversed Brayton cycle, from theoretical principles to practical applications. The reversed Brayton cycle can be employed as an air dryer, a heat pump or a refrigerating machine. In this research the use of humid air as a working fluid has an environmental advantage, as well. A new calculation method for the Braytoncycle is developed. In this method especially the expansion process in the turbine is important because of the condensation of the water vapour in the humid air. This physical phenomena can have significant effects on the level of performance of the application. Also, the influence of calculating the process with actual, achievable process equipment efficiencies is essential for the development of the future machinery. The above theoretical calculations are confirmed with two different laboratory prototypes. The high speed machinery concept allows one to build an application with only one rotating shaft including all the major parts: the high speed motor, the compressor and the turbine wheel. The use of oil free bearings and high rotational speed outlines give several advantages compared to conventional machineries: light weight, compact structure, safe operation andhigher efficiency at a large operational region. There are always problems whentheory is applied to practice. The calibrations of pressure, temperature and humidity probes were made with care but still measurable errors were not negligible. Several different separators were examined and in all cases the content of the separated water was not exact. Due to the compact sizes and structures of the prototypes, the process measurement was slightly difficult. The experimental results agree well with the theoretical calculations. These experiments prove the operation of the process and lay a ground for the further development. The results of this work give very promising possibilities for the design of new, commercially competitive applications that use high speed machinery and the reversed Brayton cycle.

Vannesahalinjan tuotantokapasiteetin kasvattaminen konstruktiota kehittämällä

Tässä tutkimuksessa selvitetään, mitä muutoksia vannesahalinjan koneisiin tulee tehdä, jotta syöttönopeutta voidaan nostaa. Lisäksi työn perusteella on onnistuttu sahaamaan tuotannossa ohuemmalla terärungolla samalla mittatarkkuudella kuin aikaisemmin paksummalla terärungolla. Työssä on kartoitettu kyseessä olevan vannesahalinjan todennäköisimmät pullonkaulat nopeutta nostettaessa. Lisäksi on tarkasteltu mittauksin eräiden kriittisten koneiden käyttäytymistä sahauksen aikana. Mittausten perusteella on tehty ehdotukset tarvittaville konstruktiomuutoksille, jotta sahaus korotetulla nopeudella onnistuu hyvällä mittatarkkuudella. Tutkimuksen aikana on kehitetty mittausjärjestelmä, jolla vannesahan teräpyörien muoto voidaan mitata ja siirtää tietokoneelle myöhempää tarkastelua ja arkistointia varten.

Kalvojen vertailu heran nanosuodatuksessa

Työssä verrattiin kaupallisia nanosuodatuskalvoja heran konsentroinnissa. Tutkitut kalvot olivat Desal-5 DK, NF45 ja Koch SR1. NF45-kalvosta tutkittiin kahta eri sukupolven kalvoa. Konsentrointiajoja tehtiin sekä laboratoriomittakaavan levysuotimella että pilot-mittakaavan spiraalimoduulilaitteella. Lisäksi tutkittiin juoksute- ja happoheran konsentrointien eroja. Erityistä huomiota kiinnitettiin permeaattivuon arvoihin konsentroinnissa ja kalvojen suolojen ja laktoosin pidätyskykyyn. NF45-kalvon uuden sukupolven malli osoittautui mittauksissa samankaltaiseksi suolojen ja laktoosin pidätyskyvyltään kuin Desal-5 DK. Koch SR1-kalvo, jonka suolojen ja laktoosin pidätyskyky on Desal-5 DK-kalvoa heikompi, puolestaan vastaa ominaisuuksiltaan NF45 vanhan sukupolven kalvoa. Vanhan sukupolven NF45-kalvon valmistus on loppunut keväällä 2000. Vaihdettaessa vanhan sukupolven NF45-kalvot uuden sukupolven kalvoihin on odotettavissa pienemmät permeaattivuot ja suuremmat suolojen ja laktoosin retentiot kuin aiemmin NF45-kalvolla. Juoksuteheran konsentroinnissa suurimmat permeaattivuot saatiin Koch SR1-kalvolla. Levysuotimella ja spiraalimoduulilla saadaan koostumukseltaan samanlainen juoksuteheratiiviste. Levysuotimella permeaattivuot ovat samalla konsentrointikertoimella suuremmat kuin spiraalimoduulilla. Tämä johtuu spiraalimoduuliin jäävistä kuolleista alueista, joissa ei ole virtausta. Uutta prosessia suunniteltaessa voidaan käyttää laboratoriomittakaavan levysuodinkokokeita, kun halutaan tietoa saatavan tuotteen koostumuksesta. Prosessin tuotantokapasiteetin arvioimiseen tarvitaan pilot-mittakaavan spiraalimoduulikokeita. Happoheratiiviste sisältää enemmän suoloja kuin samalla kalvolla valmistettu juoksuteheratiiviste. Tämä johtuu happoheran juoksuteheraa suuremmasta suolapitoisuudesta. Lisäksi happoheran konsentroinnin permeaattivuo on pienempi kuin juoksuteheran permeaattivuo, sillä happoheran alhainen pH, noin 4,5, vaikuttaa kalvon permeabiliteettiin heikentävästi.