Pregled bibliografske jedinice broj: 871824
Cooling of the plain bearing of ball mill drive in the production of Portland cement
Cooling of the plain bearing of ball mill drive in the production of Portland cement // Book of abstract 25HSKIKI / Šantić, Ana ; Đaković, Mirjana (ur.).
Zagreb: Hrvatsko kemijsko društvo, 2017. str. 179-179 (poster, međunarodna recenzija, sažetak, znanstveni)
CROSBI ID: 871824 Za ispravke kontaktirajte CROSBI podršku putem web obrasca
Naslov
Cooling of the plain bearing of ball mill drive in the production of Portland cement
Autori
Martinac, Vanja ; Radeljić, Ana ; Jakić, Jelena ; Labor, Miroslav
Vrsta, podvrsta i kategorija rada
Sažeci sa skupova, sažetak, znanstveni
Izvornik
Book of abstract 25HSKIKI
/ Šantić, Ana ; Đaković, Mirjana - Zagreb : Hrvatsko kemijsko društvo, 2017, 179-179
Skup
XXV. hrvatski skup kemičara i kemijskih inženjera
Mjesto i datum
Poreč, Hrvatska, 19.04.2017. - 22.04.2017
Vrsta sudjelovanja
Poster
Vrsta recenzije
Međunarodna recenzija
Ključne riječi
plain bearing, shell and tube heat exchenger, overall heat transfer coefficient, heat transfer surface area
Sažetak
The purpose of this study is to examine the characteristics of industrial shell and tube heat exchanger (MIT05) with fixed tube bundles, 2-pass tube side, for cooling of mineral oil that lubricated plain bearings ball-mill raw material in the production of Portland cement. Through the tube bundle, which consists of 44 copper pipes with the outer diameter of 10 x 1 mm and the length of 404 mm, in two passes, streaming cooling water inlet temperature 21 °C, with volume flow of 1 m3/h. Mineral oil flows inside the shell and around the tube, with volume flow of 8 L/min. The pipes are laid out in a triangular fashion and pitched 13 mm apart. There are 6 baffles inside the shell. The results of examination indicate the laminar flow (Re < Re, c) inside the tubes and shell. Until the oil temperature rises by 5, 5 oC the the available surface area of heat transfer is greater than required and meets the set requirements. As the oil temperature rises up of 5, 5 oC the surface required to exchange heat also rises compared with available surface, while the multi-tube exchanger no longer fulfills the requirements for cooling the mineral oil. By increasing the flow of cooling water is coming to an increase in the tube-side mass flow rate of water and the transition from laminar flow in the transitional area (2300 < Re < 10000). This increases the overall heat transfer coefficient and reduces the required surface heat exchanger to transfer the same amount of heat.
Izvorni jezik
Engleski
Znanstvena područja
Kemijsko inženjerstvo
POVEZANOST RADA
Ustanove:
Kemijsko-tehnološki fakultet, Split