{"status":"ok","message-type":"work","message-version":"1.0.0","message":{"indexed":{"date-parts":[[2025,6,2]],"date-time":"2025-06-02T06:05:09Z","timestamp":1748844309241},"reference-count":7,"publisher":"ASME International","issue":"1","content-domain":{"domain":["asmedigitalcollection.asme.org"],"crossmark-restriction":true},"short-container-title":[],"published-print":{"date-parts":[[2004,2,1]]},"abstract":"<jats:p>Process Integration has been applied in several industrial processes mainly using standard shell and tube heat exchangers (1-1 or 1-2). The flow arrangement in 1-2 multiple shell and tube heat exchangers involves part counter-current flow and part co-current flow. This fact is accounted for in the design by introducing a FT correction factor into the 1-1 heat exchanger design equation. To avoid some steep regions in the feasible space of heat exchangers design some authors introduce other parameters like XP or G. Until now it was not possible to have an overall map to give some guidelines of how to choose between the several XP approaches established in the literature. This paper summarizes the current existing criteria in a general design algorithm DeAl12 to show a path for the calculations of the main design variables of the heat exchanger. Also a new strategy design algorithm StratDeAl12 is introduced in this paper to allow the best choice between the existing XP approaches based on the heat exchanger cost minimisation. Several examples illustrate the advantage of using the developed algorithm and the deviations obtained in the heat exchanger cost if a wrong approach was chosen.<\/jats:p>","DOI":"10.1115\/1.1643087","type":"journal-article","created":{"date-parts":[[2004,3,11]],"date-time":"2004-03-11T23:04:40Z","timestamp":1079046280000},"page":"119-130","update-policy":"http:\/\/dx.doi.org\/10.1115\/crossmarkpolicy-asme","source":"Crossref","is-referenced-by-count":10,"title":["A Cost-Based Strategy to Design Multiple Shell and Tube Heat Exchangers"],"prefix":"10.1115","volume":"126","author":[{"given":"Raquel D.","family":"Moita","sequence":"first","affiliation":[{"name":"Departamento de Engenharia Qu\u0131\u00b4mica, Instituto Superior Te\u00b4cnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal"}]},{"given":"Cristina","family":"Fernandes","sequence":"additional","affiliation":[{"name":"Departamento de Engenharia Qu\u0131\u00b4mica, Instituto Superior Te\u00b4cnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal"}]},{"given":"Henrique A.","family":"Matos","sequence":"additional","affiliation":[{"name":"Departamento de Engenharia Qu\u0131\u00b4mica, Instituto Superior Te\u00b4cnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal"}]},{"given":"Clemente P.","family":"Nunes","sequence":"additional","affiliation":[{"name":"Departamento de Engenharia Qu\u0131\u00b4mica, Instituto Superior Te\u00b4cnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal"}]}],"member":"33","published-online":{"date-parts":[[2004,3,10]]},"reference":[{"key":"2019100600284557900_r1","unstructured":"Smith, R., 1995, Chemical Process Design, McGraw-Hill, New York, Chap. 7."},{"key":"2019100600284557900_r2","doi-asserted-by":"crossref","unstructured":"Ahmad, S., Linnhoff, B., and Smith, R., 1988, \u201cDesign of Multipass Heat Exchangers: An Alternative Approach,\u201d ASME J. Heat Transfer, 110, pp. 304\u2013309.","DOI":"10.1115\/1.3250484"},{"key":"2019100600284557900_r3","unstructured":"Shenoy, U. V., 1995, Heat Exchanger Network Synthesis\u2014Process Optimization by Energy and Resources Analysis, Gulf Publishing Company, Houston, pp. 255\u2013264, Chap. 6."},{"key":"2019100600284557900_r4","doi-asserted-by":"crossref","unstructured":"Gulyani, B. B. , 2000, \u201cEstimating Number of Shells in Shell and Tube Heat Exchangers: A New Approach Based on Temperature Cross,\u201d ASME J. Heat Transfer, 122, pp. 566\u2013571.","DOI":"10.1115\/1.1287159"},{"key":"2019100600284557900_r5","unstructured":"Wales, R. E. , 1981, \u201cMean Temperature Difference in Heat Exchangers,\u201d Chem. Eng., 88(4), pp. 77\u201381."},{"key":"2019100600284557900_r6","doi-asserted-by":"crossref","unstructured":"Santos, L. C., and Zemp, R. J., 2000, \u201cEnergy and Capital Targets for Constrained Heat Exchanger Networks,\u201d Braz. J. Chem. Eng., 17(4\u20137), pp. 659\u2013669.","DOI":"10.1590\/S0104-66322000000400030"},{"key":"2019100600284557900_r7","doi-asserted-by":"crossref","unstructured":"Floudas, C. A., 1995, Nonlinear and Mixed-Integer Optimization\u2014Fundamentals and Applications, Oxford University Press, Oxford, UK, pp. 314\u2013315.","DOI":"10.1093\/oso\/9780195100563.003.0011"}],"container-title":["Journal of Heat Transfer"],"original-title":[],"language":"en","link":[{"URL":"http:\/\/asmedigitalcollection.asme.org\/heattransfer\/article-pdf\/126\/1\/119\/5736991\/119_1.pdf","content-type":"application\/pdf","content-version":"vor","intended-application":"syndication"},{"URL":"http:\/\/asmedigitalcollection.asme.org\/heattransfer\/article-pdf\/126\/1\/119\/5736991\/119_1.pdf","content-type":"unspecified","content-version":"vor","intended-application":"similarity-checking"}],"deposited":{"date-parts":[[2021,6,15]],"date-time":"2021-06-15T02:46:01Z","timestamp":1623725161000},"score":1,"resource":{"primary":{"URL":"https:\/\/asmedigitalcollection.asme.org\/heattransfer\/article\/126\/1\/119\/444577\/A-CostBased-Strategy-to-Design-Multiple-Shell-and"}},"subtitle":[],"short-title":[],"issued":{"date-parts":[[2004,2,1]]},"references-count":7,"journal-issue":{"issue":"1","published-print":{"date-parts":[[2004,2,1]]}},"URL":"https:\/\/doi.org\/10.1115\/1.1643087","relation":{},"ISSN":["0022-1481","1528-8943"],"issn-type":[{"value":"0022-1481","type":"print"},{"value":"1528-8943","type":"electronic"}],"subject":[],"published":{"date-parts":[[2004,2,1]]}}}