1996
DOI: 10.1016/0098-1354(95)00217-0
|View full text |Cite
|
Sign up to set email alerts
|

Heat exchanger network design for multipurpose batch plants

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
4
1

Citation Types

0
20
0

Year Published

2001
2001
2021
2021

Publication Types

Select...
5
3
1

Relationship

0
9

Authors

Journals

citations
Cited by 50 publications
(20 citation statements)
references
References 6 publications
0
20
0
Order By: Relevance
“…Corominas and co-workers (Corominas et al, 1993(Corominas et al, , 1994Grau et al, 1996) published three papers which addressed energy and waste minimisation in multiproduct batch processes. Vaklieva-Bancheva and co-workers (Vaklieva-Bancheva and Ivanov, 1993;Vaklieva-Bancheva et al, 1996) developed a MILP solution for heat exchange network design for multipurpose batch plants in which only direct heat exchange is considered. The same authors reported a case study on heat integration for an antibiotics batch-manufacturing process .…”
Section: Energy Integration For Continuous and Batch Processesmentioning
confidence: 99%
“…Corominas and co-workers (Corominas et al, 1993(Corominas et al, , 1994Grau et al, 1996) published three papers which addressed energy and waste minimisation in multiproduct batch processes. Vaklieva-Bancheva and co-workers (Vaklieva-Bancheva and Ivanov, 1993;Vaklieva-Bancheva et al, 1996) developed a MILP solution for heat exchange network design for multipurpose batch plants in which only direct heat exchange is considered. The same authors reported a case study on heat integration for an antibiotics batch-manufacturing process .…”
Section: Energy Integration For Continuous and Batch Processesmentioning
confidence: 99%
“…Vaklieva-Bancheva and Ivanov [4] purposed a MILP formulation for heat exchange network design for multipurpose batch plants where direct heat exchange is considered. In their later work [7], a single level formulation that selects the production campaigns and the design of cost-optimal heat exchanger network simultaneously is addressed. The main limitation of the formulation is that each batch stage must operates in a zero-wait mode with a fixed processing time.…”
Section: Introductionmentioning
confidence: 99%
“…Subsequent to this, other mathematical formulations for heat integration of batch processes have been proposed by Peneva et al [14], Ivanov et al [3], Corominas et al [2], Papageorgiou et al [13], Vaklieva-Bancheva et al [17], and Adonyi et al [1]. Peneva et al [14] and Ivanov et al [3] addressed the problem of designing a minimum total cost heat exchanger network for given pair wise matches of batch vessels.…”
Section: Introductionmentioning
confidence: 99%
“…The main drawback of all discrete-time formulations is their explosive binary dimension, which requires enormous computational effort [16]. VaklievaBancheva et al [17] improved the work of Ivanov et al [3] by embedding the heat integration framework within an overall scheduling framework. However, the authors only addressed a special case in which the plant is assumed to operate in a zerowait overlapping mode, where each product must pass through a subset of the equipment stages, and production is organized in a series of long campaigns.…”
Section: Introductionmentioning
confidence: 99%