Towards energy efficient distillation technologies – Making the right choice
- 1. AkzoNobel Research, Development and Innovation, Process Technology ECG, Zutphenseweg 10, 7418 AJ Deventer (Netherlands)
- 2. Process Systems Engineering Group, Eindhoven University of Technology, P.O. Box 513, 5600 MB, Eindhoven (Netherlands)
- 3. Process and Energy Laboratory, Delft University of Technology, Leeghwaterstraat 44, 2628 CA Delft (Netherlands)
Description
In spite of claiming around half of the operational costs of chemical plants, distillation is still the most popular separation technology. Distillation has low thermodynamic efficiency, requiring the input of high quality energy in the reboiler – while rejecting a similar amount of heat at lower temperature, in the condenser. Several heat pump concepts have been proposed to upgrade that thermal energy and reduce the consumption of valuable utilities. Under certain conditions, the energy savings of heat pump assisted distillation is usually around 20–50%. This study proposes a novel selection scheme of energy efficient distillation technologies, with a special focus on heat pumps. The most promising technologies selected are vapor compression, mechanical or thermal vapor recompression, absorption, compression–resorption and thermo-acoustic heat pumps, multi-effect distillation, heat integrated distillation column, cyclic distillation, Kaibel and dividing-wall column. The scheme considers as the main selection criteria the type of separation tasks, product flow and specifications, operating pressure, difference in boiling points, reboiler duty and its temperature level. Moreover, this scheme is very practical, allowing major time and resources savings in the design of eco-efficient processes. -- Highlights: ► Heat pump assisted distillation with energy savings of 20–50%. ► Novel and practical selection scheme of energy efficient distillation technologies. ► Evaluation of promising technologies: VC, MVR, TVR, AHP, CHRP, TAHP, HIDiC, DWC, CyDist. ► Selection criteria include: ΔTb, ΔTlift, P, Treb, Qreb, volatility. ► Design of eco-efficient processes with high COP, and lower TIC and TAC.
Availability note (English)
Available from http://dx.doi.org/10.1016/j.energy.2012.09.038Additional details
Identifiers
- DOI
- 10.1016/j.energy.2012.09.038;
- PII
- S0360-5442(12)00716-5;
Publishing Information
- Journal Title
- Energy (Oxford)
- Journal Volume
- 47
- Journal Issue
- 1
- Journal Page Range
- p. 531-542
- ISSN
- 0360-5442
- CODEN
- ENEYDS
Conference
- Title
- 1. Asia-Pacific forum on renewable energy
- Acronym
- AFORE 2011
- Dates
- 16-19 Nov 2011
- Place
- Busan (Korea, Republic of)
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 45025048
- Subject category
- S42: ENGINEERING;
- Resource subtype / Literary indicator
- Conference
- Descriptors DEI
- BOILING POINTS; CHEMICAL PLANTS; COMPRESSORS; DISTILLATION; DISTILLATION EQUIPMENT; ECONOMICS; ELECTRIC UTILITIES; ENERGY EFFICIENCY; HEAT EXCHANGERS; HEAT PUMPS; OPERATING COST; VAPOR CONDENSERS
- Descriptors DEC
- COST; EFFICIENCY; EQUIPMENT; INDUSTRIAL PLANTS; PHYSICAL PROPERTIES; PUBLIC UTILITIES; SEPARATION PROCESSES; THERMODYNAMIC PROPERTIES; TRANSITION TEMPERATURE
Optional Information
- Copyright
- Copyright (c) 2012 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.