Intensified heat transfer technologies for enchanced heat recovery intheat grant agreement 262205
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Ji ří J KLEME Š, Petar S VARBANOV EC Marie Currie Chair (EXC) “INEMAGLOW” - PowerPoint PPT Presentation


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“Intensified Heat Transfer Technologies for Enchanced Heat Recovery” INTHEAT (Grant Agreement 262205). Ji ří J KLEME Š, Petar S VARBANOV EC Marie Currie Chair (EXC) “INEMAGLOW” Research Institute of Chemical Technology and Process Engineering – CPI 2 , Faculty of Information Technology

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Intensified heat transfer technologies for enchanced heat recovery intheat grant agreement 262205

“Intensified Heat Transfer Technologies for Enchanced Heat Recovery”INTHEAT (Grant Agreement 262205)

Jiří J KLEMEŠ, Petar S VARBANOV

EC Marie Currie Chair (EXC) “INEMAGLOW”

Research Institute of Chemical Technology

and Process Engineering – CPI2,

Faculty of Information Technology

University of Pannonia, Veszprém, Hungary


Outline
Outline Recovery”

  • CPI2 at the University of Pannonia

  • Research Background

  • P-graph for Process Synthesis

  • Books and Other Publications

  • Involvement of CPI2-UOP in INTHEAT


Cpi 2 at the university of pannonia
CPI Recovery”2 at the University of Pannonia




Professor ferenc friedler dean faculty of information technology
Professor Ferenc Friedler, Dean Recovery”Faculty of Information Technology

Development of P-graph and S-graph frameworks (Co-founder)

Process Network Synthesis

Batch Process Scheduling

Energy Saving and Pollution Reduction

Reaction Pathway Identification

Knight's Cross Order of Merit of the Republic of Hungary, Budapest, Hungary, 2003

László Kalmár Prize (John von Neumann Computer Science Society), Budapest, Hungary, 2003

Neumann Prize (John von Neumann Computer Science Society), Budapest, Hungary, 2007

Széchenyi Prize, Budapest, Hungary, 2010


Cpi 2 centre for process integration and intensification
CPI Recovery”2Centre for Process Integration and Intensification

Prof Jiří J Klemeš

Chair Holder

Prof Zdravko Kravanja,

University of Maribor

Assoc. Prof.

Dr Petar Varbanov

PhD Students

Dr László Sikos

CUM LAUDEGraduate

Andreja Nemet

Lidija Čuček

Luca De Benedetto

Hon LoongLam

Zsófia Fodor


Research background
Research background Recovery”


UMIST: History Recovery”

  • 1824 Created by industrialists as the Manchester Mechanics Institution

  • 1905 Faculty of Technology, University of Manchester

  • 1956 Royal Charter granted to Manchester College of Science and Technology

  • 1965 University of Manchester Institute of Science and Technology

  • 2004 Merged with University of Manchester


Centre for process integration

Centre for Recovery”Process Integration

World Leaders in Process Design Technology


Research directions
Research directions Recovery”


Most resent research
Most Resent Research Recovery”

Cell-based dynamic heat exchanger models – direct determination of the cell number and size

Petar SabevVarbanov, Jiří JaromirKlemeš, Ferenc Friedler


Heat exchange cell
Heat exchange cell Recovery”

  • H=”Hot”, C=”Cold”;

  • HI=”Hot Inlet”, HO=”Hot Outlet”

  • CI=”Cold Inlet”, CO=”Cold Outlet”

Cell model: icon representation

Cell model: detailed picture

mH

hHI

mH

hHO

QCELL

mC

hCI

mC

hCO

Assumptions

Definition

  • Perfect mixing in the fluid cells

  • Constant fluid densities

  • The tanks are completely full

  • Constant specific heat capacities

  • The thermal resistance of the wall is neglected

  • The wall heat capacity is taken into account

  • Two perfectly stirred tanks, exchanging heat only with each other through a dividing wall


Cell model of a heat exchanger
Cell model of a heat exchanger Recovery”

  • A complete heat exchanger can be modelled by a number of cells

  • The cells are combined to reflect the internal flow arrangement in the exchanger

Single-pass (1-1) heat exchanger

mHOT,

hOUT,HOT

mHOT,

hIN,HOT

mCOLD,

hOUT,COLD

mCOLD,

hIN,COLD


Cell model of a heat exchanger1
Cell model of a heat exchanger Recovery”

1-2 shell-and-tube heat exchanger (no baffles)


Cell model of a heat exchanger2
Cell model of a heat exchanger Recovery”

1-2 shell-and-tube heat exchanger (with baffles)


Minimum number of cells
Minimum number of cells Recovery”

Derivation

Temperature

Heat exchange


Summary on the cell model
Summary on the cell model Recovery”

  • Distributed models become inefficient for complex heat exchangers

  • From the lumped– mostly cell models are employed

  • The cell parameters need to be carefully estimated accounting for the underestimation of the temperature differences

  • A method for direct identification of the number of cells has been developed

  • Mostly applicable to shell-and-tube heat exchangers

  • A useful visualisation of the cell number identification procedure is provided

  • The method can be further extended to the other kinds of heat exchangers


P graph for process synthesis
P-graph for Process Synthesis Recovery”

Friedler, F., J.B. Varga, and L.T Fan. (1995), Decision-Mapping A Tool for Consistent and Complete Decisions in Process Synthesis, Chem. Eng. Sci., 50(11):1755-1768


P graph a rigorous mathematical tool
P-graph: a Rigorous Mathematical Tool Recovery”

Suite of tools

Search space

  • Axioms for feasible networks

  • Algorithm MSG

  • Algorithm SSG

103–106 x

  • Exploit the problem structure

  • Much faster

  • Superior to direct Mathematical Programming


P graph algorithms maximal structure generation msg
P-graph algorithms: Recovery”Maximal Structure Generation (MSG)

Problem Formulation

Reduction part

Consistent sets O & M

Composition part

Maximal Structure

  • Problem Formulation

    • set of raw materials

    • set of products

    • set of candidate operating units

  • Superstructure (Maximal)

    • Union of all combinatorially feasible structures

    • Rigorous super-structure

Legend:

O: set of operating units; M: set of materials


Abb algorithm even faster search
ABB Algorithm – Even Faster Search Recovery”

  • Employs the “branch-and-bound” strategy

  • Combines this with the P-graph logic (SSG algorithm)

  • Ensures combinatorial feasibility

Non-optimal decisions are eliminated from the search



Applying p graph combined heat and power using fccc
Applying P-graph: Recovery”Combined Heat and Power using FCCC


Configuration and setup
Configuration and Setup Recovery”

Demands: 10 MW power and 15 MW heat

Power: 100 €/MWh

Heat: 30 €/MWh

Natural gas: 30 €/MWh

Fertiliser from biogas digestion: 50 €/t

Plant life: 10 y

Case studies

Limit the availability of the biomass to 30 MW


Fuel preparation options
Fuel Preparation Options Recovery”

Biomass

Gasifier

Syngas

Filter

Biogas

digester

Performance per unit input

Streams / Materials

AR: Agricultural residues PR: Particulates

BR: Biomass residues SG: Syngas

RSG: Raw syngas BG: Biogas

CO2: Carbon dioxideFRT: Fertiliser


Energy conversion options
Energy Conversion Options Recovery”

Fuel Cell

Combined Cycle

Biogas

Boiler

Natural Gas

Boiler

Performance per unit input

{F}: Fuels {FCCC} {Q}: steam Steam details {Q}: steam Steam details

NG: Natural gas MCFC-GT Q1 P = 1 bar Q20 P = 20 bar

BG: Biogas MCFC-ST Q2 P = 2 bar Q40 P = 40 bar

SG: Syngas SOFC-GT Q5 P = 5 bar

SOFC-ST Q10 P = 10 bar


Results
Results Recovery”

Case 4;

Biomass at 10 €/MWh

Profit: 5.51 MM€/y

Cases 1, 2, 3;

Biomass < 18 €/MWh

Profit: 10.05 / 6.48 / 6.23 MM€/y

Biomass

MAX 30 MW


Results summary
Results Summary Recovery”

  • Biomass is profitable over a wide price range

  • Topologies relatively robust until tipping point

  • Fertiliser – marginal significance

The trade-off between the Agricultural Residues – Natural Gas prices dominates the designs


P graph for fccc summary
P-graph for FCCC Summary Recovery”

  • Biomass viable for FC

  • High efficiency  lower resource demand

  • Energy supply and conversion: complex systems

  • Synthesising : combinatorially difficult

  • P-Graph: appropriate tool effectively solving the task

  • Successfully applied to choosing FCCC - based system design



Recent publication
Recent Publication Recovery”

IF2008 = 1.712

IF2009 = 2.952

Citations: 10


Recent publication1
Recent Publication Recovery”

IF2009 = 1.987

Citations: 4


Citations
Citations Recovery”

2008

2009

2010


Handbook of Water and Energy Management in Food Processing Recovery”Edited by J Klemeš, University of Pannonia R Smith and J-K Kim, University of Manchester, UK


Coming book
Coming Book Recovery”


Eminent 2 workshop
EMINENT 2 Workshop Recovery”


Involvement of cpi 2 uop in intheat
Involvement of CPI Recovery”2-UOP in INTHEAT


Contribution to work packages
Contribution to Work Packages Recovery”

  • WP 1 (Months 1-12): Analysis of intensified heat transfer under fouling, 6 person-months, Task 1.1

  • WP 2 (Months 1-18): Combined tube-side and shell-side heat exchanger enhancement, 1 person-month, Task 2.2

  • WP 4 (Months 1-24): Design, retrofit and control of intensified heat recovery networks, 9.5 person-months, Tasks 4.1 and 4.3. This will be a development of the P-graph methodology using the ABB algorithm

  • WP 5 (Months 12-24): Putting into practice, 5 person-months, Tasks 5.2 and 5.3


Leader of wp 6 technology transfer
Leader of WP 6 “Technology transfer” Recovery”

Aim: Effective technology transfer to the wide range academic and industrial communities

  • Validation of the developed novel methodology with the SME partners.

  • Dissemination of the project results, aiming to achieve the best possible project recognition over a broad audience

  • Develop suitable training and support materials for SME partners

  • Establish an active community involving the INTHEAT partners and other users/experts for continuous knowledge management and improvement


Wp 6 technology transfer
WP 6 “Technology Transfer” Recovery”

  • Runs during months 6 – 24

  • Tasks:

    • 6.1. Technology transfer to SME consortium members

    • 6.2. Dissemination events

    • 6.3. Publications

    • 6.4. Training


Task 6 1 technology transfer to sme consortium members
Task 6.1. Technology transfer to SME consortium members Recovery”

  • Streamlined transfer of the developed and acquired technologies, licenses and know-how among the consortium all members

  • A special emphasis will be put on the technology transfer to the industrial partners

    Principles

  • All outputs/deliverables from WPs 1 to 5 will be checked for documentation in such a way, as to enable technology users to obtain reproducible results

  • Additional application procedures may be needed


Task 6 2 dissemination events
Task 6.2. Dissemination events Recovery”

Intensified heat exchangers – Novel developments

Information day for major stakeholders

Organisers: UNIPAN, PIL, UNIMAN

Has to be delivered by Month 8

Suggested: PRES’11, 8-11 May 2011, Florence, Italy



14 Recovery”th Conference Process Integration, Modelling

and Optimisation for Energy Saving and

Pollution Reduction

8-11 May 2011, Florence, Italy

Organiser & Secretariat

Raffaella DAMERIO

The Italian Association of Chemical Engineering

Via Giuseppe Colombo 81A

20133 Milano (Italy)

Phone:+39-02-70608276

Fax:+39-02-59610042

Email: [email protected]

Hon Loong LAM

(Scientific Programme Secretary)

Phone: +36-88-421664

Fax: +44 871 244 774

Email: [email protected]

Website: www.conferencepres.com


Chemical engineering transactions cet
Chemical Engineering Transactions (CET) Recovery”

<www.aidic.it/cet>


Task 6 2 dissemination events1
Task 6.2. Dissemination events Recovery”

Enhanced heat transfer

Workshop/session at a recognised international conference

Organisers: UNIPAN, CALGAVIN, EMBAFFLE, SODRU

Has to be delivered by Month 12

Suggested: 6-th Dubrovnik Conference on Sustainable Development of Energy, Water and Environment Systems, September 25 - 29, 2011, Dubrovnik, Croatia


Task 6 2 dissemination events2
Task 6.2. Dissemination events Recovery”

Software Demonstration Workshop

Workshop/session at a recognised international conference

Organisers: UNIPAN, PIL, UNIMAN

Has to be delivered by Month 18

Suggested: A dedicated workshop to be held in the summer of 2012, at PRES 2012


Task 6 2 dissemination events3
Task 6.2. Dissemination events Recovery”

Joint Hub for Intensified Heat Exchangers

Workshop held by all academic partners with the support of the industrial partners

Has to be delivered by Month 22

Suggested: A dedicated workshop to be held in Veszprém in September-October 2012


Task 6 3 publications
Task 6.3. Publications Recovery”

  • Three major conferences will be held during the project execution: PRES’11 (May 2011), SDEWES 2011 (September 2011), PRES 2012. It is expected that at least 9 conference publications will be delivered

  • Scientific articles in refereed journals: minimum 4 papers are planned

  • Wider dissemination to the public, authorities, environmentalists and decision-making bodies


Task 6 4 training
Task 6.4. Training Recovery”

  • The major training will be carried out in form of workshop at UNIPAN, scheduled for delivery by Month 23 (October 2012).

  • Suggested venue: To be organised as a follow-up event after the workshop “Joint Hub for Intensified Heat Exchangers” from Task 6.2, Veszprém in September-October 2012

  • The relevant training materials have to be available before the workshops. Suggested delivery – by June-July 2012, to allow for testing and fine-tuning



Thank you for your attention! Recovery”

Veszprém, Castle


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