Consiliul



Yüklə 354,7 Kb.
səhifə3/4
tarix22.01.2018
ölçüsü354,7 Kb.
1   2   3   4



Key persons list (their CVs are uploaded on the web platform)




Name and surname*

Scientific title

Phase

Person-month

Coordinator (CO)

Lazar Mihaela Diana

CS II Dr.

1,2,3,4

33




Almasan Valer

CS I Dr. Eng.

1,2,3,4

12

Partner 1

Cormos Calin Cristian

Assoc. Prof. Dr. Eng.

1,2,3,4

18

Cormos Ana Maria

Lecturer

Dr.


1,2,3,4

12

Partner 2

Roman Cecilia

CSI Dr.

1,2,3,4

20

Senila Lacramioara

Drd. Eng

1,2,3,4

30

Partner 3

Koncz

Iuliu-Carol



Eng.

1,3,4

10




Dan Radu Cristian

Eng.

1,3,4

4

Partner 4

Petcu Cristian Mihai

Dr. Eng

3,4

18




Dumitrescu Anca Madalina

Dr. Eng

3,4

18

Total

180



Available research infrastructure

There will be made a distinction between the infrastructure of ICT and the rest of the research infrastructure (equipments and facilities for experimentation, own or available through cooperation relationship with other institutions)

(max 1 page)

CO INCDTIM has in its laboratory all the equipment and knowhow necessary to prepare nanostructured supported metal catalysts. For catalysts characterization: Sorptomatic 1990 by Thermoelectron Corporation for adsorption desorption measurements; Bruker D8 XRD advanced diffractometer; Specs spectrometer for XPS measurements; SDT Q 600 (TA Instruments) thermogravimetric analyzer. For catalysts testing, the necessary set up composed by: Microreactivity Reference Catalytic Reactor (PID Eng.&Tech) online with gas chromatograph (produced by ITIM) and Quadrupole Mass Spectrometer (Prisma Plus from Pfeiffer Vacuum) to analyze the gaseous products, and a Waters HPLC chromatograph equipped with ultraviolet and refractive index detectors to analyze the liquid products.

P1 UBB The infrastructure used by P1 in this project is divided in (1) Information technology (IT) infrastructure composed by Computers: Intel 2000-4000 MHz, 2-6 GB RAM, and Software: ChemCAD, Aspen, Thermoflow, GaBi4, Matlab etc and (2) Experimental infrastructure: Chemical Reaction Engineering laboratory and whole infrastructure of control and analytical monitoring of chemical processes; Modeling, Simulation, Optimization and Control of Chemical Processes laboratory .

P2 ICIA performs analyses for biofuels quality certification through its laboratory CABIO according to the European standard EN 14214 for biodiesel and European standard SR EN 15376 for bioethanol. The relevant infrastructure of CABIO consists in gas chromatograph (Agilent 6890N) with mass detector (Agilent 5975B), ECD and MPD detectors (Agilent 6890N), FID detector (Agilent 7890A), liquid chromatograph (Agilent 1200 Series) coupled to mass spectrometer (Applied Biosystem 3200 Qtrap), HPLC (Perkin Elmer 1801-037 series), FT-IR Spectrometer (Perkin Elmer, Spectrum BX).

P3 Reviva developed an original technology for biodiesel production from soy oil. The relevant infrastructure consists in: horizontal oil press – pressing capacity 1t/h, 380 V electric power; tehnological line for preparation of raw materials – capacity 2t/h; pumps for viscous liquids – capacity 100 l/h, pumping high 5m; POLSTIF tanks – capacity 30t

P4 Rokura The infrastructure used by P4 in this project is: (i) Software Labview industrial monitoring option; Lab AMESIM – software; Data Acquisition portal 1,8 GB Intel PM; (ii)Autoclave Mahoney Robinson; Spinning Catalyst Basket Reactor 350 bar, 350 ⁰C;




Budget breakdown by year (lei)

Public Budget

Private cofinancing (PC)

Total

PC

2012

2013

2014

2015

Total

2012

2013

2014

2015

Total

2012

2013

2014

2015

Total

%

CO

450000

350000

400000

100000

1300000

0

0

0

0

0

450000

350000

400000

100000

1300000

0

P1

80000

110000

110000

100000

400000

0

0

0

0

0

80000

110000

110000

100000

400000

0

P2

185000

315000

200000

100000

800000

0

0

0

0

0

185000

315000

200000

100000

800000




P3

25000

0

200000

25000

250000

12000

0

97700

12000

121700

37000

0

297700

37000

371700

32.7

P4

0

0

200000

50000

250000

0

0

61700

60000

121700

0

0

261700

110000

371700

32.7

Total

740000

775000

1110000

375000

3000000

12000

0

159400

72000

243400

752000

775000

1269400

447000

3243400

7.50


Budget breakdown by category of expenses

Budget breakdown / destination (lei)1




Personnel costs

Logistics

Travel

Indirect costs

Total

Equipments

Materials

Subcontracting

Coordinator (CO)

Public Budget

603666

345000

18000

0

15000

318334

1300000

Private cofinancing

0

0

0

0

0

0

0

Partner 1

Public Budget

212000

85000

15000

0

25000

63000

400000

Private cofinancing

0

0

0

0

0

0

0

Partner 2

Public Budget

517000

45000

43000

20000

24000

151000

800000

Private cofinancing

0

0

0

0

0

0

0

Partner 3

Public Budget

43000

0

207000

0

0

0

250000

Private cofinancing

32000

0

89700

0

0

0

121700

Partner 4

Public Budget

240000

0

10000

0

0

0

250000

Private cofinancing

121700

0

0

0

0

0

121700

Total

1769366

475000

382700

20000

64000

532334

3243400



Table 4. Justification of purchasing major pieces of equipment




Equipment name and characteristics

Justification

(CO)

Integrated system for catalysts characterization

Posibility to have constant temperature, controled increase temperature, constant and controled flows. Analyser is FID coupled with mass spectrometer.



We intend to acquire at the beginning of the project (Stage 1) an integrated system for catalysts characterization. This equipment will enable us to have more rapid and accurate results to describe: (i) the surface (adsorptive) and catalytic (nature of catalytic sites) properties of a catalytic material by performing TPD and TPR measurements and (ii) the catalyst deactivation by determining the nature and quantity of deposited materials on the catalytic surface after catalyzed reaction (TPO and TPR measurements). For additivated catalysts used in this proposal these parameters are not fully explored at this hour and the results obtained by using the mentioned equipment are extremely important to fulfill the project objectives.




Gas chromatograph

Two columns, FID and TCD detectors



This equipment will be used for on-line detection of reaction products in phase of catalysts testing. It will be part of the experimental set-up used to produce hydrogen.

Partner 1

Information technology (computer/notebook, IT accessories)

Software licenses (Thermoflex; ChemCAD, Aspen, GaBi4, Matlab etc.)

These equipments will be used for mathematical modeling and simulation of hydrogen production by catalytic reforming processes (IT and softwares aquisition), model validation vs. experimental results, research and dissemination activities (writing project deliverables, articles, patent applications etc.).




On-line gas-chromatograph with multiple chanels

This equipment will be used for experimental evaluations to complete the existing experimental infrastructure devoted to study the carbon capture processes.

Partner 2

Fermentor

♦ Power mains: 190-245 V AC/50-60 Hz;Display: LDC 4 × 40 fermentor vessel Pyrex glass Temperature: control special radiation heat source with gilded reflector 100 W



Can be used for fermentation of sugars solution for bioethanol production. Fermentor ensures optimal conditions for the production of bioethanol from lignocellulosic biomass: pH, temperature, time, etc. Fermentor has 1 liter capacities, ideal for heat induction, growth of S. cerevisiae, as well as traditional anerobic and aerobic culture from recombinant microbial, yeast and fungal cells. Set-up and start-up assistance is included in fermentor




  1. Yüklə 354,7 Kb.

    Dostları ilə paylaş:
1   2   3   4




Verilənlər bazası müəlliflik hüququ ilə müdafiə olunur ©muhaz.org 2020
rəhbərliyinə müraciət

    Ana səhifə