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trans-1,3,3,3-Tetrafluoropropene

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trans-1,3,3,3-Tetrafluoropropene (HFO-1234ze(E), R-1234ze(E)) is a hydrofluoroolefin. It was developed as a "fourth generation" refrigerant to replace fluids such as R-134a, as a blowing agent for foam and aerosol applications, and in air horns and gas dusters.[3] The use of R-134a is being phased out because of its high global warming potential (GWP). HFO-1234ze(E) itself has zero ozone-depletion potential (ODP=0), a very low global warming potential (GWP < 1 ), even lower than CO2, and it is classified by ANSI/ASHRAE[4] as class A2L refrigerant (lower flammability (see below) and lower toxicity).[5]

trans-1,3,3,3-Tetrafluoropropene
Names
Preferred IUPAC name
(1E)-1,3,3,3-Tetrafluoroprop-1-ene
Other names
R-1234ze(E); HFO-1234ze(E); trans-1,3,3,3-tetrafluoro-1-propene; trans-1,3,3,3-tetrafluoropropylene; trans-1,3,3,3-tetrafluoroprop-1-ene
Identifiers
3D model (JSmol)
ChemSpider
ECHA InfoCard 100.238.116 Edit this at Wikidata
EC Number
  • 471-480-0
UNII
  • InChI=1S/C3H2F4/c4-2-1-3(5,6)7/h1-2H/b2-1+ checkY
    Key: CDOOAUSHHFGWSA-OWOJBTEDSA-N checkY
  • InChI=1/C3H2F4/c4-2-1-3(5,6)7/h1-2H/b2-1+
    Key: CDOOAUSHHFGWSA-OWOJBTEDBQ
  • F[C@H]=CC(F)(F)F
Properties
C3H2F4
Molar mass 114.043 g·mol−1
Appearance Colorless gas[1]
Melting point −156 °C (−249 °F; 117 K)[2]
Boiling point −19 °C (−2 °F; 254 K)[1][2]
Critical point (T, P) 109.4 °C, 36.36 bar[2]
0.373 g/L[1][2]
Vapor pressure 703 kPa at 310 K
Except where otherwise noted, data are given for materials in their standard state (at 25 °C [77 °F], 100 kPa).
☒N verify (what is checkY☒N ?)

Properties

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The structure of trans-1,3,3,3-tetrafluoropropene was investigated both in the gas state (gas electron diffraction) and in the crystalline phase (X-ray diffraction). In the crystal, it aggregates via C-H---F contacts from 2.44(1) to 2.63(1) Å.[6] Combustion experiments with trans-1,3,3,3-tetrafluoropropene produce carbon dioxide, carbonyl fluoride and hydrogen fluoride as the main combustion products. The determination of the flammability range leads to the classification of trans-1,3,3,3-tetrafluoropropene as a highly flammable gas.

Uses

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The increasing concerns about global warming and the related possible undesirable climate effects have led to an increasing agreement in developed countries for the reduction of greenhouse gas emissions. Given the relatively high global warming potential of most of the hydro-fluoro-carbons (HFCs), several actions are ongoing in different countries to reduce the use of these fluids. For example, the European Union's recent F-Gas regulation[7] specifies the mandatory GWP values of the refrigerants to be used as working fluids in almost all air conditioners and refrigeration machines beginning in 2020.[8]

Several types of possible replacement candidates have been proposed so far, both synthetic and natural. Among the synthetic options, hydro-fluoro-olefins (HFOs) are the ones appearing most promising thus far.

HFO-1234ze(E) has been adopted as a working fluid in chillers, heat pumps, and supermarket refrigeration systems.[9][10][11] There are also plans to use it as a propellant in inhalers.[12]

It has been demonstrated that HFO-1234ze(E) can not be considered as a drop-in replacement of HFC-134a. In fact, from a thermodynamic point of view, it can be stated that:

– The theoretical coefficients of performance of HFO-1234ze(E) is slightly lower than HFC-134a;

– HFO-1234ze(E) has a different volumetric cooling capacity when compared to HFC-134a.

– HFO-1234ze(E) has saturation pressure drops higher than HFC-134a during two-phase heat transfer under the constraint of achieving the same heat transfer coefficient.[13]

So, from a technological point of view, modifications to the condenser and evaporator designs and to compressor displacement are needed to achieve the same cooling capacity and energetic performance of HFC-134a.[8]

See also

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References

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  1. ^ a b c "MSDS Resource Centre". msds-resource.honeywell.com.
  2. ^ a b c d Solstice® ze Refrigerant (HFO-1234ze) : Low GWP Hydrofluoroolefins (HFO) : The Environmental Alternative to Traditional Refrigerants, Honeywell Belgium N.V., FPR-003/2015-01. Accessed 2024-01-05.
  3. ^ Honeywell Sells Novel Low-Global-Warming Blowing Agent To European Customers Archived 2016-03-03 at the Wayback Machine, Honeywell press release, Oct. 7, 2008
  4. ^ ANSI/ASHRAE Standard 34, 2010. Designation and Safety Classification of Refrigerants.
  5. ^ "The environmental alternative to traditional refrigerants". Honeywell. 2015. p. 2.
  6. ^ Jan Schwabedissen, Timo Glodde, Yury V. Vishnevskiy, Hans‐Georg Stammler, Lukas Flierl, Andreas J. Kornath, Norbert W. Mitzel: Structures and Properties of trans ‐1,3,3,3‐Tetrafluoro‐ propene (HFO‐1234ze) and 2,3,3,3‐Tetrafluoropropene (HFO‐1234yf) Refrigerants. In: ChemistryOpen. Band 9, Nr. 9, September 2020, ISSN 2191-1363, S. 921–928, doi:10.1002/open.202000172
  7. ^ Regulation (EU) No 517/2014
  8. ^ a b Giulia Righetti, Claudio Zilio, Simone Mancin & Giovanni A. Longo (2016): A review on in-tube two-phase heat transfer of hydro-fluoro-olefines refrigerants, Science and Technology for the Built Environment, DOI:10.1080/23744731.2016.1229528
  9. ^ Longo, Giovanni A.; Zilio, Claudio; Righetti, Giulia; Brown, J. Steven (2014). "Condensation of the low GWP refrigerant HFO1234ze(E) inside a Brazed Plate Heat Exchanger". International Journal of Refrigeration. 38: 250–259. doi:10.1016/j.ijrefrig.2013.08.013.
  10. ^ Longo, Giovanni A.; Mancin, Simone; Righetti, Giulia; Zilio, Claudio (2016). "HFO1234ze(E) vaporisation inside a Brazed Plate Heat Exchanger (BPHE): Comparison with HFC134a and HFO1234yf". International Journal of Refrigeration. 67: 125–133. doi:10.1016/j.ijrefrig.2016.04.002.
  11. ^ Longo, Giovanni A.; Mancin, Simone; Righetti, Giulia; Zilio, Claudio (2016). "Saturated flow boiling of HFC134a and its low GWP substitute HFO1234ze(E) inside a 4 mm horizontal smooth tube". International Journal of Refrigeration. 64: 32–39. doi:10.1016/j.ijrefrig.2016.01.015.
  12. ^ "AstraZeneca partners with Honeywell on development of HFO-1234ze MDIs". www.oindpnews.com.
  13. ^ Brown, J.S., C. Zilio, R. Brignoli, and A. Cavallini. 2013. Heat transfer and pressure drop penalization terms (exergy losses) during flow boiling of refrigerants. International Journal of Energy Research 37:1669–79.
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