Mixed working medium and application thereof
A technology of mixed working medium and thermal working medium, which is applied in the direction of refrigerators, heat pumps, lighting and heating equipment, etc. It can solve problems such as accidents, system performance reduction, and exhaust temperature exceeding, so as to reduce operation and use costs and volume control The effect of large heat and small temperature glide
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[0045] The preparation method of the mixed working fluid of the present invention is to physically mix each component substance (and optionally the lubricating oil, additives or additional components, etc.) according to a specified mass ratio at normal temperature.
[0046] The mixed working medium of the present invention can be applied to any conventional medium-high temperature heat pump system, but does not include a fractional condensation heat pump system, and there is no special limitation other than that.
[0047] The medium-high temperature heat pump system is a vapor compression cycle system, which is composed of a compressor, a condenser, a throttling element, an evaporator, etc., and may also include a subcooler, an oil separator, and a vapor-liquid separator. The working principle of the medium and high temperature heat pump system will be described below.
[0048]First, the low-pressure liquid mixed working medium (such as the mixed working medium of the present ...
Embodiment 1-10
[0081] 1,1,1,2,3,3,3-heptafluoropropane (R227ea), 1,1,1,3,3,3-hexafluoropropane (R236fa) and 1,1-difluoroethane (R152a) According to the composition ratio in Table 2, physical mixing is carried out in the liquid phase to obtain the mixed working fluids of Examples 1-10 of the present invention, and the working conditions are as follows: condensation dew point temperature 80°C, superheat degree 10°C, supercooling Its performance was tested under the condition of temperature of 2°C and evaporating dew point temperature of 30°C, the results are shown in Table 2.
Embodiment 11-28
[0085] 1,1,1,2,3,3,3-heptafluoropropane (R227ea), 1,1,1,3,3,3-hexafluoropropane (R236fa) and 1,1-difluoroethane (R152a) According to the composition ratio in Table 3, physical mixing is carried out in the liquid phase to obtain the mixed working fluids of Examples 11-28 of the present invention, and the working conditions are respectively: condensation dew point temperature 90°C, superheat degree 10°C, supercooling Its performance was tested under the condition of temperature of 2°C and evaporating dew point temperature of 30°C. The results are shown in Table 3.
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