Factors of inhibitory effect on cancer cell growth
It can be seen that the growth of cancer cells increases the temperature by 0.32° C. relative to the ambient temperature (incubator, 37.0° C.). Considering the effect of the RB, it is thought that the thermal radiation due to this temperature rise was reflected by the upper and lower RBs and was constantly irradiated to the cancer cells, which affected their proliferation.
In the case of the heating plate, the ambient temperature of the culture dish was 35.0°C, but continuous heat transfer from the bottom maintained the culture solution at 37.68°C, which is believed to have affected the growth of the cancer cells.
In the culture experiment where the incubator was set to 37.4°C, the temperature of the culture dish increased, but it was found that there was no thermal radiation (heat absorption by the cancer cells) from the surroundings of the culture dish (incubator, 37.4°C).
Based on the above considerations, it is believed that continuously applying heat to the cancer cells in the culture medium will have an effect on the cancer cells.
In experiments using RB, the continuous thermal radiation to cancer cells in the culture dish is thought to be influenced by the transparency of the thermal radiation of the culture dish itself, in addition to the reflection by RB. In the case of heating plate, heat is not only transferred to the culture dish by thermal conduction, but, we can consider, also by the effect of thermal radiation penetrating the culture dish.
Effects of electromagnetic waves
Since heat (energy) is transmitted (radiated) as electromagnetic waves, when RB is used, it is thought that the reflectance of electromagnetic waves by RB and the electromagnetic wave transmittance of the culture dish (polystyrene) are related. The reflectance of RB has already been measured1. The transmittance of the culture dish was as shown in FIG.2.
When using RB, the heat generated by the cancer cells themselves penetrates the culture dish, is reflected by the RB, penetrates the culture dish, and irradiates the cancer cells themselves.
When using a heating plate, the heat of the heating plate is not only transferred to the culture medium via the culture dish by heat conduction, but also electromagnetic waves from the heating plate are transferred to the cancer cells through the culture dish.
So, Planck's formula was used to investigate the spectral characteristics of both.
When using RB
The culture medium was mostly water, and the emissivity of water was assumed to be 0.96.
The heat distribution of the culture solution is as follows.
E(37.68, λ)*0.96 (F1.1)
Radiation from the culture medium is radiated into the space within the culture dish above.
Heat is transferred downward to the culture dish by thermal conduction.
The culture dish (upper) (37.0°C) receives radiation from the culture medium (37.68°C) at 96% intensity,
A portion of this radiation that has passed through the culture dish (polystyrene) (transmittance = α) is reflected by RB (reflectance = δ), passes through the culture dish again, and is radiated to the culture solution. (δ = 0.95.)
E(37.68,λ)*0.96*α*0.95*α (F1.2)
The culture dish (bottom) is at 37.68°C due to heat conduction from the culture solution (37.68°C).
Then radiant heat is emitted to the gap (space) between the RB and the culture dish and is reflected by the RB.
Assuming that the transmittance of the culture dish (polystyrene) is α and the reflectance is 0, the emissivity is (1-α). (Reflectance + Transmittance + Absorptivity = 1.0, Absorptivity = Emissivity)
Radiation from the culture dish (bottom) to the RB below is reflected by the RB, transmitted through the culture dish (bottom), and radiated into the culture medium.
E(37.68,λ)*(1-α)*0.95*α (F1.3)
The ratio of the total heat distribution reflected by RB (F1.2 + F1.3) to the heat distribution of the culture medium (F1.1) was calculated. The results of this calculation are shown in FIG. 4 (vertical axis: energy intensity and ratio, horizontal axis: wavelength in µm).
When using a heating plate
At equilibrium, the heat from the heating plate (40.1°C) is transferred through the culture dish to the culture, resulting in the culture at 37.68°C. Since the absorption rate of the culture dish is (1-α), it is thought that the culture solution also absorbs heat at that ratio, so the heat distribution of the culture solution was assumed as follows.
E(37.68,λ)*(1-α) (F2.1)
Radiation from the heating plate (aluminum plate) and radiation from the culture dish (bottom) are considered.
The emissivity of the heating plate (aluminum) is generally 0.06, and the culture medium is irradiated through the culture dish.
E(40.1,λ)*0.06*α (F2.2)
The emissivity of the culture dish (40.1°C) changes from transmittance (α) to (1-α), and the heat is reflected by the aluminum plate (reflectance = 0.9), passes through the culture dish, and irradiates the culture solution.
E(40.1)*(1-α)*0.9*α (F2.3)
In addition, the ratio of the total heat distribution transferred from the heating plate (F2.2 + F2.3) to the heat distribution of the culture medium (F2.1) was calculated. The results of this calculation are shown in FIG. 5 (vertical axis: energy intensity and ratio, horizontal axis: wavelength: µm).
Mid-infrared wavelength that inhibits cancer cell growth
The ratio peaks (52.59%, 60.36%) at 4.8 µm both with RB and with the hot plate. In addition, in experiments using mid-infrared irradiation, electromagnetic waves of 4.5, 4.8, 5.4, and 5.9 µm were irradiated, and the effect on cancer cells was confirmed only at 4.8 µm. (4.8µm of mid-infrared laser is 2100cm-1, so it is 4.7619µm.)
Also, polystyrene is measured in units of 2 µm, and even in the case of RB/heating plate calculation, it cannot be said that the peak is exactly 4.8 µm.
However, from the results of these experiments and calculations, it is considered reasonable that the effects of electromagnetic waves around 4.8 µm suppressed the growth of cancer cells.
In the previous report1, it was pointed out that the effects of far-infrared rays in the range of 4 to 25 µm are due to the structural characteristics of RB, but the suppression of prostate cancer cell growth is not due to the structural characteristics of RB. It is presumed that there is a difference in the heat distribution (mid-infrared around 4.8 µm) of cancer cells due to the function of the culture dish (polystyrene) as a filter.