Structure of warm-up field in liquids near bottom of channel and share of energy, walking  on the evaporation.

   Will Value first temperature of overheat of water under the channel. As far as energy on the evaporation is deliver to the border to the account of heat conduction from the depth of liquid, possible value a gradient of temperature near of borders dT/dZ , Z - the coordinate in depth of liquids, ensuring density of heat    flow  on the vaporization: , where x - the heat conduction of water: .
For the expected value  @  1000 Wt \ cm × cm  will have
dT/ dZ  @  130000 degree/cm .
For rough evaluation will take that maximum of warm-up profile in liquids happens to approximately on depth of penetration
 of light  Z@  a - 1 , where    a - a factor of absorbing a light in water
(a @ 5 00/ cm  - on the length of wave 10,6 mkm). Then for temperature in maximum an will have
 
 that answers an enourmous overheat (near critical temperature of water
T = 374° C under the atmospheric pressure) Pic.7a.
This evaluation is uprate on two reasons. As far as in experiment near of
the bottom of channel are obviously observe turbulent moving a liquid -
(Photo d,b), the heat conduction can be realize in turbulent mode, i.e. efficient factor of the thermal diffusivity , where  DV - a distinctive scale of the turbulent fluctuation of the velocity of flow, l - distinctive (maximum) amount of turbulence. Upper border for  1cm /sec ×  0.1@  0.1 cm × cm  / sec , that on two orders above the heat conduction of water. So at presence of the turbulent
transfer are  potentially possible reduce an overheat of liquid before  »  2,5° .Other mechanism, not allow observable overheat, is ablation away heats from the area heat release by the convection flows downwards from the point of channel - refer to Pic.2. Follows to notice that value  gives  a share of energy , walking upwards, i.e. to surfaces of evaporation, and are consumption on the vaporization. Exactly this part of the heat release accounts for the area Z< Zn , where flow of heat is direct to surfaces. Remaining portion of the select heat , account for Z< Zn , leaves downwards and disperses on heating up of the main mass of liquid,rather then on its evaporation. On experimental given this share   » 0.5, that allows to expect that  Zn  »  1.The most,stabilization of overheat must occur, mainly, to the account of turbulence, rather then the convection ablation of the heat.

                      The radiation screen by vapours a water.

      As far as in the experiment less than 25% lazer power disperses on the evaporation and heating of liquid, possible expect that before the surface of bottom reaches only small share of powers of lazer bunch. Value a possibility an the radiation screen a ferry in the most channel and on the route from the lens before the surface of water.
       Factor of absorbing molecular pair nongreat ( @  0.0005·1/ cm  - under
@ 1atm), that gives very small values of absorbing ~ 0.01 , that can not explain an observed effect. However, necessary to take into consideration, that vapour,
moving on the increase crater, is coolled and so it is condense. As shown in the book [4], for the pair in the manner of drops with the amount ~ 10 mkm (order of wavelength) each droplet absorbs and diffuses practically all fall on
 it radiation. Using results [4 ], possible value a factor of absorbing a pair a n as follows:  , where a -absorbing factor of water.,  r  - density a pair, density a water  = 1g /cm3 , x  - a share of a condensation pair , Rk - a radius of drop of a condensation part. Under  r   ~ 0.001 g / cm3  and  x  ~ 1 for a n   will have  evaluation a n ~ 0.1 × 1 / cm . This means that big part of the light will absorption on the distance  ~10cm. Thereby , the screen is wholly possible.
     Since this fact is confirm in following experiments , we see a natural way of raising efficiency of lazer influence on the liquid an airflow route of spreading a ray from the lens before the surface. Possible hope that  îáäóâà routes will sufficiently, to raise efficiency before limiting, as far as condensation will occur, mainly, outside of the steam channel, where vapour inheres under the action of powerful irradiating  - 1000 Wt / cm× cm , under which condensations effectively prevents an evaporation of drop ( bleaching aerosol) by the powerful
 light influence.  Time lifes dripped under such influence ~ 0.01 sec, that corresponds to the order a time of the passage of gas on the channel.