Reflections
on the motive power on heat of the environment and on machines fitted to
develop that power
I imagined
that the issue goes beyond physics and moves in the field of chemistry, and
will have to leave ... but it is not easy to me stop thinking about it. These are
ten years till now - think themselves come, whether I want or do not want. So
since I announced that I stop, I saw development for the physical framework of
the process of making the cold part of the unit with endothermic chemical
processes. Even a "devil" whispered to me: "Do not be silly!
Patented it!" The "devil"
managed to tempt me ,and I handed application with the patent office. Here's
how things went with endothermic processes:
Previous post
ended like this:
I thought,
Wait a minute! You should be warm and working substance in the environment. I was thinking about chemical processes and have neglected the physical basis for them and engine. But physics should outline the basics to open bigger opportunities for chemistry. So
things came to diagram 4
Then they
seized me thinks - Will I get cold in the cold part after heat up the working
substance in the environment, and then again with the exothermic reaction
between α and β ? Instead of turning to energy equations I saw technical solution:
We will use the mixer – diagram 5
Control
valves 13 and 14, and so the temperature of the working substance we can change
from the temperature of the heat
exchanger 1 (when the valve 14 is closed) to ambient temperature (when the
valve 13 is closed).
Then I saw
the flaw in this chart - waste a cold. Unit will become more efficient if we use
cold working substance and compound out of the cold part to cool the α and β before entering the heat exchanger 1. So the device evolved as chart 6
Evolution
underwent and unit using an endothermic solution for low temperatures in the cold
part diagram 7
For example -
solvent α is ammonia (240K; boiling
point). At a temperature of 290K (17C) ammonia gases have a pressure of 8 MPa.
Solute αβ to be a mystical salts AxBy.
Hypothetically - AxBy was dissolved in ammonia by this chemical process is
endothermic.
Working substance
γ let's fluoromethyl CH3F (R-41; 195K bp).
In the heat
exchanger 1 of the drawing 7 ammonia boils and the solution was separated
into ammonia and AxBy. Ammonia gases perform work in the turbine 5, where they
enter the heat exchanger 2. In heat exchanger 2 ammonia liquefies due to heat
exchange with the liquid working substance CH3F. A pump (7) takes the liquid
ammonia in the heat exchanger 3.
Salts AxBy
separated from the solution pump 8 (probably screw) them ending up at 4 heat
exchanger to cool them before you take them in a heat exchanger 3 diagram 7.
Working substance CH3F is pre-cooled and
liquefied to a temperature between its boiling point and its freezing point. In
heat exchanger 2, it is heated to a temperature of 240K. The pressure is increased
and it is boiling. Gases CH3F perform work in the turbine 6. From there enter
the heat exchanger 3 where liquefy due to low temperature created by the
dissolution of salts AxBy in the solvent ammonia. Pump 7 takes liquified working
substance CH3F first in heat exchanger 4 to cool the solute AxBy and then in
heat exchanger 2 to receive heat from the gases ammonia and so the cycle of
working substance is repeated.
Ammonia
boiling in the heat exchanger 1, perform work in the turbine 5, salts are
dissolved in ammonia in the heat exchanger 3, solution heat exchange first with
AxBy in a heat exchanger 4, then (possibly) with ammonia and fluoromethyl in a
heat exchanger 2 and out of the heat insulating part where is heat exchanger 1 to heat from the surrounding
environment and the process to begin again. In this renewable process would
receive mechanical energy from both turbines 5 and 6 at the expense of the heat
of the environment:
